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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145784310.1021/acsomega.7b00848ArticleMagnetic Co-Doped MoS2 Nanosheets for Efficient
Catalysis of Nitroarene Reduction Nethravathi C. Prabhu Janak Lakshmipriya S. Rajamathi Michael *Materials Research Group,
Department of Chemistry, St. Joseph’s
College, 36 Lalbagh Road, Bangalore 560027, India* E-mail: mikerajamathi@rediffmail.com.18 09 2017 30 09 2017 2 9 5891 5897 23 06 2017 30 08 2017 Copyright © 2017 American Chemical Society2017American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
Co-doped
MoS2 nanosheets have been synthesized through
the hydrothermal reaction of ammonium tetrathiomolybdate and hydrazine
in the presence of cobalt acetate. These nanosheets exhibit a dominant
metallic 1T phase with cobalt ion-activated defective basal planes
and S-edges. In addition, the nanosheets are dispersible in polar
solvents like water and methanol. With increased active sites, Co-doped
MoS2 nanosheets exhibit exceptional catalytic activity
in the reduction of nitroarenes by NaBH4 with impressive
turnover frequencies of 8.4, 3.2, and 20.2 min–1 for 4-nitrophenol, 4-nitroaniline, and nitrobenzene, respectively.
The catalyst is magnetic, enabling its easy separation from the reaction
mixture, thus making its recycling and reusability simple and efficient.
The enhanced catalytic activity of the Co-doped 1T MoS2 nanosheets in comparison to that of undoped 1T MoS2 nanosheets
suggests that incorporation of cobalt ions in the MoS2 lattice
is the major reason for the efficiency of the catalyst. The dopant,
Co, plays a dual role. In addition to providing active sites where
electron transfer is assisted through redox cycling, it renders the
nanosheets magnetic, enabling their easy removal from the reaction
mixture.
document-id-old-9ao7b00848document-id-new-14ao-2017-00848eccc-price
==== Body
1 Introduction
Two-dimensional
(2D) MoS2 nanosheets1 have garnered
interest as a potential noble-metal-free
catalyst for the electrochemical generation of hydrogen from water2−4 and hydrodesulfurization of petroleum.5,6 Theoretical
and experimental studies indicate that the catalytic activity of the
thermodynamically stable 2H polymorph of MoS2 is associated
with its metallic edges, whereas its semiconducting basal plane is
catalytically inert.2,4
In this context, nanostructures
of MoS2, amorphous7−9/crystalline,10−13 and vertically aligned structures14,15 have been
explored to maximize the number of active edge sites. MoS2 is also hybridized with conducting/semiconducting/magnetic materials
(graphene15−19/CoSe220/CoS21−24/CdS25,26/Fe3O427) to enhance
the catalytic activity through synergetic coupling effects. Metastable,
intrinsically metallic, octahedral 1T MoS2 obtained through
exfoliation of trigonal prismatic 2H MoS2 has proven to
be an excellent catalyst for H2 evolution reactions as
the 1T phase facilitates electrode kinetics by increasing the electric
conductivity and proliferation of the catalytic active sites.28−30 Introducing transition metal ions (Co, Ni, Fe) into the MoS2 matrix has been the classic route to maximize the catalytic
activity of MoS2, as the doped ions alter the electronic
properties at the coordinatively unsaturated catalytic S-edges.10,31,32 These strategies have been designed,
largely, to either optimize the density of active edge sites by reducing
the dimensions along the z direction or xy direction (nanostructures)33 or increase
the conductivity by stabilizing the 1T MoS2 polytype.19,28,29 The question is, would it be
possible to tune both the structural features and electronic properties
simultaneously to increase the catalytic active sites? Doping 2H MoS2 with Co has been shown to increase its catalytic efficiency
through increased active sites in the basal planes in addition to
edges.34 It would be of interest to prepare
Co-doped 1T MoS2 because in addition to all of the above
effects, there would be increased conductivity.
One of the standard
reactions to test the electron transfer catalytic
action is the reduction of nitroarenes by NaBH4. Nitroarenes,
with aromatic rings associated with H-bonding −NH2 and −OH groups, enable the reduction to be carried out in
water, making it a green reaction. This study demonstrates a single-step
robust strategy to synthesizing 1T Co-doped MoS2 nanosheets.
With increased active sites, Co-doped MoS2 nanosheets exhibit
exceptional catalytic activity in the reduction of nitroarenes. The
observed turnover frequency (TOF) is far superior in comparison to
that of other MoS2 architectures and noble-metal-based
catalysts, reported so far.
2 Results and Discussion
The XRD pattern of as-prepared Co-doped MoS2 nanosheets
(Figure 1A,a) exhibits
a broad 002 reflection at 11.0 Å, indicating the presence of
guest species in the interlayer.35,36 The guest
entity could possibly be NH3/NH4+ ions released as byproducts of hydrazine used as a reductant in
the hydrothermal reaction.
Figure 1 (A) XRD patterns of Co-doped MoS2 nanosheets (a) as-prepared
and (b) treated with 1 N HCl and of (c) MoS2 prepared in
the absence of cobalt. (B) Raman spectrum of Co-doped MoS2 nanosheets in comparison with bulk MoS2.
On treating Co-doped MoS2 nanosheets
with 1 N HCl solution,
the 002 reflection (Figure 1A,b) disappears, indicating deintercalation of the guest species.
However, the low intensity of the 002 reflection or its absence (Figure 1A,a,b) suggests that
Co-doped MoS2 nanosheets are poorly ordered along the stacking
direction and comprise largely exfoliated layers. The asymmetric 2D
reflections at 2θ = 33 and 57° reveal the presence of stacking
faults37,38 within the few-layered Co-doped MoS2. The undoped MoS2 is also poorly ordered and exhibits
increased basal spacing due to NH3/NH4+ intercalation (Figure 1A,c).
The Raman spectrum of Co-doped MoS2 (Figure 1B) exhibits the in-plane
E2g (380 cm–1) and out-of-plane A1g (406 cm–1) Mo–S vibration modes,
characteristic
of the MoS2 layered structure. An additional peak at 220
cm–1 in Figure S1 (Supporting Information, SI) indicates the presence
of 1T polytype. Increased full width at half-maximum and the shift
in the A1g and E2g modes of Co-doped MoS2 in comparison to those of bulk MoS2 clearly indicate
softening of A1g and E2g modes and phonon confinement
that is expected for mono- to few-layer MS2, thus indicating
that the Co-doped MoS2 comprises mono to few layers.39,40
The chemical composition of the Co-doped MoS2 was
further
probed by X-ray photoelectron spectroscopy (XPS). Mo 3d and S 2p spectra
(Figure 2a,b; Table 1) correspond to
Mo4+ and S2– of the 1T polytype of MoS2. A small proportion of the 2H polytype coexists with the
1T phase.41 The N 1s spectrum (Figure 2c; Table 1) indicates the presence of
NH3 and NH4+ ions, which are accommodated
in the interlayer of MoS2 nanosheets, as suggested by the
XRD pattern (Figure 1a).35 The core-level Co 2p spectra (Figure 2d; Table 1) confirm the presence of Co2+ species. The XRD pattern (Figure 1a) and the XPS Co 2p spectra confirm the
absence of CoS2 and CoMo2S4. The
binding energy of 779.2 eV is close to what has been observed for
CoMo2S4, suggesting that Co2+ substitutes
Mo atoms along the {002} or the S-edge planes of MoS2.
The atomic percentages of Co, Mo, S, and N are 4.68, 24.66, 59.38,
and 11.27, respectively, leading to a chemical composition of Co0.16Mo0.83S2(NH3)0.38.
Figure 2 XPS spectra showing Mo 3d (a), S 2p (b), N 1s (c), and Co 2p (d)
core-level peak regions of Co-doped MoS2.
Table 1 Summary of the Binding Energies of Mo, S, Co and N in Co-doped MoS2
binding energy
(eV)
Mo 3d phase S 2p Co 2p N 1s
Mo0.83Co0.16S2(NH3)0.38 228.6 & 231.8 1T 161.49
& 162.80 779.2 &
794.0 397.6 – NH3
229.0 & 232.5 2H 163.97 & 164.77 400.4 – NH4+
To understand the nature of the chemical
environment of Co2+, the Co-doped MoS2 was treated
with 1 N HCl when
the intercalated or undoped Co2+ species, if any, was expected
to be leached out. Cobalt estimation of the leachate showed that only
about 30% of the cobalt could be leached out by acid. This was further
confirmed by the atomic percentages (Co-3.36, Mo-27.11, S-69.54) in
the acid-leached Co-doped MoS2 arrived at from XPS data.
The composition of the acid-leached sample is Co0.1Mo0.78S2. The XPS spectra of acid-treated Co-doped
MoS2 (SI, Figure S2) indicate
that whereas the nitrogen-containing species, NH3 and NH4+ ions, are absent, Co2+ and 1T phase
of MoS2 nanosheets are retained. These further suggest
that Co2+ is present in the MoS2 lattice. Hydrothermally
synthesized MoS2 has been shown to have a defective basal
plane as well as unsaturated S-edges.42 Recent studies by Liu et al.34 demonstrate
that Co2+ is doped at S vacancies in basal planes as well
as at the unsaturated S-edges.
The magnetic hysteresis loop
measured on the powder sample indicates
a weak ferromagnetic behavior (Figure 3). The saturation magnetization (MS) at 300 K of Co-doped MoS2 nanosheets is
0.0029 emu g–1, which is comparable to that of exfoliated
1T MoS2 reported in the literature.43 Because our control 1T MoS2 is nonmagnetic,
it is fair to assume that the magnetism in Co-doped MoS2 arises as a consequence of doping. The magnetism in monolayer MoS2 and its doped analogues depends on the nature of edges, type
of edge defects, lattice strain, and the dopant concentration. Theoretical
calculations by Wang et al.44 reveal that
low concentrations of 4 and 6% of Co2+ doping in the Mo
vacant sites of the basal planes result in stable magnetic moments
at room temperature. Yun et al.45 and Saab
et al.46 also reported tuning of electronic
and magnetic properties due to doping of metal ions in the MoS2 lattice. The very low MS observed
for Co-doped MoS2 suggests that the weak ferromagnetism
here originates from the strain in the layer rather than from ordering
of Co2+ ions. Co-doped MoS2 (Figure 3) as well as the acid-leached
product is weakly magnetic, suggesting that Co2+ ions are
doped in the MoS2 layers. In addition, the presence of
Co2+ in the MoS2 lattice could be the reason
for the retention of metastable 1T structure even after deintercalation
of the intercalants (SI, Figure S2). All
of these results indicate that Co2+ is possibly doped in
the basal plane and S-edge planes of MoS2 layers.
Figure 3 Hysteresis
loop of the Co-doped MoS2 nanosheets at 300
K.
Clusters of layers are observed
in the SEM image (Figure 4a) of as-synthesized Co-doped
MoS2. The bright-field transmission electron microscopy
(TEM) image (Figure 4b) indicates that the transparent layers are few-layer thick and
few hundred nanometers in lateral dimensions. The HRTEM image (Figure 4c) shows lattice
fringes with a spacing of 1.1 nm, which correlates with the basal
spacing observed in the XRD pattern (Figure 1a), suggesting the presence of intercalants.
The HRTEM image in Figure 4d clearly shows that the layers are crystalline, exhibiting
(100) lattice planes. Except for the circled regions representing
the 2H phase, the layers largely exist as the 1T polytype.43
Figure 4 (a) SEM image, (b) low-magnification bright-field TEM
image, and
(c, d) HRTEM images of Co-doped MoS2.
Figure 5 schematically
depicts the catalytic reduction of nitroarenes. Catalytic performance
of Co-doped MoS2 in the reduction of 4-nitrophenol (4-NP)
in water is summarized in Figure 6a,d–f. UV–visible absorption spectra
(Figure 6a) of the
reaction mixture indicate that 4-nitrophenol converts to 4-aminophenol
within 7 min. The absorption peak at 400 nm is due to the nitro phenolate
ion, and the intensity of this peak decreases with time and disappears
completely at 7 min. Peaks at 235 and 308 nm emerge due to the formation
of amino phenolate, and their intensities increase with time. The
log (absorbance) versus time plot (Figure 6e) is linear (R2 = 0.979), indicating a pseudo-first-order kinetics47,48 with a rate constant of 1.976 × 10–3 s–1. The turnover frequency (TOF) values, defined as
the number of moles of the product formed per unit time per mole of
the catalyst, of the materials studied are given in Table 2.
Figure 5 Schematic representation
of the catalytic reduction of nitroarenes
using Co-doped 1T MoS2.
Figure 6 Reduction of nitroarenes was traced through UV–visible absorption
spectra of the reaction mixture containing 10 mg of the Co-doped MoS2 catalyst, 400 mM NaBH4, and nitroarene. Evolution
of absorption spectra with time in the case of 4-nitrophenol (a),
4-nitroaniline (b), and nitrobenzene (c). Plots of absorbance (d)
and log (absorbance) (e) against time for 4-nitrophenol reduction.
Efficiency of the catalyst (as TOF) in six consecutive cycles of 4-nitrophenol
reduction (f).
Table 2 Catalytic
Activity of the Catalysts
in the Reduction of Nitroarenes
substrate catalyst time (min) TOF (min–1)
4-nitrophenol (37 mM) Co-doped MoS2 (4.7% doping) 7 8.41
Co-doped MoS2 (∼2% doping) 13.5 4.36
Co-doped MoS2 (∼1% doping) 18 3.27
acid-leached Co-doped MoS2 8 7.36
ammoniated MoS2 90 0.65
4-nitroaniline (14 mM) Co-doped MoS2 (4.7% doping) 7 3.15
nitrobenzene (50 mM) Co-doped MoS2 (4.7% doping) 4 20.2
Apart from exhibiting a high TOF, the catalyst also
has the advantage
of recyclability. As the catalyst is weakly magnetic, it is easily
separated from the reaction mixture using a strong magnet, enabling
easy recycling (Figure 5). The catalytic activity of Co-doped MoS2 remains nearly
constant over a number of cycles (Figure 6f). The morphology and composition of the
catalyst remain almost the same after six cycles of catalysis. Earlier
attempts to make MoS2-based catalysts magnetic have been
through hybridization of MoS2 nanosheets with magnetic
nanoparticles such as Fe3O4.27 One of the shortcomings of such approaches is the increased
net weight of the catalyst because the magnetic component of the hybrid
does not provide sites for catalytic action. Here, the advantage is
that the dopant that improves the catalytic efficiency also makes
the catalyst magnetic.
Treating Co-doped MoS2 with
an acid leads to deintercalation
of interlayer NH3/NH4+ and removal
of about 30% of Co2+, which were either intercalated or
in the edge planes. Catalytic reduction of 4-NP using acid-leached
Co-doped MoS2 exhibits a slight decrease in catalytic activity
(Table 2). In contrast,
ammoniated 1T-MoS2 synthesized in the absence of a cobalt
source exhibits relatively very poor catalytic activity toward 4-NP
reduction (Table 2).
The comparison of the catalytic activities (Table 2) of the catalysts used in 4-NP reduction
suggests that incorporation of cobalt ions in the MoS2 lattice
is crucial to maximizing the efficiency of the catalyst.
Figure 6b,c traces
the reduction of nitroaniline and nitrobenzene, respectively, in the
presence of as-prepared Co-doped MoS2. The results show
that the catalyst is universally effective in the reduction of nitro
groups in different substrates and in at least two polar solvents.
In fact, the catalyst is most efficient in the reduction of nitrobenzene,
a reaction that is of importance in the removal of toxic nitrobenzene
from effluents. In all of the cases, reduction of nitroarene does
not occur in the absence of the catalyst.
In comparison to what
has so far been reported in the literature
(Table 3), the enhanced
TOF and recyclability make Co-doped MoS2 a superior catalyst.
The TOF of Co-doped MoS2 is 1 order greater than that of
the best MoS2-based catalyst and ∼20% higher than
the best value reported so far.
Table 3 Comparison of TOF
for the Reduction
of Nitroarenes by Various Catalytic Materials Reported in the Literature
catalyst TOF (min–1) reference
4-nitrophenol reduction
Co-doped MoS2 8.41 present work
1T chemically exfoliated MoS2 0.74 (49)
2H chemically exfoliated MoS2 0.015
MoS2-Fe3O4 4.0 × 10–2 (27)
MoS2-Fe3O4/Pt 6.0 × 10–4 (50)
MoS2-Pd 3.2 × 10–3 (51)
MoS2-Pt
MoS2 2.5 × 10–3
MoS2-Au
MoS2-Ag
Ni0.33Co0.66 2.0 × 10–3 (52)
citrate capped Au nanoparticles 1.4 (53)
Ag dendrites 0.13 (54)
Pd supported on CNTs 6.3 (55)
4-nitroaniline reduction
Co-doped MoS2 3.15 present work
1T chemically exfoliated MoS2 1.39 (49)
Au nanowires 0.10 (56)
dodecahedral Au nanoparticles 0.10 (57)
In Co-doped MoS2, Co2+ takes residence at
the coordinatively unsaturated sulfur vacancies on the basal plane
and edge sites.10,58 This leads to a conversion of
a fraction of Mo4+ to Mo3+, thus stabilizing
the 1T polytype.15 Doped Co2+ distorts the close-packed sulfur layer of MoS2 and induces
lattice strain.59,60 These sites would lower the reaction
free energy.28 Nitroarenes are adsorbed
at the strained active sites of the MoS2 surface.59−61 At these sites, the electron transfer to the substrate is facilitated
by Co2+/Co3+ redox couple. The electrons generated
by the hydrolysis of NaBH4 are transferred to the Co2+-accommodated basal and edge sites of 1T MoS2 and
are promoted into the MoS2 conduction band.59 The Co-substituted sites not only instigate
faster electron transfer for nitroarene reduction through reversible
reduction–oxidation reactions but also serve as an electron
reserve and aid in the retention of the 1T phase with enhanced electrical
conductivity.
The role of Co in improving the catalytic efficiency
is very clear
from the fact that the control MoS2, which has intercalated
NH3/NH4+ and hence has similar access
to surface as that of Co-doped MoS2, shows poor activity
(TOF is 1 order lower). As Co-doped MoS2 is largely few-layer
thick, the lattice expansion by intercalated species may not be very
important and this is borne out from the almost similar activity of
the acid-treated sample, which does not have intercalated species.
This observation may be important when these catalysts are used in
the hydrogen evolution reaction, the reaction medium of which is usually
fairly acidic. To further ascertain the role of Co sites in catalysis,
the catalytic activity of Co-doped MoS2 with varying cobalt
contents was studied. The increase in TOF of 4-nitrophenol reduction
with an increase in Co doping (Table 2) further confirms the importance of Co sites in the
catalyst.
3 Conclusions
Magnetic, 1T Co-doped MoS2 nanosheets with the cobalt
ion-activated defective basal planes and S-edges are synthesized in
a single-step hydrothermal reaction. Readily dispersible in polar
solvents like water or methanol, Co-doped MoS2 nanosheets
exhibit exceptional catalytic activity toward reduction of nitroarenes
at ambient temperature. In addition to exhibiting a high turnover
frequency, the catalyst can be magnetically separated from the reaction
mixture, thus enabling recyclability simple and efficient. The superior
catalytic activity of the Co-doped MoS2 layers may be due
to a combination of (a) stabilization of the metallic 1T phase and
(b) better electron capture from the hydride and electron supply to
the nitroarene substrates through reversible redox reactions at the
Co sites.
4 Experimental Section
4.1 Preparation
of Co-Doped MoS2 Nanosheets
Cobalt acetate (0.214
g) was dissolved in 45 mL of water. Ammonium
tetrathiomolybdate (0.442 g) was added to the pink Co2+ solution, and the mixture was stirred for 15 min. Hydrazine hydrate
(5 mL) was added to the solution, and stirring was continued for another
15 min. The black-brown solution was transferred to a teflon-lined
autoclave and sealed in a stainless steel canister. The autoclave
was heated in a hot-air oven at 180 °C for 24 h and cooled to
room temperature under ambient conditions. The pH of the supernatant
at the end of the reaction was ∼12. The black precipitate was
washed with distilled water till the pH of the washings is ∼7,
followed by washing with acetone. The product was dried in air at
ambient temperature. The preparation was repeated using 0.107 and
0.054 g of cobalt acetate to vary the cobalt content in the product.
4.2 Acid Leaching of Co-Doped MoS2 Nanosheets
To extract the intercalated and free cobalt species, 100 mg of
Co-doped MoS2 was stirred in 5 mL of 1 N HCl for 24 h.
The supernatant was collected. The process was repeated thrice. The
cobalt content in the supernatant was estimated. The black solid was
washed with water followed by acetone and dried in air at ambient
temperature.
4.3 Preparation of MoS2 Nanosheets
As a control experiment, the synthesis
was repeated in the absence
of cobalt acetate, which results in ammoniated MoS2 nanosheets.
4.4 Reduction of Nitroarenes Using Co-Doped MoS2 Nanosheets as a Catalyst
4.4.1 Reduction
of 4-Nitrophenol (4-NP)
The catalyst (10 mg) was dispersed
in 100 mL of water by stirring
for 1 h. 4-NP (512 mg, 37 mM) was dissolved in 100 mL of the catalytic
dispersion. An excess of NaBH4 (1.51 g, 400 mM) was added
with constant stirring [4-NP:NaBH4 molar ratio was 1:12].
The progress of the reaction was monitored by measuring the absorbance
of 4-NP at 400 nm.
4.4.2 Reduction of 4-nitroaniline
(4-NA)
The catalyst (10 mg) was dispersed in 100 mL of water
by stirring
for 1 h. 4-NA (192 mg, 14 mM) was dissolved in 100 mL of the catalytic
dispersion. An excess of NaBH4 (1.51 g, 400 mM) was added
with constant stirring [4-NA/NaBH4 molar ratio was 1:28].
The progress of the reaction was monitored by measuring the absorbance
of 4-NA at 380 nm.
4.4.3 Reduction of Nitrobenzene
(NB)
The catalyst (10 mg) was dispersed in 100 mL of methanol
by stirring
for 1 h. Nitrobenzene (0.52 mL, 50 mM) was dissolved in the dispersion.
An excess of NaBH4 (1.51 g, 400 mM) was added with constant
stirring [NB/NaBH4 molar ratio was 1:8]. The progress of
the reaction was monitored by measuring the absorbance of nitrobenzene
at 259 nm.
In all of the cases, an excess amount of NaBH4 was used to ensure that its concentration could be considered
constant throughout the reaction and the molar ratio in each case
was optimized at the lowest NaBH4 concentration that results
in the shortest reaction time.
For comparison, the nitroarene
reduction reactions were carried
out (a) in the absence of the catalyst, (b) using control ammoniated
MoS2 nanosheets as a catalyst, and (c) acid-treated Co-MoS2 nanosheets.
4.5 Characterization
All of the samples
were analyzed by recording powder X-ray diffraction (XRD) patterns
using a PANalytical X’pert pro diffractometer (Cu Kα
radiation, secondary graphite monochromator, scanning rate of 1°
2θ/min). The amount of Co2+ was estimated by a Varian
AA240 atomic absorption spectrometer using a Co hallow cathode lamp
in an air–acetylene flame at a wavelength of 324.4 nm. X-ray
photoelectron spectroscopy (XPS) measurements were carried out with
Kratos axis Ultra DLD. All spectra were calibrated to the binding
energy of the C 1s peak at 284.51 eV. Scanning electron microscopy
(SEM) analysis was carried out using a Zeiss, Ultra 55 field emission
scanning electron microscope equipped with energy-dispersive X-ray
spectroscopy (EDS). Transmission electron microscopy (TEM) images
were acquired with Tecnai T20 operated at 200 kV. UV–visible
spectra of the reaction mixtures were recorded on a PerkinElmer (LS
35) UV–visible spectrometer. The Raman spectra of the samples
were recorded on HORIBA Jobin-Yvon LabRAM HR800 at 532 nm excitation
wavelength. Isothermal magnetization [M vs H] was measured using a superconducting quantum interference
device (SQUID) magnetometer.
Supporting Information Available
The Supporting Information
is available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.7b00848.Raman spectrum
of Co-doped MoS2, and XPS
data of acid leached Co-doped MoS2 (PDF)
Supplementary Material
ao7b00848_si_001.pdf
The authors
declare no competing financial interest.
Acknowledgments
This work
was funded by SERB, India (EMR/2015/001982).
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145783710.1021/acsomega.7b00699ArticleResonance Control of a Graphene Drum Resonator in
a Nonlinear Regime by a Standing Wave of Light Inoue Taichi Anno Yuki Imakita Yuki Takei Kuniharu Arie Takayuki Akita Seiji *Department of Physics and Electronics, Osaka Prefecture University, Sakai 599-8531, Japan* E-mail: akita@pe.osakafu-u.ac.jp.14 09 2017 30 09 2017 2 9 5792 5797 29 05 2017 30 08 2017 Copyright © 2017 American Chemical
Society2017American Chemical
SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
We demonstrate the control of resonance
characteristics of a drum-type
graphene mechanical resonator in a nonlinear oscillation regime using
the photothermal effect, which is induced by a standing wave of light
between graphene and a substrate. Unlike the resonance characteristics
of a conventional Duffing-type nonlinearity, those of the nonlinear
oscillation regime are modulated by the standing wave of light with
a contribution of the scattered light of an actuation laser, despite
a slight variation of amplitude. Numerical calculations conducted
with a combination of equations of heat and motion with the Duffing-type
nonlinearity explain this modulation: the photothermal effect delays
the modulation of graphene stress or tension.
document-id-old-9ao7b00699document-id-new-14ao-2017-00699hccc-price
==== Body
1 Introduction
Graphene
has attracted much attention as a nanoelectromechanical
system (NEMS) component because of its superb mechanical and electrical
properties. Especially in terms of a graphene NEMS, a graphene mechanical
resonator (G-MR)1−10 is expected to be a highly sensitive mass and force sensor and a
component of the computing application. To improve the G-MR sensitivity,
it is important to realize a nanomechanical resonator with a high
quality factor (Q-factor). The intrinsic Q-factor depends solely on the material itself, so the modulation
of the intrinsic Q-factor is not easy. By contrast,
the apparent Q-factor can be modulated easily by
modulating the loss part of the motion of the resonator by application
of the active11,12 or passive feedback13−15 to the resonating system under a linear response regime. In the
case of passive feedback, the photothermal self-oscillation and laser
cooling of the G-MR with a Fabry–Perot cavity between graphene
and the substrate have been demonstrated by photothermal back-action
induced, respectively, by positive and negative feedback under a linear
oscillation regime.3 This photothermal
back-action was analyzed based on the delayed response component in
the resonating system.8,15 In addition to linear oscillation,
nonlinear effects on mechanical resonators, which are commonly described
by the Duffing effect at large oscillation amplitude, are important
for the improvement of sensitivity or other applications such as mode
coupling toward computing applications.6,7,16−22 Nevertheless, few reports describe resonance control of the G-MR
in a nonlinear resonance regime with the delayed component using optical
back-action.4,6 In addition, the delayed component
using optical back-action with a steep optical field gradient should
have position dependence. Therefore, we must analyze the combination
of the Duffing-type nonlinear equation and the delayed-time component
with position dependence. Unfortunately, because equations of this
type present difficulty in obtaining accurate analytical solutions,
detailed analysis of the nonlinear resonance and control of its resonance
properties of the G-MR in a nonlinear regime persist as challenging
tasks. This study demonstrates resonance control of the G-MR in the
nonlinear resonance regime with a Fabry–Perot cavity using
optical back-action induced by the standing wave of light in the Fabry–Perot
cavity. In addition to the experiment, we conduct numerical calculations
to investigate the relation between nonlinearity and the position-dependent
delayed-time component induced by optical back-action in the nonlinear
oscillation regime.
2 Results and Discussion
This study investigated a drum-type
G-MR similar to that presented
schematically in Figure 1a. Figure 1b shows
that the drum-type G-MR with a 5.4 μm diameter was fabricated
successfully. Raman spectroscopy was used to investigate the graphene
degradation after the fabrication process. Figure 1c shows that the D band originating from
the defects on the Raman spectrum at the suspended part of the G-MR
is rarely observed. This result implies that this fabrication process
induces no significant degradation of graphene.
Figure 1 Drum-type G-MR with a
Fabry–Perot cavity. (a) Schematic
illustration of the drum-type G-MR with a Fabry–Perot cavity.
(b) SEM image of a drum-type G-MR with a drum diameter of 5.4 μm.
The scale bar is 5 μm. (c) Raman spectrum for whole of the suspended
part of the drum-type G-MR.
Figure 2a
shows
that the resonance of the drum-type G-MR was measured using optical
detection methods in vacuum at approx. 10–3 Pa.
The intensity of light interference induced between the G-MR and the
Si substrate was measured to ascertain the displacement of the G-MR.
A laser, used as a probe, irradiated the center of the drum with wavelengths
of 406 or 521 nm. To oscillate the G-MR, a 660 nm wavelength laser
was irradiated on the substrate near the support edge of the G-MR
with a spot diameter of approx. 1 μm, as illustrated schematically
in Figure 2a, which
was modulated at a certain frequency f through an
objective lens with a numerical aperture (NA) of 0.7.
Figure 2 Measurement setup for
resonance characteristics with probe lasers.
(a) Schematic illustration of the optical detection and actuation
system. (b) Position dependence of the heat induced by the interference
of the probe laser (406 or 521 nm) between the substrate surface and
the graphene membrane obtained from finite element method analysis.
(c) Resonance curve measured under various actuation laser intensities,
where the wavelength and the intensity of the probe laser are 406
nm and 6.3 μW, respectively. Frequency f is
normalized by the resonance frequency f0 (approx. 9.83 MHz) at linear oscillation.
Figure 2b
portrays
the graphene position dependence of the induced heat on the G-MR by
the interfered probe laser light between the graphene and the Si substrate,
which were calculated using the finite element method, where the complex
refractive indexes of graphene (2.6 – 1.3i)23 and Si (5.6 – 0.4i at 400 nm)24 were used. The gray area between 300 and 335 nm corresponds
to the graphene height from the substrate deduced from the SiO2 and electrode thickness, as illustrated schematically in
the inset of Figure 2b, where the possibility that the graphene edge partially adheres
to the side of the Au electrodes exists. The graphene height was difficult
to measure accurately using atomic force microscopy (AFM) because
of insufficient tension of graphene, which caused unexpected perturbation
on the AFM image. In the gray area, the slopes of the profiles for
wavelengths λp of 406 and 521 nm were opposite. This
difference causes a different response of the photothermal effect
induced by the probe laser on the drum-type G-MR for respective λp. The thermal expansion coefficient, α, of graphene
is negative (−8 × 10–6 K–1) at around room temperature.25 Therefore,
higher heat generation at graphene induces higher stress10 or tension of the graphene membrane.
Figure 2c presents
an example of a frequency response curve of the drum-type G-MR taken
from lower frequency (f0 ≈ 9.83
MHz at the resonance of the linear oscillation regime), where the
actuation laser intensity (Pact) was changed
from 296 to 736 μW with λp = 406 nm. All frequency
response curves presented in this paper were taken from the lower
frequency. At a higher intensity of actuation, a hardening-type nonlinear
vibration is clearly observed, where the resonance curve deforms from
symmetrical to unsymmetrical and where the resonance peak shifts toward
a higher frequency with increasing actuation.
The nonlinear
vibration observed here can be excited by increasing
the amplitude, which led to the appearance of the nonlinearity term
in resilience. In this case, the Duffing-type equation of motion with
an external force F cos ωt is applicable with amplitude x described as 1 where m stands for the mass
of the G-MR, γ signifies linear damping related to the Q-factor, k0 represents the
intrinsic spring constant, β is the nonlinear coefficient (the
Duffing constant), and ω denotes the angular frequency. The
spring constant of the drum-type G-MR is ascertained from the stress
or tension acting on the graphene. At low amplitude, k0 is deduced to be constant, whereas at larger amplitude,
the graphene deflection induces additional hardening like k0 + Δk, which results
in nonlinear vibration. Results confirmed that the resonance properties
under the linear regime showed no marked dependence of Pp (6.30–9.28 μW), as shown in Figure S2 of
the Supporting Information. This result
implies that no marked modulation of γ or k0 under the linear regime is induced by the photothermal
effect attributable to the standing wave of the probe lasers.
To modify the resonance characteristics of the G-MR in the nonlinear
oscillation regime using the interference light, the probe laser intensity
(Pp) dependence was investigated at Pact = 516 μW corresponding to the weak
nonlinear oscillation presented in Figure 2c. Figure 3a depicts the frequency response curves obtained at
various probe laser intensities from 6.30 to 9.28 μW for respective
λp. The frequency responses show weak nonlinearity
for both λp. For detailed analysis of the nonlinearity,
we evaluated the slopes of the frequency response of the phase shift
dφ/df at the resonance as the measure of its
nonlinearity, where φ is the phase shift between the deflection
of the G-MR and the actuation force. Briefly, in the linear oscillation
regime, dφ/df is determined by 2m/γ, which is expected to be independent of λp. For the nonlinear oscillation regime, the frequency response of
the phase shift shows an abrupt change from positive to negative,
so-called the jumping phenomenon, so that dφ/df at the resonance is infinity. Consequently, one can expect that
the weak nonlinear condition corresponding to the intermediate region
gives a certain slope dφ/df depending on the
nonlinearity. It is noteworthy that, in the case of the conventional
nonlinear oscillation governed by eq 1, the frequency at the resonance shifts to a higher
frequency with increasing amplitude. The nonlinearity increases with
increasing amplitude.
Figure 3 Nonlinearity control of the drum-type G-MR by the interference
of light. (a) Frequency response curves with various probe laser intensities Pp measured by λp = 406 and
521 nm under Pact = 516 μW. Arrows
indicate respective resonances, where the frequency f is normalized by the resonance frequency at the linear response
measured under weak actuation. (b) Probe laser intensity Pp dependence of the amplitude at the resonance shown in
(a). (c) Probe laser intensity Pp dependence
of nonlinearity determined by dφ/df. Solid
lines are a guide for the eyes.
Figure 3b,c
present
the probe laser intensity dependence of the maximum amplitude and
nonlinearity dφ/df at the resonance, respectively.
For λp = 406 nm, the dφ/df at the resonance decreased despite the slight increase in amplitude
that occurred with increasing Pp. Moreover,
as clearly portrayed in Figure 3a, the peak position for λp = 406 nm shifts
0.4% toward lower frequency with increasing Pp. These changes induced by the probe laser are completely
opposite for the conventional nonlinear phenomenon explained by eq 1. For λp = 521 nm, the amplitude at the resonance shows no significant probe
laser intensity dependence. The peak position at the resonance fluctuates
within 0.3% and shows no specific dependence. Only nonlinearity dφ/df increases with increasing Pp, which is the opposite dependence observed at λp = 406 nm, which might derive from the opposite slopes of the profiles
of the standing wave of the probe laser presented in Figure 2b. The changes cannot be explained
using the conventional Duffing equation described by eq 1. It is noteworthy that the resonance
characteristics in the linear regime show no significant change for
changing the probe laser intensity as described above. Note that the
scattered light from the actuation laser may modify the nonlinear
property because of the additional photothermal effects on the resonance.
To investigate the unexpected resonance properties in the nonlinear
regime, we consider the delayed time response, which was regarded
as the origin of the modification of the resonance properties in the
linear resonance regime.13 For the linear
resonance regime, the delayed time response on the oscillating system
acts on the phase component, which leads to the modulation of damping,
γ.13,14 A similar delay component induced by the
photothermal effect of the standing wave of light should be considered
for the G-MR under a nonlinear regime. The temperature change of the
G-MR, Δθ, modifies the stress or tension acting on graphene.
Actually, Δθ depends not only on position x but also on time t attributable to thermal relaxation
time τth determined by the heat capacity and the
thermal resistance, where the heat capacity considered here is expected
to include not only graphene itself but also the substrate in contact
with the graphene. In the case of a nonlinear oscillator with the
time-delayed component, the analytical solution is difficult to obtain.
Assuming a linear relation between the spring constant and temperature,
the ratio of the spring constant Δk/k is given as 2 where α denotes the temperature coefficient
of the spring constant difference. In the case of an one-atom-thick
resonator, the spring constant mainly comes from its tension.26 For simplicity, we assumed the graphene resonator
as a linear string with length l and concentrated
mass m at the center of the string, the spring constant
and the resonance frequency ω0 are expressed as k = 4T0/l and , where T0 is
the internal strain of the resonator. The internal strain of graphene, T0, can be obtained from the resonance frequency
(9.86 MHz) at the linear response regime to be 1 × 10–7 N. Using the thermal expansion coefficient, α, and Young’s
modulus, E, of graphene (−8 × 10–6/K and 1 TPa), the tension is modified by temperature
with αAE ≈ 1.36 × 10–8 N/K, where A is the cross-sectional area of the
graphene resonator (5 μm wide and 0.34 nm thick). As a result,
one can estimate it as α0 = 0.15/K from αAE/T0.
Additionally, the
position dependence of the probe laser-induced
heat is approximated as linear because of its small oscillation amplitude
compared to the gap separating graphene and the substrate. For simplicity,
the time t is scaled by ω0 as τ
= ω0t, which is a nondimensional
parameter. In addition, we infer that this simplified model with a
lumped capacitance model for the heat equation, Δθ, is
applicable as 3 where q0 is a
slope of the position dependence of the induced heat normalized by
the system heat capacity on graphene given by mC and
ω0, which is defined from Pp and profiles of the photogenerated heat, as presented in Figure 2b, where C is the heat capacity of graphene. In addition, the photothermal
effect from the scattered light of the actuation laser is also implemented
as described by the third term of the right hand side, where Pscat is the light intensity of the scattered
light of the actuation laser normalized by the system heat capacity
on graphene and ω0. This expression is similar to
the case described in an earlier report13 for linear oscillation, except for the position dependence term q0x(t) proposed
here. Consequently, the additional spring constant Δk is expected to be a function with nonlinear dependence
on t and x as Δk(x,t). In this case, the Duffing-type
motion equation described by eq 1 using τ = ω0t is
now modified to 4 where Q is the quality factor
determined as Q–1 = γ/mω0 and x0 = F/mω02 = F/k. The term Δk(x,t) consists of higher order
terms of x with certain phase shifts resulting from
the time-delayed component, which gives rise to the modification of Q and β in addition to the spring constant itself.
In the case of the one-atom-thick resonator, the Duffing term comes
mainly from its tension depending on the vibration amplitude.26 On the basis of the same assumption as the string
mentioned before, the Duffing term is expressed as 5 where ωE2 = 4AE/ml. Solving simultaneous differential eqs 2–5 numerically,
one can qualitatively evaluate the photothermal
effect induced by the probe laser, where we also scaled the position
variable x by x0 for
simplicity. Parameters used in this calculation are presented in Table 1. As a reference,
the nonlinear behavior of this model was examined as portrayed in Figure 4a, where the driving
amplitude x0 was changed without the photothermal
effect induced by the probe laser. A linear response is obtainable
at x0 = 1. Nonlinearity with an apparent
hardening effect increases with increased driving amplitude. The jumping
phenomenon on the frequency response curve is readily apparent.
Figure 4 Numerical calculation
of the Duffing-type nonlinear resonance with
a delayed effect without the scattered light of the actuation. (a)
Conventional Duffing resonance curves with various driving amplitudes.
(b,c) Frequency response curves calculated with delayed time constants.
(d) Frequency response curves calculated with various probe laser
intensities Pp.
Table 1 Parameters Used for Numerical Calculations
f0 (MHz) ω0 (rad s–1) l (μm) A (m2) Q ρ (kg/m3) C (J/kg K) ε (TPa) β (K–1)
9.86 2πf0 5 1.7 × 10–15 300 2250 700 1 0.15
To evaluate the effect of the delayed time constant
τth on nonlinearity, ω0τth is used as a parameter13 with
the ratio
of the oscillation period at linear oscillation, ω0–1, and the delayed time constant τth. At ω0τth < 1 corresponding
to the faster response of temperature to the oscillation period, the
nonlinearity decreases with increasing ω0τth, which indicates that the fast response, that is, no delay
effect, imparts no effect on the phase component of the resonator.
Consequently, the nonlinearity returns to the original state with
decreasing ω0τth. In the case of
ω0τth > 1 corresponding to a
slow
temperature response, the nonlinearity increases with increasing ω0τth as observed in Figure 4c. The temperature modulation induced by
the oscillation is decreased, finally becoming zero at longer τth, which results in the elimination of the delayed effect.
The delayed time response greatly influences the resonance characteristics.
The condition of ω0τth ≈
2 is most efficient to suppress the nonlinearity of the resonator
as shown in Figure S3 of the Supporting Information, which closely resembles the case for laser cooling of the mechanical
resonator.8
Figure 4d presents
the light intensity of the probe laser dependence of the frequency
response at ω0τth = 2 without the
scattering of the actuation laser, that is, Pscat = 0. The nonlinearity decreases with increasing light
intensity. The amplitude at the resonance is ∼0.7, which is
much greater than the 0.2 obtained in the case of no delay effect
portrayed in Figure 4a. Further increase of q0 has a softening
effect on the resonance characteristics. These results indicate that
the delay effect does not merely suppress the nonlinearity by decreasing
the amplitude as the conventional nonlinear oscillator: it directly
reduces the nonlinear term in eq 4. However, the effect of the slope difference of the standing
wave of the probe laser cannot be explained.
Figure 5 shows simulated
frequency response curves for ω0τth and probe light intensity dependences with a positive or negative
slope of the profiles of the probe laser, where the contribution of
the scattered light from the actuation laser (1% of x0) was implemented as described in eq 3. In this case, a clear slope dependence of
nonlinearity appeared. In the case of the negative slope corresponding
to the 406 nm probe laser, nonlinearity is suppressed at larger ω0τth without a certain minimum as shown in Figure 5a and Figure S3c
of the Supporting Information. On the contrary,
the clear nonlinearity at the positive slope of the probe laser profile
corresponding to the 521 nm probe laser is observed at all of ω0τth even with the larger ω0τth, which is different from the case without the
scattered light effect as shown in Figure 5b (see also Figure S3d of Supporting Information). As can be observed in Figure 5c, the decrease of the suppression
of the nonlinearity is enhanced at higher q0 at the negative slope. Further increase of q0 induces softening nonlinearity. In the case of the positive
slope, the suppression of the nonlinearity is hardly observed. Thus,
the combination of the probe laser and the scattered light of the
actuation laser is required for the development of the slope dependence
of the nonlinearity modification.
Figure 5 Numerical calculation of the Duffing-type
nonlinear resonance with
a delayed effect with the scattered light of the actuation. (a,b)
Frequency response curves calculated with various delayed time constants
for the negative or positive slope of the probe laser profile. (c,d)
Frequency response curves calculated with various q0 for the negative or positive slope of the probe laser
profile.
We performed numerical simulations
to fit the simulated results
to experimental data as shown in Figure S4, where the probe laser intensity dependences of the amplitude and
nonlinearity were investigated under the condition of the presence
of the probe laser and the scattered light of the actuation laser. Figure 6 represents the best
fit to the experimental data. Note that the actual laser intensity
dependence of q0 on the photothermal effect
is unknown, so that the horizontal axis was adjusted with an arbitrary
ratio of the actual probe laser intensity and q0. The thermal relaxation time ω0τth, and the scattered light intensity are the dominant fitting
parameters. Apparently, both the vibration amplitude and the nonlinearity
(dφ/df) obtained from the experiments agree
with the results of the numerical simulation.
Figure 6 Comparison between the
experimental data and simulations. (a,b)
Probe laser intensity dependence of vibration amplitude and nonlinearity
determined by dφ/df obtained from the experiments
shown in Figure 3c
and the simulations, where solid lines are smooth fitting for the
numerical calculations indicated by tiny dots.
3 Conclusions
We demonstrated control of drum-type
G-MR nonlinearity using the
photothermal effect induced by the standing wave of light between
graphene and the substrate, that is, a Fabry–Perot cavity.
Unlike the conventional Duffing-type nonlinearity, the nonlinearity
was modulated with a slight oscillation amplitude variation by changing
the probe laser wavelength and intensity. This phenomenon is explainable:
the delayed thermal response induced by the photothermal effect causes
the modulation of the effective spring constant of the graphene membrane
in the phase space. We used numerical calculations consisting of the
heat equation and the Duffing-type equation of motion with the delayed-time
response to investigate the modulation of resonance characteristics
in a nonlinear oscillation regime. Results show that the weak amplitude
dependence of nonlinearity observed in the experimentally obtained
results was qualitatively consistent with the calculated results.
We believe that this modification of oscillation characteristics in
a nonlinear regime opens the way to realize an NEMS circuit using
nonlinear effects such as up-conversion of the frequency or mode coupling.
4 Experimental Section
The sample fabrication process
is illustrated schematically in
Figure S1 of the Supporting Information. First, metal electrodes consisting of Cr/Au (5 nm/30 nm) as a support
of the graphene drum were fabricated on a heavily doped Si substrate
with a 300 nm-thick SiO2 layer using conventional photolithography
processing (Figure S1b). Subsequently,
after the monolayer graphene was transferred onto the substrate using
polymethyl methacrylate (Figure S1c), it
was trimmed using oxygen plasma etching to form the drum-type G-MR
(Figure S1d), where graphene was synthesized
using low-pressure chemical vapor deposition at 1000 °C using
a Cu foil as a catalyst.27,28 To form the drum-type
G-MR suspended by metal electrodes, the SiO2 layer underneath
the graphene drum was etched using buffered hydrofluoric acid (Figure S1e), where the metal electrodes are used
as the metal mask for etching. Trenches at both sides of the drum
were necessary for uniform etching of the SiO2 layer. They
served as an evacuation channel for the air between the graphene drum
and the substrate during the measurement of resonance characteristics.
The samples thus fabricated were finally dried using supercritical
drying to prevent sticking of the suspended graphene induced by the
surface tension of water.
Supporting Information Available
The Supporting
Information is
available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.7b00699.Schematic illustration
of the flow of device fabrication,
resonance properties of the G-MR under a linear oscillation regime,
simulated delayed time constant dependence of nonlinearity of the
G-MR with or without the scattering light effect, and simulated delayed
time constant dependence of amplitude and nonlinearity of the G-MR
with the scattering light effect (PDF)
Supplementary Material
ao7b00699_si_001.pdf
The authors
declare no competing financial interest.
Acknowledgments
This work was partially supported by JSPS KAKENHI
grant numbers JP15H05869, JP16K14259, JP16H00920, JP17H01040, and
JP16H06504.
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145887010.1021/acsomega.8b00767ArticleComparative Study of Potassium Salt-Loaded MgAl Hydrotalcites
for the Knoevenagel Condensation Reaction Devi Rasna Begum Pakiza Bharali Pankaj Deka Ramesh C. *Department of Chemical Sciences, Tezpur University, Napaam, Tezpur 784028, India* E-mail: ramesh@tezu.ernet.in. Tel: +91 3712 275058. Fax: +91 3712 267005/6.29 06 2018 30 06 2018 3 6 7086 7095 20 04 2018 07 06 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
A series of potassium
salt-loaded MgAl hydrotalcites were synthesized
by wet impregnation of KNO3, KF, KOH, K2CO3, and KHCO3 salts over calcined MgAl hydrotalcite
(Mg–Al = 3:1). The samples were characterized by X-ray diffraction,
Fourier transform infrared, thermogravimetry–differential thermal
analysis, scanning electron microscopy, and N2 absorption–desorption
techniques to investigate their structural properties. The results
showed formation of well-developed hydrotalcite phase and reconstruction
of layered structure after impregnation. The prepared hydrotalcites
possess mesopores and micropores having pore diameters in the range
of 3.3–4.0 nm and Brunauer–Emmett–Teller surface
area 90–207 m2 g–1. Base strengths
calculated from Hammett indicator method were found increasing after
loading salts, where KOH-loaded hydrotalcite showed base strength
in the range of 12.7 < H– < 15, which was
found to be the preferred catalyst. Subsequently, KOH loading was
increased from 10 to 40% (w/w) and catalytic activity was evaluated
for the Knoevenagel condensation reaction at room temperature. Density
functional theory calculations show that among all of the oxygen atoms
present in the hydrotalcite, the O atom attached to the K atom has
the highest basic character. In this study, 10% KOH-loaded hydrotalcite
showing 99% conversion and 100% selectivity was selected as the preferred
catalyst in terms of base strength, stability, and catalytic efficiency.
document-id-old-9ao8b00767document-id-new-14ao-2018-00767nccc-price
==== Body
1 Introduction
Design,
synthesis, and application of solid base catalysts have
been of major concern in recent years due to their tunable basicity,
environmentally acceptable nature, and capacity to catalyze diverse
reactions.1,2 Although a large number of basic materials
have been reported in the literature, the study of structure–property
relationship of supported solid bases and their basic properties has
aroused renewed interest recently.3 Host
materials like zeolites (e.g., NaY, KL, NaX), porous metal oxides
(e.g., Al2O3, ZrO2), mesoporous silica
(e.g., SBA-15, MCM-41), mixed metal oxides, montmorillonite clay,
ALPO series, etc. are employed to prepare solid strong bases and super
bases.4,5 Among various guest materials and alkali
and alkaline earth metal salts, transition metals like Ag, Cu, Co,
etc. are the most common.6,7 Among various alkali
metal salts, potassium salt-loaded catalysts, e.g., KNO3/Al2O3, KNO3/ZrO2, KF/NaY,
K2CO3/Y zeolite, KOH/NaX, KOH/Al2O3, KOH/ZrO2, KOH/MgO, etc., have been reported
as excellent basic materials for a good number of organic reactions.8−10 On the other hand, oxide hosts due to their low surface area and
silicon-containing hosts due to reaction with some basic guests have
limited their use for many reactions.11 Hydrotalcites (HTs) and hydrotalcite-like layered materials are
another class of solid hosts that are used to generate strong bases.12 This is a class of solid superbase that can
catalyze a large number of organic reactions, such as transesterification,
aldol condensation, Knoevenagel condensation, isomerization, and epoxidation
reaction.13,14 However, selection of metal salts to suit
the host material and their effect over structure and basicity of
the host are yet to be explored for hydrotalcite-like compounds. Besides,
conditions for a suitable catalyst in terms of its base strength,
catalytic activity, stability of host material, recovery, etc. are
not easily met.15 Recently, Zhao et al.
have reported that potassium-loaded MgAl mixed oxides using KOH has
base strength (H–) above 26.5 and shows high catalytic
activity for the Knoevenagel condensation reaction at room temperature.16 On the basis of the aforementioned ideas, we
aimed to investigate the structure and basicity of Mg–Al hydrotalcite
after modification with a series of potassium salts.
The Knoevenagel
condensation is a versatile C–C bond-forming
reaction between a carbonyl compound and an active hydrogen compound
to form an unsaturated compound, which can lead to the formation of
various chemically and biologically important intermediates, such
as α-cyanocinnamates, α,β-unsaturated esters, α,β-unsaturated
nitriles, cinnamic acid, etc. These intermediates are commonly used
for the production of perfumes, cosmetics, drugs, antihypertensives,
calcium antagonists, polymers, fine chemicals, pharmaceuticals, etc.
Kantam et al. reported a modified method for activation of MgAl hydrotalcite
and applied them for the quantitative formation of the Knoevenagel
condensation product in liquid phase.17 In another report, Ebitani et al. showed that reconstructed hydrotalcite
is more active than untreated hydrotalcite and provides a unique acid–base
bifunctional surface capable of promoting the Knoevenagel and Michael
reactions.18 They have also found that
reconstructed hydrotalcite gives three times more yield than untreated
hydrotalcites for aldol and Knoevenagel condensation reactions. Similarly,
modified Mg–Al hydrotalcite with tert-butoxide
anion, layered double hydroxide fluoride, and hydrotalcite in ionic
liquid medium are reported as efficient catalysts for this reaction.19 Garcia et al. and Čejka et al. have recently
reviewed varieties of effective catalysts, such as cation-exchanged
zeolites,20 metal-organic frameworks,21−24 mesoporous molecular seives,25 etc.,
for the Knoevenagel condensation reaction. Other types of solids like
ZnO, MgO, alumina, potassium carbonates, zeolites, modified zeolites,
natural phosphates, etc. are reported as potential catalysts for this
reaction.26 These are considered as more
benign in comparison to traditionally used alkaline hydroxides.27
In this work, we have impregnated a series
of potassium salts,
i.e., KNO3, KF, KOH, K2CO3, and KHCO3, over calcined Mg–Al hydrotalcite (3:1 ratio), studied
the effect of base precursors on the structure and basicity of the
host, and finally employed for the Knoevenagel condensation reaction.
2 Results and Discussion
Powder X-ray diffraction (XRD)
patterns of parent hydrotalcite
and potassium salt-loaded hydrotalcites are presented in Figure 1. Reflections at
2θ values of 11.5, 23.05, 34.7, 38.35, 45.95, 60.5, and 61.75°
corresponding to (003), (006), (102), (105), (108), (110), and (113)
planes indicate the formation of highly crystalline layered structure
of hydrotalcite, which corroborates well with literature reports.28 Again all potassium salt-loaded samples show
strong peaks for (003) and (006) planes, which clearly shows the presence
of hydrotalcite phase; this confirms rehydration and reconstruction
of hydrotalcite phase after loading. However, shifting of 2θ
positions to slightly higher or lower values and diminished intensity
of loaded samples can be attributed to the presence of potassium salts
on hydrotalcite structure. It has been observed from Figure 1 that the salts KOH, KHCO3, and K2CO3 are well dispersed over
the support, whereas KF- and KNO3-loaded samples showed
some additional diffraction lines in the XRD pattern. Hence, preferred
catalyst can be chosen among KOH, KHCO3, and K2CO3 in terms of phase stability. This observation was
further investigated through crystallinity study, which did not follow
the similar trend. The crystallinity study revealed that the highest
crystallinity after loading was achieved for KOH/HT and the lowest
was for KHCO3/HT (Figure S1,
Supporting Information). It shows that although KHCO3 disperses
better than KF and KNO3 onto the host, it decreases the
crystallinity of the overall catalyst. Thus, crystallinity loss is
dependent on the nature of the salt but not on dispersion. Thus, observing
both crystallinity and phase stability, we can observe that KOH/HT
is a stable and highly crystalline catalyst among KOH, KHCO3, and K2CO3. Therefore, KOH/HT is chosen as
the preferred salt from XRD. We have also calculated crystallite sizes,
unit cell parameters (a), and basal spacing between the layers (d),
which are summarized in Table 1. Peaks for (003) and (006) reflections were considered to
calculate basal spacings between the layers. Peak for (110) reflection
was used to calculate unit cell parameter “a” according to the formula a = 2d, whereas the (003) plane was used to calculate “c” according to the formula c = 3d.29 Comparison of the original hydrotalcite
to the loaded hydrotalcites shows that the basal spacings and unit
cell parameters increase after loading. Increase of basal spacings
and unit cell parameters further supports increase of Mg (+2) ions
gradually in the LDH, indicating interaction of some Al (+3) ions
with potassium salts and decrease of Coulombic interaction between
interlayer anions and brucite-like layers.30,31 The increases of both “d” and a are larger for KOH/HT, K2CO3/HT,
and KNO3/HT (d003 = 7.80–7.93; d006 = 3.88–3.91; a =
3.06–3.07) than for KF/HT and KHCO3/HT (d003 = 7.70–7.73; d006 = 3.85–3.86; a = 3.05–3.06).
Figure 1 Powder
X-ray diffraction pattern of potassium-loaded hydrotalcites.
Table 1 Calculation of Lattice
Parameter and
Basal Spacings for Potassium Salt-Loaded Hydrotalcites
sample (003) reflection, 2θ (deg) d003 (Å) (006) reflection, 2θ (deg) d006 (Å) (110) reflection, 2θ (deg) d110 (Å) a (Å) c (Å) crystallite
size (003)
HT 11.50 7.70 23.05 3.85 60.50 1.53 3.06 23.10 128.09
KF/HT 11.50 7.70 23.00 3.86 60.60 1.52 3.05 23.10 135.56
KHCO3/HT 11.45 7.73 23.10 3.85 60.55 1.52 3.05 23.19 153.65
K2CO3/HT 11.35 7.80 22.70 3.91 60.35 1.53 3.06 23.40 135.70
KNO3/HT 11.35 7.80 22.90 3.88 60.20 1.53 3.07 23.40 164.93
KOH/HT 11.15 7.93 22.85 3.89 60.35 1.53 3.06 23.79 82.31
Thus,
a stability order of the salts over the support can be understood
from overall results of X-ray diffraction study, which follows the
trend KOH/HT ∼ K2CO3/HT > KHCO3/HT > KF/HT ∼ KNO3/HT. Hence, among the
studied
salts over hydrotalcite support, KOH is chosen as the preferred salt.
Smaller crystallite size of KOH/HT in comparison to the others is
again in favor of its selection as preferred catalyst for base-catalyzed
reaction.32 Following these results, we
have loaded KOH amount of 15–40% (w/w) by identical impregnation
method to gain better understanding of the effect of the salt over
the support.
Figure 1 shows that
hydrotalcite layered structure preserves up to 20% loading of KOH
and collapses above it, where the reflection for the (003) plane was
completely destroyed for 25–40% loaded samples. However, crystallinity
loss was quite higher for 15–40% loaded samples. When 15% KOH
was loaded, crystallinity loss was increased 7 times more in comparison
to 10% loaded sample. Therefore, KOH loading beyond 10% is believed
to be not effective over hydrotalcite support. Hence, 10% KOH/HT has
been conceded as the best catalyst in this study.
The thermogravimetric
analysis (TGA) and differential thermal analysis
(DTA) results obtained from thermal analysis of uncalcined samples
in the temperature range of 20–500 °C shows four decomposition
steps, which are typical for hydrotalcite-like compounds (Figure S2, Supporting Information). The first
weight loss step in the temperature range 20–90 °C corresponds
to the loss of physically adsorbed water on the surface, which is
found to be in the range of 1–12% of the total weight loss
(Table S1, Supporting Information). In
the second step, 12–15% weight loss takes place in the range
of 80–250 °C due to the loss of interlayer water molecules.
We have observed that the weight loss steps of all loaded samples
are similar to the parent hydrotalcite, except the step for interlayer
water loss. For HT, KF/HT, and KNO3/HT, interlayer water
loss takes place only in a single step, whereas it takes place in
several steps for KOH/HT, KHCO3/HT, and K2CO3/HT. This shows that the water molecules may be linked in
different environments in the presence of different guest molecules.
In the third step i.e., 250–415 °C, dehydroxylation and
partial loss of carbon dioxide take place, showing 13–22% weight
loss. It is noteworthy that dehydroxylation becomes slower after loading
of the salts and collapse of the brucite layers starts at low temperature
in comparison to the parent hydrotalcite. Besides, dehydroxylation
is the fastest in case of KNO3/HT and the slowest in case
of KOH/HT, which in turn confirms that the HT phase is thermally less
stable in the presence of KNO3 salt and more stable in
the presence of KOH. In the fourth weight loss step, loss of carbon
dioxide from the samples takes place in the temperature range of 395–518
°C, showing a weight loss of 2–4%. Thus, TGA analysis
reveals that the hydrotalcite layer collapses earlier for KNO3/HT and KF/HT in comparison to the other three, i.e., KOH/HT,
KHCO3/HT, and K2CO3/HT, which gives
thermal stability order of the loaded salts as KNO3/HT
< KF/HT < KHCO3/HT < K2CO3/HT < KOH/HT. Thus, TGA analysis also reveals that KOH/HT is the
most thermally stable catalyst and the preferred catalyst in our study.
The Fourier transform infrared (FTIR) spectra of prepared hydrotalcites
are presented in Figure 2. Characteristic bands for hydrotalcite at around 3450, 1640, 1380,
860, 661, and 510 cm–1 clearly indicate the presence
of interlayer water molecules, hydroxyl groups in the brucite-like
layers, carbonate ions in the interlayer galleries, and Mg–O
and Al–O bonds in all samples. Again, bands at around 3600–2800
cm–1 for KOH/HT, K2CO3/HT,
and KHCO3/HT samples are broader compared to KNO3/HT and KF/HT, which may be due to the high water content of these
samples in the surface as well as in the interlayer spaces. This again
correlates well with thermogravimetric analysis of the samples, confirming
high water content of these samples in the interlayer spaces.
Figure 2 FTIR patterns
of hydrotalcites loaded with potassium salts.
Nitrogen adsorption–desorption measurements were carried
out to investigate the surface areas, pore sizes, and pore volumes
of the materials. Table 2 shows textural properties of the parent hydrotalcite and potassium
salt-loaded hydrotalcites. The parent hydrotalcite exhibits a Brunauer–Emmett–Teller
(BET) surface area of 207 m2 g–1. Introduction
of potassium species decreases the BET surface area of all of the
samples. The surface area of hydrotalcite loaded with K2CO3 is lost to a greater extent compared to the other
four salts and decreases up to 90 m2 g–1. This is due to the blockage of pores and interlayer spaces of hydrotalcite
by CO32– anions of K2CO3 salt, thus preventing N2 molecules to adsorb onto
the surface. This observation has been further confirmed by the pore
volume calculation of the samples, which shows that the pore volume
of K2CO3/HT is the smallest and decreases from
0.23 cm3 g–1 of parent hydrotalcite to
0.19 cm3 g–1 of the loaded one. On the
other hand, surface areas of KNO3/HT and KF/HT are 201
and 197 m2 g–1, respectively. This can
be expected for low water content of these materials, as described
in TGA and DTA analysis. We have found intermediate values of surface
areas for the samples KOH/HT and KHCO3/HT. This can be
attributed to the high water content in these samples. On the other
hand, the KOH/HT sample shows the largest pore volume and pore diameter
with comparable surface area to the parent hydrotalcite. Thus, surface
areas and pore sizes of loaded hydrotalcites other than K2CO3 salt are not abruptly affected after loading the salts.
The N2 adsorption–desorption measurements showed
that all hydrotalcites exhibit type II isotherm and H3 hysteresis
loop characteristics of both monolayer and multilayer adsorption typical
for aggregated powders like clays or cements having no uniform pore
structures (Figure S3, Supporting Information).33,34 Type H3 hysteresis loops are generally found for nonrigid aggregates
of platelike particles or assemblages of slit-shaped pores in the
sample. It has again been confirmed from the pore size distribution
curves of the samples, which show broad range of pore sizes in the
samples. However, narrow pore size distribution centered at a pore
radius of 20 Å and large pore volume of KOH/HT has led us to
select it as the optimum sample in this study.
Table 2 Textural Properties of Potassium Salt-Loaded
Hydrotalcites
entry sample BET area (m2 g–1) pore volume (cm3 g–1) pore diameter
(nm) base strengths
(H–) total basicity (mmol g–1) soluble basicity (mmol g–1)
1 HT 207 0.23 3.30 9.6 < H– < 11.1 0.12 0.00a
0.00b
2 KF/HT 197 0.32 3.38 12.7 < H– < 15 0.18 0.02
3 KHCO3/HT 184 0.25 3.95 9.6 < H– < 11.1 0.18 0.03
4 K2CO3/HT 90 0.19 3.99 12.7 < H– < 15 0.23 0.05
5 KNO3/HT 201 0.32 3.66 12.7 < H– < 15 0.19 0.00
6 KOH/HT 185 0.36 4.00 12.7 < H– < 15 0.22 0.03
a Hydrotalcite.
b Reconstructed hydrotalcite
obtained
by immersion of MgAl mixed oxide in water for 24 h.
The scanning electron microscopy
(SEM) images of parent hydrotalcite
and KOH/HT in magnification of X5500 and X4000 are shown in Figure 3. The parent hydrotalcite
has crystal sizes in nanometer ranges with homogeneous shapes of the
crystals. On loading KOH onto it, particle size decreases, showing
layers of agglomerated sheets in the range of 1–2 μm.
Figure 3 Scanning
electron micrographs of (a1, a2) HT and (b1, b2) KOH/HT
at two different resolutions.
The results of base strengths of all hydrotalcites, which
were
determined by the Hammett indicator method, are summarized in Table 2. Hydrotalcites loaded
with KF, K2CO3, KNO3, and KOH after
drying at 80 °C for 15 h showed color change in the presence
of Tropaeolin O (H– = 11.1–12.7)
indicator and could not change the color of 2,4-dinitroaniline (H– = 15). Therefore, they showed similar
base strength in the range of 12.7 < H– < 15. On the other hand, the unloaded parent hydrotalcite
and KHCO3/HT showed color change with phenolphthalein (H– = 8.0–9.6), whereas no change
was observed with Tropaeolin O (H– =
11.1–12.7). Thus, their base strengths lie in the range of
9.6 < H– < 11.1. Total basicity
measurement of the samples shows that the number of total basic sites
for K2CO3/HT and KOH/HT are higher than the
other samples. This is reflected in the catalytic activities shown
in Table 4 that the
conversions for KOH/HT and K2CO3/HT are higher
than the other catalysts. On the other hand, the total number of basic
sites of all of the catalysts is relatively low compared to calcined
hydrotalcites reported in the literature. However, it is quite obvious
from the results that although the number of total basic sites is
not quite high, uncalcined hydrotalcites also can fairly catalyze
the Knoevenagel condensation reaction with its moderate base strengths.
Thus, loading of alkali metal compounds over hydrotalcites would be
acknowledged to catalyze some mild base-catalyzed organic reactions,
such as the Knoevenagel condensation reaction, nitroaldol condensation
reaction, aldol condensation, etc. Soluble basicities of all of the
samples are low, where no soluble base was found at all for KNO3/HT. This again indicates more interaction of KNO3 with host hydrotalcite structure, thus preventing their loss as
soluble base.
We again calculated the reactivity of the O atoms
using density
functional-based reactivity descriptor, the Fukui function. Fukui
functions, fO+ and fO–, are evaluated using Hirshfeld
population analysis (HPA) and Mulliken population analysis (MPA) schemes
to locate the nucleophilic and electrophilic sites, respectively.
Although an analytical expression for the Fukui function is not available,
it is usually calculated by finite difference approximation, which
is called the condensed Fukui function. The condensed Fukui function
of an atom “O” in a molecule with N electrons at constant
external potential v(r⃗)
can be expressed as 1a 1b where ρO(No), ρO(No + ΔN), and ρO(No + ΔN) are
charge densities on
atom O of the system with No, No + ΔN, and No – ΔN electron systems,
respectively. In conventional Fukui function computations, a value
of 1.0 is used for ΔN. In the present calculation,
we have used a value of 0.1 for ΔN. The values
of Fukui functions are given in Table 3. We have calculated the Fukui functions (fO+ and fO–), relative electrophilicity (fO+/fO–), and relative
nucleophilicity (fO–/fO+) for those oxygen atoms in the
hydrotalcite system having higher values of these reactivity parameters.
In general, it is observed that for a particular atom in a molecule,
the increase in fO– values is the indication of high basicity.
From Table 3, it has
been seen that the highest fO– value is obtained for
the oxygen atom number 38, which is the one attached to the potassium
atom. Relative electrophilicity (fO+/fO–) and relative
nucleophilicity (fO–/fO+) are better reactivity parameters
to locate the preferable site for nucleophilic and electrophilic attacks,
respectively, in a chemical system.35,36 The basicity
of a system increases with the increase of the fO–/fO+ ratio. Thus, the oxygen attached to the potassium having the highest
value of relative nucleophilicity (fO–/fO+) will be the most basic site. From this calculation, we have inferred
that the O atom attached to the K atom has highest values of fO– as well as fO–/fO+. Therefore, we can conclude that
O 38 is the most basic site in the hydrotalcite system. The optimized
structure of the hydrotalcite is shown in Figure 4. The oxygen atoms for which the reactivity
parameters have been evaluated are marked, and these are the atoms
having higher basic character in the system.
Figure 4 Optimized structure for
the most stable geometry of Mg3Al(OH)8KOH. The
green balls represent magnesium, pink
balls represent aluminum, purple balls represent potassium, red balls
represent oxygen, and gray balls represent hydrogen atoms in the optimized
geometry. The oxygen atoms having larger values of f(−) (higher basicity) are numbered, and the bond lengths are
in angstrom.
Table 3 Values
of Fukui Functions with Respect
to Mulliken and Hirshfeld Charges of the Basic Oxygen Atoms of the
Metal Oxide
Fukui function (fO+) Fukui function (fO–) relative electrophilicity (fO+/fO–) relative nucleophilicity (fO–/fO+)
atom MPA HPA MPA HPA MPA HPA MPA HPA
O 38 0.026 0.025 0.019 0.027 1.37 0.93 0.73 1.08
O 65 –0.001 0.006 0.002 0.005 –0.50 1.20 –2.00 0.83
O 69 0.021 0.022 0.021 0.022 1.00 1.00 1.00 1.00
O 80 0.004 0.006 0.002 0.006 2.00 1.00 0.50 1.00
O 83 0.017 0.019 0.017 0.020 1.00 0.95 1.00 1.05
The catalytic activities
of the parent and potassium salt-loaded
hydrotalcites were evaluated for liquid-phase Knoevenagel condensation
reaction (Scheme 1)
at room temperature with a variety of aldehydes. The conversion of
reactants to the products in an organic reaction is mainly influenced
by parameters such as solvent, temperature, effect of substituted
groups in the substrates, amount of catalysts, etc. Taking these points
into consideration, we have optimized the reaction conditions by varying
the conditions. First, the reaction was performed at room temperature without any catalyst by
taking malononitrile and p-nitrobenzaldehyde as model
reactants and methanol as solvent. To our expectation, no formation
of the product was observed. Therefore, we have performed all other
reactions in the presence of catalysts, i.e., with modified hydrotalcites
and rehydrated hydrotalcite under the same reaction conditions. The
results are summarized in Table 4. Reaction with rehydrated hydrotalcite
is comparatively slower than with the loaded hydrotalcite (Table 4, entry 2). It has
been observed that the reaction in methanol is not selective with
all of the catalysts and conversions are lower than reported methods.
However, KNO3/HT and KF/HT (Table 4, entries 3 and 4) catalysts show better
results than the other catalysts in terms of selectivity and it can
be correlated to their larger surface areas than the other loaded
catalysts. This can be correlated again from TGA results described
above that due to low water content in KNO3/HT and KF/HT,
aprotic environment of the catalyst makes the aldol-type intermediate
dehydrate easily, thus showing better selectivity of the Knoevenagel
product compared to KOH/HT, KHCO3/HT, and K2CO3/HT (Table 4, entries 5–7), where more interlayer water content
of these catalysts offers protic environment in the catalysts, thus
stabilizing the intermediate aldol-type product before the dehydration
step. However, low conversions of the product with KNO3/HT and KF/HT catalysts can be attributed to the interaction of the
salts with the support forming new phases and thus reducing active
sites of the catalysts (XRD). On the other hand, the preferred catalyst
of this study, i.e., KOH/HT (Table 4, entry 7), showed the highest conversion, largest
pore volume, longest pore diameter, and good selectivity within 30
min and therefore the reaction was further carried out with this catalyst
to optimize the reaction conditions. High conversion of KOH/HT is
also supported by its small crystallite sizes (Table 1), which favors the active hydroxyl groups
to take part in the reaction.37
Scheme 1 Table 4 Knoevenagel Condensation Reaction
with Different Potassium Salt-Loaded Hydrotalcites at Room Temperaturea
entry sample time (min) % conversionb % selectivityb
1 no catalyst 30 0 0
2 HTc 30 41 90
3 KNO3/HT 30 57 91
4 KF/HT 30 42 90
5 K2CO3/HT 30 63 69
6 KOH/HT 30 66 81
7 KHCO3/HT 30 61 76
8 KOHd 30 0 0
a Conditions: p-nitrobenzaldehyde
(1 mmol), malononitrile (1 mmol), methanol (3 mL), catalyst amount:
(25 mg, 8 w % of potassium ion), reaction temperature: room temperature.
b Obtained from 1H
NMR
analysis of the crude reaction mixture.
c Reconstructed hydrotalcite obtained
by immersion of MgAl mixed oxide in water for 24 h.
d Reaction with KOH salt (8 wt % of
25 mg).
Following this study,
we have investigated the effect of solvents
with 10% KOH/HT at room temperature by taking six different solvents
of different polarities. It is observed that solvents play a significant
role on both conversions and selectivities. When aprotic polar solvents
were used (Table 5,
entries 2, 4, and 5), 81–99% conversion was observed giving
100% selectivity of the product within 15 min. On the other hand,
when protic polar solvent methanol was used, the reaction was slow
and both conversion and selectivity was poor (Table 5, entry 3). Nonpolar solvents like toluene
and diethyl ether (entries 1 and 6) take longer reaction time than
polar solvents, giving 61–99% conversion and 100% selectivities
within hours. It is noteworthy to mention that in this study dimethylformamide
(DMF) is superior to the most commonly used solvent toluene for the
Knoevenagel condensation reaction in the presence of hydrotalcite
catalysts. It can be attributed to the fact that the reactants are
miscible well in polar environment and the catalyst mixes homogeneously
in the reaction mixture during vigorous stirring condition. Thus,
interaction of the catalyst with reactants becomes feasible in DMF
compared to nonpolar solvents toluene or diethyl ether. Therefore,
it is clear from Table 5 that DMF is the best choice in terms of conversion, selectivity,
and reaction time, and 10% KOH/HT can be chosen as the optimum catalyst
with DMF.
Table 5 Effect of Various Solvents on the
Knoevenagel Condensation Reaction at Room Temperaturea
entry solvent time % conversionb % selectivityb
1 toluene 40 min 99 100
2 DMF 15 min 99 100
3 MeOH 30 min 66 81
4 acetonitrile 15 min 81 100
5 DCM 15 min 99 100
6 diethyl ether 4 h 61 100
a Conditions: p-nitrobenzaldehyde
(1 mmol), malononitrile (1 mmol), solvent (3 mL), catalyst (25 mg);
catalyst: 10% KOH/HT.
b Obtained
from 1H NMR
yield of the crude reaction mixture.
We next used 10% KOH/HT for the Knoevenagel condensation
reaction
with various aldehydes bearing electron-donating and electron-withdrawing
groups, active methylene compounds (malononitrile and diethyl malonate),
and DMF at room temperature. The results are summarized in Table 6. The Knoevenagel
condensation reaction has been reported previously with hydrotalcite-like
catalysts, such as rehydrated Mg–Al hydrotalcite and metal-loaded
Mg–Al hydrotalcite in different reaction media and optimized
reaction conditions.38 At this time, rehydration
and loading have been done in the same step and found an efficient
catalyst for this reaction. Aldehydes with both electron-donating
and electron-withdrawing groups reacted efficiently with malononitrile
under similar reaction condition to give 99% conversions and 100%
selectivity of the corresponding olefins (entries 5 and 7). Aldehydes
containing electron-withdrawing groups in ortho and para positions
do not have much effect over the reaction time (Table 6, entries 2 and 5) and reacted faster than
aldehydes bearing electron-donating groups (entries 7 and 8). On the
other hand, unloaded catalyst takes comparatively longer reaction
time than loaded catalysts and gives 99% conversion and 100% selectivity
within 1.5 h (Table 6, entry 3). It may be due to the presence of potassium salts and
improved basicity of the loaded catalysts, thus completing the reaction
within short time. Heterocyclic aldehyde, i.e., 2-furaldehyde, also
reacted faster, giving 99% conversion within 15 min. However, reactions
with aliphatic aldehydes and aldehydes with big molecular size are
comparatively slower than simple aldehydes showing moderate yield
(52–65%, entries 12–13) within 5 h. With diethyl malonate
as active methylene compound, the acidity of the acidic protons decreases
due to two ester groups, thereby increasing the reaction time for
all substrates and giving 70–90% conversion and 100% selectivity
within 4–8 h. Polycyclic aromatic aldehydes, such as 1-naphthaldehyde,
also reacted efficiently, giving high conversion to the product. It
is observed that uncalcined KOH/HT with base strength in the range
of 12.7 < H– < 15 shows comparable
results to calcined mixed oxide catalyst, i.e., 21 wt % MgO–ZrO239 and 10.3 wt % K–MgAl(O),40 having base strength 26.5 ≤ H– < 33.0 (Table 6, footnotes c and d). This can be understood
as high BET surface area of KOH/HT compared to other two made the
reaction comparable to each other. We have also evaluated the efficiency
of the catalyst by performing the reaction between malononitrile and
4-chlorobenzaldehyde for four repetitive cycles. It is observed that
the catalyst is active even at the fourth cycle of the reaction, which
gives 99% conversion and 100% selectivity within 15 min (Table 6, entry 20). On the
whole, potassium hydroxide-loaded MgAl hydrotalcite acts as an efficient
solid base catalyst for the Knoevenagel condensation reaction at room
temperature.
Table 6 Knoevenagel Condensation Reaction
of Different Aldehydes and Active Methylene Compounds with 10% KOH/HTa
entry R X Y time % conversionb % selectivityb
1 Ph CN CN 30 min 99 100
2 4-NO2C6H4 CN CN 15 min 99 100
15 min 97c
10 min 99d
3 4-NO2C6H4 CN CN 40 min 99e 100
4 4-NO2C6H4 CN CN 90 min 99f 100
5 2-NO2C6H4 CN CN 15 min 99 100
6 4-ClC6H4 CN CN 10 min 99 100
7 4-CH3C6H4 CN CN 60 min 99 100
8 4-OHC6H4 CN CN 60 min 99 100
9 1-naphthyl CN CN 60 min 99 100
10 2-furyl CN CN 15 min 99 100
11 propionyl CN CN 90 min 99 100
12 isobutyl CN CN 5 h 52 100
13 cinnamic CN CN 5 h 65 100
14 4-NO2C6H4 COOEt COOEt 4 h 99 100
15 2-NO2C6H4 COOEt COOEt 4 h 99 100
16 4-ClC6H4 COOEt COOEt 4 h 99 100
17 4-CH3C6H4 COOEt COOEt 8 h 82 100
18 4-OHC6H4 COOEt COOEt 8 h 77 100
19 1-naphthyl COOEt COOEt 8 h 68 100
20 4-ClC6H4 CN CN 15 min 99g 100
a Conditions: aldehyde (1 mmol), active
methyl compound (1 mmol), DMF (3 mL), 10% KOH/HT (25 mg).
b Obtained from 1H NMR
yield of the crude reaction mixture.
c Aldehyde (2 mmol), active methylene
compound (2 mmol), 21 wt % MgO–ZrO2 (20 mg), DMF
(1 mL).
d Aldehyde (2 mmol),
active methylene
compound (2 mmol), 10.3 wt % K–MgAl(O) (20 mg), DMF (1 mL).
e Reaction with rehydrated hydrotalcite.
f Reaction with as-prepared hydrotalcite
after drying at 80 °C for 15 h.
g Fourth run with recovered catalyst.
Following this, the leaching of
potassium species into solution
was tested by flame photometry study. For this purpose, the reaction
was performed with 2 mmol p-nitobenzaldehyde, 2 mmol
malononitrile, and 100 mg of 10% KOH/HT in DCM solvent. After completion
of the reaction, 10 mL of water was added to dissolve the leached
out potassium and to separate organic portion. We observed that 0.355
mg of K was leached out from 100 mg of catalyst, which is quite low
compared to the loading amount. Thus, leaching of a small amount of
potassium does not affect the overall reaction speed and conversion.
3 Conclusions
In conclusion, we have found that KOH-loaded
MgAl hydrotalcite
prepared through wet impregnation of potassium salts over calcined
MgAl hydrotalcite is the most stable while KNO3-loaded
hydrotalcite is the least stable among a variety of potassium salt-loaded
MgAl hydrotalcites, i.e., KF, KOH, KNO3, KHCO3, and K2CO3. It was found that 10% (w/w) KOH/HT
is the best catalyst and DMF is the best solvent in the study and
catalyzes the reaction efficiently giving 99% conversion and 100%
selectivity within 10 min. It is also concluded that polar aprotic
solvents like DMF and acetonitrile speed up the reaction, whereas
nonpolar solvents slower the reaction.
4 Experimental
Section
4.1 Preparation of MgAl Hydrotalcite and MgAl(O)
Mixed Oxide
Magnesium aluminum carbonate (MgAl-CO3) hydrotalcite was prepared according to the procedure reported by
Nyambo et al.41 In this method, solution
A containing 38.46 g of Mg(NO3)2·6H2O (0.15 mol) and 18.75 g of Al(NO3)2·9H2O (0.05 mol) in 125 mL of deionized water was
added dropwise over 1 h to solution B containing 14 g of NaOH (0.35
mol) and 15.9 g of Na2CO3 (0.1 mol) in 145 mL
of deionized water at pH 10–12 with vigorous stirring. The
solution was kept stirring vigorously for another 1 h and the white
precipitate formed was aged without stirring for 24 h at 65 °C,
cooled to room temperature, filtered, and washed several times with
deionized water until the filtrate becomes neutral. Finally, the precipitate
was dried at 80 °C for 15 h and then calcined at 450 °C
for 6 h to obtain MgAl(O) support.
4.2 Preparation
of Potassium Salt-Loaded MgAl
Hydrotalcites
The potassium salt-modified hydrotalcites (HTs)
containing same amount of potassium ions (8% w/w) were prepared by
a wet impregnation method reported earlier. In this method, a solution
of the metal salt containing 1 mmol of the salt (except for K2CO3, where 0.5 mmol was taken) in 8 mL of deionized
water was stirred with 500 mg of calcined hydrotalcite for 24 h and
the slurries were dried at 80 °C for 15 h to obtain the loaded
catalysts. The samples were denoted as KNO3/HT, KOH/HT,
K2CO3/HT, KHCO3/HT, and KF/HT. Following
the same procedure, 10–40% KOH/HT was prepared by taking appropriate
quantity of KOH and the support.
4.3 Theoretical
Calculations
For the
theoretical part, density functional calculations were performed using
DMol3 program package,42 as implemented
in the Materials Studio program system.43 Geometry optimization was done by treating the exchange–correlation
interaction with generalized gradient approximation (GGA) using the
Perdew, Burke, and Ernzerhof (PBE) functional.44 We used the double numerical with polarization1 basis set for our calculations. The PBE functional
was demonstrated to be reliable for predicting structures of inorganic
oxides and it is one of the most universally applied GGA functionals.45
4.4 Characterization
Powder X-ray diffraction
patterns were recorded on a Rigaku (MiniFlex, U.K.) X-ray diffractometer
with Cu Kα radiation (1.5418 Å) at a scan speed of 7°
min–1 and 2θ range of 5–70° at
30 kV and 15 mA. The percentage crystallinities of the samples were
determined by integrating XRD peaks and using the formula, % crystallinity
= (AS × 100)/AR, where AR is the integrated area
of the reference material under the peaks between a set of 2θ
limits and AS is the integrated area of
the sample under the peaks between the same set of 2θ limits
as that of the reference. The crystallite sizes were determined by
X-ray line broadening method considering 003 reflection plane and
using the Debye–Scherrer equation (t = 0.89/β cos θ,
where “t” is the crystallite size,
“β” is the full width at half-maximum, and “θ”
is the angle of diffraction).37 FTIR spectra
of various catalysts were recorded on a Nicolet Impact model-410 spectrometer
with 1 cm–1 resolution and 32 scans in the mid-IR
(400–4000 cm–1) region using the KBr pellet
technique. The SEM measurements were carried out using a JEOL JSM-6390LV
scanning electron microscope. Thermogravimetric analysis was performed
using a Shimadzu thermogravimetric analyzer (TGA-50) in the temperature
range of 25–600 °C at a heating rate of 10 °C min–1, and differential scanning calorimetric analysis
was performed using a Shimadzu differential scanning calorimeter (DSC-60)
in the temperature range of 25–300 °C at a heating rate
of 10 °C min–1. Both analyses were performed
under nitrogen atmosphere using 10–15 mg of sample. The specific
surface areas were determined from N2 adsorption–desorption
isotherms obtained by the Brunauer–Emmett–Teller method
using a Quantachrome NOVA 1000e surface area and pore size analyzer
at −196 °C. Pore size distributions were calculated using
the Barrett–Joyner–Halenda equation from the amount
desorbed at a relative pressure of about 0.05–1 using N2 desorption branches of the isotherm. Flame photometry analysis
was performed in Systronics Flame Photometer 128.
The strengths
of basic sites were determined by the Hammett indicator method, following
the procedure reported by Fraile et al.46 The following Hammett indicators were used: neutral red (H– = 6.8–8.0), phenolphthalein (H– = 8.0–9.6), Tropaeolin O (H– = 11.1–12.7), and 2,4-dinitroaniline
(H– = 15). In this procedure, 25 mg
of loaded catalyst was shaken with 1 mL of indicator solution (0.1%
in methanol) and allowed to equilibrate for 2 h. The color of the
catalyst was then noted. The base strength was reported as stronger
than the weakest indicator, which exhibits a color change, and weaker
than the strongest indicator, which exhibits no color change.47 Total basicities of the samples were determined
by titration with benzoic acid. In this method, a suspension of the
loaded hydrotalcite (0.15 g) in a toluene solution of phenolphthalein
(2 mL, 0.1 mg mL–1) was stirred for 30 min and titrated
with a toluene solution of benzoic acid (0.01 M). To determine the
leachable basicities, 100 mg of loaded hydrotalcite was added to 10
mL water and the mixture was shaken well at room temperature for 1
h. The catalyst was filtered off, and a methanol solution of phenolphthalein
(1 mL, 0.1 mg mL–1) was added to the filtrate, which
was then titrated with a methanol solution of benzoic acid (0.01 M).
4.5 Catalytic Reactions
The Knoevenagel
condensation reaction was carried out in a 50 mL round-bottom flask
at room temperature. The catalysts were oven-dried at 80 °C for
12 h prior to use. In the typical procedure, 0.025 g of catalyst was
added to a mixture of 1 mmol aldehyde, 1 mmol active methylene compound,
and 3 mL of DMF at room temperature. The whole mixture was stirred
for the required time and monitored by thin-layer chromatography.
After completion of the reaction, DMF was evaporated and the product
was extracted with ethyl acetate, dried over anhydrous Na2SO4, evaporated, purified, and finally analyzed using
a 1H NMR spectrometer (JEOL JNM-ECS 400) taking Me4Si as the internal standard and CDCl3 as solvent.
The used catalysts were washed several times with acetone, dried,
and then reused. The conversions (%) were determined from integration
of 1H NMR signal of the crude reaction mixtures.
Supporting Information Available
The Supporting Information
is available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b00767.Crystallinity
(%) of potassium-loaded hydrotalcites
(Figure S1); thermogravimetric analysis and differential thermal analysis
patterns (Figure S2); nitrogen adsorption–desorption isotherms
(Figure S3); and weight loss percentage of hydrotalcites (Table S1)
(PDF)
Supplementary Material
ao8b00767_si_001.pdf
The authors
declare no competing financial interest.
Acknowledgments
R.D. thanks Department of Science and Technology,
New Delhi,
for the Women Scientist Fellowship (SR/WOS-A/CS-43/2017). This study
was financially supported by the Science & Engineering Research
Board (SERB), New Delhi (EMR/2016/003195).
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145905110.1021/acsomega.8b01018ArticleCavitand-Decorated Silicon Columnar Nanostructures
for the Surface Recognition of Volatile Nitroaromatic Compounds Tudisco Cristina †∥Motta Alessandro ‡Barboza Tahnie §Massera Chiara §Giuffrida Antonino E. †Pinalli Roberta §Dalcanale Enrico *§Condorelli Guglielmo G. *†† Dipartimento
di Scienze Chimiche, Università di
Catania, and INSTM UdR Catania, V.le A. Doria 6, 95125 Catania, Italy‡ Dipartimento
di Chimica, Università degli Studi
di Roma “La Sapienza” and INSTM UdR Roma, P.le A. Moro 5, 00185 Roma, Italy§ Dipartimento
di Scienze Chimiche, della Vita e della Sostenibilità Ambientale, Università di Parma and INSTM UdR Parma, Parco Area delle Scienze 17/A, 43124 Parma, Italy* E-mail: enrico.dalcanale@unipr.it (E.D.).* E-mail: guido.condorelli@unict.it (G.G.C.).15 08 2018 31 08 2018 3 8 9172 9181 16 05 2018 19 07 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under a Creative Commons Non-Commercial No Derivative Works (CC-BY-NC-ND) Attribution License, which permits copying and redistribution of the article, and creation of adaptations, all for non-commercial purposes.
Nanocolumnar
Si substrates (porous silicon (PSi)) have been functionalized
with a quinoxaline-bridged (EtQxBox) cavitand in which the quinoxaline
moieties are bonded to each other through four ethylendioxy bridges
at the upper rim of the cavity. The receptor, which is known to selectively
complex aromatic volatile organic compounds (VOCs) even in the presence
of aliphatic compounds, has been covalently anchored to PSi. The larger
surface area of PSi, compared to that of flat substrates, allowed
one to study the recognition process of the surface-grafted receptors
through different techniques: Fourier-transform infrared spectroscopy,
thermal desorption, and X-ray photoelectron spectroscopy. The experiments
proved that surface-grafted cavitands retain the recognition capability
toward aromatic VOCs. In addition, the affinities of EtQxBox for various
aromatic compounds (i.e., benzene, toluene, nitrobenzene, and p-nitrotoluene) have been studied combining density functional
theory computations and thermal desorption experiments. Computational
data based on the crystal structures of the complexes indicate that
this cavitand possesses a higher affinity toward aromatic nitro-compounds
compared to benzene and toluene, making this receptor of particular
interest for the detection of explosive taggants. The results of computational
studies have been validated also for the surface-grafted receptor
through competitive recognition experiments. These experiments showed
that EtQxBox-functionalized PSi can recognize nitrobenzene in the
presence of a significant excess of aromatic vapors such as benzene
(1:300) or toluene (1:100).
document-id-old-9ao8b01018document-id-new-14ao-2018-01018bccc-price
==== Body
Introduction
The detection of volatile
nitroaromatic compounds is an area of
active research, particularly regarding environmental monitoring and
social security.1 Among nitroaromatics,
nitrobenzene (NB) and 4-nitrotoluene (NT) are molecules of particular
interests because NB, which is widely used in organic industries,
is considered a highly polluting substance due to its toxicity, carcinogenicity,
and biological persistence,2 whereas NT
is an explosive taggant.3
Previous
papers reported the detection of these nitroaromatic compounds
adopting different analytical techniques such as liquid chromatography/mass
spectrometry,4−6 spectrophotometry,7 chromatography,8 fluorescence quenching methods,9,10 electrochemical methods,11 surface-enhanced
Raman spectroscopy,12,13 and using various organic and
inorganic materials such as metallic nanoparticles,2,14 metal–organic
frameworks,15−17 polymers,18 carbon nanostructures,19,20 and self-assembled monolayers.21,22 General overviews
of nitroaromatic detection approaches can be found in some recent
reviews.23−25 Although all of these methods allow the detection
of NB at low concentrations, they often require complex instruments
and time-consuming sample preparations and, in some cases, suffer
from low selectivity or lack of reversibility. On the contrary, detection
methods based on supramolecular receptors (such as quinoxaline-bridged
and iptycene-roofed cavitands for aromatic volatile organic compounds
(VOCs) or higher iptycenes for nitrocompound detection26−28) have recently been explored as alternatives to classical approaches
for a fast and easy recognition of the presence of aromatic contaminants.29−35 Conformationally mobile quinoxaline-based cavitand (QxCav, Chart 1)36 showed remarkable selectivity and sensitivity for the detection
of benzene, toluene, ethylbenzene, and xylenes (BTEX) in air.29 The complexation properties of this receptor
are due to the presence of a deep, hydrophobic cavity capable of engulfing
aromatic rings, interacting with them via a set of CH···π
and π-stacking interactions.33 These
complexation proprieties are retained after the covalent anchoring
of this receptor on different surfaces (i.e., Si and ZnO).37,38 Recently, a new conformationally rigid quinoxaline cavitand (EtQxBox)
delimited by four quinoxaline walls linked via ethylendioxy bridges
(Chart 1) was synthetized.39 This new receptor exhibits an enhanced trapping
efficiency for BTEX compared to the parent QxCav receptor in air.
Moreover, the conformational rigidity of this cavitand maximizes the
binding of toluene, ethylbenzene, and xylenes (TEX) with respect to
benzene by increasing the number and strength of their synergistic
CH···π interactions.39
Chart 1 Chemical Structures of the Cavitands Discussed in this Study
However, the use of cavitands
as bulk material limits the degree
of miniaturization achievable and, in addition, it can affect the
receptor selectivity due to residual nonspecific adsorptions at the
solid–gas interface. On the contrary, one of the limitations
of the use of monolayers on flat substrates is related to the low
surface area and, in turn, to the low amount of material involved
in the recognition process, thus jeopardizing sensitivity. A possible
solution to these limitations is the deposition of receptor monolayers
on high surface area substrates.40−42
Herein, we report
on the covalent anchoring of a specifically designed
EtQxBox cavitand to columnar porous silicon (PSi) through hydrosilylation
of the undecylenic feet decorating the lower rim of the receptor.
The high surface area of PSi allowed us to study the heterogeneous
recognition process of the surface-grafted receptors versus aromatic
analytes through different analytical techniques: Fourier-transform
infrared spectroscopy (FTIR), thermal desorption, and X-ray photoelectron
spectroscopy (XPS). An unprecedented selectivity of EtQxBox@PSi toward
nitroaromatic compounds compared to benzene and toluene has been assessed
and rationalized combining thermal desorption experiments with a density
functional theory (DFT) approach.
Results and Discussion
Material
Synthesis and Characterization
The desired
cavitand was prepared following a step-by-step synthetic approach,
starting from resorcinarene Res [C10H19, H]
(Scheme 1) presenting
four terminal double bonds at the lower rim, essential for the grafting
of the cavitand onto porous silicon.
Scheme 1 Synthesis of EtQxBox
Resorcinarene Res [C10H19, H] was obtained
from the standard condensation of resorcinol and undecylenic aldehyde
in acidic conditions;43 Res [C10H19, H] was reacted in anhydrous conditions with four
equivalents of 2,3-dicloro-5,8-dimethoxyquinoxaline A, in a microwave reactor, in the presence of K2CO3 as the base and dimethylformamide (DMF) as the solvent, affording
the octamethoxy-quinoxaline cavitand 1 in good yields.
The subsequent reaction step was the deprotection of the methoxy groups
to have four couples of neighboring free OHs on the quinoxaline ring
for cavity rigidification by the introduction of four ethylendioxy
bridges. In a previously reported procedure,39 the deprotection of the methoxy groups of quinoxaline was performed
by aluminum trichloride in anhydrous toluene. In this case, the presence
of the four double bonds at the lower rim of the resorcinarene is
not compatible with the use of AlCl3 as a deprotecting
agent. Therefore, new deprotection conditions were elaborated to preserve
the presence of the four double bonds. The deprotection of cavitand 1 was performed in two steps. The first one consisted in the
oxidative elimination of the eight methoxy groups by cerium ammonium
nitrate, leading to the tetraquinone-quinoxaline cavitand 2. Crude 2 was purified by column chromatography, and
the deprotection was confirmed through 1H NMR by the disappearance
of the methoxy signal. Owing to its low stability, cavitand 2 was immediately used in the next step, which consisted in
the reduction of the quinone groups by sonication in the presence
of metallic zinc (reducing agent) and acetic acid (proton donor) to
give cavitand 3. The final reaction step was the rigidification
of the cavitand via introduction of four ethylendioxy groups bridging
the eight OH moieties at the upper rim. Cavitand 3 was
reacted in dry conditions under microwave irradiation with ethylene
glycol ditosylate in the presence of anhydrous Cs2CO3 as base and dry DMF as solvent, affording the desired EtQxBox
cavitand in 50% yield (Figure S1).
PSi functionalization was performed through thermal hydrosilylation
of the EtQxBox terminal double bonds at the lower rim, following a
reported procedure.44 FTIR and XPS were
carried out to characterize porous silicon slides (PSi) functionalized
with EtQxBox receptors (EtQxBox–PSi). Figure 1 compares the following FTIR spectral regions
of bare PSi (black line) and EtQxBox–PSi (red line): (a) the
C–H stretching region between 3200 and 2700 cm–1; (b) the Si–H stretching region between 2300 and 2000 cm–1; and (c) the region between 1500 and 950 cm–1, which contains SiOx and C–O
stretching vibrations. The EtQxBox–PSi spectrum shows two strong
bands due to the CH2 symmetric (νs(CH2)) and antisymmetric (νa(CH2))
stretches at 2852 and 2928 cm–1 and a lower band
at 3050 cm–1 assigned to the aromatic C–H
(ν(CH)) stretches of the cavitand.44 The presence of these bands, combined with the absence of the analogue
ones in the PSi spectrum, indicates that the receptor is grafted to
the PSi surface. In the spectrum of bare PSi, three distinct signals
at 2085, 2107, and 2267 cm–1, due to SiH, SiH2, and SiH3 stretches, respectively, are present.45 After EtQxBox anchoring, these SiHx peaks broaden
slightly and decrease, leading to a single broad band, as a result
of the hydrosilylation reaction, which causes the partial replacement
of Si–H terminations with Si–C bonds. In addition, the
low broad band at 2251 cm–1 observed in the EtQxBox–PSi
spectrum can be assigned to the OSi–Hx stretches of the partially
oxidized silicon substrate.46 The 1500–950
cm–1 region of the EtQxBox–PSi spectrum shows
two bands at 1172 and 1272 cm–1 attributed to the
aromatic C–O bond of the ethylendioxy bridges. In addition,
the EtQxBox–PSi spectrum shows also some features in the 1500–1300
cm–1 region associated with the breathing modes
of the aromatic ring. All of these features are not detectable in
the PSi spectrum.
Figure 1 FTIR spectral regions in the 3200–2700 cm–1 (left), 2300–2000 cm–1 (middle), and 1500–950
cm–1 (right) ranges of bare PSi (black line) and
EtQxBox–PSi (red line).
XPS characterization gives further indication of the success
of
the anchoring process. XPS C 1s and N 1s spectral regions of PSi and
EtQxBox–PSi samples are shown in Figure 2. The C 1s spectrum of PSi (Figure 2a) mainly consists of a component
centered at 285.0 eV due to adventitious carbon and a low shoulder
around 286.0 eV due to oxidized adventitious carbons. The EtQxBox–PSi
spectrum (Figure 2b)
consists of three main components. The first component, centered at
285.0 eV, represents aliphatic and aromatic hydrocarbons, whereas
the second one, centered at 286.5 eV, can be attributed to the carbon
in the cavitand phenyl ring bonded to one oxygen. Note that the possible
formation of Si–O–C groups due to the reaction between
Si–H and Si–OH termination with oxidized carbon species
can contribute to this latter component. The third component at 287.6
eV is due to quinoxaline carbons that bond both oxygen and nitrogen
atoms. The N 1s spectrum of EtQxBox–PSi (Figure 2d) consists of a main band centered at 399.9
eV due to the nitrogens of the quinoxaline rings.47 A much less intense side component at 401.1 eV could be
due to protonated N atoms or forming H bonds. The presence of these
bands, combined with the absence of the analogue signals on PSi (Figure 2c), is a clear evidence
of the grafting of EtQxBox on the surface.
Figure 2 XPS C 1s (left) and N
1s (right) spectral regions of PSi (a, c)
and EtQxBox–PSi (b, d) samples.
Complexation Studies
Crystal Structure of NT@EtQxBox
To evaluate
the inclusion ability of EtQxBox toward nitroaromatic compounds, the
crystal structure of complex NT@EtQxBox·10DMSO was determined
by single-crystal X-ray diffraction methods (Figure S2). This complex was obtained by slow evaporation of a dimethyl
sulfoxide (DMSO) solution of hexyl-footed EtQxBox39 and NT from a 1:1 stoichiometric ratio mixture. Crystallographic
details for the structures are reported in the Supporting Information, Table S1.
Different views of the molecular
structure are shown in Figure 3, whereas geometrical details of the interactions responsible
for the complex formation are given in Figure S3 and Table S2. NT enters the cavity with the methyl group,
which interacts with the aromatic walls at the lower rim of the host
via two C–H···π interactions, dictating
the orientation of the guest into the cavity. These interactions are
strengthened by the presence of the nitro substituent on the aromatic
ring, which renders the methyl group more “acidic”.
The guest is further stabilized by the presence of two bifurcated
C–H···N weak H bonds involving the aromatic
hydrogen atoms ortho to the methyl group and the nitrogen atoms of
two quinoxaline rings (see Figure S3 and Table S2). The nitro group does not interact with the cavity rim.
Figure 3 Side and
top views of the molecular structure of NT@EtQxBox. Color
code: C, gray; O, red; N, blue. Hydrogen atoms and solvent molecules
have been omitted for clarity. The guest is represented in space-filling
mode.
Nitroaromatic Vapor Complexation
by EtQxBox–PSi
The affinity of the cavitand-grafted
silicon surfaces toward aromatic
compounds has been evaluated by exposing EtQxBox–PSi to either
NB (about 30 Pa) or NT (about 15 Pa) vapors calculated according to
the Antoine equation.48 The detection of
the surface-complexed molecules was performed using both XPS and FTIR
techniques. In addition, a control reference surface (Ref-PSi) was
prepared and similarly exposed to the nitroaromatic vapors. Ref-PSi
consisted of a PSi surface functionalized with an inactive organic
monolayer formed by a mixture (4:1) of 1-dodecene and a linear naphtyridine,
the 2,7-diamido-1,8-naphthyridine.49 The
mixed alkene/naphtyridine monolayer was chosen for its elemental composition
(C/N/O = 14:1:0.5) similar to that of EtQxBox (C/N/O = 13.5:1:2).
Figure 4a shows the
evolution of EtQxBox–PSi FTIR spectra in the 1800–1200
cm–1 range after exposure to NB or NT vapors. The
spectrum of Ref-PSi after NB exposure has been reported as reference.
The spectra of EtQxBox–PSi after exposure to the analytes show
the characteristic bands at 1345 and 1523 cm–1 associated
with the asymmetric and symmetric N–O stretching of NO2, respectively. These bands are absent in the Ref-PSi spectrum
under the same conditions (Figure 4a bottom), indicating that surface-bound EtQxBox is
needed for the recognition and that nonspecific interactions can be
neglected.
Figure 4 (a) FTIR spectra in the 1800–1200 cm–1 range of EtQxBox–PSi after exposure to NB (up) or NT (middle)
vapors. The spectrum of Ref-PSi after NB exposure (bottom) has been
added for reference. (b) Intensity variation of the 1523 cm–1 band of NO2 after cycles of absorption/desorption of
NB with EtQxBox–PSi.
The reversibility of the complexation process was then evaluated
through the FTIR monitoring of the intensity variation of NO stretches
during NB adsorption/desorption cycles. These cycles were obtained
through sample exposure to NB vapors (adsorption), followed by a mild
treatment at 80 °C under N2 flushing for 20 min (desorption).
The decrease of the feature associated with the NO2 group
down to a 20% of the maximum after the desorption step indicates that
the process operates with good reversibility (Figure 4b).
The complexation process was also
monitored by XPS. Figure 5 reports the N 1s spectral
regions of EtQxBox–PSi (Figure 5a) and Ref-PSi (Figure 5b) before and after the complexation process with NB.
After the exposure to NB, the N 1s region of EtQxBox–PSi (Figure 5a middle trace) shows
a new broad peak at ∼406.0 eV, besides the typical peak at
399.9 eV, attributable to the presence of the NO2 group
of NB in the cavity. In the case of Ref-PSi, only the N 1s band centered
at 400.0 eV assigned to the nitrogens of the 2,7-diamido-1,8-naphthyridine
is present before and after vapor exposure (Figure 5b).
Figure 5 N 1s spectral regions of (a) EtQxBox–PSi
and (b) Ref-PSi
before and after the NB exposure.
The NB desorption induced by sample heating was also monitored
by XPS analysis, confirming the process reversibility observed in
the FTIR experiments (Figure 5a upper trace).
Nitroaromatic vs Aromatic Complexation at
the Gas–Solid
Interface
The complexation of benzene (104 Pa),
NB (30 Pa), and NT (15 Pa) vapors on EtQxBox–PSi slides and
their thermal desorption under ultra-high vacuum (UHV) conditions
(total pressure = 10–8 Torr) were studied by in
situ mass spectrometry. Various ions associated with the fragmentation
of the desorbing molecules have been detected by the mass spectrometer
during the heating of the substrate (Figure 6). In the case of benzene desorption, the
molecular C6H6+ (main ion) ion and
the C6H5+ fragment (<20%) start
to desorb below 50 °C, and the desorption is completed at about
150 °C.
Figure 6 Thermal desorption experiments of EtQxBox–PSi (left)
and
Ref-PSi (right) after the adsorption of benzene (up) and NB (bottom).
In the case of NB, the complexation
is proved by the desorption
of the C6H5+ fragment, which in this
case is the most intense, whereas the observed molecular C6H5NO2+ ion is about 30% of the main
fragment. Note that the desorption temperature range of NB is broader
than the one observed for benzene. The same trend is observed for
the thermal desorption of NT (Figure S4). Similar experiments performed on the inert Ref-PSi slides showed
a minimal uptake of the guests, further confirming that the presence
of the cavitand on the surface is essential for the aromatic compound
complexation.
To evaluate the different affinities of EtQxBox–PSi
toward
aromatic and nitroaromatic compounds, a set of experiments with simultaneous
adsorptions of vapors of NB/benzene (1:300 ratio) and of NB/toluene
(1:100 ratio) was performed. The comparison between benzene and NB
adsorption emphasizes the effects on the cavitand–arene complex
if a nitro group is added to the aromatic ring. On the contrary, through
experiments adopting toluene and NB mixtures, the role of the two
substituents can be compared. After the adsorption of the benzene/NB
mixture, the main ions observed during the thermal desorption were
C6H5+, which is the most intense
peak arising from NB fragmentation, and the C6H5NO2+ molecular ion (Figure 7). Despite the large excess of benzene in
the gas phase, only a reduced amount of benzene (peak C6H6+) was released during heating. Note that
the contribution of benzene to the intensity of the fragment C6H5+ is below 10% because the amount
of this ion, deriving from benzene fragmentation, is less than 20%
of C6H6+. This experiment has shown
that NB is preferentially complexed with respect to benzene by EtQxBox–PSi.
It therefore indicates that the addition of the nitro group to the
aromatic ring increases the stability of the cavity–arene complex.
Figure 7 Thermal
desorption experiments of EtQxBox–PSi (up) and Ref-PSi
(bottom) after the adsorption of (left) benzene/NB (300:1) and (right)
toluene/NB (100:1) mixtures.
During thermal desorption after toluene/NB exposure, the
characteristic
toluene ions (i.e., C7H8+ e C7H7+) and the NB C6H5NO2+ and C6H5+ ions are clearly present.
Despite the excess of toluene in
the gas phase, the amount of adsorbed
NB is comparable to that of the adsorbed toluene, suggesting a higher
affinity of EtQxBox toward NB. However, in this case, the gap is less
marked when compared to that of the benzene/NB mixture.
Rationalization
of the Observed Selectivity via a DFT Study
DFT calculations
of the insertion of aromatic compounds inside
the EtQxBox cavity were performed to rationalize the higher affinity
of the cavitand toward nitroaromatics compared to that toward simple
aromatic hydrocarbons. In particular, complex formation with benzene,
toluene, NB, and NT is compared. In all cases, deep insertion of the
aromatic moiety into the cavity is observed (Figure 8).
Figure 8 Optimized structures for the host–guest
complex between
aromatic guests and the EtQxBox cavitand: (a) benzene@EtQxBox; (b)
NB@EtQxBox; (c) toluene@EtQxBox; and (d) NT@EtQxBox.
Benzene and toluene insert deeper than the respective
nitro derivatives
(see also the corresponding crystal structures in ref (39)). In the case of toluene,
both orientations of the methyl group with respect to the cavity are
energetically accessible, but the one with the methyl group protruding
outside the cavity is preferred (Figure 8c). The nitro group is always positioned
outside the cavity (Figure 8b,d).
The host–guest formation is in all cases
exothermic and
exoergonic (Figure 9). The stabilization energies are mostly due to the CHguest···πhost and CHguest···Nhost interactions, as also evidenced by the NT@EtQxBox crystal
structure. In the cases of NB and NT, a further stabilizing contribution
of about 7 kcal/mol, compared to benzene and nitrobenzene, respectively,
is ascribable to the dipole–dipole interaction between the
nitroaromatics and EtQxBox (Figure S5).
The much higher affinity of the cavity toward NB compared to benzene,
observed in the adsorption/desorption experiments, is due to this
difference. Smaller differences are observed in the adsorption affinity
between NB and toluene, as confirmed by the calculated lower energy
gap (about 3 kcal/mol) between the host–guest complexes. In
the case of toluene, the lack of the dipole–dipole stabilization
due to the nitro group is partially balanced by the formation of the
CHguest···πhost interactions
of the methyl group.39 The process is entropy
opposed due to the confinement of the guest inside the cavity. In
fact, we found that Gibbs free energy values are always 13–16
kcal/mol higher than the respective enthalpy values (at 298 K). The
entropic loss is quantified in about 13–16 kcal/mol in the
gas phase.
Figure 9 Interaction energy of the four guests with EtQxBox.
Conclusions
In this work, we report
the synthesis, characterization, and complexation
properties of a new organic–inorganic hybrid material based
on a porous silicon surface decorated with a conformationally rigid
quinoxaline-bridged cavitand. The recognition properties of EtQxBox
toward aromatic VOCs have been transferred to the silicon surface.
The success of the grafting protocol has been demonstrated by combining
different analytic techniques (XPS and FTIR). Reversible host–guest
complexation of aromatic and nitroaromatic compounds on the functionalized
porous surface has been evaluated by XPS, FTIR, and desorption experiments.
We demonstrated through the combination of experimental results and
DFT modeling that the affinity of the EtQxBox–PSi system toward
nitroaromatic compounds is significantly higher than the one toward
benzene because of the stabilizing contribution due to the dipole–dipole
interaction.
Experimental Section
Materials
Purchased
chemicals were used as received
unless otherwise noted. Water used in PSi preparation and functionalization
was Milli-Q grade (18.2 MΩ cm) and was passed as a final step
through a 0.22 μm filter.
Unless stated otherwise, reactions
were conducted in flame-dried glassware under an atmosphere of argon
using anhydrous solvents (either freshly distilled or passed through
activated alumina columns). Silica column chromatography was performed
using silica gel 60 (Fluka 230–400 mesh or Merck 70–230
mesh). 1H NMR spectra were obtained using a Bruker Avance
300 (300 MHz) and a Bruker Avance 400 (400 MHz) spectrometer at 298
K. All chemical shifts (δ) were reported in ppm relative to
the proton resonances resulting from incomplete deuteration of the
NMR solvents. High-resolution matrix assisted laser desorption ionization-time
of flight (MALDI-TOF) was performed on AB SCIEX MALDI-TOF-TOF 4800
Plus (matrix: α-cyano-4-hydroxycinnamic acid). 2,3-Dicloro-5,8-dimethoxyquinoxaline A(50) and undecylenic-footed resorcinarene
Res [C10H19, H]43 (Scheme 1) were prepared
according to published procedures.
Synthesis of Cavitand EtQxBox
Synthesis
of Octametoxy-Quinoxaline Cavitand 1
First,
1 g (9.61 × 10–4 mol) of resorcinarene
Res [C10H19, H] was dissolved in 50 mL of dry
DMF; K2CO3 (2.12 g, 0.01 mol) and quinoxaline
A (0.99 g, 3.84 × 10–3 mol) were then added.
The reaction was conducted in a microwave reactor, in open-vessel
modality, at 120 °C for 1.5 h. The crude was diluted in a large
excess of ethyl acetate and washed with water. The organic phase was
dried over sodium sulfate and evaporated. The compound was purified
by flash column chromatography (SiO2, CH2Cl2/acetone 95:5–90:10), affording a yellow solid, active
in fluorescence, in 69% yield. 1H NMR (CDCl3, 300 MHz): 7.43 (s, 4H, Hup), 6.93 (s, 8H, ArHQuin), 6.84 (s, 4H, Hdown), 5.79 (m, 4H, −CH=CH2), 4.96 (m, 8H, −CH=CH2), 4.02 (s,
24H, −OCH3), 3.95 (t, 4H, ArCH–R, J3 = 7.9 Hz), 2.30 (m, 8H, −ArCH–CH2), 1.33 (m, 56H, −CH2−). MALDI: m/z = 1787.89 [M + H]+.
Synthesis
of Tetraquinone-Quinoxaline Cavitand 2
Cavitand 1 (1.02 g, 5.72 × 10–4 mol) was dissolved
in 100 mL of tetrahydrofuran, and cerium ammonium
nitrate (3.76 g, 6.86 × 10–3 mol, previously
diluted in a minimum amount of water) was added. The mixture was stirred
at room temperature for 30 min and then quenched by the addition of
water. After extraction with ethyl acetate and evaporation, the compound
was purified by flash column chromatography (SiO2, CH2Cl2/acetone 85:15), affording an orange solid in
80% yield. Owing to its poor stability, the compound was characterized
only through 1H NMR and immediately used for the next reaction. 1H NMR (CDCl3, 300 MHz): 7.38 (s, 4H, Hup), 7.18 (s, 8H, ArHQuin), 6.80 (s, 4H, Hdown), 5.80 (m, 4H, −CH=CH2), 4.97 (m, 8H, −CH=CH2), 3.63 (t, 4H, ArCH–R, J3 = 7.4 Hz), 2.30 (m, 8H, ArCH–CH2−), 1.33
(m, 56H, −CH2−).
Synthesis of Octahydroxy
Quinoxaline Cavitand 3
Tetraquinone-quinoxaline
cavitand 2 (0.21
g, 1.26 × 10–4 mol) was dissolved in 6 mL of
acetone. Zinc (0.92 g, 0.01 mol) and 0.5 mL of acetic acid were added
in this order. The suspension was sonicated for 5 min. The crude was
filtered over celite, dissolved in ethyl acetate, and washed with
water, until complete removal of acetic acid. After evaporation, the
pure compound was obtained as a bright yellow solid in 90% yield. 1H NMR (DMSO- d6, 400 MHz): 8.32
(s, 8H, ArOH), 8.10 (s, 4H, Hup), 7.90 (s, 4H, Hdown), 6.94 (s, 8H, ArHQuin), 5.83 (m, 4H, −CH=CH2), 4.95 (m, 8H, −CH=CH2−),
4.08 (t, 4H, ArCH–R, J3 = 7.3 Hz),
2.30 (m, 8H, −ArCH–CH2−), 1.22 (m,
56H, −CH2−). MALDI-MS: m/z =1673.71 [M + H]+.
Synthesis
of Cavitand EtQxBox
Cavitand 3 (80 mg, 4.78
× 10–5 mol) was dissolved in
5 mL of dry DMF in a microwave vessel. Cs2CO3 (202 mg, 6.20 × 10–4 mol) and ethylene glycol
ditosylate (106 mg, 2.86 × 10–4 mol) were added
under nitrogen. The mixture was reacted in a microwave reactor at
120 °C for 1.5 h. The crude was extracted with CH2Cl2/H2O, dried over sodium sulfate, and evaporated.
The compound was purified by preparative thin layer chromatography
(SiO2, acetone 100%), affording the desired compound as
a bright yellow solid, in 50% yield. 1H NMR (CDCl3, 400 MHz): 8.31 (s, 4H, Hup), 7.55 (s, 4H, Hdown), 6.74 (s, 8H, ArHQuin), 5.88 (m, 4H, −CH=CH2), 5.81 (t, 4H, ArCH–R, J3 = 7.6 Hz), 5.04 (m, 8H, −CH=CH2), 4.64–4.50
(m, 16H, ArOCH2CH2OAr), 2.11 (m, 8H, −ArCH–CH2−), 1.32 (m, 56H, −CH2−).
MALDI-MS: m/z = calculated for C108H113N8O16 [M + H]+ 1777.82745, found 1777.8230, calculated for C108H112N8NaO16 [M + Na]+ 1799.8094,
found 1799.8094 [M + Na]+.
PSi Preparation
PSi has been prepared by wet metal-assisted
chemical etching according to a published method.39,ref40 In particular, Czochralski-grown, p-type Si(100) slides having a
resistivity of 1.5–4 Ω cm were treated for 5 min with
an hydrofluoric acid (HF) (0.14 M) and AgNO3 (5 ×
10–4 M) water solution. After the deposition of
Ag particles, the slides were dipped in HF, H2O2, and H2O (40% HF/30% H2O2/H2O 25:10:4 v/v) solution for 1 min and then rinsed with Milli-Q
water and dried under N2 flow.
Cavitand Grafting
For grafting on porous substrates,
the etched PSi was dipped in a EtQxBox solution in mesitylene. The
solution was refluxed at 200 °C under N2 for 5 h;
then functionalized PSi slides were cleaned by two washing cycles
in an ultrasonic bath (5 min each) in dichloromethane.
Cavitand Complexation
Tests
Adsorption experiments
were performed by placing samples for 30 min in a closed chamber saturated
with aromatic VOC vapors. The saturated chamber at 25 °C was
obtained by placing one beaker (or two beakers for the mixtures) containing
3 mL of the aromatic compound (benzene, toluene, or NB) and allowing
vapor saturation for 4 h. The saturation of NT vapor was obtained
by placing for 2 h ∼50.0 mg of NT in a closed chamber kept
at 50 °C.
Sample Characterization
XPS spectra
were obtained with
a PHI 5600 multitechnique ESCA-Auger spectrometer equipped with a
monochromated Al Kα X-ray source. Analyses were carried out
with a photoelectron takeoff angle of 45° (relative to the sample
surface) with an acceptance angle of ±7°. The XPS binding
energy scale was calibrated by centering the C 1s peak due to hydrocarbon
moieties and “adventitious” carbon at 285.0 eV.
FTIR spectra were obtained with JASCO FTIR 430, using 100 scans per
spectrum (scan range 560–4000 cm–1, resolution
4 cm–1).
Thermal desorption experiments were
performed in a UHV chamber
(basic pressure ∼ 10–8 Torr). For the experiments,
the holder (Vacuum Science, Italy) was resistively heated with a ramp
of about 10 °C/min from 30 to 200 °C. The desorbed molecules
were detected with a Smart-IQ + (Thermo Electron Corporation) quadrupole
mass spectrometer equipped with an electron filament as ion source
and a multiplier detector (mass range 1–300).
Crystal Structure
of NT@EtQxBox
The crystal structure
of NT@EtQxBox was determined by single-crystal X-ray diffraction methods.
Intensity data and cell parameters were obtained at 190 K on a Bruker
APEX II equipped with a charge-coupled device area detector and a
graphite monochromator (Mo Kα radiation λ = 0.71073 Å).
The data reduction was carried out using the SAINT and SADABS51 programs. The structure was solved by Direct
Methods using SIR9752 and refined on Fo2 by full-matrix least-squares procedures,
using SHELXL-2014/753 in the WinGX suite
version 2014.1.54 All of the nonhydrogen
atoms were refined with anisotropic atomic displacements, with the
exclusion of some atoms belonging to the disordered DMSO lattice molecules
and of a terminal methyl carbon atom of the alkyl chain. The hydrogen
atoms were included in the refinement at idealized geometries (C–H
0.95/0.99 Å) and refined “riding” on the corresponding
parent atoms. The weighting schemes used in the last cycle of refinement
was w = 1/[σ2Fo2 + (0. 0.1232P)2 +
5.6500P], where P = (Fo2 + 2Fc2)/3. Geometric calculations were performed with the PARST97 program.55 Crystallographic data (excluding structure factors)
for the structure reported have been deposited with the Cambridge
Crystallographic Data Centre as supplementary publication no. CCDC-1831062
and can be obtained free of charge on application to the CCDC, 12
Union Road, Cambridge, CB2 IEZ, U.K. (fax: +44-1223-336-033; e-mail deposit@ccdc.cam.ac.uk or http://www.ccdc.cam.ac.uk).
Computational Details
Calculations were performed adopting
the M06 hybrid meta-generalised gradient approximation functional.56 The standard all-electron 6-31G** basis57 was used for all atoms. Molecular geometry optimization
of stationary points was carried out without symmetry constraints
and used analytical gradient techniques.58 Frequency analysis was performed to obtain thermochemical information
about the reaction pathways at 298 K using the harmonic approximation.
All calculations were performed using the G16 code59 on Linux cluster systems.
Supporting Information Available
The Supporting Information
is available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b01018.1H
NMR spectrum of the EtQxBox cavitand;
crystallographic data, refinement details, and ORTEP view of NT@EtQxBox·10DMSO;
crystallographic geometrical parameters and view of the host–guest
interaction for the complex NT@EtQxBox; thermal desorption experiments
for NT vapors; DFT calculated values of the dipole moment of the EtQxBox
host and used guests (PDF)
Supplementary Material
ao8b01018_si_001.pdf
Author Present Address
∥ Laboratory of Adsorption and Catalysis, Department of Chemistry,
University of Antwerpen (CDE), Universiteitsplein 1, 2610 Wilrijk,
Antwerpen, Belgium (C.T.).
The authors
declare no competing financial interest.
Acknowledgments
This work
was supported by the European Union through the DOGGIES
project (Grant FP7-SEC-2011-285446) and University of Catania through
the project “Piano della Ricerca di Ateneo 2016–2018”.
Centro Interfacoltà di Misure “G. Casnati” and
the “Laboratorio di Strutturistica Mario Nardelli” of
the University of Parma are kindly acknowledged for the use of NMR
and MALDI facilities and of the Diffractometer.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145802110.1021/acsomega.8b01868ArticleRoom-Temperature, Copper-Free Sonogashira Reactions
Facilitated by Air-Stable, Monoligated Precatalyst [DTBNpP] Pd(crotyl)Cl Pohida Katherine Maloney David J. ‡Mott Bryan T. *†Rai Ganesha *National Center for Advancing
Translational Sciences, National Institutes
of Health, 9800 Medical
Center Drive, Rockville, Maryland 20850, United
States* E-mail: bmott12@uab.edu (B.T.M).* E-mail: bantukallug@mail.nih.gov. Phone: 301-827-1756 (G.R).10 10 2018 31 10 2018 3 10 12985 12998 03 08 2018 26 09 2018 Copyright © 2018 American Chemical
Society2018American Chemical
SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
A novel application of [DTBNpP] Pd(crotyl)Cl
(DTBNpP = di-tert-butylneopentylphosphine) (P2), an air-stable,
commercially available palladium precatalyst that allows rapid access
to a monoligated state, has been identified for room-temperature,
copper-free Sonogashira couplings of challenging aryl bromides and
alkynes. The mild reaction conditions with TMP in dimethyl sulfoxide
afford up to 97% yields, excellent functional group tolerability,
and broad reaction compatibility with access to one-pot indole formation.
document-id-old-9ao8b01868document-id-new-14ao-2018-01868wccc-price
==== Body
Introduction
The Sonogashira reaction,
catalyzing C(sp)-C(sp2) bond
formation, is a vital tool in academia and industry, for its ability
to increase conjugation and rigidity in natural product synthesis,
drug development, molecular electronics, nanoscale scaffolds, and
heterocyclic chemistry.1−4 Historically, the use of copper co-catalysts with palladium allowed
for mild reaction conditions due to transmetallation, as reported
by Sonogashira.5 However, undesirable homocoupling
of acetylenes, air sensitivity, moisture sensitivity, and difficulties
in pharmaceutical purification processes prompted the need for well-refined,
copper-free systems while broadening the scope for challenging substrates.
Classic addition of a ligand to an air-stable Pd-source (such as Pd(OAc)2 or Pd2(dba)3) may encounter disruption
from inadvertent ligand coordination, catalyst impurity, or delayed
catalyst generation due to in situ formation.6−10 Even with the variety of palladium sources and ligands
currently available, arguably the most popular conditions for Sonogashira
reactions are Pd(PPh3)4, a catalyst lacking
air stability, and Pd(PPh3)2Cl2.
These reactions frequently require high temperatures, copper salts,
or additional ligands that may be pyrophoric or noncommercial, limiting
feasibility.11 Among newly published protocols
some call for atypical solvents, additives, or catalysts, and many
requiring long reaction times and show few examples of pharmaceutically
relevant heteroaromatics.12−17 Although few attractive methods are available in the literature,18,19 it is still desirable to develop a more robust protocol broadly
applicable for complex substrates.
Recently developed preformed
palladacycles20 and palladium dimers21,22 allow for a defined ligand ratio
and exhibit greater catalytic rates than their individual counterparts,
exemplifying the utility of preformed palladium complexes for numerous
carbon–carbon couplings. Additionally, these palladium precatalysts
pose an improvement to traditional catalysts by exhibiting greater
stability and feasibility in reaction set up while still providing
the same active catalyst. Despite the coordinative potential of palladium,
monoligated adducts (L1Pd0) frequently produce
a more efficient catalyst and thus there is a desire for precatalysts
capable of producing monoligated palladium in situ.23−25 The proposed
mechanism for monoligated precatalysts begins by activation to the
LPd0 state, utilizing bulky, electron-rich ligands to stabilize
a reactive catalytic species that facilitates faster oxidative addition
and efficient catalytic cycle.26,27 One of the prominent
monoligated precatalyst backbones was introduced by Buchwald in 2007:
air-stable palladacycles that are readily activated by deprotonation
under mild reaction conditions to obtain the monoligated Pd0 complex via reductive elimination of the intramolecular amine–aryl
group.28−32 Another successful, commercially available precatalysts synthesized
in 2002 by Nolan and co-workers utilize an allyl-based palladium precatalyst
that incorporates the NHC-carbene ligand. This monoligated precatalyst
is air stable, room-temperature activated and capable of performing
efficient Suzuki, Buchwald, and other cross-couplings.33,34 In 2010, Shaughnessy35 and Colacot36 found success replacing the NHC-ligand on Pd(allyl)Cl
complexes with bulky phosphines or varying the π-allyl substituents
in Suzuki, α-arylation, and amination reactions. These base-promoted,
bench-stable precatalysts reductively eliminate a noninhibitory olefin
byproduct while creating an active palladium complex proficient in
a wide range of cross-coupling reactions, including Sonogashira.27,37−39
Results and Discussion
The Sonogashira
coupling has become a prominent intermediate step
and functional group addition for medicinal chemistry projects. A
quick survey of prominent medicinal chemistry journals finds 18 references
already this year and 75 in 2017 employing the alkyne coupling, yet,
Pd(PPh3)4, Pd(PPh3)2Cl2, and palladium salts with copper-dominated catalyst conditions.
During our medicinal chemistry efforts in synthesizing novel inhibitors
of human lactate dehydrogenase, we required a reliable and facile
Sonogashira coupling condition for library synthesis. These classical
conditions were minimally successful with our diversely functionalized
substrates and risked catalyst poisoning by incorporating nitrogen
and sulfur containing aryl groups, especially when attempting scale-up
procedures. We sought an improved catalyst and optimized condition
applicable to a wide variety of functional groups for application
in our work as well other medicinal chemistry projects that experienced
limitations similar to those listed above. The initial catalyst search
was based off the work of Soheili et al.,40 who performed Sonogashira couplings at room temperature with allyl
palladium chloride and P(t-Bu)3, without
copper, and hypothesized the formation of a monoligated active L1Pd0 catalyst using these substrates. In view of
the success of Buchwald and allyl monoligated palladium catalysts
in numerous cross-coupling reactions,41 we envisioned that preformed Buchwald and allyl monoligated palladium
precatalysts with bulky, electron-rich phosphines, have the capability
to be a bench-stable, monoligated precatalyst for copper-free Sonogashira
couplings. These next generation catalysts would provide a powerful
synthetic solution by expanding the scope, increasing catalytic rates,
and eliminating the use of pyrophoric ligands. Herein, we report the
catalytic efficiencies of several Buchwald palladacycles and allyl
monoligated palladium catalysts (Figure 1) applied to the Sonogashira reaction.
Figure 1 Currently established
palladium precatalysts: P1–P4, P6–P15. Ligand for in
situ catalyst: L1. P5 was synthesized in
house.
Initial efforts were focused on
the screening of precatalysts P1–P14 using challenging coupling partners.
The 3,5-dimethoxyphenyl bromide (1), which does not give
any product under classical Sonogashira conditions40 (entry 1 in Table 1) due to hindered oxidative addition step, and an electron-deficient
heteroaromatic alkyne (2), a representative for difficult
heteroaromatic alkynes that are frequently employed in medicinal chemistry
and pharmaceutical development, were coupled with base DABCO in tetrahydrofuran
(THF), conditions similar to those used by Soheli et al. For comparison,
several difficult electron-rich substrates, such as p-bromophenol (entry 5m), p-bromoaniline
(entry 5n), or 3-bromothiophene (entry 5r), were coupled using our protocol. The π–allyl palladium-based
catalyst (P1), which incorporated P(t-Bu)3 and a crotyl ligand, successfully produced coupling
product 3, without copper, in moderate yield (52%, entry
2). In changing the phosphine ligand to DTBNpP (P2) and
XPhos (P4) with the same palladium precatalyst, the P2 catalyst revealed to be a more efficient catalyst with
a 75% yield (entries 3 and 5).42 However,
the activity diminished dramatically when P(t-Bu)3 was replaced with P(Cy)3 (P3, entry
4). Attempting to improve yields with the η3-1-t-Bu-indenyl ligand (P5) (investigated by Hazari
et al.)43 led to only 53% yield (entry
6). The original π–allyl palladium complex without a
bulky phosphine ligand, unsurprisingly showed no appreciable product
(entries 7 and 8). Switching to Buchwald type precatalysts, both the P8 and P9 catalysts that contain the P(t-Bu)3 ligand were able to produce the desired
product, but much less effectively than P2 (23–27%
yield, entries 9 and 10). However, P10 and P11 incorporating the DTBNpP ligand markedly increased the yields to
63 and 56%, respectively (entries 11 and 12). Furthermore, P12 and P13 catalysts with P(t-Bu)2(Me) and P(t-Bu)2(n-Bu) ligand,
respectively, almost completely diminished catalyst activity (entries
13 and 14), proving the specificity of the DTBNpP ligand for this
system. The catalyst P14, a precursor to L1Pd0 and successfully used in amination reactions,10 demonstrated negligible activity within these
conditions (entry 15). Additionally, a commercially available NHC
precatalyst, P15, with a cinnamyl and chloride ligand
similar to the phosphine-based allyl precatalysts, was tested for
comparison; however, it afforded no product (entry 16). After finding P2 as the most efficient precatalyst, we then compared its
reactivity with the catalyst formed in situ. The catalyst formed from
1:1 (Pd/P) ratio of P6/L1 exhibits a slightly
higher yield after 18 h compared to P2, but a lower yield
within the first hour, likely due to formation of the active catalyst
(entry 17). Exchanging the crotyl ligand for cinnamyl to form the
in situ catalyst exhibited no significant improvement and provided
comparable product formation over time (entry 18). The addition of L1 to P2 (1:1) significantly retarded P2 activity with almost no conversion observed during the first 3 h
(entry 19). However, the activity progressed gradually to produce
a similar yield as independent P2 after 18 h (Figure 2 and entry 17 vs
entry 3). This could be due to the initial formation of the coordinately
saturated 14-electron L2Pd0. The remainder of
catalysts in Figure 2 tapered off their rate of product formation after 6 h, except for P10, which exhibited an increase in activity after 3 h possibly
due to delayed release of the aromatic amine. A comparison of the
DTBNpP-containing catalysts in Figure 2 demonstrates the efficiency of P2 compared
to its individual ligand/palladium sources and over the Buchwald precatalysts
for the Sonogashira reaction.
Figure 2 Conversion of 2 over an 18 h period
using catalysts
containing the DTBNpP ligand.
Table 1 Catalyst Screening with 1-Bromo-3,5-dimethoxybenzene
(1) and 3-Ethynylpyridine (2)a
entry catalyst 3 (yield, %)b
1 Pd(PPh3)2Cl2, CuI 0c
2 P1 52
3 P2 75
4 P3 0
5 P4 57
6 P5 53
7 P6 0
8 P7 0
9 P8 27
10 P9 23
11 P10 63
12 P11 56
13 P12 0
14 P13 4
15 P14 1
16 P15 0
17 P6 with L1 (1:1) 84d
18 P7 with L1 (1:1) 78d
19 P2 with L1 (1:1) 71d
20 P2 2e
a Reaction conditions: 1 (0.5 mmol), 2 (0.8
mmol), cat. (.025 mmol), DABCO (1.0
mmol), THF (2.5 mL), rt for 18 h under argon atmosphere.
b Yield was determined by liquid chromatography/mass
spectrometry (LC/MS) with pyrene as internal standard.
c Followed standard Sonogashira reaction
procedure.
d Catalyst and
ligand stirred for
5 min prior to reagent addition.
e Without degassing using argon or
nitrogen.
With the finding
of efficient catalyst P2, the effects
of base and solvent were next examined (Table 2). By using DABCO as the base, the reaction
achieved less than 50% yield with nonpolar (e.g., DCM and MTBE) or
polar protic solvents (e.g., MeOH and EtOH) (entries 1–4).
In contrast, using polar aprotic solvents (e.g., THF, ACN, DMF, and
DMSO) provided better conversions with 62–100% yield, DMSO
being the best solvent in this reaction condition (entries 5, 7, 8,
and 11). Several exceptions were also observed during the solvent
screening. For instance, a good yield (74%) was observed by using
the nonpolar 1,4-dioxane solvent (entry 6), but the reaction performed
poorly in NMP, a polar solvent (40% yield, entry 9). Moderate
yields were found by using Lipshutz’s Sonogoshira protocol
in water using 3% nonionic amphiphile PTS (entry 10).44 DMSO was carried through the screening of various bases
(entries 12–29). As expected, the lack of base afforded no
product (entry 12). A wide variety of inorganic bases produced excellent
yield over the course of 18 h (entries 13–16). Among them,
NaOAc was the only one that reached a high yield (86%) in 2 h (entry
13). Although KHCO3 as the base is less effective, Cs2CO3 and TBAF were found to be totally ineffective
(entries 17–19). Continuously, various organic bases were screened
under the same conditions. Sterically hindered amines, such as TMP, t-BuNH2, (i-Pr)2NH,
and Hunig’s base, reached high yields (>84%) in 2 h (entries
20–24). However, using Et2NH and Et3N
as the bases only produced product in moderate yield (56–58%)
after 18 h (entries 24 and 25). Some cyclic amines, e.g., pyrrolidine
and piperidine, were also effective bases, but required 18 h to reach
completion (entries 26 and 27). Morpholine and DBU were found to be
much less effective (entries 28 and 29). Of the bases, (i-Pr)2NH and TMP afforded product 3 (100%)
within 2 h, making them both attractive bases for this reaction. TMP
was used in subsequent optimization due to faster product formation
within 2 h; although, (i-Pr)2NH is a valuable
cost-effective substitute.
Table 2 Optimization of Base
and Solvent in
the Coupling of 1 and 2a
3 (yield, %)b
entry base solvent t = 2 h t = 18 h
1 DABCO MTBE 42 54
2 DABCO DCM 25 35
3 DABCO MeOH 27 35
4 DABCO EtOH 26 40
5 DABCO THF 46 72
6 DABCO 1,4-dioxane 40 74
7 DABCO ACN 67 82
8 DABCO DMF 42 62
9 DABCO NMP 26 40
10 DABCO 3 wt % PTS in H2O 33 50
11 DABCO DMSO 91 100
12 none DMSO 0 0
13 NaOAc DMSO 86 100
14 KOH DMSO 50 100
15 K2CO3 DMSO 50 100
16 K3PO4 DMSO 51 100
17 KHCO3 DMSO 26 43
18 Cs2CO3 DMSO 0 0
19 TBAF DMSO 0 0
20 t-BuNH2 DMSO 86 89
21 iPr2NH DMSO 100 100
22 Hunigs’ base DMSO 84 100
23 TMP DMSO 100 100
24 Et2NH DMSO 15 56
25 Et3N DMSO 53 58
26 pyrrolidine DMSO 27 100
27 piperidine DMSO 42 100
28 morpholine DMSO 20 58
29 DBU DMSO 2 10
a Reaction conditions: 1 (0.5
mmol), 2 (0.8 mmol), P2 (0.025 mmol,
5 mol %), base (1.0 mmol), solvent (2.5 mL), rt for 18 h under argon
atmosphere.
b Yield was determined
by LC/MS with
pyrene as internal standard.
TMP was re-evaluated with alternative and sustainable solvents45 to broaden the applicability of these conditions
for purposes, such as process chemistry (Table S1). Although the THF/TMP combination was not as productive
as DMSO/TMP (Table S1, entry 1), high yields
were still obtained after 18 h (70%). Sustainable solvents, such as
2-MeTHF and sulfolane, were able to provide acceptable yields after
18 h if a greener solvent is desired (Table S1, entries 2 and 3). EtOAc, a solvent recommended for environmentally
friendly chemistry and a top 10 solvent used in GSK pilot operations
in 2005, was able to produce a 62% yield in 18 h that could likely
be increased with heating (Table S1, entry
4). ACN was the most effective solvent from this table (Table S1, entry 5) with product formation similar
to DMSO as the solvent, a positive result considering its use in process
chemistry and recommended use in medicinal chemistry.
TMP and
DMSO were chosen to evaluate catalyst loading (Table 3). The 5 mol % catalyst
loading produced a 96% yield in only 0.5 h, whereas a 2.5 mol % achieved
77% (entries 1 and 2). Both conditions were highly effective, reaching
100% yield in 1.5 h. Decreasing loading to 1 or cot0.5 mol % resulted
in significant product formation delays (48 and 42%, respectively),
though both went to completion by 18 h (entries 3 and 4). Increasing
the temperature to 60 and 100 °C allowed the catalyst load to
be decreased to 0.5 mol % while still achieving 80 and 85% yield,
respectively, in 0.5 h. For our purposes, a 2.5 mol % catalyst load
was chosen to limit palladium usage while retaining rapid product
formation at room temperature.
Table 3 Effect of Catalyst
Loading in the
Coupling of 1 and 2a
3 (yield, %)b
entry catalyst load (%) temperature (°C) t = 0.5 h t = 1.5 h t = 18 h
1 5 rt 96 100 100
2 2.5 rt 77 100 (86)c 100
3 1.0 rt 25 48 92
4 60 100 100 100
5 100 100 100 100
6 0.5 rt 15 42 88
7 60 80 97 100
8 100 85 93 100
9 0.1 60 15 33 56
10 100 25 26 39
11 0.01 60 0 0 2
12 100 4 5 10
a Reaction conditions: 1 (0.5 mmol), 2 (0.8 mmol), [DTBNpP] Pd(crotyl)Cl,
TMP
(1.0 mmol), DMSO (2.5 mL), rt for 18 h under argon atmosphere.
b Yield was determined by LC/MS with
pyrene as internal standard.
c Parentheses indicate an isolated
yield.
The attention was
then shifted to exploration of coupling partner
scope using the optimized reaction condition, namely, P2 (2.5 mol %), TMP, and DMSO. Various bromides were tested, and the
results are summarized in Scheme 1. In general, electron-withdrawing group-substituted
aryl bromides (5a–d and 5f–i) and heteroaryl bromides (5o–r) were completed within 2–4 h with high isolated yields
(65–92%). The exception was the 2-CF3 substitution
(5e), requiring 18 h to reach completion. Though the
aryl bromides with electron-donating substitutions (5j–n) had slightly lower yields (52–78%),
the electronic substitution effect seemed minimal. These examples
also demonstrated excellent tolerability of functional groups, including
nitrile, nitro group, ketone, carboxylic acid, ester, amide, as well
as unprotected hydroxyl (5l, 5m) and amino
(5n) groups. However, some heterocycles, such as 5t–aa, required slightly elevated temperature
(60 °C) to push to completion with moderate to good yields (42–87%).
Despite the challenging sterics of 4-bromo-3,5-dimethylisoxazole,
it achieved 61% conversion over 32 h, however, difficulty in purification
likely due to instability limited isolated yields (5z). In addition, an 87% yield was attained using 4-bromo-1H-indole in 6 h (5aa). The present protocol
is not applicable for aryl chlorides, as exemplified by 5i, only exhibiting bromide coupling.
Scheme 1 Scope of Bromides,,
Reaction conditions: 4 (0.5 mmol), 2 (0.8 mmol), P2 (2.5 mol
%), TMP (1.0 mmol), DMSO (2.5 mL), rt under argon atmosphere.
Isolated yield.
Stir at rt for 3 h then increase temperature
to 60 °C.
With the broad scope of bromides
obtained, various aryl- and alkyl-substituted
alkynes with electron-donating bromide 1 were then evaluated
(Scheme 2). The phenylacetylene
and aryl acetylene with electron-donating groups typically proceeded
to completion in 2 h with excellent isolated yields (7a–c). The heteroaryl acetylene, such as N-methylated
imidazole (7d), and aryl acetylene with electron-withdrawing
substitutions (7e–g) required prolonged
reaction time (12–24 h) to secure a good yield, but were still
completed at room temperature. Finally, the alkenyl- (7h) and alkyl (7i–n)-substituted alkynes
were efficiently coupled with 1 under similar conditions
to produce the desired product in excellent yield (75–96%).
Scheme 2 Coupling of 1 with Aryl and Alkyl Acetylenes,,
Reaction conditions: 4 (0.5 mmol), 6 (0.8
mmol), P2 (2.5 mol
%), TMP (1.0 mmol), DMSO (2.5 mL), rt with argon atmosphere.
Isolated yield.
Stir at rt for 3 h then increase temperature
to 60 °C.
To test the feasibility in
large-scale preparation, a 2 g scale
reaction was performed on 1 and 2 using
2.5 mol % catalyst loading. To our gratification, the reaction reached
100% conversion in 2 h with 92% isolated yield that further confirmed
the efficiency and effectiveness of this coupling protocol (Scheme 3).
Scheme 3 Indole Synthesis
via Sonogashira Coupling with 2-Bromoanilines,
Reaction conditions: 1. 8 (0.5 mmol), 9 (0.63 mmol), P2 (5.0
mol %), TMP (1.0 mmol), ACN (2.0 mL), rt under argon atmosphere. 2.
HCl (2.5 mmol), 90 °C.
Isolated yield.
To further test the utility
of these conditions, 2-bromoanilines
were coupled with various alkynes in hopes of intramolecular cyclization
to form the indole. Moderate yields were achieved using an unoptimized
one-pot indole synthesis utilizing the Sonogashira protocol followed
by refluxing in the presence of concentrated HCl. The method accommodated
both electron-withdrawing and electron-donating functionalities on
the bromide (10a–d), producing isolated
yields up to 78%. Additionally, the cyclization tolerated alkynes
containing an alkyl or phenol substituent while still maintaining
yields around 55% (10e, 10f). With further
optimization, we believe this one-pot approach may provide a rapid
pathway toward diverse indole library synthesis.
Conclusions
In
summary, a robust, copper-free Sonogashira coupling reaction
is described. Through extensive optimization campaign, the homogeneous
precatalyst P2, [DTBNpP] Pd(crotyl)Cl, was found to be
the most effective catalyst. Together with optimized base (TMP) and
solvent (DMSO), this condition provides a simple, mild, scalable,
and versatile alternative for the coupling of variety of aryl bromides
and alkynes. Additionally, this precatalyst provides rapid access
to indoles via the one-pot method, further expanding on the utility
of P2. We believe the preformed, air-stable P2 provides a reliable and more effective alternative to the commonly
used catalysts, such as Pd(PPh3)4 and PdCl2(PPh3)2, by retaining or surpassing
coupling efficiencies, bypassing in situ catalyst formation, forgoing
usage of pyrophoric agents, and decreasing the likelihood of catalyst
poisoning. A broad scope of both coupling partners together with high
functional group tolerability and excellent isolated yield makes it
an attractive addition to the existing Sonogashira coupling conditions
for chemical library generation, medicinal chemistry, and with potential
use in process chemistry.
Experimental Section
All commercial
solvents and reagents were purchased from commercial
sources and used without alteration. The modified water solvent (3%
PTS in H2O) was created using a 15% PTS in H2O stock from Sigma-Aldrich and water from our lab, heating to achieve
uniform consistency. Precatalysts were purchased from Strem Chemicals
(46-0028 (P8), 46-0365 (P13), 46-0358 (P11), 46-0385 (P9), 46-0275 (P6),
and 46-0295 (P7)), Johnson Matthey (Pd-162 (P1), Pd-163 (P2), Pd-170 (P4), Pd-178 (P3), and Pd-113 (P14)), and Sigma-Aldrich (RNI00185
(P10) and 794198 (P12)). Additional P2 was synthesized with procedures published by Seechurn et
al.36 NMR data comparing the commercially
available and homemade catalyst is provided in spectral data. Reaction
monitoring was performed on the Agilent 1200 series LC/MS containing
a Luna C18 (3 mm × 75 mm, 3 μm) reversed-phase column,
utilizing UV detection at λ = 220 nm. The LC/MS ran a 3 min
gradient spanning 4–100% acetonitrile in H2O modified
by trifluoroacetic acid (0.05%) at a flow rate of 0.8 mL/min. Flash
column chromatography was carried out on Teledyne Isco CombiFlash
Rf+ systems using 24G Isco Silica Gel columns (230–400 mesh)
and HPLC grade solvents. Products purified on 1H NMR and 13C NMR spectra were analyzed by the Varian 400 MHz in DMSO-d or CDCl3. 1H NMR spectra were referenced
to 7.26 ppm for CDCl3 and 2.50 ppm for DMSO-d. 13C NMR were referenced to 77.23 ppm for CDCl3 and 39.5 ppm for DMSO-d6. 31P NMR was referenced externally to 0.00 ppm for H3PO4. Splitting patterns are reported as: singlet (s), doublet
(d), triplet (t); quartet (q), septet (s), and other combinations
of these patterns. Coupling constants are reported in Hertz. High-resolution
mass spectrometry (HRMS) was obtained by the Agilent 6210 Time-of-Flight
(TOF) LC/MS system. Proton and sodium adducts may be observed from
the salt exposure in the purification and mass spectrometry instrument.
In certain cases, heating was utilized.
General Procedure for Synthesis
of (3), (5), and (7)
To an oven-dried Biotage
microwave process vial (#355630), bromide (0.50 mmol, 1.00 equiv),
alkyne(0.75 mmol, 1.50 equiv), 2,2,6,6-tetramethylpiperidine (169
μL, 1.00 mmol, 2.00 equiv), and P2 (5.17 mg, 0.013
mmol, 0.025 equiv) were added to DMSO (1.5 mL). Remaining DMSO (1
mL) was added to rinse the sides. The reaction vessel was sealed and
bubbled with in-house argon for 5 min. The reaction stirred at room
temperature for the designated time. Work up involved ammonium chloride,
EtOAc, and brine. The organic layer was concentrated and purified
on Isco silica gel columns to give the resulting product using a gradient
of 0–100% for ethyl acetate/hexanes with a 0.1% NH4OH modifier, 0–20% for methanol/DCM with a 0.1% NH4OH modifier, or 0–100% water/ACN with a 0.1% TFA modifier.
3-((3,5-Dimethoxyphenyl)ethynyl)pyridine
(3)
Tan solid. Yield: 97 mg, 85%. Time: 1.5
h. 1H NMR (400
MHz, DMSO-d6) δ 8.75 (dd,
J = 2.2, 1.0 Hz, 1H), 8.59 (dd, J = 4.9, 1.6 Hz, 1H), 7.97 (dt, J = 7.9, 1.9 Hz,
1H), 7.46 (ddd, J = 7.9, 4.9, 0.9 Hz, 1H), 6.75 (d, J = 2.3 Hz, 2H), 6.59 (t, J = 2.3 Hz, 1H),
3.78 (s, 6H). 13C NMR (101 MHz, DMSO-d6) δ 160.41, 151.59, 149.02, 138.51, 123.57, 123.07,
119.22, 109.17, 102.26, 92.29, 85.64, 55.40. HRMS (ESI+) in m/z: Expected 240.1019 [M + H+] (C15H14NO2+). Observed
240.1015.
4-(Pyridin-3-ylethynyl)benzonitrile (5a)
While solid. Yield: 92 mg, 90%. Time: 0.5 h. 1H NMR (400
MHz, DMSO-d6) δ 8.84–8.77
(m, 1H), 8.63 (dd, J = 4.9, 1.7 Hz, 1H), 8.03 (dt, J = 7.9, 1.9 Hz, 1H), 7.95–7.88 (m, 2H), 7.82–7.75
(m, 2H), 7.50 (ddd, J = 7.9, 4.9, 0.9 Hz, 1H). 13C NMR (101 MHz, DMSO-d6) δ
151.78, 149.60, 138.79, 132.62, 132.23, 126.51, 123.65, 118.59, 118.29,
111.39, 90.68, 89.96. HRMS (ESI+) in m/z: Expected 528.1904 [M + H+] (C14H9N2+). Observed 205.0758. 5a is
a known compound.46
1-(4-(Pyridin-3-ylethynyl)phenyl)ethan-1-one
(5b)
White solid. Yield: 102 mg, 92%. Time:
0.5 h. 1H NMR (400 MHz, DMSO-d6) δ 8.80
(dd, J = 2.3, 0.9 Hz, 1H), 8.62 (dd, J = 4.9, 1.6 Hz, 1H), 8.08–7.96 (m, 3H), 7.78–7.69 (m,
2H), 7.49 (ddd, J = 7.9, 4.9, 0.9 Hz, 1H), 2.61 (s,
3H). 13C NMR (101 MHz, DMSO-d6) δ 197.18, 151.71, 149.38, 138.68, 136.56, 131.69, 128.45,
126.17, 123.62, 118.87, 91.42, 88.97, 26.73. HRMS (ESI+) in m/z: Expected 222.0913 [M + H+] (C15H12NO+). Observed 222.0914. 5b is a known compound.47
3-(Phenylethynyl)pyridine
(5c)
Tan solid.
Yield: 79 mg, 88%. Time: 1 h. 1H NMR (400 MHz, DMSO-d6) δ 8.76 (dd, J = 2.2,
0.9 Hz, 1H), 8.59 (dd, J = 4.9, 1.6 Hz, 1H), 7.98
(dt, J = 7.9, 2.0 Hz, 1H), 7.59 (ddd, J = 6.7, 3.0, 1.6 Hz, 2H), 7.46 (tt, J = 6.2, 1.8
Hz, 4H). 13C NMR (101 MHz, DMSO-d6) δ 151.55, 148.96, 138.47, 131.43, 129.18, 128.77,
123.56, 121.64, 119.32, 92.21, 86.08. HRMS (ESI+) in m/z: Expected 202.0627 [M + Na+] (C13H9NNa+). Observed 202.0634. 5c is a known compound.48
3-((3-Nitrophenyl)ethynyl)pyridine
(5d)
Tan solid. Yield: 99 mg, 87%. Time: 2 h. 1H NMR (400 MHz,
DMSO-d6) δ 8.83 (d, J = 2.1 Hz, 1H), 8.63 (dd, J = 4.9, 1.7 Hz, 1H),
8.39 (t, J = 1.9 Hz, 1H), 8.28 (ddd, J = 8.4, 2.5, 1.1 Hz, 1H), 8.04 (ddt, J = 7.6, 5.6,
1.6 Hz, 2H), 7.75 (t, J = 8.0 Hz, 1H), 7.55–7.44
(m, 1H). 13C NMR (101 MHz, DMSO-d6) δ 151.82, 149.53, 147.89, 138.79, 137.54, 130.49,
125.97, 123.85, 123.64, 123.25, 118.62, 89.89, 88.20. HRMS (ESI+)
in m/z: Expected 225.0659 [M + H+] (C13H9N2O2+). Observed 225.0657.
3-((2-(Trifluoromethyl)phenyl)ethynyl)pyridine
(5e)
Yellow oil. Yield: 88 mg, 71%. Time: 18
h. 1H NMR (400 MHz, DMSO-d6) δ 8.74
(dd, J = 2.1, 1.0 Hz, 1H), 8.64 (dd, J = 4.9, 1.7 Hz, 1H), 7.97 (dt, J = 7.9, 1.9 Hz,
1H), 7.86 (dd, J = 7.6, 1.4 Hz, 2H), 7.80–7.71
(m, 1H), 7.66 (tdd, J = 8.6, 2.2, 1.1 Hz, 1H), 7.50
(ddd, J = 7.9, 4.9, 1.0 Hz, 1H). 13C NMR
(101 MHz, DMSO-d6) δ 151.42, 149.59,
138.53, 134.03, 129.57, 123.74, 122.13, 119.45, 118.70, 91.26, 87.89.
HRMS (ESI+) in m/z: Expected 248.0682
[M + H+] (C14H9F3N+). Observed 248.0675. 5e is a known compound.49
3-(Pyridin-3-ylethynyl)benzoic Acid (5f)
Tan solid. Yield: 69 mg, 65%. Time: 4 h. 1H NMR (400 MHz,
DMSO-d6) δ 13.24 (s, 1H), 8.80 (dd, J = 2.2, 0.9 Hz, 1H), 8.61 (dd, J = 4.9,
1.6 Hz, 1H), 8.10 (t, J = 1.7 Hz, 1H), 8.01 (ddt, J = 13.2, 7.8, 1.7 Hz, 2H), 7.83 (dt, J = 7.7, 1.4 Hz, 1H), 7.59 (t, J = 7.8 Hz, 1H), 7.49
(ddd, J = 7.9, 4.9, 0.9 Hz, 1H). 13C NMR
(101 MHz, DMSO-d6) δ 166.38, 151.61,
149.09, 138.74, 135.37, 132.08, 131.42, 129.79, 129.29, 123.63, 122.08,
119.08, 91.21, 86.83. HRMS (ESI+) in m/z: Expected 224.0706 [M + H+] (C14H10NO2+). Observed 224.0706.
4-(Pyridin-3-ylethynyl)benzaldehyde
(5g)
Tan solid. Yield: 91 mg, 88%. Time: 2 h. 1H NMR (400 MHz,
DMSO-d6) δ 10.05 (s, 1H), 8.83–8.77
(m, 1H), 8.63 (dd, J = 4.9, 1.7 Hz, 1H), 8.03 (dt, J = 7.9, 2.0 Hz, 1H), 8.00–7.94 (m, 2H), 7.84–7.77
(m, 2H), 7.50 (ddd, J = 7.9, 4.9, 0.9 Hz, 1H). 13C NMR (101 MHz, DMSO-d6) δ
192.42, 151.75, 149.49, 138.74, 135.82, 132.13, 129.64, 127.44, 123.65,
118.77, 91.35, 89.54. HRMS (ESI+) in m/z: Expected 208.0757 [M + H+] (C14H10NO+). Observed 208.0755. 5g is a known compound.50
Methyl 3-(Pyridin-3-ylethynyl)benzoate (5h)
Tan solid. Yield: 103 mg, 87%. Time: 2 h. 1H NMR (400
MHz, DMSO-d6) δ 8.80 (dd, J = 2.2, 1.0 Hz, 1H), 8.61 (dd, J = 4.9,
1.7 Hz, 1H), 8.14–8.08 (m, 1H), 8.05–7.97 (m, 2H), 7.86
(dt, J = 7.8, 1.4 Hz, 1H), 7.65–7.58 (m, 1H),
7.48 (ddd, J = 7.9, 4.9, 0.9 Hz, 1H), 3.88 (s, 3H).13C NMR (101 MHz, DMSO-d6) δ
165.35, 151.71, 149.23, 138.65, 135.77, 131.87, 130.24, 129.59, 129.47,
123.58, 122.29, 118.97, 90.95, 87.07, 52.37. HRMS (ESI+) in m/z: Expected 238.0863 [M + H+] (C15H12NO2+). Observed
238.0851.
3-((4-Chlorophenyl)ethynyl)pyridine (5i)
White solid. Yield: 95 mg, 89%. Time: 2 h. 1H NMR (400
MHz, DMSO-d6) δ 8.76 (d, J = 2.6 Hz, 1H), 8.60 (dd, J = 4.3, 2.2
Hz, 1H), 7.99 (dd, J = 8.0, 2.3 Hz, 1H), 7.66–7.57
(m, 2H), 7.52 (dd, J = 8.7, 2.2 Hz, 2H), 7.50–7.43
(m, 1H). 13C NMR (101 MHz, DMSO-d6) δ 151.63, 149.19, 138.58, 133.97, 133.22, 129.00,
123.63, 120.56, 119.08, 91.06, 87.17. HRMS (ESI+) in m/z: Expected 214.0418 [M + H+] (C13H9ClN+). Observed 214.0413. 5i is a known compound.51
3-([1,1′-Biphenyl]-2-ylethynyl)pyridine
(5j)
Yellow oil. Yield: 101 mg, 79%. Time: 2
h. 1H NMR (400 MHz, DMSO-d6) δ 8.58–8.46
(m, 2H), 7.78–7.68 (m, 2H), 7.68–7.62 (m, 2H), 7.58–7.38
(m, 7H). 13C NMR (101 MHz, DMSO-d6) δ 151.20, 148.90, 143.44, 139.59, 138.05, 132.79,
129.64, 129.53, 129.07, 128.12, 127.79, 127.58, 123.62, 119.89, 119.48,
92.24, 88.64. HRMS (ESI+) in m/z: Expected 256.1121 [M + H+] (C19H14N+). Observed 256.1118. Anal. Calcd for C19H13N: C, 88.86; H, 5.39; N: 5.76. Found: C, 88.75; H,
5.14; N, 5.38.
3-(p-Tolylethynyl)pyridine
(5k)
Tan solid. Yield: 75 mg, 78%. Time: 2 h. 1H
NMR (400 MHz, DMSO-d6) δ 8.74 (dd, J = 2.2, 1.0 Hz, 1H), 8.58 (dd, J = 4.9,
1.6 Hz, 1H), 7.96 (dt, J = 7.9, 1.9 Hz, 1H), 7.53–7.40
(m, 3H), 7.26 (d, J = 7.8 Hz, 2H), 2.35 (s, 3H). 13C NMR (101 MHz, DMSO-d6) δ
151.48, 148.79, 139.05, 138.37, 131.35, 129.39, 123.54, 119.52, 118.63,
92.45, 85.51, 21.02. HRMS (ESI+) in m/z: Expected 194.0964 [M + H+] (C14H12N+). Observed 194.0958. 5k is known compound.52
2-Hydroxy-5-(pyridin-3-ylethynyl)benzamide
(5l)
White solid. Yield: 90 mg, 76%. Time: 6
h. 1H NMR (400
MHz, DMSO-d6) δ 13.42 (s, 1H), 8.75–8.69
(m, 1H), 8.61–8.50 (m, 2H), 8.17 (d, J = 2.1
Hz, 1H), 8.05 (s, 1H), 7.94 (dt, J = 7.9, 1.9 Hz,
1H), 7.62 (dd, J = 8.6, 2.0 Hz, 1H), 7.46 (ddd, J = 8.0, 4.9, 0.9 Hz, 1H), 6.95 (d, J =
8.6 Hz, 1H). 13C NMR (101 MHz, DMSO-d6) δ 171.10, 161.73, 151.35, 148.73, 138.25, 136.89,
131.74, 123.60, 119.57, 118.21, 114.84, 111.58, 92.01, 84.57. HRMS
(ESI+) in m/z: Expected 239.0815
[M + H+] (C14H11N2O2+). Observed 239.0808. Anal. Calcd for C14H10N2O2: C, 70.58; H, 4.23; N, 11.76.
Found: C, 70.48; H, 4.31; N, 11.78.
4-(Pyridin-3-ylethynyl)phenol
(5m)
Tan
solid. Yield: 50 mg, 52%. Time: 2 h. 1H NMR (400 MHz, DMSO-d6) δ 10.00 (s, 1H), 8.70 (d, J = 2.1 Hz, 1H), 8.54 (dd, J = 4.9, 1.6 Hz, 1H),
7.91 (dt, J = 7.9, 1.9 Hz, 1H), 7.48–7.36
(m, 3H), 6.85–6.77 (m, 2H). 13C NMR (101 MHz, DMSO-d6) δ 158.40, 151.31, 148.42, 138.13, 133.16,
123.51, 119.96, 115.78, 111.78, 93.04, 84.18. HRMS (ESI+) in m/z: Expected 196.0759 [M + H+] (C13H10NO+). Observed 196.0757.
4-(Pyridin-3-ylethynyl)aniline (5n)
Tan
solid. Yield: 60 mg, 62%. Time: 2 h. 1H NMR (400 MHz, DMSO-d6) δ 8.65 (d, J = 2.1
Hz, 1H), 8.50 (dd, J = 4.9, 1.7 Hz, 1H), 7.86 (dt, J = 7.9, 2.0 Hz, 1H), 7.40 (dd, J = 7.9,
4.9 Hz, 1H), 7.28–7.19 (m, 2H), 6.63–6.52 (m, 2H), 5.63
(s, 2H). 13C NMR (101 MHz, DMSO-d6) δ 151.07, 149.86, 147.92, 137.78, 132.70, 123.46,
120.48, 113.57, 107.33, 94.49, 83.35. HRMS (ESI+) in m/z: Expected 195.0917 [M + H+] (C13H11N2+). Observed 195.0919. 5n is a known compound.53
1,2-Di(pyridin-3-yl)ethyne
(5o)
Tan solid.
Yield: 83 mg, 92%. Time: 2 h. 1H NMR (400 MHz, DMSO-d6) δ 8.80 (dd, J = 2.2,
1.0 Hz, 2H), 8.62 (dd, J = 4.9, 1.7 Hz, 2H), 8.02
(dt, J = 7.9, 1.9 Hz, 2H), 7.49 (ddd, J = 7.9, 4.9, 0.9 Hz, 2H). 13C NMR (101 MHz, DMSO-d6) δ 151.66, 149.37, 138.64, 123.62, 118.81,
89.05. HRMS (ESI+) in m/z: Expected
181.076 [M + H+] (C12H9N2+). Observed 181.0762. 5o is a known compound.54
5-(Pyridin-3-ylethynyl)isoquinoline (5p)
Tan solid. Yield: 90 mg, 78%. Time: 2 h. 1H NMR (400 MHz,
DMSO-d6) δ 9.42 (d, J = 1.0 Hz, 1H), 8.93 (dd, J = 2.2, 0.9 Hz, 1H),
8.71–8.61 (m, 2H), 8.27–8.19 (m, 2H), 8.15 (dt, J = 7.9, 2.0 Hz, 1H), 8.10 (dd, J = 7.2,
1.1 Hz, 1H), 7.75 (dd, J = 8.2, 7.2 Hz, 1H), 7.52
(ddd, J = 7.9, 4.9, 0.9 Hz, 1H). 13C NMR
(101 MHz, DMSO-d6) δ 152.91, 151.80,
149.33, 144.30, 138.73, 134.94, 134.61, 129.08, 127.90, 127.22, 123.63,
119.06, 118.32, 118.09, 91.94, 88.69. HRMS (ESI+) in m/z: Expected 231.0919 [M + H+] (C16H11N2+). Observed 231.0917.
Anal. Calcd for C16H10N2: C, 83.46;
H, 4.38; N: 12.17. Found: C, 83.22; H, 4.53; N, 12.07.
5-(Pyridin-3-ylethynyl)pyrimidine
(5q)
Tan solid. Yield: 72 mg, 90%. Time: 2 h. 1H NMR (400 MHz,
DMSO-d6) δ 9.23 (s, 1H), 9.06 (s,
2H), 8.82 (dd, J = 2.2, 1.0 Hz, 1H), 8.65 (dd, J = 4.9, 1.7 Hz, 1H), 8.04 (dt, J = 7.9,
1.9 Hz, 1H), 7.51 (ddd, J = 7.9, 4.9, 1.0 Hz, 1H). 13C NMR (101 MHz, DMSO-d6) δ
158.79, 157.14, 151.72, 149.77, 138.77, 123.69, 118.35, 118.33, 92.34,
85.79. HRMS (ESI+) in m/z: Expected
182.0713 [M + H+] (C11H10N3+). Observed 182.0713. 5q is a known compound.55
3-(Thiophen-3-ylethynyl)pyridine (5r)
Tan solid. Yield: 72 mg, 78%. Time: 2 h. 1H
NMR (400 MHz,
DMSO-d6) δ 8.73 (dd, J = 2.2, 1.0 Hz, 1H), 8.58 (dd, J = 4.9, 1.6 Hz,
1H), 7.98–7.91 (m, 2H), 7.68 (ddd, J = 5.0,
2.9, 1.0 Hz, 1H), 7.45 (ddd, J = 7.9, 4.9, 1.0 Hz,
1H), 7.30 (dt, J = 5.0, 1.1 Hz, 1H). 13C NMR (101 MHz, DMSO-d6) δ 151.42,
148.83, 138.35, 130.65, 129.53, 127.10, 123.56, 120.53, 119.42, 87.83,
85.41. HRMS (ESI+) in m/z: Expected
186.0372 [M + H+] (C11H8NS+). Observed 186.0368. 5r is a known compound.56
Methyl 4-Oxo-6-(pyridin-3-ylethynyl)-1,4-dihydroquinoline-2-carboxylate
(5s)
Yellow solid. Yield: 38 mg, 25%. Time:
6 h. 1H NMR (400 MHz, DMSO-d6) δ 12.30 (s, 1H), 8.86–8.71 (m, 1H), 8.60 (dd, J = 4.8, 1.7 Hz, 1H), 8.24 (d, J = 2.0
Hz, 1H), 8.05–7.95 (m, 2H), 7.87 (dd, J =
8.7, 2.0 Hz, 1H), 7.48 (ddd, J = 7.9, 4.9, 0.9 Hz,
1H), 6.69 (s, 1H), 3.97 (s, 3H). 13C NMR (101 MHz, DMSO-d6) δ 162.69, 151.71, 149.12, 138.68, 134.78,
128.32, 126.19–124.88 (m), 123.72, 120.13 (d, J = 157.9 Hz), 117.30, 110.62, 91.87, 86.68, 53.62, 29.03. HRMS (ESI+)
in m/z: Expected 327.0752 [M + Na+] (C18H12N2O3Na+). Observed 327.0755.
5-(Pyridin-3-ylethynyl)-3,4-dihydroquinolin-2(1H)-one (5t)
White solid. Yield: 66
mg, 53%.
Time: 4 h. 1H NMR (400 MHz, DMSO-d6) δ 8.76 (dd, J = 2.2, 0.9 Hz, 1H),
8.59 (dd, J = 4.9, 1.6 Hz, 1H), 7.98 (dt, J = 7.9, 2.0 Hz, 1H), 7.59 (ddd, J = 6.7,
3.0, 1.6 Hz, 2H), 7.46 (tt, J = 6.2, 1.8 Hz, 4H). 13C NMR (101 MHz, DMSO-d6) δ
169.90, 151.53, 149.04, 138.76, 138.47, 127.26, 125.40, 125.29, 123.58,
120.49, 119.29, 116.01, 90.28, 90.01, 29.80, 23.28. HRMS (ESI+) in m/z: Expected 249.1025 [M + H+] (C16H13N2O+). Observed
249.1022.
3-(Pyridin-3-ylethynyl)imidazo[1,2-a]pyrimidine
(5u)
Tan solid. Yield: 46 mg, 42%. Time: 6 h,
Temperature: 60 °C. 1H NMR (400 MHz, DMSO-d6) δ 9.17 (dd, J = 6.8,
1.9 Hz, 1H), 8.90 (dd, J = 2.2, 0.9 Hz, 1H), 8.70
(dd, J = 4.1, 2.0 Hz, 1H), 8.62 (dd, J = 4.9, 1.7 Hz, 1H), 8.22 (s, 1H), 8.10 (dt, J =
7.9, 1.9 Hz, 1H), 7.51 (ddd, J = 8.0, 4.9, 1.0 Hz,
1H), 7.29 (dd, J = 6.8, 4.2 Hz, 1H). 13C NMR (101 MHz, DMSO-d6) δ 151.91,
151.34, 149.16, 148.33, 139.63, 138.15, 134.53, 123.55, 118.84, 110.17,
106.07, 95.71, 79.04. HRMS (ESI+) in m/z: Expected 221.0822 [M + H+] (C13H9N4+). Observed 221.0826.
1-Methyl-4-(pyridin-3-ylethynyl)-1H-pyrazole-3-carbaldehyde
(5v)
Tan solid. Yield: 69 mg, 63%. Time: 20
h, Temperature: 60 °C. 1H NMR (400 MHz, DMSO-d6) δ 9.98–9.93 (m, 1H), 8.71 (dd, J = 2.2, 1.0 Hz, 1H), 8.58 (dd, J = 4.9,
1.6 Hz, 1H), 8.31 (s, 1H), 7.93 (dt, J = 7.9, 1.9
Hz, 1H), 7.46 (ddd, J = 7.9, 4.9, 1.0 Hz, 1H), 4.00
(s, 3H). 13C NMR (101 MHz, DMSO-d6) δ 184.92, 151.33, 149.42, 148.91, 138.30, 136.69,
123.59, 119.49, 102.13, 88.69, 82.95. HRMS (ESI+) in m/z: Expected 212.0818 [M + H+] (C12H10N3O+). Observed 212.0822.
3-((1-Methyl-1H-imidazol-5-yl)ethynyl)pyridine
(5w)
Tan solid. Yield: 63 mg, 69%. Time: 24
h, 60 °C. 1H NMR (400 MHz, DMSO-d6) δ 8.76 (dd, J = 2.2, 1.0 Hz,
1H), 8.59 (dd, J = 4.9, 1.6 Hz, 1H), 7.98 (dt, J = 7.9, 1.9 Hz, 1H), 7.81 (s, 1H), 7.47 (ddd, J = 7.9, 4.9, 0.9 Hz, 1H), 7.37 (d, J = 1.0 Hz, 1H),
3.73 (s, 3H). 13C NMR (101 MHz, DMSO-d6) δ 151.22, 149.01, 139.85, 138.12, 134.44, 123.57,
119.03, 114.54, 92.74, 80.76, 31.73. HRMS (ESI+) in m/z: Expected 184.0869 [M + H+] (C11H10N3+). Observed 184.0868. 5w is a known compound.57
4-(Pyridin-3-ylethynyl)furan-2-carbaldehyde
(5x)
Brown solid. Yield: 101 mg, 83%. Time:
20 h, Temperature:
60 °C. 1H NMR (400 MHz, DMSO-d6) δ 9.64 (d, J = 0.9 Hz, 1H), 8.75
(dd, J = 2.2, 1.0 Hz, 1H), 8.61 (dd, J = 4.9, 1.6 Hz, 1H), 8.56 (d, J = 0.9 Hz, 1H), 7.98
(dt, J = 8.0, 1.9 Hz, 1H), 7.76 (d, J = 0.9 Hz, 1H), 7.48 (ddd, J = 7.9, 4.9, 1.0 Hz,
1H), 1.64 (s, 0H). 13C NMR (101 MHz, DMSO-d6) δ 178.61, 152.39, 151.86, 151.49, 149.30, 138.52,
123.62, 123.51, 118.79, 108.88, 88.69, 82.06. HRMS (ESI+) in m/z: Expected 198.055 [M + H+] (C12H8NO2+). Observed
198.0549.
4-(Pyridin-3-ylethynyl)thiazole (5y)
Tan
solid. Yield: 73 mg, 78%. Time: 18 h, Temperature: 60 °C. 1H NMR (400 MHz, DMSO-d6) δ
9.20 (d, J = 1.9 Hz, 1H), 8.78 (dd, J = 2.2, 1.0 Hz, 1H), 8.62 (dd, J = 4.9, 1.6 Hz,
1H), 8.21 (d, J = 1.9 Hz, 1H), 8.01 (dt, J = 7.9, 1.9 Hz, 1H), 7.53–7.43 (m, 1H). 13C NMR (101 MHz, DMSO-d6) δ 154.99,
151.59, 149.31, 138.63, 136.28, 125.41, 123.63, 118.71, 86.72, 85.38.
HRMS (ESI+) in m/z: Expected 187.0324
[M + H+] (C10H7N2S+). Observed 187.0324.
3,5-Dimethyl-4-(pyridin-3-ylethynyl)isoxazole
(5z)
Yellow oil. Yield: 30 mg, 30%. Time: 32
h, Temperature:
60 °C. 1H NMR (400 MHz, DMSO-d6) δ 8.76 (dd, J = 2.3, 1.0 Hz, 1H),
8.59 (dd, J = 4.9, 1.8 Hz, 1H), 7.98 (dq, J = 8.0, 1.9 Hz, 1H), 7.51–7.41 (m, 1H), 2.52 (d, J = 1.7 Hz, 4H), 2.30 (d, J = 1.7 Hz, 4H). 13C NMR (101 MHz, DMSO-d6) δ
172.12, 160.04, 151.54, 149.13, 138.46, 123.59, 119.08, 99.88, 90.96,
80.45, 11.72, 10.07. HRMS (ESI+) in m/z: Expected 199.0866 [M + H+] (C12H11N2O+). Observed 199.0860. Anal. Calcd for C12H10N2O: C, 72.71; H, 5.08; N, 14.13.
Found: C, 72.96; H, 5.24; N, 13.85.
4-(Pyridin-3-ylethynyl)-1H-indole 9 (5aa)
Tan solid. Yield:
95 mg, 87%. Time: 6 h. 1H NMR (400 MHz, DMSO-d6) δ
11.39 (s, 1H), 8.85–8.79 (m, 1H), 8.58 (dt, J = 4.9, 1.4 Hz, 1H), 8.08–7.99 (m, 1H), 7.54–7.42 (m,
3H), 7.31–7.23 (m, 1H), 7.19–7.09 (m, 1H), 6.67 (ddt, J = 3.0, 1.9, 1.0 Hz, 1H). 13C NMR (101 MHz,
DMSO-d6) δ 151.50, 148.59, 138.33,
135.50, 128.92, 126.60, 123.55, 122.88, 120.89, 119.97, 113.02, 112.42,
100.48, 91.91, 87.93. HRMS (ESI+) in m/z: Expected 219.0917 [M + H+] (C15H11N2+). Observed 219.0918.
1,2-Bis(3,5-dimethoxyphenyl)ethyne
(7a)
Tan solid. Yield: 136 mg, 91%. Time: 2
h. 1H NMR (400
MHz, DMSO-d6) δ 6.71 (dd, J = 2.4, 0.8 Hz, 4H), 6.56 (t, J = 2.3
Hz, 2H), 3.77 (d, J = 0.8 Hz, 12H). 13C NMR (101 MHz, DMSO-d6) δ 160.40,
123.57, 109.07, 101.99, 88.95, 55.41. HRMS (ESI+) in m/z: Expected 299.1278 [M + H+] (C18H19O4+). Observed 299.1268. 7a is a known compound.58
3-((3,5-Dimethoxyphenyl)ethynyl)phenol
(7b)
Yellow solid. Yield: 116 mg, 91%. Time:
2 h. 1H NMR (400
MHz, DMSO-d6) δ 9.71 (s, 1H), 7.21
(t, J = 7.9 Hz, 1H), 6.97 (dt, J = 7.6, 1.2 Hz, 1H), 6.91 (dd, J = 2.5, 1.5 Hz,
1H), 6.82 (ddd, J = 8.2, 2.5, 1.1 Hz, 1H), 6.70 (dd, J = 2.3, 1.1 Hz, 2H), 6.57–6.52 (m, 1H), 3.77 (d, J = 1.3 Hz, 6H). 13C NMR (101 MHz, DMSO-d6) δ 160.40, 157.37, 129.89, 123.74, 122.98,
122.24, 117.77, 116.38, 109.05, 101.84, 89.02, 88.79, 55.40. HRMS
(ESI+) in m/z: Expected 255.1016
[M + H+] (C16H15O3+). Observed 255.1017. Anal. Calcd for C16H14O3: C, 75.57; H, 5.55; N, 0. Found: C, 75.53;
H, 5.64; N, <0.02.
1,3-Dimethoxy-5-(phenylethynyl)benzene (7c)
Brown oil. Yield: 113 mg, 95%. Time: 2 h. 1H NMR (400
MHz, DMSO-d6) δ 6.54–6.46
(m, 3H), 5.41 (s, 1H), 3.74 (s, 5H), 1.83 (dd, J =
12.0, 4.8 Hz, 2H), 1.75–1.36 (m, 9H), 1.30–1.16 (m,
1H). 13C NMR (101 MHz, DMSO-d6) δ 160.41, 131.40, 128.87, 128.76, 123.68, 122.12, 109.05,
101.90, 89.39, 88.87, 55.40. HRMS (ESI+) in m/z: Expected 239.1067 [M + H+] (C14H15N2O2+). Observed 239.1072. 7c is a known compound.59
5-((3,5-Dimethoxyphenyl)ethynyl)-1-methyl-1H-imidazole (7d)
Yellow solid. Yield:
112 mg,
92%. Time: 12 h. 1H NMR (400 MHz, DMSO-d6) δ 7.78 (s, 1H), 7.31 (d, J =
1.1 Hz, 1H), 6.71 (d, J = 2.3 Hz, 2H), 6.56 (t, J = 2.3 Hz, 1H), 3.77 (s, 6H), 3.71 (s, 3H). 13C NMR (101 MHz, DMSO-d6) δ 160.43,
139.61, 134.02, 123.29, 108.73, 101.91, 95.89, 77.33, 55.44, 31.74.
HRMS (ESI+) in m/z: Expected 243.1128
[M + H+] (C14H15N2O2+). Observed 243.1134. Anal. Calcd for C14H14N2O2: C, 69.41; H, 5.82; N, 11.56.
Found: C, 69.34; H, 5.87; N, 11.37.
Methyl 4-((3,5-Dimethoxyphenyl)ethynyl)benzoate
(7e)
Tan solid. Yield: 136 mg, 92%. Time: 24
h. 1H NMR (400 MHz, DMSO-d6) δ 8.02–7.97
(m, 2H), 7.74–7.65 (m, 2H), 6.75 (d, J = 2.3
Hz, 2H), 6.59 (t, J = 2.3 Hz, 1H), 3.87 (s, 4H),
3.78 (s, 6H). 13C NMR (101 MHz, DMSO-d6) δ 165.60, 160.44, 131.71, 129.42, 129.36, 126.90,
123.10, 109.24, 102.36, 92.36, 87.95, 55.44, 52.34. HRMS (ESI+) in m/z: Expected 297.1135 [M + H+] (C18H17O4+). Observed
297.1135. Anal. Calcd for C18H16O4: C, 72.96; H, 5.44; N, 0. Found: C, 72.79; H, 5.48; N, <0.02.
4-((3,5-Dimethoxyphenyl)ethynyl)benzonitrile (7f)
White solid. Yield: 123 mg, 93%. 1H NMR (400
MHz, DMSO-d6) δ 7.95–7.85
(m, 2H), 7.79–7.67 (m, 2H), 6.76 (d, J = 2.3
Hz, 2H), 6.60 (t, J = 2.3 Hz, 1H), 3.78 (s, 6H). 13C NMR (101 MHz, DMSO-d6) δ
160.45, 132.61, 132.18, 127.03, 122.84, 118.42, 111.03, 109.31, 102.54,
93.34, 87.45, 55.47. HRMS (ESI+) in m/z: Expected 286.0838 [M + Na+] (C17H14NO2Na+). Observed 286.0834.
4-((3,5-Dimethoxyphenyl)ethynyl)benzoic
Acid (7g)
Yellow solid. Yield: 79 mg, 56%. 1H NMR (400
MHz, DMSO-d6) δ 13.16 (s, 1H), 7.97
(d, J = 8.1 Hz, 2H), 7.67 (d, J =
8.1 Hz, 2H), 6.75 (d, J = 2.3 Hz, 2H), 6.59 (t, J = 2.3 Hz, 1H), 3.78 (s, 6H). 13C NMR (101 MHz,
DMSO-d6) δ 166.67, 164.03, 160.44,
131.57, 130.62, 129.56, 126.46, 123.19, 109.22, 102.32, 92.03, 88.13,
55.45, 40.43, −1.92. HRMS (ESI+) in m/z: Expected 283.0978 [M + H+] (C17H15O4+). Observed 283.0973. Anal.
Calcd for C17H14O4: C, 72.33; H,
5.00; N, 0. Found: C, 71.88; H, 4.95; N, <0.02.
1-(Cyclohex-1-en-1-ylethynyl)-3,5-dimethoxybenzene
(7h)
Orange oil. Yield: 101 mg, 83%. Time: 2
h. 1H NMR (400 MHz, DMSO-d6) δ 6.55
(d, J = 2.3 Hz, 2H), 6.49 (t, J =
2.3 Hz, 1H), 6.19 (tt, J = 3.8, 1.6 Hz, 1H), 3.74
(s, 6H), 2.13 (dtdd, J = 9.6, 5.8, 4.1, 2.3 Hz, 4H),
1.69–1.49 (m, 4H). 13C NMR (101 MHz, DMSO-d6) δ 160.29, 135.51, 124.25, 119.88, 108.78,
101.30, 90.81, 86.80, 55.28, 28.68, 25.18, 21.77, 20.94. HRMS (ESI+)
in m/z: Expected 243.138 [M + H+] (C16H19O2+).
Observed 243.1376.
4-(3,5-Dimethoxyphenyl)-2-methylbut-3-yn-2-ol
(7i)
Yellow oil. Yield: 100 mg, 91%. Time: 20
h. 1H NMR (400 MHz, DMSO-d6) δ 6.57–6.39
(m, 3H), 5.45 (d, J = 1.2 Hz, 1H), 3.74 (d, J = 1.3 Hz, 6H), 1.45 (s, 6H). 13C NMR (101 MHz,
DMSO-d6) δ 160.31, 124.09, 108.82,
101.35, 95.67, 80.37, 63.57, 55.32, 31.57. HRMS (ESI+) in m/z: Expected 221.1172 [M + H+] (C13H17O3+). Observed
221.1171. 7i is a known compound.60
1-((3,5-Dimethoxyphenyl)ethynyl)cyclohexan-1-ol
(7j)
White solid. Yield: 112 mg, 86%. Time:
5 h. 1H NMR (400 MHz, DMSO-d6) δ 6.50
(dt, J = 6.5, 2.3 Hz, 3H), 5.41 (s, 1H), 3.74 (s,
6H), 1.83 (dd, J = 12.5, 4.8 Hz, 2H), 1.71–1.58
(m, 2H), 1.58–1.41 (m, 5H), 1.29–1.18 (m, 1H). 13C NMR (101 MHz, DMSO-d6) δ
160.32, 124.19, 108.87, 101.29, 94.60, 82.56, 66.87, 55.32, 39.63,
24.90, 22.74. HRMS (ESI+) in m/z: Expected 261.1485 [M + H+] (C16H21O3+). Observed 261.1481. Anal. Calcd for C16H20O3: C, 73.82; H, 7.74; N, 0. Found:
C, 73.9; H, 7.95; N, <0.02.
tert-Butyl
1-((3,5-Dimethoxyphenyl)ethynyl)-3-azabicyclo[3.1.0]hexane-3-carboxylate
(7k)
Clear oil. Yield: 128 mg, 75%. Time: 2
h. 1H NMR (400 MHz, DMSO-d6) δ 6.56–6.52 (m, 2H), 6.48 (dd, J =
2.7, 1.7 Hz, 1H), 3.73 (d, J = 1.1 Hz, 6H), 3.68
(dd, J = 10.1, 5.6 Hz, 0H), 3.54–3.29 (m,
3H), 2.02–1.93 (m, 1H), 1.47–1.32 (m, 9H), 1.22 (dd, J = 8.2, 4.8 Hz, 1H), 0.74 (t, J = 5.0
Hz, 1H). 13C NMR (101 MHz, DMSO-d6) δ 160.28, 153.77, 123.99, 109.05, 101.39, 78.89, 55.31,
51.13, 50.81, 47.58, 47.33, 28.05, 26.05, 25.21, 17.64. HRMS (ESI+)
in m/z: Expected 366.1687 [M + Na+] (C20H25NO4Na+). Observed 366.169. Anal. Calcd for C20H25NO4: C, 69.95; H, 7.34; N, 4.08. Found: C, 70.05; H, 7.49;
N, 4.04.
tert-Butyl 4-((3,5-Dimethoxyphenyl)ethynyl)-4-methylpiperidine-1-carboxylate
(7l)
Clear oil. Yield: 174 mg, 97%. Time: 24
h. 1H NMR (400 MHz, DMSO-d6) δ 6.55 (d, J = 2.3 Hz, 2H), 6.48 (t, J = 2.3 Hz, 1H), 3.88 (d, J = 13.1 Hz,
2H), 3.73 (s, 5H), 3.04 (s, 3H), 1.72–1.64 (m, 2H), 1.40 (s,
11H), 1.28 (s, 4H). 13C NMR (101 MHz, DMSO-d6) δ 160.28, 153.78, 124.27, 109.06, 101.31, 93.85,
82.77, 78.64, 55.33, 31.43, 28.95, 28.09. HRMS (ESI+) in m/z: Expected 382.1989 [M + Na+] (C21H29NO4Na+). Observed 382.1985.
Anal. Calcd for C21H29NO4: C, 70.17;
H, 8.13; N, 3.90. Found: C, 70.45; H, 8.34; N, 3.93.
1-(Cyclopropylethynyl)-3,5-dimethoxybenzene
(7m)
Orange oil. Yield: 97 mg, 96%. Time: 10
h. 1H NMR (400 MHz, DMSO-d6) δ 6.50
(d, J = 2.3 Hz, 2H), 6.45 (t, J =
2.3 Hz, 1H), 3.72 (s, 6H), 1.52 (tt, J = 8.3, 5.0
Hz, 1H), 0.93–0.82 (m, 2H), 0.76–0.66 (m, 2H). 13C NMR (101 MHz, DMSO-d6) δ
160.25, 124.64, 108.98, 100.93, 93.42, 75.67, 55.26, 8.34. HRMS (ESI+)
in m/z: Expected 203.1067 [M + H+] (C13H15O2+).
Observed 203.1060. 7m is a known compound.61
2-(4-(3,5-Dimethoxyphenyl)but-3-yn-1-yl)isoindoline-1,3-dione
(7n)
White solid. Yield: 141 mg, 84%. Time:
8 h. 1H NMR (400 MHz, DMSO-d6) δ 7.95–7.88 (m, 2H), 7.86 (dt, J =
5.0, 3.4 Hz, 2H), 6.45 (t, J = 2.3 Hz, 1H), 6.39
(d, J = 2.3 Hz, 2H), 3.82 (t, J =
6.9 Hz, 2H), 3.68 (s, 6H), 2.78 (t, J = 6.9 Hz, 2H). 13C NMR (101 MHz, DMSO-d6) δ
167.66, 160.23, 134.57, 131.50, 124.03, 123.13, 108.86, 101.15, 86.55,
81.91, 55.24, 36.20, 18.44. HRMS (ESI+) in m/z: Expected 336.123 [M + H+] (C20H18NO4+). Observed 336.1229. Anal. Calcd
for C20H17NO4: C, 71.63; N, 5.11;
H, 4.18. Found: C, 71.65; H, 5.19; N, 4.13.
General Procedure
for Synthesis of (10)
To an oven-dried Biotage
microwave process vial (#355630), 2-bromoaniline
(0.50 mmol, 1.00 equiv), alkyne (0.63 mmol, 1.25 equiv), 2,2,6,6-tetramethylpiperidine
(169 μL, 1.00 mmol, 2.00 equiv), and P2 (10.33
mg, 0.025 mmol, 0.05 equiv) were added to ACN (1.0 mL). Remaining
ACN (1.0 mL) was added to rinse the sides. The reaction vessel was
sealed and bubbled with in-house argon for 5 min. The reaction was
stirred at room temperature for the designated time. Concentrated
HCl (2.50 mmol, 5.0 equiv) was added via syringe directly to the reaction
mixture and stirred at 90 °C for 9 h. Work up involved ammonium
chloride, EtOAc, and brine. The organic layer was concentrated and
purified on Isco silica gel columns to give the resulting product
using a gradient of 0–100% for ethyl acetate/hexanes.
2-Phenyl-1H-indole (10a)
Tan solid. Yield: 49
mg, 51%. Time: 1. 1 h; 2. 9 h. 1H
NMR (400 MHz, chloroform-d) δ 8.31 (s, 1H),
7.71–7.63 (m, 3H), 7.46 (t, J = 7.7 Hz, 2H),
7.41 (d, J = 8.1 Hz, 1H), 7.34 (t, J = 7.5 Hz, 1H), 7.26–7.18 (m, 1H), 7.15 (t, J = 7.4 Hz, 1H), 6.85 (d, J = 2.2 Hz, 1H). 13C NMR (101 MHz, chloroform-d) δ 138.02, 136.96,
132.52, 129.42, 129.16, 127.85, 125.30, 122.50, 120.81, 120.42, 111.03,
100.15. HRMS (ESI+) in m/z: Expected
194.0964 [M + H+] (C14H12N+). Observed 194.0967. 10a is a known compound.62
2,2-Difluoro-6-phenyl-5H-[1,3]dioxolo[4,5-f]indole (10b)
Yellow solid. Yield:
40 mg, 29%. Time: 1. 3 h; 2. 9 h. 1H NMR (400 MHz, chloroform-d) δ 8.37 (s, 1H), 7.66–7.57 (m, 2H), 7.45
(t, J = 7.6 Hz, 2H), 7.37–7.30 (m, 1H), 7.22
(s, 1H), 7.08 (s, 1H), 6.79 (dd, J = 2.3, 1.1 Hz,
1H). 13C NMR (101 MHz, chloroform-d) δ
140.90, 139.50, 138.20, 131.89, 131.86, 129.10, 127.82, 124.86, 124.24,
100.35, 100.25, 92.61. HRMS (ESI+) in m/z: Expected 274.0686 [M + H+] (C15H10F2NO2+). Observed 274.0682.
Methyl
2-(4-Methoxyphenyl)-1H-indole-7-carboxylate
(10c)
Tan solid. Yield: 66 mg, 47%. Time: 1.
1 h; 2. 9 h. 1H NMR (400 MHz, chloroform-d) δ 10.04 (s, 1H), 7.92–7.73 (m, 2H), 7.73–7.63
(m, 2H), 7.14 (t, J = 7.8 Hz, 1H), 7.03–6.94
(m, 2H), 6.75 (d, J = 2.3 Hz, 1H), 4.01 (d, J = 1.2 Hz, 3H), 3.86 (d, J = 1.2 Hz, 3H). 13C NMR (101 MHz, chloroform-d) δ 168.25,
159.77, 139.19, 136.93, 130.70, 126.83, 125.92, 124.78, 123.89, 119.48,
114.62, 112.20, 98.42, 55.50, 51.98. HRMS (ESI+) in m/z: Expected 282.1125 [M + H+] (C17H16NO3+). Observed 282.1133.
2-Phenyl-1H-indol-7-amine (10d)
Brown solid. Yield: 81 mg, 78%. Time: 1. 8 h; 2. 8 h. 1H NMR (400 MHz, chloroform-d) δ 8.20
(s, 1H), 7.76–7.59 (m, 2H), 7.49–7.41 (m, 2H), 7.36–7.30
(m, 1H), 7.19 (d, J = 8.0 Hz, 1H), 6.97 (td, J = 7.7, 2.0 Hz, 1H), 6.82 (d, J = 2.1
Hz, 1H), 6.61 (d, J = 7.3 Hz, 1H), 3.66 (s, 2H). 13C NMR (101 MHz, DMSO-d6) δ
136.25, 133.66, 132.52, 129.25, 128.86, 127.07, 126.42, 124.66, 120.56,
108.51, 105.21, 99.24. HRMS (ESI+) in m/z: Expected 209.1073 [M + H+] (C14H13N2+). Observed 209.1077. 10d is
a known compound but no analytical data can be found online.
2-Cyclopropyl-5-(trifluoromethoxy)-1H-indole
(10e)
Brown solid. Yield: 73 mg, 61%. Time:
1. 1 h; 2. 8 h. 1H NMR (400 MHz, chloroform-d) δ 8.01 (s, 1H), 7.34 (d, J = 2.5 Hz, 1H),
7.23 (d, J = 8.7 Hz, 1H), 7.03–6.91 (m, 1H),
6.21–6.06 (m, 1H), 1.96 (tt, J = 8.4, 5.1
Hz, 1H), 1.07–0.94 (m, 2H), 0.84–0.72 (m, 2H). 13C NMR (101 MHz, chloroform-d) δ 144.00,
143.28, 134.15, 129.12, 122.26, 119.72, 114.97, 112.31, 110.72, 98.35,
9.04, 7.64. HRMS (ESI+) in m/z:
Expected 242.0787 [M + H+] (C12H11F3NO+). Observed 242.0790.
3-(1H-Indol-2-yl)phenol (10f)
Tan solid.
Yield: 54 mg, 52%. Time: 1. 1 h; 2. 9 h. HRMS (ESI+)
in m/z: 1H NMR (400 MHz,
chloroform-d) δ 8.30 (s, 1H), 7.63 (d, J = 7.8 Hz, 1H), 7.40 (d, J = 8.1 Hz, 1H),
7.31 (t, J = 7.8 Hz, 1H), 7.25–7.17 (m, 1H),
7.16–7.10 (m, 2H), 6.82–6.76 (m, 2H), 4.85 (s, 1H). 13C NMR (101 MHz, chloroform-d) δ 156.19,
137.59, 136.94, 134.22, 130.45, 129.31, 122.66, 120.88, 120.48, 117.89,
114.87, 112.29, 111.06, 100.48. Expected 210.0913 [M + H+] (C14H12NO+). Observed 210.0915. 10f is a known compound, but no analytical data can be found
online.
Supporting Information Available
The Supporting Information
is available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b01868.Catalyst and compound
characterization data (PDF)
Supplementary Material
ao8b01868_si_001.pdf
Author Present Address
† UAB
School of Medicine, 1670 University Blvd, Birmingham, Alabama
3523, United States (B.T.M.).
Author Present Address
‡ Nexus
Discovery Advisorsm 7820B Wormans Mill Road, Suite 208, Frederick,
Maryland 21701, United States (D.J.M.).
The authors
declare no competing financial interest.
Acknowledgments
We thank
Shyh-Ming Yang, Patrick Morris, Dan Jansen, Samarjit
Patnaik, and Sara Kearney for valuable suggestions; Dingyin Tao and
Yuhong Fang for analytical chemistry support. The authors gratefully
acknowledge funding by the Intramural Research Program, National Center
for Advancing Translational Sciences (NCATS), National Institutes
of Health (NIH).
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American
Chemical Society 3145884910.1021/acsomega.8b00835ArticleVersatile Approach for Reducing Propagation Loss in
Wet-Electrospun Polymer Fiber Waveguides Ishii Yuya *†Omori Keisho ‡Sakai Heisuke §Arakawa Yuki ∥Fukuda Mitsuo ‡† Faculty
of Fiber Science and Engineering, Kyoto
Institute of Technology, Kyoto, Kyoto 606-8585, Japan‡Department of Electrical and Electronic
Information Engineering and ∥Department of
Environmental and Life Sciences, Toyohashi
University of Technology, Toyohashi, Aichi 441-8580, Japan§ School
of Materials Science, Japan Advanced Institute of Science and Technology, Nomi, Ishikawa 923-1292, Japan* E-mail: yishii@kit.ac.jp.22 06 2018 30 06 2018 3 6 6787 6793 27 04 2018 08 06 2018 Copyright © 2018 American Chemical
Society2018American Chemical
SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
Wet-electrospun (WES) polymer micron
and submicron fibers are promising
building blocks for small, flexible optical fiber devices, such as
waveguides, sensors, and lasers. WES polymer fibers have an inherent
cylindrical geometry similar to that of optical fibers and a relatively
large aspect ratio. Furthermore, WES fibers can be produced using
low-cost and low-energy manufacturing techniques with large-area fabrication
and a large variety of materials. However, the high propagation loss
in the fibers, which is normally on the order of tens or thousands
of decibels per centimeter in the visible light region, has impeded
the use of these fibers in optical fiber devices. Here, the origin
of propagation losses is examined to develop a comprehensive and versatile
approach to reduce these losses. The excess light scattering that
occurs in fibers due to their inhomogeneous density is one of the
primary factors in the propagation loss. To reduce this loss, the
light transmission characteristics were investigated for single WES
polymer fibers heated at different temperatures. The propagation loss
was significantly reduced from 17.0 to 8.1 dB cm–1 at 533 nm wavelength, by heating the fibers above their glass transition
temperature, 49.8 °C. In addition, systematic verification of
the possible loss factors in the fibers confirmed that the propagation
loss reduction could be attributed to the reduction of extrinsic excess
scattering loss. Heating WES polymer fibers above their glass transition
temperature is a versatile approach for reducing the propagation loss
and should be applicable to a variety of WES fibers. This finding
paves the way for low-loss WES fiber waveguides and their subsequent
application in small, flexible optical fiber devices, including waveguides,
sensors, and lasers.
document-id-old-9ao8b00835document-id-new-14ao-2018-00835accc-price
==== Body
Introduction
Wet electrospinning is a simple, versatile,
and widely used technique
for producing submicron and micron polymer fibers. This technique
has considerable potential for low-cost and low-energy manufacturing
with large fabrication area, providing high material utilization ratios
and high positional accuracy.1,2 The electrospinning
technique can instantaneously and continuously produce fibers with
lengths of more than tens of centimeters that have an inherent cylindrical
geometry similar to that of optical fibers.3 Furthermore, wet-electrospun (WES) fibers can be produced from a
wide variety of spinnable polymers and composites, including highly
transparent polymers and optically active composites.4−6 Thus, WES fibers are promising building blocks for small, flexible
optical fiber devices, such as waveguides, sensors, and lasers.6−11 However, high propagation loss in WES fibers, normally on the order
of tens or thousands of decibels per centimeter in the visible light
region,6,7,9−15 has impeded their widespread use.
Fasano et al. reduced the
propagation loss caused by the surface
morphology of WES conjugated polymer fibers by producing the fibers
in a precisely controlled nitrogen atmosphere,14 but this approach could only be applied to specific materials.
We previously reported that the high propagation loss in WES fibers
could be attributed to (i) excess light scattering in the fibers resulting
from their inhomogeneous density and (ii) loss at the interface between
the fiber core and cladding, originating from nonuniformity of the
fiber diameters.7
In this study,
we reduced the propagation loss in WES polymer fibers
by reducing excess light scattering in the fibers by a versatile heat
treatment approach. The light transmission characteristics of single
WES polymer fibers treated at different post-electrospinning temperatures
revealed that the propagation loss was reduced significantly by 5.9
dB cm–1 at 532 nm wavelength when the fibers were
heated above their glass transition temperature (Tg).
Experimental Details
Fiber Fabrication and Morphological
Characterization
Amorphous poly(lactic acid) composed of
a racemic mixture of d- and l-lactic acid units
(PDLLA) was used as the
fiber material because it exhibits high transparency in the visible
ranges16 and has a lower Tg than other well-known amorphous transparent polymers
such as poly(methyl methacrylate) (PMMA) and polystyrene (PS).17 The lower Tg value
enables easier investigation of the thermal properties of samples
in this initial study. The as-received PDLLA pellets (Mw = 300 000–600 000, Polysciences,
Inc.) were dissolved in chlorobenzene (99.0%, Wako Pure Chemicals
Industries, Ltd.) with a concentration of 16 wt %. The solution was
then loaded into a glass syringe equipped with a 0.18 mm-diameter
stainless-steel needle and was supplied continuously at a rate of
0.02 mL h–1 using a syringe pump (KDS-100, KD Scientific,
Inc.). A high-voltage power supply (HVU-30P100, MECC Co., Ltd.) was
connected to the needle at 4.8 kV. The alternating biased-collector
electrospinning method18 was used to fabricate
single-aligned PDLLA fibers. Two stainless-steel collectors with 3
cm separation were placed 8 cm below the tip of the needle, one of
which was biased with a negative voltage (−800 V) using a high-voltage
power source (HJPM-1N3, Matsusada Precision Inc.). The electrospinning
experiments were performed in air at temperatures of 24–25
°C with a relative humidity of 53–63%. The single-aligned
electrospun PDLLA fibers were collected in two lengths. One length
was placed on a silicon substrate to characterize the shape of each
fiber before heating. The other length was attached to two tapered
optical silica fibers (Fine Glass Technologies Co., Ltd.) to conduct
waveguiding measurements (see Figure 1, STEP 1). The morphology of the single-aligned fibers
was investigated using field-emission scanning electron microscopy
(FESEM, SU8000, Hitachi) operating at 5.0 kV after a 4 nm-thick Os
coating was applied. The mean diameter of each fiber was determined
by averaging diameters taken from FESEM images at more than 12 800
positions along the 250 μm-long fibers using image analysis.
A number of aligned WES PDLLA fibers were prepared by collecting the
fibers for 30 min using a 15 cm-diameter gear-shaped rotating collector
to conduct thermal, X-ray, and spectroscopic characterizations. The
rotating speed of the collector was maintained at 100 rpm to prevent
the as-spun fibers from being stretched by the collector.
Figure 1 Schematic of
the experimental setup for measuring the propagation
loss and transmitted light intensity in a single PDLLA fiber.
Waveguiding Measurements
First, a collimated 532 nm
laser (LCM-T-111, Laser-Export Co. Ltd.) beam with a 440 μm
radius was irradiated to each fiber at different positions [Figure 1, STEP 1] to investigate
the propagation loss in single WES PDLLA fibers. The laser beam was
applied at a 43° angle to the fiber axis, and the polarization
direction of the beam was perpendicular to the fiber axis. A portion
of the laser beam was coupled to a guiding mode in the PDLLA fiber
and collected via a right-tapered optical fiber after being guided
through the PDLLA fiber. The intensity of the collected light was
measured with a spectrometer (USB4000, Ocean Optics, Inc.). Then,
a 632.8 nm He–Ne laser (GLG5370, NEC Corp.) beam was introduced
to the PDLLA fiber from the left tapered optical silica fiber, and
the intensity of the guided light collected via the right tapered
optical fiber was monitored while using different heating temperatures
(see Figure 1, STEP
2). After cooling of the heated PDLLA fibers by stopping the heating,
the measurement performed in STEP 1 was repeated in STEP 3 (see Figure 1, STEP 3). After
the measurement, each fiber was placed on a silicon substrate to characterize
the fiber shape. The propagation loss was also investigated at the
following wavelengths using collimated laser diode modules in the
same manner as that in STEP 1 and STEP 3: 450 nm (CPS450, Thorlabs
Inc.), 521 nm (CPS520, Thorlabs Inc.), 639 nm (CPS635, Thorlabs Inc.),
and 849 nm (CPS850, Thorlabs Inc.). Each collimated laser beam was
irradiated to the single PDLLA fiber though a 1.0 mm-diameter pinhole.
Thermal, X-ray, and Spectroscopic Characterization
The thermal
properties of the WES PDLLA fibers and PDLLA pellets
were investigated with a differential scanning calorimeter (DSC-60,
Shimadzu Corp.) under a nitrogen gas flow at a rate of 50 mL min–1. Each sample of the WES PDLLA fibers (1.6 mg) or
PDLLA pellets (3.0 mg) was heated at a rate of 10 °C min–1 from ambient temperature to 200 °C.
The
molecular structure of the PDLLA in the WES fibers was investigated
using an X-ray diffractometer (RINT-2500, Rigaku Corp.) with a Cu
Kα source (wavelength of 1.5418 Å), which was operated
at 40 kV and 200 mA.
The specific optical rotation of the PDLLA
was measured in chloroform
at a concentration of 10 g L–1 at 25 °C using
a polarimeter (P-2100, JASCO) with a wavelength of 0.589 μm.
The ultraviolet (UV)–visible (Vis)–near infrared
(NIR) attenuation spectra were measured using a UV–Vis–NIR
spectrophotometer (U-4100, Hitachi). A fused glass cell with a 1.0
cm path length was used to measure the transmittance spectra of pure
PDLLA, chlorobenzene, and 16 wt % PDLLA solution in chlorobenzene.
The pure PDLLA sample was prepared by filling the PDLLA pellets into
the cell and melting them at 120 °C for 12 h.
The polymer
chain orientation in the WES PDLLA fibers was evaluated
using a Fourier transform infrared (FT-IR) spectrometer (Thermo Nicolet
6700, Thermo Fisher Scientific Inc.) equipped with a wire grid polarizer
(KRS-5 Wire Grid Polarizer, S. T. Japan). The FT-IR spectrometer resolution
was 4 cm–1, and 128 scans were collected and averaged.
In parallel polarization, the direction of the oscillating electric
field of the incident IR beam is parallel to the aligned fiber axis;
in perpendicular polarization, it is perpendicular to the fiber axis.
Results and Discussion
The specific optical rotation of
the used PDLLA was measured to
be approximately zero, while the optical rotations of poly(lactic
acid) composed of pure optical isomers, namely poly(l-lactic
acid) (PLLA) or poly(d-lactic acid), are reported to be −156
and 156° dm–1 g–1 cm3, respectively.19 This result confirmed
that the PDLLA used in this study was comprised of equivalent amounts
of l- and d-lactic acid20 to form an amorphous polymer. The X-ray diffraction patterns of
the WES PDLLA fibers were also measured, but no obvious diffraction
peaks were found at 2θ between 15° and 20°, even though
crystallized PLLA exhibits diffraction peaks within this angle range.21 This result confirmed that the WES PDLLA fibers
were amorphous.
Five single-aligned WES PDLLA fibers, which
were approximately
3 cm long, (Fibers A–E) were fabricated. One part of each fiber
was placed on a silicon substrate to investigate the fiber morphology. Figure 2a shows an FESEM
image of a single-aligned PDLLA fiber (Fiber A). The fiber was obtained
with a smooth surface. The mean and standard deviation of the fiber
diameters of each fiber are summarized in Table 1. The mean diameter ranges from 1.60 to 1.76
μm.
Figure 2 (a) FESEM image of a single WES PDLLA fiber. (b) Bright- and (c)
dark-field microscopy images of a single WES PDLLA fiber attached
to two tapered optical fibers, where a 632.8 nm laser beam is introduced
from the left tapered fiber to the PDLLA fiber.
Table 1 Mean and Standard Deviation of the
Fiber Diameters before and after Heating
fiber A B C D E
before heating mean diameter (μm) 1.68 1.69 1.67 1.60 1.76
standard deviation (μm) 0.29 0.14 0.32 0.15 0.18
after heating mean diameter (μm) 1.71 1.49 1.51 1.57 1.60
standard deviation (μm) 0.14 0.13 0.22 0.23 0.20
Then, a part of each fiber was attached to two tapered
optical
silica fibers, as shown in the bright-field microscopy image in Figure 2b. The PDLLA fibers
were manually attached to the facing tapered fibers without much difficulty
because electrostatic attraction appeared to act between the charged
electrospun PDLLA fibers and tapered fibers. As shown in the bright-
[Figure 2b] and dark-field
[Figure 2c] microscopy
images, a red laser beam with 632.8 nm wavelength was coupled to the
PDLLA fiber from the left tapered fiber, although part of the laser
beam was radiated at the tip of the left tapered fiber. The thin red
line observed in Figure 2b,c along the PDLLA fiber position demonstrates that the light was
guided in the fiber. Relatively bright dots observed along the PDLLA
fiber in Figure 2c
could be attributed to scattering of the guided light at the points
with locally inhomogeneous morphology.
Figure 3 shows dependence
of the transmitted light intensity, normalized by the peak intensity,
on the fiber temperature, using the same setup as that illustrated
in Figure 1 STEP 2.
The fiber temperature was increased from room temperature by 1.1–1.4
°C min–1 until the PDLLA fiber was broken.
Even at room temperature (25–28 °C), the transmitted light
intensity was more than 160 times higher than that after the PDLLA
fiber was broken, which confirmed that direct light coupling from
the left-tapered silica fiber to the right-tapered silica fiber, which
was primarily caused by the radiated light at the tip of the left
fiber, was negligible. Consequently, the introduced laser beam was
mainly guided in the PDLLA fiber and was collected via the right-tapered
optical fiber. The transmitted light intensity increased with increasing
temperature, showing significant increases at around 45–55
°C. Moreover, the intensity showed peaks at around 55–60
°C. Over this temperature range, the intensity showed a saturated
and/or unstable value until the intensity drop occurred because of
the break of the PDLLA fiber. The transmitted light intensity was
3.5 times higher after heating than that before heating. These results
indicated that the propagation loss in the PDLLA fibers was reduced
by heating, but reduction of the connection loss between the PDLLA
fiber and the tapered silica fibers remained a possible reason for
the increased transmitted light intensity because the connection area
was also heated in the present setup, as shown in Figure 1 STEP 2.
Figure 3 Normalized intensity
of the 632.8 nm light after transmission through
each PDLLA fiber attached to the tapered optical fibers with increasing
temperature. The different colored plots correspond to the different
single fibers.
The thermal properties
of the WES PDLLA fibers and the as-received
PDLLA pellets were investigated using DSC, as shown in Figure 4. The Tg value was determined to be 49.8 °C for the fibers (first
heating), 53.1 °C for the fibers (second heating), and 53.5 °C
for the pellets (second heating). Both samples from the second heating
showed approximately equivalent Tg values
because their erased thermal history allowed the thermal properties
of the PDLLA material to dominate; however, the Tg value for the first heating fibers showed a slight decrease.
Similar Tg decreases were previously reported
for WES PDLLA fibers22 and thin polymer
films.23,24 The evaluated Tg of the WES fibers corresponded to the temperature range of 45–55
°C, where the transmitted light intensity significantly increased.
Excess light scattering loss in PMMA bulks has been reduced by polymerization
or by heating the material above Tg;25,26 thus, the increase in the transmitted light intensity near and above
the Tg value could be partially attributed
to the reduction of excess light scattering loss in the PDLLA fibers.
Figure 4 DSC thermograms
of WES PDLLA fibers and as-received PDLLA pellets.
To understand the change in propagation loss in
each WES fiber
due to heating and avoiding the effects of the connection loss, we
measured the propagation loss before and after heating using the procedure
shown in Figure 1.
Here, the maximum heating temperature was determined to be around
55 °C because this temperature was above Tg of the WES PDLLA fibers and where the transmitted light intensity
showed the maximum intensity (Figure 3).
The propagation loss was determined by measuring
the guided light
intensity with different propagation lengths (l)
using the procedure explained above. Here, l was
determined as the length from the center of the spot at which the
collimated laser was irradiated to the tip of the right tapered silica
fiber. Figure 5a shows
the normalized guided light intensity with different l, measured for a single WES PDLLA fiber (Fiber A) before and after
heating. The wavelength of the irradiated light was 532 nm. The intensity
decreased with increasing l, and the plots adequately
fit the function e–al [solid lines
in Figure 5a], where a is the loss coefficient. The propagation loss was evaluated
using the following formula: −10 log(e–al|l=1cm/e–al|l=0cm) = 10a log(e) [dB cm–1]. Figure 5b summarizes the evaluated propagation loss
of each PDLLA fiber before and after heating. The propagation loss
was significantly reduced after heating for all five PDLLA fibers.
For example, the propagation loss of Fiber A was reduced from 17 to
8.1 dB cm–1, which corresponded to an 8.2-fold increase
in the transmitted light intensity when the light is guided through
1.0 cm of the fiber. These results demonstrated that heating of the
WES PDLLA fibers above Tg significantly
reduced the propagation loss in the fibers. The propagation loss of
Fiber E was reduced to 5.9 dB cm–1, which was the
lowest propagation loss reported for WES polymer fibers.6,7,9−15 Increase in fiber diameters normally decreases the propagation loss
in the fibers,27−29 but significant increase in the mean diameter was
not observed after heating, as shown in Table 1, although the propagation loss was significantly
reduced for all five fibers. This result shows that some other loss
factors were reduced after heating.
Figure 5 (a) Normalized guided light intensity
for Fiber A with different
propagation lengths before and after heating, where the wavelength
was 532 nm. Solid lines show single exponential fittings. (b) Propagation
losses of the five single PDLLA fibers, evaluated before and after
heating.
The possible loss factors for
WES fibers (from refs30−32) are summarized in Figure 6, separated into intrinsic
and extrinsic factors.
Figure 6 Possible loss factors for waveguiding in WES fibers summarized
in refs.30−32
To investigate the absorption loss in the WES PDLLA fibers,
UV–Vis–NIR
measurement was conducted. Figure 7 shows the UV–Vis–NIR attenuation spectra
of pure PDLLA, chlorobenzene, 16 wt % PDLLA solution in chlorobenzene,
and water in a 1.0 cm path-length fused glass cell. Each attenuation
spectrum was converted from the transmittance spectrum of the respective
sample; thus, the measured attenuation included attenuation due to
light reflection and scattering at each interface including that between
air and the fused glass cell. Unique attenuation peaks due to the
electronic transition absorption or molecular vibration absorption
of materials were observed at wavelengths shorter than 450 nm and
longer than 700 nm for pure PDLLA, chlorobenzene, and PDLLA solution.
On the other hand, in the wavelength range from 450 to 680 nm, the
attenuation spectra decreased with increasing wavelength as a result
of the light reflection and scattering at each interface and the light
scattering inside each filled material. Consequently, the intrinsic
absorption loss in the wavelength range of 450–680 nm was estimated
to be less than 0.02 dB cm–1 from the attenuation
spectrum of pure PDLLA, by subtracting the gradually decreasing attenuation
and considering the 1 cm pass length. The extrinsic absorption loss
caused by transition metals and organic contaminants was estimated
to be less than 0.02 dB cm–1 from the attenuation
spectrum of the pure PDLLA, chlorobenzene, and PDLLA solution because
no peaks exceeding 0.02 dB were observed at this wavelength range.
Although the attenuation spectrum of water indicated that its absorption
loss was less than 0.5 dB cm–1 in the wavelength
range of 450–680 nm, as shown in Figure 7, the absorption loss of WES PDLLA fibers
could decrease to less than 0.05 dB cm–1 if the
fibers contained 10% water relative to the fiber volume. These results
confirmed that the intrinsic and extrinsic absorption losses were
much lower than the propagation loss in the WES PDLLA fibers.
Figure 7 UV–Vis–NIR
attenuation spectra of pure PDLLA, chlorobenzene,
16 wt % PDLLA solution in chlorobenzene, and water, which were placed
in a 1.0 cm path-length fused glass cell.
The intrinsic scattering loss originating from the intrinsic
density
inhomogeneity of the materials was the lower limit of scattering loss
inherent to each material that remained even after the extrinsic scattering
loss, namely the excess light scattering loss.33 Thus, the intrinsic scattering loss was not significantly
reduced by the heat treatment. By roughly estimating the intrinsic
loss from the measured attenuation spectrum of pure PDLLA [Figure 7], the intrinsic
scattering loss was estimated to be less than 0.8 dB cm–1. However, this value of the intrinsic scattering loss should be
an overestimation because both the light reflection loss and extrinsic
light scattering loss were included in the measured attenuation spectrum.
Moreover, the intrinsic scattering loss for other amorphous polymers,
namely PMMA and PS, has been estimated to be less than 1 × 10–3 dB cm–1 at wavelengths of around
533 nm.32,34
Extrinsic scattering due to dust in
the environment may occur during
the measurements for transmitting light intensity and propagation
loss; however, no large dust particles were observed in the bright-field
microscope image of the PDLLA fiber [Figure 2b]. The dark-field microscope image of the
fiber [Figure 2c] indicated
relatively bright scattering points because of small dust particles
or other factors not visible in the bright-field image, and the plots
of the guided light intensity showed some variation [Figure 5a]. However, the variation
was smoothed by fitting the plots with a single exponential function
before the propagation loss was determined. Therefore, the local scattering
loss due to dust should be negligible for the measured propagation
loss. Moreover, the heat treatment could not reduce the scattering
loss due to dust; thus, other factors caused the propagation loss
reduction after heating. Additionally, the extrinsic radiation loss
due to bends in the PDLLA fibers was negligible because the PDLLA
fibers were kept straight during the optical measurements [Figure 2b].
The extrinsic
scattering loss and radiation loss due to fluctuations
in the fiber diameter are possible factors influencing the propagation
loss in the WES PDLLA fibers, as previously indicated for WES PMMA
fibers.7 Higher fluctuations in the fiber
diameter cause higher propagation loss.29 To discuss the fluctuations before and after heating, the root-mean-square
roughness (RRMS) for each fiber was calculated
using the FESEM images of each 250 μm long PDLLA fiber; more
than 12 800 readings for each fiber were recorded using image
analysis. The RRMS was calculated using
the following formula 1 where D, Dave, and l are the measured diameter
of the fibers, the mean diameter of each fiber, and the position where
the diameter was measured, respectively. Figure 8 summarizes RRMS of each fiber before and after heating. No clear reduction of the RRMS was observed after heating even though all
five WES PDLLA fibers demonstrated reduced propagation loss [Figure 5b]. This result confirmed
that extrinsic scattering loss and radiation loss due to the fluctuations
in the fiber diameter must be excluded from the factors for propagation
loss reduction due to heat treatment.
Figure 8 RRMS of each
PDLLA fiber before and
after heating.
Extrinsic scattering
loss due to the extrinsic density inhomogeneity
resulting from microvoids, microscopic density variation, and birefringence
is the only possible remaining loss factor for the propagation loss
reduction because of post-fabrication heat treatment. Consequently,
extrinsic scattering loss must be the primarily reduced loss factor
to account for the observed propagation loss reduction. Extrinsic
density inhomogeneity causes excess light scattering, including Rayleigh,
Mie, or geometric scattering, so that excess light scattering results
in extrinsic scattering loss. Moreover, excess light scattering was
recently reported to be one of the main factors for propagation loss
in WES PMMA fibers,7 and the excess light
scattering in PMMA bulks was reported to be reduced by heating them
above Tg.25,26 These reports
support the present reduction of propagation loss in WES PDLLA fibers
because of heat treatment. Figure 9 shows the measured propagation loss in an WES PDLLA
fiber with different wavelengths before and after heating. The propagation
loss significantly decreased with the increasing wavelength, which
was also observed in the as-WES PMMA fibers.7 This result confirmed that the propagation loss in the PDLLA fiber
included extrinsic scattering loss. The propagation loss was significantly
reduced after heating, especially at shorter wavelengths, which indicated
that the enhanced excess light scattering at shorter wavelengths,
for example, enhanced Rayleigh scattering35 proportional to (wavelength)−4, was significantly
reduced after heating.
Figure 9 Propagation loss of the PDLLA fiber with different wavelengths
before and after heating.
To investigate birefringence in the WES PDLLA fibers, polarized
FT-IR spectra of aligned PDLLA fibers were measured, as shown in Figure 10a. The peak at
1755 cm–1 was assigned to C=O stretching,
and the peaks at 1186 and 1090 cm–1 were assigned
to C–O–C stretching.36,37 These stretchings
are parallel to the polymer backbone. The main chains of PDLLA in
the as-electrospun PDLLA fibers were modestly aligned along the fiber
axis because the absorbance was higher with parallel polarization
at around 1090, 1186, and 1755 cm–1 than that with
perpendicular polarization. The dichroic ratio was calculated to be
2.14 by integrating the polarized absorbance in the range from 1650
to 1850 cm–1. The alignment of the PDLLA chains
was relaxed after heating because the dichroic ratio after heating
decreased to 1.35, as shown in Figure 10b. This alignment relaxation should reduce
the birefringence in the PDLLA fibers and partially decrease the extrinsic
scattering loss. The effects of microvoids and microscopic density
variation are still unclear, but wet-electrospinning produces fibers
with rapidly evaporating solvents so that microvoids and microscopic
density variation are generated. Several papers reported inhomogeneous
inner structures of polymers in WES fibers,5,38 and
the WES PDLLA fibers in the present study showed higher propagation
loss at shorter wavelength, reflecting the extrinsic density inhomogeneity.
A previous work reported that PMMA bulks without heat treatment above Tg included inhomogeneous structures with a dimension
of about 100 nm, which caused excess light scattering and increased
scattering loss.25,26 Additionally, the inhomogeneous
structures disappeared after heat treatment above Tg, and the scattering loss was reduced. On the basis of
these results, inhomogeneous structures in the WES PDLLA fibers, microvoids,
and microscopic density variation, should be reduced after heat treatment
above Tg.
Figure 10 Polarized FT-IR spectra
of the aligned PDLLA fibers (a) before
and (b) after heating. Here, parallel and perpendicular represent
the polarized directions of the oscillating electric field of the
incident IR beam to the fiber direction.
We demonstrated that heating amorphous WES fibers above Tg is a versatile approach for reducing their
propagation loss. This technique should be applicable to a variety
of WES fibers composed of amorphous polymers. Moreover, optimizing
the heating conditions should reduce the propagation loss below the
loss observed in this study (lower than 5 dB cm–1 at 533 nm wavelength).
Conclusions
We demonstrated a comprehensive
and versatile approach for reducing
propagation loss in WES polymer fibers by heating the fibers above
the glass transition temperature of PDLLA. This heat treatment significantly
reduced the propagation loss in amorphous WES PDLLA fibers from 17.0
to 8.1 dB cm–1 at a wavelength of 533 nm. The propagation
loss reduction could be attributed to the reduction of extrinsic excess
scattering losses due to the extrinsic density inhomogeneity in the
fibers. These findings pave the way for low-loss WES fiber waveguides
and their application in small, flexible optical fiber devices such
as waveguides, sensors, and lasers.
Author Contributions
The manuscript
was written through contributions of all authors. All authors have
given approval to the final version of the manuscript.
The authors
declare no competing financial interest.
Acknowledgments
This work was partially supported by the Leading
Initiative for Excellent Young Researchers (LEADER) of the Ministry
of Education, Culture, Sports, Science and Technology of Japan, the
Toyota Physical & Chemical Research Institute, and the Tatematsu
Foundation.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145904810.1021/acsomega.8b00877ArticleLarge-Scale Fabrication of High-Performance Ionic Polymer–Metal
Composite Flexible Sensors by in Situ Plasma Etching and Magnetron
Sputtering Fu Ruoping †‡Yang Ying ‡Lu Chao ‡Ming Yue ‡Zhao Xinxin ‡Hu Yimin ‡Zhao Lei ‡Hao Jian †Chen Wei *‡§† Department of Chemistry,
College of Sciences, Shanghai University, Shanghai 200444, P. R. China‡ i-Lab, Suzhou Institute of Nano-Tech and
Nano-Bionics, Chinese Academy of Sciences, Suzhou 215123, P. R. China§ Nanotechnology Centre for Intelligent Textiles
and Apparel, Institute of Textiles and Clothing, The Hong Kong Polytechnic University, Kowloon, Hong Kong 999077, P. R. China* E-mail: wchen2006@sinano.ac.cn (W.C.).15 08 2018 31 08 2018 3 8 9146 9154 02 05 2018 01 08 2018 Copyright © 2018 American Chemical
Society2018American Chemical
SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
Flexible electronics has received
widespread concern and research. As a most-fundamental step and component,
polymer metallization to introduce conductive electrode is crucial
in successful establishment and application of flexible and stretchable
electronic system. Ionic polymer–metal composite (IPMC) is
such an attractive flexible mechanical sensor with significant advantages
of passive and space-discriminative capability. Generally, the IPMC
sensor is fabricated by the electroless plating method to form structure
of ionic polymer membrane sandwiched with two metallic electrodes.
In order to obtain high-quality interface adhesion and conductivity
between polymer and metal, the plating process for IPMC sensor is
usually time-consuming and uncontrollable and has low reproducibility,
which make it difficult to use in practice and in large-scale. Here,
a manufacturable method and equipment with short processing time and
high reproducibility for fabricating IPMC sensors by in situ plasma
etching and magnetron sputtering depositing on flexible substrates
is developed. First, the new method shortens the fabrication period
greatly from 2 weeks to 2 h to obtain IPMC sensors with sizes up to
9 cm × 9 cm or arrays in various patterns. Second, the integrated
operation ensures all sample batch stability and performance repeatability.
In a typical IPMC sensor, nearly 200 mV potential signal due to ion
redistribution induced by bending strain under 1.6% can be produced
without any external power supply, which is much higher than the traditional
electroless plating sensor. This work verified that the in situ plasma
etching and magnetron sputtering deposition could significantly increase
the interface and surface conductivity of the flexible devices, resulting
in the present high sensitivity as well as linear correlation with
strain of the IPMC sensor. Therefore, this introduced method is scalable
and believed to be used to metalize flexible substrates with different
metals, providing a new route to large-scale fabrication of flexible
devices for potential wearable applications in real-time monitoring
human motion and human–machine interaction.
document-id-old-9ao8b00877document-id-new-14ao-2018-00877uccc-price
==== Body
Introduction
In order to overcome
application problems of the electronic system in the large deformation
and arbitrarily curved surfaces, flexible electronics that is compatible
with movable parts has been driven to the advent and growth over the
last few decades. Flexible electronics create a wide range of revolutionary
functional devices, including sensors, actuators, robots, and other
electronic devices that are bendable, curved, and even stretchable.1−9 As the most basic component of electronics, the thin-film conductive
electrode of polymer metallization fabrication has become a key part
of the successful application of flexible and stretchable electronic
systems. Recently, ionic polymer–metal composites (IPMCs) have
extensively been studied for their excellent properties and potential
applications in the areas of science and technology as flexible sensors.10−16 An IPMC sample typically consists of a thin ion-exchange membrane
(e.g., Nafion) and metallic electrodes on both surfaces with a noble
metal.17 Also, IPMC can induce voltages
by bending or stretching the membrane, which makes IPMC an ideal flexible
sensor. Compared with electronic sensors,18−20 these IPMC
sensors show significant advantages of no power supply and the ability
to distinguish bending directions.
IPMC sensors are generally
fabricated by electroless plating21 to
achieve polymer metallization on the flexible Nafion membrane. Polymer
metallization use conventional conductive materials, such as rigid
metal nanoparticles (mainly including Cu, Ag, or Au) on polymer film
to realize flexibility and stretchability. However, these conductive
materials may not be suitable for flexible electronics. The flexible
polymeric material (from fractions to hundreds of MPa) and the hard
electrode material (from tenths to hundreds of GPa)22 have the large Young’s modulus mismatch, which causes
electrode cracking, stripping, and delamination during multicycle
bending and further limits the lifetime and the bending stability
of the IPMC sensors.23 Thus, in view of
applications, fabrication of compliant and well-adherent electrodes
that are closely integrated with the polymer layer is crucial.24 Besides, fabrication of IPMC sensors still remains
a big challenge mainly because the traditional electroless plating
method is manual operation. This process not only consumes a long
period, but it also has many uncontrollable factors. Most importantly,
reliability of manual operation is not strong, resulting in low reproducibility.
What’s more, they have difficulty for batch production. Therefore,
in order to develop production techniques of industrial interest,
a non-manual preparation method with high efficiency should be developed.
Here, in order to solve the aforementioned problems, we develop
a manufacturable and integrative method and equipment with short processing
time and high reproducibility for fabricating IPMC sensors by in situ
plasma etching and magnetron sputtering depositing on flexible substrates.
Some literature studies have only used plasma to etch Nafion membrane.
Omosebi and Besser25 used plasma to etch
the Nafion membrane for multiple electrochemical applications. Van
Nguyen26 etched with argon on the surface
Nafion membrane and investigated its performance in a proton-exchange
membrane fuel cell. Also, some literature studies have only reported
to prepare IPMC using magnetron sputtering. Zhou27 sputter-coated a gold seed layer of 0.4 μm thickness.
Siripong28 employed sputter coating for
deposition of gold on Nafion for fast and economical fabrication of
IPMC. Thus, we place two devices into a single chamber to rapidly
and large-scale prepare IPMC. Plasma etching is a potentially attractive
method to control polymer surface modification without affecting the
bulk properties of the material.29 Plasma
treatment depends heavily on the adjustment of parameters such as
power and treatment duration.30 We can
quantify and repeat the degree of etching with defined parameters.
Magnetron sputtering has developed rapidly over the last decades to
the point where it has become established as the process of choice
for the deposition of a wide range of industrially important coatings
on plastic substrates at room temperature.31 For equipment, plasma etching filament and magnetron sputtering
target are installed in one chamber and the control panel was operated
to achieve the integrative fabrication. Plasma etching increases the
roughness of the intermediate layer surface to improve the adhesion
of the electrode layer. Magnetron sputtering deposits silver particles
to metallize Nafion membrane. Silver is considered as a high conductive
material and is much cheaper than gold, platinum, or other precious
metals.
The integrative preparation method provides the possibility
of batch and reproducible production of flexible IPMC sensors. First,
the new method shortens the fabrication period greatly from 2 weeks
to 2 h to obtain IPMC sensors with sizes up to 9 cm × 9 cm or
arrays in various patterns. Second, the integrated operation ensures
all sample batch stability and performance repeatability. In a typical
IPMC sensor, nearly 200 mV potential signal under a bending-induced
strain as small as 1.6% can be produced without any external power
supply, which is 63 times higher than that of the sensor fabricated
by traditional electroless plating. We verified that the in situ plasma
etching and magnetron sputtering depositing could significantly increase
the interface and surface conductivity of the flexible devices. Plasma
etching processing improves the degree and uniformity of etching on
the Nafion film surface, resulting in a much lower equivalent series
resistance. The magnetron sputtering-based sensor shows a good interface
contact between the electrolyte and electrode as well as excellent
electronic conductivity of the electrode material. Moreover, this
flexible IPMC sensor has better bending cycle stability and high sensitivity
as well as linear correlation with strain. Then, we mainly optimize
the parameters of etching power, etching time and magnetron sputtering,
sputtering time, sputtering power, working pressure, and working argon
flow rate to get an IPMC sensor with excellent performance. In a word,
this introduced method is scalable and believed to be used to metalize
flexible substrates with different metals, providing a new route to
large-scale fabrication of flexible devices for potential wearable
applications in real-time monitoring human motion and human–machine
interaction.
Results and Discussion
Preparation and Characterization
The equipment used to fabricate the flexible IPMC sensor is shown
in Figure 1a. The sample
holder (①), the filament (③) for plasma etching, and
the magnetron sputtering target (④) are installed in the chamber
of the equipment. The equipment is also equipped with a mechanical
handle (②) for inverting the sample on the sample holder, which
ensures that both sides of the sample are plasma-etched and magnetron
sputtering-coated with silver particles to achieve integrative fabrication.
In the fabrication process, we only need to operate and set the plasma
etching and magnetron sputtering parameters on the control panel instead
of manual operation, which is a simple and controllable process. A
schematic representation of the fabrication process of the flexible
IPMC sensor is presented in Figure 1b. Before plasma etching, the Nafion substrate (suitable
for different sizes and array pattern) is fixed on the hollow part
of rotatable sample holder allowing the rotation of the substrate
along a direction, which assures sample uniformity of etching and
metalizing over the entire surface. The picture of simple holder is
shown in Figure S1. Then, plasma etching
with defined energy is used to control Nafion membrane surface modification.
After completing, the holder is turned over 180° by the mechanical
handle, and the opposite side of the Nafion polymer is processed.
Finally, magnetron sputtering deposited silver particles on the metallic
Nafion polymer. Once the electrode with appropriate conductivity has
been deposited, the holder is turned over 180° by the mechanical
handle, and the opposite side of the Nafion polymer is deposited with
silver particles. The details can be found in the Experimental Methods section.
Figure 1 Schematic of the fabrication process.
(a) Equipment used to manufacture the IPMC sensor. (b) Schematic of
the fabrication process of the IPMC sensor.
The pictures of fabricated IPMC sensors are shown in Figure 2. The IPMC sensor
is flexible and can be easily bent. What’s more, the specular
IPMC sensor surface is shiny and bright; in other words, the fabricated
silver electrode layer has very high quality. We can obtain IPMC sensors
with size up to 9 cm × 9 cm (Figure 2a) or arrays in various patterns (Figure 2b–d). Moreover,
mechanical operation ensures high performance of each batch samples.
Figure 2 Pictures
of the fabricated IPMC sensors. (a) Pictures of large-scale IPMC sensors.
(b–d) Pictures of various array patterns of IPMC sensors.
Then, the observation of microscopic
morphology of the IPMC sensor is done by using an electron microscope. Figure 3a displays the scanning
electron microscopy (SEM) image of the IPMC sensor surface, which
clearly shows the homogeneous silver layer coated on the surface of
the polymer membrane layer and the silver nanoparticles are closely
integrative, having a diameter between 50 and 160 nm. Figure 3b displays a detail of the
cross-sectional SEM image of the IPMC sensor, which clearly indicates
that the silver nanoparticle layer and the Nafion membrane interlayer
are well-interconnected. The structure benefits the cyclic stability
of the sensor. In the inset of Figure 3c, the Nafion membrane interlayer with an average thickness
of 183 μm is sandwiched between two silver electrodes, forming
the IPMC sensor. In order to verify the distribution of the Ag electrode
layer in the IPMC sensor, Figure 3c shows the energy-dispersive X-ray spectroscopy (EDX)
signal, which is collected from the vertical cross section of the
IPMC in the inset SEM image. Ag is mainly concentrated on both sides
of IPMC. Moreover, typical X-ray diffraction (XRD) powder diffraction
pattern of the surface layer of the IPMC sensor is shown in Figure 3d. The peaks at 38.1°,
44.21°, 64.44°, and 77.33° correspond to the (111),
(200), (220), and (311) crystalline planes of the face-centered cubic
crystal structure of Ag (JCPDS, file no. 04-0783), which demonstrates
the existence of Ag electrode layer.
Figure 3 Characterization of the morphology of
the IPMC sensor. (a) SEM image of the IPMC sensor surface. (b) Cross-sectional
SEM image of the IPMC sensor. (c) EDX line scan of the cross section
of the IPMC sensor. The inset shows the corresponding SEM image. (d)
Typical XRD pattern of the surface layer of the IPMC sensor.
Sensing Performance of
the IPMC Sensor
An IPMC sample typically consists of a thin
ion-exchange membrane and a noble metal as electrodes on both surfaces. Figure 4a displays the sensing
mechanism of the IPMC sensor. As we know, the Nafion membrane contains
the sulfonic acid group and can be ionized and release the mobile
hydrions with adsorbed water. When the sensor is in a flat state,
mobile hydrions uniformly disperse in the Nafion membrane. When a
bend deformation is applied on the sensor, an elastic stress gradient
is generated along the thickness. The mobile hydrions on the compressed
side of the membrane migrate and accumulate on the lower hydraulic
pressure side of the membrane. More hydrions accumulate on the stretched
side, resulting in a positive potential. The voltage signal is generated
from ion movement and accumulation in the deformation process, so
the sensor could generate electrical signal without external energy
supply.
Figure 4 Sensing mechanism and sensing performance of IPMC sensors. (a) Schematic
of the sensing mechanism. (b) Potential of the in situ plasma etching
and magnetron sputtering depositing silver particle-based IPMC sensor
and the electroless plating-based IPMC sensor. (c) Voltage responses
of the IPMC sensor to the recognization of the bending direction.
(d) Potential of the sensor with variations of the bending deformation
of 1, 2, 3, 4, 5, 6, and 7 mm. (e) Potential signal of the sensor
vs strain (ε). (f) Bending and recovery of the IPMC sensor for
3000 cycles of 3 mm displacement.
For the sensing mechanism of the sensor, we buit a corresponding test platform and obtained
signals of sensors under different strains. The test method can be
found in the Experimental Methods section.
The output electrical signals of magnetron sputtering depositing silver
particle-based sensor and conventional electroless plating-based sensor
are shown in Figure 4b. Output voltage shows a periodic alternation of positive
voltage, and output voltage of the magnetron sputtering sensor is
112.55 mV. However, when the IPMC sensor returns back after bending,
hysteresis is produced because the movement of the ions is not as
fast as electron transport. Thus, the signal peak is asymmetric. Output
potential of the electroless plating sensor is 1.80 mV. The signal
of magnetron sputtering is much larger than that of the electroless
plating sensor. The ability of the IPMC sensor to recognize the orientation
is shown in Figure 4c. The insets in Figure 4c display the real operation scenes of upward-bending and
downward-bending in the test process. For the first six times, the
sensor bends downward to get the negative voltage, and for the latter
six times, the sensor bends up and gets a positive voltage. As the
sensor bends to opposite directions, positive and negative relative
potentials appear in turn, respectively. A series of bending deformations
of 1, 2, 3, 4, 5, 6, and 7 mm are repeatedly measured (Figure 4d). Different displacements
produce different signals, indicating high repeatability and sensibility
of IPMC sensors.
We use the Euler–Bernoulli theory to
build a model to calculate the strain at the corresponding displacement.
The film sensor has a thickness of h and a length
of L. When the displacement platform moves x, the film is curved. A schematic diagram is shown in Figure S2. Assuming that the central angle of
the curved arc is θ, the radius is R. According
to the geometric relations, we can list the equations 1 2
We know L and x and can
get θ and R from eqs 1 and 2. Finally, the
Euler–Bernoulli approximation theory is used to calculate the
bending strain, and the strain corresponding to the displacement is
obtained. 3
Using this method, the strain of our IPMC is 1.03% at a displacement
of 3 mm.
Potential signal as a function of a series of strain
is given in Figure 4e, which exhibits an approximately linear correlation. Small error
bars (standard deviations) are taken from 10 times measurement. Therefore,
the IPMC sensor has perfect repeatability. The sensor potential under
the maintained extended state is also detected (Figure S3). When the sensor keeps bending, the signal continues
to increase and then begins to fall slowly. The output signal declines
around 5% slowly when the sensor maintained 10 s bending state (Figure S3a). The output signal declines around
27.5% while maintaining 60 s bending state (Figure S3b). In order to analyze the durable performance of the IPMC
sensor, cyclical bending deformation and recovery of the sensor was
measured for 3000 cycles of 3 mm displacement and is shown in Figure 4f. The insets in Figure 4f show the details
of the cyclic test. The output potential signals of the sensor are
stably maintained with a relative small variation. Although the signal
has slight attenuation, the signal is still much larger than the signal
of the electroless plating-based sensor, and the peak type is consistent.
It is proved that the sensors have a relatively good cycle stability.
Therefore, the sensor fulfills the requirement for practical application.
This is the result of our preliminary experimental stage. In the future,
we will continue to explore and improve its durable performance. The
electromechanical behavior of IPMC under electrical voltage stimulation
of ±1 V is also investigated (Figure S4). The bending displacement is monitored by a laser displacement
meter. Bending displacement reaches 11.0 μm. The size of the
mobile ions in the IPMC is small. If we increase the number of mobile
ions and soak large-size ions in the Nafion membrane, the electromechanical
behavior of IPMC will be improved.
The traditional method for
preparing an IPMC sensor is manual processing for roughing Nafion
film and electroless plating for electrode layers. The signal of our
sensor (112.55 mV, Figure 4b) is about 63 times compared with that of electroless plating-based
sensor (1.80 mV, Figure 4b). We read the relevant literature studies and found that the signal
of the sensor made by electroless plating is relatively low. The IPMC
sensor prepared by Song32 can generate
a voltage signal of 20 mV. This is the largest signal of IPMC we have
seen from the literature so far. However, the signal of our IPMC sensor
is much larger than this value. The electrode layer thickness of the
electroless plating-based IPMC sensor is about 3–5 μm.
The electrode layer thickness of the magnetron sputtering-based IPMC
sensor is 280–300 nm. For the electroless plating-based IPMC
sensor, the impregnation–reduction steps were repeated five
times. The reduction step is a process of electrode layer growth,
and the reduction takes a total of 25 h. The growth rate is 0.12–0.2
μm/h. For the magnetron sputtering-based IPMC sensor, magnetron
sputtering lasts for 30 min and the electrode layer thickness increases
to 280–300 nm. The growth rate is 0.56–0.6 μm/h.
In order to evaluate the effect of the in situ etching and magnetron
sputtering depositing method to increase potential signal, first,
the average root mean square (rms) surface roughness (Rq) value of the treated Nafion membrane is measured and
analyzed. Figure 5a,b
shows 3D atomic force microscopy (AFM) images of Nafion membrane of
plasma etching processing and manual processing, respectively. The
average Rq value of Nafion membrane of
plasma etching processing is about 72.9 nm. The measured Rq value for manual processing Nafion membrane is about
65.6 nm and is relatively lower. It is clear from the AFM image that
surface grooves of the plasma etching-treated membrane are evenly
distributed and have comparatively consistent depth compared with
those of the manual processing membrane, which greatly benefits for
the proper microstructural development. The observed more uniform
rough surface is a desirable two-dimensional layer by layer growth
mode (Frank–van der Merwe mode).33Figure 5c shows Nyquist
plots of the IPMC sensors. The equivalent series resistance of the
magnetron sputtering-based IPMC sensor is 2 Ω, which is much
lower than that of electroless plating-based sensor (equivalent series
resistance of is 145 Ω). The magnetron sputtering-based IPMC
sensor shows a good interface contact between the electrolyte and
electrode as well as excellent electronic conductivity of the electrode
material. The surface sheet resistance of the electrode film is as
high as 0.08–0.15 Ω/□, further confirming excellent
electronic conductivity. In summary, it is proved that the in situ
plasma etching and magnetron sputtering depositing method is effective
for fabricating high-performance IPMC sensors.
Figure 5 (a) 3D AFM image of the
plasma etching-based Nafion membrane. (b) 3D AFM image of the manual
processing-based Nafion membrane. (c) Nyquist plots of three electrodes
of the IPMC sensor with electroless plating and the IPMC sensor with
magnetron sputtering. The inset picture clearly displays Nyquist plots
of three electrodes of the IPMC sensor with magnetron sputtering.
However, the plasma etching power
and duration have a great influence on the degree and uniformity of
the film surface etching. In addition, magnetron sputtering time,
sputtering power, working pressure, and working argon flow rate also
have great impact on the performance of the sensor. Consequently,
the conditions of the preparation process are optimized to obtain
excellent IPMC sensors. Cho et al.34 studied
that the etching procedure did not alter the chemical character of
the membrane. Only the physical roughness does not affect performance.
The surface morphologies of the modified Nafion membranes are investigated
by using SEM, as shown in Figure 6a–i. The surface roughness enhances with increase
of power (Figure 6a–f)
or time (Figure 6g–i)
because of the effect of the plasma etching treatment. Output potential
signals of IPMC sensors of different plasma etching powers or time
can be used as a parameter to determine the best conditions, which
is shown in Figure 7a,b. When the etching power is 8 or 10 W, the prepared sensor cannot
obtain a stable output signal. The output signal increases to the
maximum and then significantly goes down as the etching power increases.
When the etching time is 360 s, the sensor has maximum output signal.
The Nafion membrane surface can be etched efficiently, which affects
the output signal of IMPC.
Figure 6 SEM images of different plasma etching powers
and constant 180 s etching duration on the Nafion membrane surface:
(a) 8 W; (b) 10 W; (c) 12 W; (d) 14 W; (e) 16 W; and (f) 18 W. SEM
images of different plasma etching durations and constant 14 W etching
power on the Nafion membrane surface: (g) 180 s; (h) 360 s; and (i)
540 s.
Figure 7 (a) Output potential signals of IPMC sensors
of different plasma etching powers and constant 180 s etching duration
on the Nafion membrane surface. (b) Output potential signals of IPMC
sensors of different plasma etching durations and constant 14 W etching
power on the Nafion membrane surface.
In the same method, the effects of sputtering time, sputtering
power, working pressure, and working argon flow rate on the film performance
are tested with indicators such as electrode layer thickness and output
potential signal while keeping other parameters constant.
Figure 8a shows output potential
signals and electrode layer thicknesses of sensors under different
sputtering power. In a certain range, the greater the sputtering power,
the deposited particles have higher energy and the metal element deposition
on the substrates is accelerated. Therefore, the particles have higher
adhesion with the substrate. The film thickness increases with the
increase of sputtering power. Output potential signal reaches the
maximum value at 100 W power; the value of the output potential is
an important parameter of device performance. Therefore, the sputtering
power at 100 W is considered as a better value to ensure outstanding
sensor performance.
Figure 8 Curve of output potential signals and electrode layer
thicknesses of sensors under different magnetron sputtering conditions:
(a) 90–130 W different sputtering power and constant sputtering
30 min duration, 1.0 Pa working pressure, 30 sccm argon flow rate;
(b) 5–60 min different sputtering time and constant sputtering
120 W power, 1.0 Pa working pressure, 30 sccm argon flow rate; (c)
0.25–3.5 Pa different sputtering working pressure and constant
sputtering 120 W power, 30 min duration, 30 sccm argon flow rate;
and (d) 20–40 sccm different sputtering argon flow rate and
constant sputtering 120 W power, 30 min duration, 30 sccm argon flow
rate.
Figure 8b depicts output potential signals and electrode
layer thicknesses of sensors under different sputtering times. It
is observed that the electrode layer thickness increases with increase
of sputtering time. To be more specific, with the increase of sputtering
time, the content of silver increases. The number of particles deposits
onto the Nafion substrate increases. ZAO films were prepared by magnetron
sputtering conducted by Song,35 who has
already shown that for a longer sputtering time, the thickness of
the film increases as well, and interestingly shows a linear correspondence
to sputtering time. Output potential signal reaches the maximum value
at 30 min. With a shorter deposition time, there are less particles
on the substrate. As the deposition time increases, the number of
particles increases, and the layer thickens. The electrode layer has
good compactness. However, with a longer deposition time, the electrode
layer thickness increases, which is not conducive to sensors bending
deformation. The electrode is easy to peel and split as the thickness
increases. Thus, the sputtering time at 30 min is considered as a
better value to ensure sensor performance excellent.
It can
be seen from Figure 8c that with the increase of working pressure, the electrode layer
thickness decreases. With a lower deposition pressure, there are less
collisions in the path of particles to the substrate. Particles can
easily reach the substrate to form a film and the film has good performance.
However, when the deposition pressure increases, there are more collisions
in the path of particles to the substrate, thus the particles energy
decreases. The amount of particles reaching the substrate decreases,
which causes more defects in the films and leads to the decrease of
electrode layer thickness. Output potential signal of sensor increases
from 2.2 mV (0.25 Pa) to a maximum value at 29.4 mV (1.0 Pa) and then
goes down to 9.5 mV at 3.4 Pa. Considering appropriate electrode layer
thickness and electrical signals, the sensor performance is more excellent
when the deposition pressure at 1.3 Pa.
Figure 8d shows the variety of electrode layer thicknesses
and output potential signals of sensors as a function of different
the argon flow rate. Apparently, the electrode layer thickness decreases
with the increase of argon flow rate. When the magnetron sputtering
starts, the electrons collide with the argon atoms in the process
of flying to the substrate under the action of the electric field
and produce argon ions and new electrons. Argon ions in the electric
field accelerate toward the cathode target and high-energy bombard
the target surface, and the target sputtering occurred. Neutral target
atoms or molecules are deposited on the substrate to form a thin film.
The higher argon flow rate increases the working pressure, and there
is lower mobility and a great number of native defects. The output
potential signal of the sensor rises to a peak value at an argon flow
rate of 30 sccm and then decreases as the argon flow rate further
increases.
From inspection, the maximum voltage signal is found
to be 29.55 mV for the sample grown using an argon flow rate of 30
sccm. Considering the stability of the sensors and the output of the
electrical signal, the optimal argon flow rate is 28 sccm.
Conclusions
In this work, an Ag electrode-based IPMC sensor is fabricated on
a flexible Nafion substrate by the in situ plasma etching and dc balanced
magnetron sputtering deposition technique. The new method shortens
the fabrication period greatly from 2 weeks to 2 h to obtain IPMC
sensors with sizes up to 9 cm × 9 cm or arrays in various patterns.
The integrated operation ensures all sample batch stability and performance
repeatability. These IPMC sensors can generate electrical signals
under the external bending deformation for mobile hydrions migrate
and accumulate on the lower hydraulic pressure side. IPMC sensors
we fabricated can generate nearly 200 mV potential signal without
external power supply under a 1.6% bending-induced strain and recognize
different directions of the bending strain. The signal of our sensor
is much larger than that of the traditional electroless plating-based
sensor. What’s more, this IPMC sensor is suitable for in long-term
and large-scale bending and have high sensitivity as well as linear
correlation with strain.
The plasma etching-based Nafion membrane
has higher rms surface roughness (Rq)
values. Surface grooves of membrane are evenly distributed and have
comparatively consistent depth. The equivalent series resistance of
the magnetron sputtering-based IPMC sensor is 2 Ω, which is
much lower than that of the electroless plating-based sensor (equivalent
series resistance of is 145 Ω). The magnetron sputtering-based
sensor shows a good interface contact between the electrolyte and
electrode as well as excellent electronic conductivity of the electrode
material. Optimal properties of the IPMC sensor are obtained with
plasma etching power at 14 W, plasma etching duration at 360 s, magnetron
sputtering power at 100 W, magnetron sputtering time at 30 min, magnetron
sputtering working pressure at 1.3 Pa, and a magnetron sputtering
working argon flow rate at 28 sccm. From these data, the IPMC sensor
fabricated by in situ plasma etching and magnetron sputtering has
high performance of large and stable output signal. The study provides
a manufacturable and integrative method and equipment with short processing
time and high reproducibility for large-scale preparing flexible sensors
of mechanical bending durability on flexible substrates. This preparation
method is scalable and silver electrodes can be replaced with other
metallic materials such as gold, copper, chromium, indium tin oxide
(ITO), aluminum oxide, and so forth. We believe that this method provides
a new route to short-time and quantifiably fabricate IPMC sensors
for potential wearable applications in real-time monitoring human
motion and human–machine interaction.
Experimental Methods
Materials
and Instruments
Hydrogen peroxide, sulfuric acid, HAuCl4, 1,10-phenanthroline monohydrate (Phen), and sodium sulfite
were purchased from Sinopharm Chemical Regent Co. Ltd. The Nafion
117 membrane was purchased from the Dupont. Equipment with the commercial
dc balanced magnetron sputtering system and the inductive coupled
plasma-reactive ion etcher was customized.
Preparation of the IPMC
Sensor by in Situ Plasma Etching and Magnetron Sputtering Depositing
Before etching, the Nafion membrane was cleaned by hydrogen peroxide
(5% mass fraction) and diluted sulfuric acid (1 mol L–1). Then, the Nafion membrane (suitable for different size) was fixed
on the hollow part of the rotatable sample holder in the chamber allowing
the rotation at a speed of 5 rpm of the substrate along a direction,
which assures sample uniformity of etching and metallizing over the
entire surface. The chamber pressure was pumped down to below 3 ×
10–4 pa in order to prevent residual atmosphere
effects on the composition of the Nafion films. Then, the argon valve
was opened and the argon flow rate was set as 8 sccm. All of the specimens
were grown by using pure argon (99.99%) as etching and sputtering
gas. We controlled the screen voltage, the screen current, and etching
duration during plasma etching to get a sample with uniform etching
and excellent performance. After completing treatment of one side
of the Nafion membrane, the holder was turned over 180° by the
mechanical handle, and the opposite side of the membrane was etched.
Then, magnetron sputtering deposited silver particles on the metallic
polymer. The sputtering process was performed at room temperature.
The chamber pressure was adjusted to appropriate value. The argon
flow rate was set to what we want. Then, the deposition power and
duration parameters were set. Once the deposition was completed, the
holder was turned over 180° by the mechanical handle, and the
opposite side of the polymer was processed. No post annealing was
performed after deposition. The substrate temperature was maintained
at 20 °C approximately during the deposition process. The Nafion
membrane is cleaned with ionized water, vacuumed in the chamber, etched,
and sputtered to plate the electrodes. The Nafion membrane retains
its intrinsic water, which assures the migration of ions in the membrane,
thereby generating the sensing signal. The IPMC sensor was cut into
a size of 25 mm × 5 mm for the experimental test.
Preparation
of the Electroless Plating-Based Sensor
The Nafion membrane
was roughed by 1200 sandpaper polishing 800 times both sides. Then,
the Nafion membrane was cleaned. Next step, the Nafion membrane was
placed into a solution of [Au(Phen)Cl2]Cl for 24 h to allow
the sufficient impregnation of cations. After that, the Nafion membrane
was immersed into deionized water in water-bath heating. A Na2SO3 solution of 5 mmol L–1 was
slowly dropped into the water till the Au cations at the membrane’s
surface are reduced to Au particles totally. The impregnation–reduction
steps were repeated five times.
Sensing Measurement
The IPMC sensors need to be deformed to produce a voltage signal.
We built a corresponding test platform, including signal generation
section and signal collection section. The signal generation section
includes fixtures, displacement platform (MTS121), and displacement
stepper motor. The signal collection section includes an electrochemical
workstation and a controller computer. The displacement platform can
realize precise displacement control in the X-axis
direction, with an accuracy of 0.005 mm. Moreover, the displacement
platform can realize and control different movement rates, the number
of cycle displacements, and the distance of displacement, including
any distance of 0–7 mm. The electrochemical workstation can
collect and display on the computer the electrical signals generated
by the deformation of the sensor. Therefore, we can use this measurement
platform to realize the basic bending performance test of our sensor.
The IPMC sensor in response to the cyclic bending and resuming flat
state is tested. The sensor is placed on the displacement platform
and is clamped by fixtures. The sensors we test have an effective
length of 1.8 cm. Also, the maximum displacement of the platform is
set as 3 mm. The displacement platform gradually moves from 0 to 3
mm, the signal generated by the sensor gradually increases from 0,
and then the displacement platform gradually returns from 3 to 0 mm.
The signal generated by the sensor gradually decreases from the maximum
value.
Characterization
Surface morphology and cross-sectional
SEM images were obtained with a Hitachi S-4800 filed emission scanning
electron microscope. The 3D AFM images and the average rms surface
roughness (Rq) values were obtained with
a Dimension 3100 atomic force microscope. EDX was performed on Quanta
400FEG (FEI). XRD patterns were obtained on a X’Pert-Pro MPD
(Cu Kα). The surface sheet resistance of the electrode film
was tested by using a multifunctional digital four-probe tester (ST-2258C).
Supporting Information Available
The Supporting Information is available free of
charge on the ACS Publications
website at DOI: 10.1021/acsomega.8b00877.Picture of a simple
holder; schematic diagram of analytical model of the sensor; potential
change of IPMC under overtime state maintaining; and electromechanical
behavior of IPMC under electrical voltage stimulation of ±3 V
(PDF)
Supplementary Material
ao8b00877_si_001.pdf
The authors
declare no competing financial interest.
Acknowledgments
This work was supported
by the External Cooperation Program of BIC from Chinese Academy of
Sciences (grant no. 121E32KYSB20130009) and the Science and Technology
of Jiangsu Province (grant no. BE2016086).
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145799710.1021/acsomega.8b00813ArticleSolution-Processed BiI3 Films with 1.1
eV Quasi-Fermi Level Splitting: The Role of Water, Temperature, and
Solvent during Processing Williamson B. Wesley Eickemeyer Felix T. Hillhouse Hugh W. *Department of Chemical Engineering,
Clean Energy Institute, and Molecular Engineering & Sciences Institute, University of Washington, Seattle, Washington 98105, United States* E-mail: h2@uw.edu (H.W.H.).05 10 2018 31 10 2018 3 10 12713 12721 25 04 2018 08 05 2018 Copyright © 2018 American Chemical
Society2018American Chemical
SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
We present a mechanistic explanation
of the BiI3 film
formation process and an analysis of the critical factors in preparing
high-quality solution-processed BiI3 films. We find that
complexation with Lewis bases, relative humidity, and temperature
are important factors during solvent vapor annealing (SVA) of films.
During SVA, water vapor and higher temperatures limit the formation
of the BiI3–dimethylformamide coordination complex.
SVA with an optimized water content and temperature produces films
with 300–500 nm grains. Films that formed solvent coordination
compounds at lower temperatures showed preferential crystal orientation
after solvent removal, and we elucidate its implications for carrier
transport. Addition of dimethyl sulfoxide to highly concentrated tetrahydrofuran–BiI3 inks prevents film cracking after spin-coating. We have measured
a quasi-Fermi level splitting of 1.1 eV and a diffusion length of
70 nm from films processed with optimal temperature and humidity.
The best device produced by optimized SVA has a power conversion efficiency
of 0.5%, Isc of ∼4 mA/cm2, and VOC of ∼400 mV. The low
photocurrent and voltage we attribute to the low diffusion length
and the unfavorable band alignment between the absorber and the adjacent
transport layers. The deep understanding of the relationship between
morphology/crystal structure and optoelectronic properties gained
from this work paves the way for future optimization of BiI3-based solar cells.
document-id-old-9ao8b00813document-id-new-14ao-2018-00813rccc-price
==== Body
Introduction
Photovoltaic (PV) materials
such as copper zinc tin sulfoselenide
(CZTS),1−3 copper indium gallium sulfoselenide (CIGS),4−6 and, more recently, hybrid perovskites (HPs)7−9 are all solution-processable.
Solution-processed materials are exciting because they can be spray-coated,
blade-coated, or slot die-coated onto large substrates, often at low
temperatures,10 and thus may reduce the
upfront capital expenditure (CAPEX) to begin manufacturing.11 The CAPEX of roll-to-roll processing may be
as low as 0.06$/WaCap versus 0.68 to 1.01$/WaCap for CdTe and polysilicon processes ($/WaCap is $ per
annual production capacity in watts). However, materials such as CZTS
are not yet commercializable as device efficiencies are still less
than 15%, mainly because of low minority carrier diffusion lengths12 and low open-circuit voltages. However, CIGS
cells are commercial and have demonstrated module efficiencies of
16.5% for vacuum-deposited absorbers.13 Solution-processed CIGS is also being developed with laboratory-scale
efficiencies of 14.7%.6 The process still
requires a high-temperature step, and indium (used in CIGS) is considered
by some to add financial risk because of indium price volatility or
constraints on the manufacturing growth rate.14 Solution-processed HP efficiencies have increased rapidly and are
over 20% with the added benefit of requiring no high-temperature steps.15 As promising as these material are, they possess
several shortcomings. All high-efficiency HP materials contain lead,
which has environmental health risk.16 HP
materials also have limited lifespans owing to low thermodynamic stability
of the compound,17 degradation in the presence
of light and moisture,18 or light-induced
phase segregation.17 However, these materials
have remarkable properties and defect tolerance. The origin of this
defect tolerance is believed to come from a partial oxidation of the
Pb2+ cation, withholding its 6s2 electrons.19 These 6s2 electrons give rise to
a valence band maximum consisting of antibonding orbitals. In addition,
relativistic spin–orbit effects increase the width of the conduction
band considerably. As a result, dangling bonds from vacancy formation
appear as resonances within the bands, rather than as trap states
in the band gap.20 Bi3+ likewise
possesses this beneficial electronic structure, and it is expected
to possess a similar defect tolerance.20 BiI3 is composed of layers of edge-sharing BiI6 octahedra held together in part by van der Waals interactions.21 Lehner et al. have found that BiI3 has a large static dielectric constant with principal components
of the static dielectric tensor of εxx∞ = 18.9 and εzz∞ = 15.0, which may indicate effective screening of charged point
defects, thus improving transport.22 BiI3 has also shown lifetimes of over 7 ns.19 Materials with lifetimes of at least 1 ns (such as CZTS,
InP, and CIGS) have achieved device efficiencies of greater than 10%.19 Furthermore, materials such as BiI3 are well-investigated materials for room-temperature gamma-ray detectors23 owing to the high interaction cross section.
One of the biggest advantages of Bi3+ over Pb2+ is that it is less toxic. For instance, bismuth is already in use
as a component of lead-free solders. Compared to lead, mercury, and
arsenic, bismuth is the least toxic because of its low water solubility.24 While the World Health Organization (WHO) has
set a standard of 10 ppb for lead in drinking water,25 in contrast, no limits have been imposed for bismuth. Finally,
BiI3 has a 1.8 eV band gap and high absorption coefficient.21 Using the absorption coefficient data presented
by Brandt et al.,21 a 500 nm thick film
would be sufficient to absorb 95% of incident above-band gap photons.
A 1.8 eV-band gap BiI3 top cell would be well-matched with
a 1.12 eV Si bottom cell, which would give a maximum theoretical efficiency
of 45.3% in a four-terminal tandem configuration.26
Processing variables such as substrate temperature
during physical
vapor deposition or choice of solvent for solution processing21 greatly impact the morphology of the BiI3 film. Bridgman growth23 and vacuum-based
methods21 are well-developed techniques
for making BiI3 films. Solution-processing routes are less
well-developed. BiI3 has been solution-deposited from dimethylformamide
(DMF),21,27 tetrahydrofuran (THF),27 and dimethyl sulfoxide(DMSO).28 In fact, bismuth trihalides are known to form coordination compounds
with all of these solvents.28,29 These solvents are
similar in that they possess Lewis base sites, which result in the
solvent and BiI3 forming Lewis acid-base adducts. Hamdeh
et al. have applied DMF solvent vapor annealing (SVA) on a spin-coated
BiI3 film from THF solution to grow large grains, and by
this, they have achieved the highest power conversion efficiency (PCE)
to date for a BiI3-based solar cell of 1.0%.27 In SVA, films are heated in the presence of
solvent vapor using solvents that have affinity for BiI3. The presence of solvent vapor increases the mobility of molecular
species in the film and allows the film to reorganize and achieve
larger grains. DMF SVA has been also used previously in the hybrid
perovskites to grow grains of 1 μm in diameter.30,31 However, SVA is sensitive to the environment, which causes severe
reproducibility issues, and the key parameters, which have an impact
on the morphology, are neither known nor understood. Further, state-of-the-art
BiI3 solar cells with a PCE of around 1% suffer from significant
current and voltage losses. The materials chemistry reasons for these
deficiencies are not known to date.
Here, we address both issues.
We present an investigation of important
variables affecting SVA of BiI3 films, such as temperature
and water concentration. We used DMF as the SVA solvent as it forms
a mildly stable BiI3–DMF complex,28 which plays a role in growing good morphologies. We show
that tuning of water vapor concentration and temperature is crucial
to grow large-grained, void-free solution-processed BiI3 films and that the presence of ambient oxygen is less crucial. We
present a mechanism for the action of both water and temperature.
Through this understanding, we present an optimized SVA process for
growing continuous BiI3 films on TiO2 substrates.
For the first time, we apply absolute intensity photoluminescence
(AIPL) measurements on BiI3 films to assess the maximum
possible open-circuit voltage and lateral dc photoconductivity measurements
to assess the carrier transport. These measurements give us access
to the two key parameters for solar cell operation, the quasi-Fermi
level splitting (QFLS) and the average electron–hole diffusion
length. By correlating different SVA processes with these material
property measurements and PV device performance, we reveal the limiting
factors for the low device performance.
Results and Discussion
Effect
of Water, Temperature, and Solvent on Morphology
Pre-SVA
films are dense but small-grained (Figure 1a). SVA grows the grains (Figure 1b,c), but the morphologies
are not always the same. We noticed that films prepared in the fume
hood with SVA at 100 °C on different days have very different
morphologies. These films were prepared under the exact same conditions,
with the only difference being the humidities on these days. Indeed,
it is known that relative humidity (RH) can have a significant influence
on SVA.36 We see disconnected disk-shaped
grains (Figure 1b),
whereas films prepared at a different day showed large, uniform, and
dense grains (Figure 1c). To better understand this, we treated BiI3 films with
SVA at different temperatures and RHs.
Figure 1 Scanning electron microscopy
(SEM) images of BiI3 films
grown on FTO/TiO2 substrates (a) after spin-coating and
before SVA; post DMF SVA on days with (b) lower RH and (c) higher
RH.
We prepared films treated with
SVA at 0, 35, and 70% RH at 80,
100, and 120 °C both in a fume hood but also inside a glovebox
to investigate the effect of ambient atmosphere. The relevant parameter
behind RH is the activity of water, which is proportional to the vapor
phase mole fraction. The vapor phase mole fraction is related to the
water concentration, assuming that all water introduced during the
start of SVA goes into the vapor phase. Water concentrations for a
RH/T combination are given in Table S1.
Multiplying this number by the SVA inner Petri dish volume gives the
total mass of water needed for SVA. It is this mass of water that
was mixed with DMF to create the water–DMF SVA solvent mixtures.
We observe that the SVA solvent is completely evaporated throughout
the SVA process. Some minor solvent and water loss is expected as
the SVA Petri dishes are not sealed. SVA is performed inside a smaller
Petri dish enclosed in a larger Petri dish to maintain the temperature,
reduce airflow effects, and limit material loss. It is important to
note that films prepared in ambient air have additional water exposure
from ambient RH. On the days we prepared our films in air, RH was
42% at 20 °C, which corresponds to an additional water content
of 7.2 × 10–6 g/cm3, which is between
1 and 7% of the total water concentration for the 35 and 70% RH conditions
at 80–120 °C and will hence be neglected in the following.
Films prepared from concentrated inks exhibited cracking after
spin-coating (Figure S2a). Note that the
BiI3 concentration in this study is twice that in previous
work.27 This cracking comes from tensile
stresses in the film as the THF rapidly evaporates.37,38 We developed a modified ink to prohibit cracking. Addition of 1–2
vol % DMSO to the THF inks prevented cracking and resulted in smooth
films (Figure S2b). The colors of the pure
THF and THF + DMSO films are different. The pure THF films are black
after spin-coating owing to the rapid THF evaporation leaving a pure
BiI3 phase behind. The THF + DMSO films are dark red after
spin-coating. This red color indicates the presence of a BiI3–DMSO complex in the film.28 Within
20 min of exposure to ambient air, these films gradually turn black,
indicating that the BiI3–DMSO complex is not stable
at room temperature and thus decomposes to leave behind the pure BiI3 phase. This slow decomposition process accompanied by the
evaporation of DMSO helps in obtaining uniform BiI3 film
nucleation and growth, which is similar to the behavior observed in
hybrid perovskites.7 We also tested DMF
as an additive to the BiI3–THF inks, but this resulted
in films that were not dense (Figure S3).
SEM images of films after SVA treatment in a fume hood with
different
RHs and temperatures are presented in Figure 2. Each of the panels in Figure 2 represents one film, prepared
at a specific SVA condition. For some SVA conditions, the films turned
orange after some time during solvent vapor exposure in the second
step of SVA. This is indicated by the colored swatch in the lower
right-hand corner of each panel. A brighter orange swatch means the
film turned orange early on during the second step of SVA. The darker
the swatch, the longer the film took to turn orange. All black swatches
mean the films never changed color. The times listed in the orange
swatches are the durations the films were orange. The films prepared
at 80 °C and 0% RH (Figure 2a) remained orange until it was uncovered. This indicates
that even though the Petri dishes are not sealed, they retain SVA
solvent for the duration of SVA.
Figure 2 SEM images of BiI3 films on
FTO/TiO2 prepared
in air with the given RH (rows) and temperature (columns) during SVA
[(a) 0% RH/80 °C, (b) 0% RH/100 °C, (c) 0% RH/120 °C,
(d) 70% RH/80 °C, (e) 70% RH/100 °C, and (f) 70% RH/120
°C]. The upper and lower halves of each panel are low- and high-magnification
images of the same sample made at the given RH and T, respectively.
Scale bars are labeled in each image. The colored swatches in the
lower right corners of each panel represent the approximate amount
of time the sample remained orange during the second step of SVA.
Swatches that are primarily orange mean the sample turned orange early
on, whereas all black swatches mean the sample never changed color.
Times inside the swatches indicate the duration for which the films
remained orange.
All films prepared with
SVA at 80 °C turned orange during
step 2 (solvent exposure) of the SVA process, independent of RH. However,
the time it took the films to turn orange increases with RH. The film
prepared at 80 °C and 0% RH (Figure 2a) turned completely orange within 30 s of
solvent addition. For the same temperature, films prepared at 35%
(Figure S5b) and 70% RH (Figure 2d) turned completely orange
7 and 9 min into SVA, respectively. The film prepared at 100 °C
and 0% RH showed a nonuniform behavior: part of the film turned orange
60 s into SVA and part remained black (Figure S6a). The SEM images of the orange part of this film are shown
in Figures 2b and S6b.
This is in good agreement to our initial findings where we observed
morphological differences with films treated with 100 °C SVA
under different ambient humidities. The partial color change indicates
that the portion of the substrate that turned orange experienced a
higher DMF partial pressure than the portion that stayed black. The
region that turned orange was the side of the substrate closest to
the DMF source. During the final step of SVA, where the lid is opened
so that the solvent could escape, all of the films that had turned
orange during SVA immediately turned black again. No color change
was observed for 100 °C + 35% RH (Figure S5e), 100 °C + 70% RH (Figure 2e), or any of the films made at 120 °C
(Figure 2c,f). Visually,
there is a difference between films that turned orange during SVA
and those that stayed black: films that turned orange are hazy, whereas
those that did not change color remain relatively shiny. The haziness
of the films that turned orange during SVA comes from light scattering
at larger domains (1–20 μm) that developed in the film
(Figures 2a,b,d and
S6b).
The films that changed color during SVA at 80 °C
(Figures 2a,d and S5)
have
larger domains sitting on top of the films. Looking at the higher
magnification images, we see that the film is primarily made of clusters
of small (<100 nm diameter) grains. The film that experienced the
plume of DMF (Figure 2b) consists of large platelets (∼15 μm diameter). The
differences between this case and the 80 °C cases are attributable
to the high DMF concentration in the plume. All of the films that
did not change color are similar (Figure 2c–f), consisting of apparent grain
sizes of 300–500 nm diameter, as determined by SEM. This means
that as long as the films do not change color during SVA, dense, large-grained
films can be grown.
Films made inside and outside of a glovebox
with the same SVA condition
have similar morphologies. For instance, films made with SVA at 120
°C and 70% RH inside (Figure S7a)
and outside (Figure S7b) a glovebox show
similar SEM grain size (300–500 nm) and polydispersity. This
shows that the ambient environment does not have a big impact on morphology.
We will focus on films prepared outside a glovebox for the rest of
our discussion. Full comparison of glovebox and air films is given
in the Supporting Information (Figures S4 and S5).
Mechanism behind the Effects of Water, Temperature,
and Solvent
We explain the role of SVA temperature and water
concentration
by considering the BiI3–DMF complexation chemistry.
Nørby et al.28 have determined via
single-crystal X-ray diffraction (XRD) that the carbonyl oxygen in
DMF complexes with the Bi3+ center to give a solvent complex
crystal with a unit cell of Bi(DMF)8–Bi3I12. Octahedral complexes such as BiI3 typically
undergo ligand exchange via a dissociative interchange mechanism (Id).39 In an Id mechanism, the bond with the incoming group
is formed at the same time the bond with the leaving group is broken.
In our case, the incoming group is the carbonyl group on the DMF and
the leaving group is an iodide anion. Bi3+ is a Lewis acid
of intermediate hardness. The oxygen in the DMF carbonyl group is
a hard base, and the iodide anion is a soft base.40 As a result, Bi3+ is expected to have a similar
ability to complex with the carbonyl oxygen in DMF and the iodide.
Furthermore, as has been shown by Sanderson et al., the bond dissociation
enthalpy of the Bi–I bond is the smallest for the Bi–halides
(i.e., the Bi–I bond is easier to break than other Bi–halide
bonds).41 The character of the bond is
largely ionic, and the large ionic radius of the iodide anion means
it is held less strongly by the Bi3+ center because of
electron–electron repulsion between Bi and I. The ionic character
of the Bi–I bond is critical for facile DMF complexation. The Id mechanism requires a good leaving group. Because
the Bi–I bond is more ionic than covalent and thus more easily
broken, the iodide makes a good leaving group, allowing the DMF to
readily complex with the Bi3+ center.
We first consider
the water-free (DMF vapor only) 80 °C case. The spin-coated crystalline
BiI3 film is made up of BiI6 octahedra arranged
in two-dimensional (2D) sheets.21 Consider
a single BiI6 octahedron exposed to DMF vapor. The DMF
approaches the Bi3+ center and begins to form a Bi–OR
complex with the DMF carbonyl oxygen. At the same time, the Bi–I
bond is being broken and the I– leaves. This reaction
continues to take place until the Bi center is coordinated to eight
DMF molecules [Bi(DMF)8]3+, which is charge-balanced
by a [Bi3I12]3– group. If
enough DMF is present, the entire film is transformed to a DMF–BiI3 coordination compound. This compound may crystallize with
a unit cell composed of four Bi(DMF)8–Bi3I12 pairs, as shown by Nørby et al.28 We note that BiI3 also coordinates with DMSO
and THF, the solvent system for our inks (a more detailed discussion
about this can be found in the Supporting Information).
The BiI3–DMF coordination compound is
the orange
phase witnessed under low RH and low T. The solvent
complex film is thicker than the BiI3 film because of DMF
uptake. The unit cell volume of the BiI3–DMF solvent
crystal is 6507.2 Å3, and it contains four Bi(DMF)8–Bi3I12 moieties, that is, a
volume of 406.7 Å3 per BiI3.28 Pure BiI3, in contrast, has a unit
cell volume of 1016.7 Å3 with six BiI3 moieties
per unit cell,42 that is, a volume of 169
Å3 per BiI3. This means that there is a
volume increase and, concomitantly, a thickness increase of the orange
phase of a factor of 2.4 compared with the BiI3 film. Upon
drying, this film collapses back to the BiI3 film, which
results in a different morphology relative to the initial (pre-SVA)
BiI3 film. This can lead to very rough films with large
BiI3 clusters, as shown in Figure 2a,d or to films with large disconnected platelets,
as shown in Figure S6b. If a BiI3 film is exposed to DMF vapor for a much longer time than 9 min in
our SVA process, then macroscopic morphologies can form, as shown
in Figure S9.
Now, consider the case
of SVA at higher temperatures (T ≈ 120 °C).
We did not observe the orange phase formation
during SVA at this temperature with the DMF concentrations considered.
To better understand this, we collected data to perform a van’t
Hoff analysis (details in the Supporting Information). The reaction considered is 4BiI3 + 8DMF ↔ [Bi(DMF)8]3+[Bi3I12]3–. BiI3 films were placed in sealed vials with different
DMF dosings. The BiI3 films were allowed to complex with
the DMF at room temperature until the orange solvent complex formed.
The vials were then heated in a box oven, slowly increasing the temperature
until the films turned black again. From these temperatures, we get
the equilibrium constant for the BiI3–DMF complexation.
By plotting ln(Keq) versus 1/T, we can extract ΔHrxn and ΔSrxn for the system. On the basis of the stoichiometry
of the above reaction, this yielded values of ΔHrxn of–3 ± 1 eV and ΔSrxn of −0.006 ± 0.003 eV/K per molecular of
the coordination compound. If one assumes that each successive DMF
addition has similar thermodynamics, the enthalpy and entropy are
ΔHrxn of −0.4 eV and ΔSrxn of −0.0007 eV/K per DMF, respectively.
This means that this reaction is enthalpically favorable up to 140
°C, at which point the entropic term begins to dominate. At temperatures
exceeding 140 °C, no concentration of DMF would result in the
films turning orange. The important point here is that at elevated
temperatures, it is more favorable for the DMF to be in the vapor
phase rather than to be complexed with BiI3. It is this
effect that prevents the orange solvent complex from forming at higher
SVA temperatures, independent of RH. For an efficient crystal growth
during SVA, the maximum DMF concentration below the level which leads
to the orange phase is desirable. Thus, our DMF concentration (10
ppm) during SVA is chosen so that the orange solvent complex forms
up to a temperature of 100 °C, which is the ideal temperature
for the SVA process shown previously.27 Larger DMF concentrations would lead to the formation of the orange
phase at higher temperatures; for smaller DMF concentration, the films
would stay black at lower temperatures.
Now, we discuss the
effect of water on the SVA process. At 80 °C,
RH slows down the transformation of the BiI3 into the orange
solvent complex. At 100 °C, the presence of water (≥35%
RH) prevents the film from turning orange at all and results in more
uniform grain growth. To understand this, we note that hydrogens in
water will hydrogen bond with the oxygen in DMF. As a result, the
electron-donating strength (i.e., the Lewis basicity) of the carbonyl
oxygen is reduced. Thus, the DMF is rendered less reactive and will
complex less readily with the BiI3. This would be expected
for cases where the water concentration is equal to or greater than
the DMF concentration, which is true at the DMF–water dosings
used during SVA. This explains the difference we see between films
prepared at 100 °C with 0 and 70% RH.
Effect of Substrates on
Film Morphology
We spin-coated
200 mg/mL BiI3 in THF + 1–2 vol % DMSO onto FTO/TiO2, FTO/ZnO, and ITO/Cu/NiOx substrates.
We observe significantly different film morphologies with the different
substrates. Films grown on TiO2 (Figure 3a) are made of 300–500 nm densely
packed grains. Films grown on ZnO (Figure 3b) are more polydisperse and contain small
and large platelets with sharp edges. Films prepared on copper-doped
nickel oxide (Cu/NiOx) (Figure 3c) are also more polydisperse
than the films grown on TiO2 but also contain large (1
μm dia.) platelets. We rationalize these observations by noting
that film–substrate surface energy differences can influence
film growth. In the cases where substrate surface energy is smaller
than film + interface surface energies, island growth is expected.43 Other factors such as deposition temperature
also can impact crystal growth.21 This
means that by optimizing parameters such as SVA solvent, water concentration,
and temperature, we might be able to obtain dense films with the desired
grain size for each choice of substrate.
Figure 3 SEM images of BiI3 films grown with SVA at 120 °C
and 70% RH on (a) FTO/TiO2, (b) FTO/ZnO, and (c) ITO/Cu/NiOx.
Crystallographic Orientation
XRD spectra for BiI3 films grown at different SVA temperatures and water vapor
concentrations are shown in Figure 4a). The films that turned orange during SVA, that is,
those grown at 80 °C (0% RH and 70% RH) and 100 °C (0% RH)
show a pattern significantly different from the black ones. The most
pronounced XRD peaks for those films are due to reflections at the
(003), (006), and (009) planes, which belong to the same family of
(00l) planes. This indicates a texturing of those
films. In contrast, the films that did not change color during SVA
show much smaller peaks for the (00l) planes. We
observe pronounced reflections at (113) and (300) in these films,
indicating less texturing.
Figure 4 (a) XRD spectra as a function of SVA temperature
and RH. The green
and blue curves show the spectra for those areas that turned orange
and that stayed black, respectively (see Figure 2). The dotted vertical lines indicate BiI3 powder peaks. The solid black vertical lines indicate the
peaks of the FTO substrate. (b) TCs related to the (300) plane (green),
(113) plane (blue), and (003) plane (red) as a function of SVA temperature
for 0% RH (open squares) and 70% RH (open pyramids).
To further study this texturing effect, we evaluate
the texture
coefficient (TC). The TC of a plane (hkl) is defined
as , where I(hkl) is the measured intensity, I0(hkl) is the intensity of the powder
diffraction, and N is the number of planes considered.44 A TC equal to 1 indicates no preferred orientation.
The
TCs for the (300), (113), and (003) planes are shown in Figure 4b for different SVA temperatures
and water concentrations. All films that turned orange during SVA,
that is, at 80 °C show a TC of around 3 for the (003) plane and
of close to 0 for the (113) and (300) planes. We note that the same
TCs are also observed for the films that turned orange during SVA
at 100 °C, 0% RH (not shown in Figure 4b). This indicates a strong texturing: these
films are oriented with their (003) plane predominantly parallel to
the substrate; that is, the BiI3 film is layered in such
a way that the planes which contain edge-shared BiI6 octahedra
are parallel to the substrate. The films that did not change color
do not show this texturing: TCs for the (003) and (113) planes are
between 0.5 and 0.9, whereas the TC for the (300) plane is around
1.5. This indicates a slightly preferred orientation in such a way
that the edge-shared BiI6 planes are perpendicular to the
substrate. Similar texturing has been found in BiI3 films
that have formed from BiI3–DMSO complexes.28 Because the 2D sheets of edge-shared BiI6 octahedra are only weakly connected by van der Waals forces,
it is expected that in-plane transport should exhibit larger mobility
than perpendicular to the 2D sheets. Hence, the films that turned
orange during SVA should show a better carrier transport parallel
to the substrate and worse transport perpendicular to the substrate
plane than the films that did not change color. We will come back
to this point later.
Optoelectronic Quality
We performed
AIPL measurements
at a PV device relevant excitation laser intensity comparable to one
sun. PL measurements on BiI3 films have been carried out
previously;21,27 however, because the PL quantum
yield (PLQY) is very low, those measurements used laser excitation
intensities comparable to >100 sun. Here, we were able to measure
BiI3 AIPL at 1 sun effective intensity. This was enabled
by both the high quality of the films and a modification to our measurement
technique (see the Supporting Information for details).
The AIPL is peaked at 1.78 eV with a full width
at half-max of 180 meV (Figure 5a, blue trace). This is very close to the measured band gap
of 1.79 eV determined from UV–vis absorption measurements (Figure 5a, red trace). The
fact that the PL peak is right at the band edge indicates that sub-band
gap states should not cause a significant loss of voltage. From AIPL,
we get the PLQY, which we used to calculate the QFLS (Figure 5b) with the method described
in Braly and Hillhouse.33 The QFLS is an
indication of the maximum voltage Voc achievable
by a solar cell device. QFLS is proportional to kT ln(1/PLQY). Therefore, what may appear as larger differences in
PLQY does not correspond to as large differences in QFLS. In Figure 5b, we also show the
ratio of the measured QFLS to the Shockley–Queisser QFLS (QFLSSQ) for a material with the same band gap, χ = QFLS/QFLSSQ.33 χ may be considered
to be the optoelectronic quality of the material. All films prepared
at 80 °C as well as the film prepared at 100 °C with 0%
RH have PLQY < 1 × 10–7. Those were the
films that turned orange during SVA. The films prepared at 100 °C
with 35 and 70% RH and all 120 °C films have PLQY values of 2
× 10–7%. These films remained black during
SVA.
Figure 5 (a) Absorption coefficient (red curve) and PL spectral flux spectrum
of BiI3 with a peak at 1.78 eV (blue curve). (b) PLQY,
QFLS, and χ from 1 sun AIPL of BiI3 films prepared
with different SVA temperatures and RHs. (c) Two-point lateral dc
photoconductive diffusion length measurements of BiI3 films
grown with different SVA temperatures and RHs.
The lower PLQY films were the films that had turned orange
during
SVA, whereas the higher PLQY values were obtained from the films that
did not change color during SVA. PLQY was greater by 2–6 times
in the films that did not change color during SVA. This may be understood
as an effect of the grain size. The films that turned orange during
SVA have grains with diameters ≤100 nm. The films that remained
black have grains 300–500 nm in size. The differences in PLQY
may be attributed to nonradiative recombination at the grain boundaries.
The smaller grained films have a greater number of grain boundaries,
meaning that nonradiative recombination would be greater. However,
we cannot exclude differences in the bulk. Films that turned orange
during SVA may have entrained DMF within the crystalline BiI3. This may give rise to different point defects and contribute to
nonradiative recombination.
Coming back to our discussion on
transport, a lateral dc photoconductivity
method34,35 was used to estimate the lateral diffusion
length to assess the impact of SVA on carrier transport. The diffusion
length (LD) determined from this technique
is an average (root mean square) of the electron and hole diffusion
lengths. A slight trend is observed toward higher diffusion lengths
with increasing temperature and RH from 40 nm at 80 °C/0% RH
to 55 nm at 120 °C/0% RH and 70 nm at 120 °C/70% RH, as
shown in Figure 5c.
Because these are lateral diffusion lengths, that is, the carriers
flow parallel to the substrate, this behavior is contradictory to
what we would expect from the above discussion on texturing of the
films: carrier transport is expected to be better for films that turned
orange during SVA (i.e., at 80 °C/0% RH and 80 °C/70% RH),
which is obviously not the case. One likely reason for this is the
much lower grain size of the films that changed color during SVA compared
to the films that did not change color (see Figure 2), giving rise to significantly more grain
boundaries, which reduces the carrier mobility. In addition, the lifetime
of photoexcited carriers in the films that turned orange during SVA
is significantly lower than that in the films that did not change
color because of the higher recombination rate as indicated by the
lower PLQY. Because the diffusion length is proportional to the mobility-lifetime
product, the latter two effects counterbalance the beneficial texturing
effects of the films that turned orange during SVA as compared to
the films that did not change color.
PV Devices
We
made PV devices to assess the impact
of SVA on PV performance. An ideal band diagram (assuming no ion migration,
intrinsic BiI3, no mass transport across the interfaces,
and no surface chemistry/interface dipoles) and a device architecture
schematic are shown in Figure 6a and the inset of 6b, respectively.
We report current density versus voltage (JV) curves
and time-dependent PCE (using maximum power-point tracking45) under continuous simulated AM1.5G illumination.
The best solar cell with the optimized SVA process (120 °C +
70% RH) has a stabilized PCE (Figure 6b, blue curve) of 0.51%. A device made from a film
that turned orange during SVA (e.g., 80 °C + 70% RH) in the same
architecture shows a much lower stabilized PCE of 0.04% (Figure 6b, orange curve).
Figure 6 (a) Equilibrium
band diagram of FTO/TiO2/BiI3/spiro-OMeTAD (SOMT)
at short circuit. The dashed red line indicates
the Fermi level. (b) Maximum power-point tracking curves for devices
made with 120 °C/70% RH (blue curve) and 80 °C/70% RH (orange
curve). The inset shows device stack. (c) Light (blue) and dark (orange) JV curves for the 120 °C and 70% RH device. (d) Light
(blue) and dark (orange) JV curves for the 80 °C
and 0% RH device.
This more than 1 order
of magnitude lower PCE comes mainly from
two factors, a significantly lower photocurrent and a much lower fill
factor due to the s-shaped JV. We note that the lower
photocurrent very likely stems from a much lower carrier diffusion
length perpendicular to the substrate for the films that turned orange
during SVA. This is expected from the texturing effects discussed
above, the lower carrier lifetime due to the lower PLQY, and the lower
mobility due to the increased number of grain boundaries.
While
the band alignment shown in Figure 6a suggests that an electric field should
be present across the device to assist with carrier collection, if
charged iodide vacancies migrate (as in hybrid perovskite solar cells)
to screen the internal field, then carrier diffusion would have to
be relied on for carrier collection.23,46 The relatively
low diffusion lengths measured (70 nm) could then partly explain the
low short-circuit current (Jsc) of 4.14
mA/cm2. Another contributing factor to the low photocurrent
could be the misalignment of the conduction band edges (CBES) of TiO2 and BiI3. An ab initio calculated value for the
CBE for BiI3 is 4.1 eV, and the accepted value for TiO2 is 4.2 eV below vacuum.22 These
are very close, and if correct would not yield a barrier for electron
extraction. However, if the actual band edge position of BiI3 is different, it may cause a barrier for electron injection from
BiI3 into TiO2.
The large differences
between the light and dark curves suggest
further device issues, such as a light-dependent saturation current,
photoexcited carrier screening of electrostatic barriers at the interfaces
(not shown in the band diagram), voltage-dependent photocurrent, and
light-dependent shunt and series resistances. The table in Figure S10b shows the results of fitting the
nonideal diode equation to the light and dark curves for the device
made at 120 °C and 70% RH (Figure S10a). The reverse saturation currents (J0), series resistances, and shunt resistances all differ by more than
an order of magnitude.
With regard to the low voltage, the low
diffusion length may play
a role as well, as it signifies significant nonradiative recombination.
Furthermore, the band alignment also likely plays an important role.
With regard to the hole-extracting contact, the band edge of the spiro-OMeTAD
lies 5.1 eV below vacuum,47 and the position
of the BiI3 valence band is 6.0 eV below vacuum.22 While one would not expect a barrier for hole
extraction, voltage could be lost because of the large offset between
the BiI3 valence band and the spiro-OMeTAD Fermi level.
Conclusions
We have
explored the mechanisms behind the BiI3 film
formation process and demonstrated the roles that temperature and
water play in the solvent annealing process for BiI3 layers.
We developed a reliable process for growing large-grained, continuous
films. Films with small grains and poor morphologies result in reduced
device performance and optoelectronic quality. Performing SVA with
precise dosing of water and DMF grows uniform films with a SEM-based
morphological grain size of 300–500 nm. Water acts to moderate
the influence of DMF during the SVA process, allowing more controlled
growth to occur. Higher temperatures also moderate the action of DMF.
We used highly concentrated BiI3–THF inks (200
mg/mL) and observed severe cracking of the films upon spin-coating
and drying. Modifying the ink chemistry by addition of 1–2
vol % DMSO, we successfully prevented film cracking and obtained homogeneous
and smooth films.
Formation of the orange BiI3–DMF
complex during
SVA at low temperatures results in films with a preferred orientation:
the planes corresponding to the 2D sheets of BiI6 octahedra
are oriented parallel to the substrate. From diffusion length measurements
and device characterization, we obtained clear indication for very
poor transport in the direction perpendicular to these planes. The
reason is the weak van der Waals interaction of these 2D sheets. This
shows that for the structurally two-dimensional material BiI3, the film texture is an essential parameter for its application
in optoelectronic devices.
From AIPL measurements, we determined
a QFLS of 1.1 eV at 1 sun,
which is a measure for the maximum photovoltage that can be obtained
in a solar cell. This is a promising result because an optimized solar
cell with BiI3 as the absorber material only limited by
this QFLS could achieve >15% PCE.
A QFLS of 1.1 eV is 73%
of the Shockley–Queisser limit for
BiI3, which indicates that there is still room for improvements
via defect passivation. However, it also indicates that bulk nonradiative
recombination is not the main reason for the low voltage of state-of-the-art
BiI3 solar cells. Both the large voltage deficit and current
deficit seen in BiI3 devices are a consequence of low diffusion
length and nonoptimal band alignment.
This work reveals the
mechanisms behind the film formation process
of BiI3 films, which are potentially also applicable to
other metal halide materials. It further expands the understanding
of the relationship between the chemistry and physics of BiI3 films and devices, opening the door for improving device efficiencies.
Further development of this material could enable it to become a competitor
to PbI2-based hybrid perovskites while avoiding the toxicity
and potentially also the stability issues of the perovskite material.
Experimental
Section
Materials
BiI3 inks (200 mg/mL) were prepared
by dissolving BiI3 (99.999%, Alfa Aesar) in anhydrous THF
(99.9%, inhibitor-free, Sigma-Aldrich) inside a N2-filled
glovebox. The inks were sealed and then mixed with an ultrasonicator
immediately before use. Fluorine-doped tin oxide (FTO) substrates
(14 × 14 mm2) (TEC 7, Sigma-Aldrich) were sequentially
cleaned by sonication in a detergent solution, DI water, acetone,
and 2-propanol for 10 min. Substrates were cleaned with an Ar plasma
immediately before use. TiO2 solutions were prepared by
mixing 10 mL of ethanol (200 proof, Sigma-Aldrich), 69 μL of
HCl (37 wt %, aq, Macron Fine Chemicals), and 0.727 mL of Ti(IV) ethoxide
(Aldrich) and sonicating it for 30 min. This solution was spin-coated
onto the FTO substrates in air at 2000 rpm for 15 s. Substrates were
coated twice, with a 500 °C anneal in a box oven between layers.
BiI3 inks were deposited on the TiO2-coated
substrates by spin-coating at 2000 rpm for 35 s inside a N2-filled glovebox and in a fume hood. After spin-coating, the films
were solvent vapor-annealed for 10 min with DMF–water mixtures.
SVA consists of three steps: (1) the as spin-coated BiI3 film is set inside a Petri dish on a hot plate; (2) after 60 s,
the solvent is added to the Petri dish with the film and the lid is
closed; and (3) after 9 min, the lid is removed so that the film is
exposed to the ambient atmosphere for 60 s to remove residual DMF
and water. DMF volume was held constant at 6.4 μL, and water
content was varied to achieve 0, 35, or 70% RH at 80, 100, or 120
°C. See Figure S1 and Table S1 in the Supporting Information for details on the SVA setup and water concentrations.
hole transport layers were prepared by spin-coating spiro-OMeTAD,
as described elsewhere.9 The spiro-OMeTAD
was doped with Li and Co and oxidized overnight. Devices were finished
by thermal evaporation of 100 nm Au at a base pressure of 1 ×
10–6 Torr.
Characterization
SEM images were
collected at a 5 kV
accelerating voltage with an FEI XL830 Dual Beam SEM/FIB. Crystallographic
measurements were collected with a Bruker D8 Discover XRD. AIPL measurements
were collected at 1 sun photon flux with an apparatus described previously.32,33 The 1 sun condition used corresponds to a photon flux of 1.28 ×
1021 photons/s m2 at a laser wavelength of 532
nm. A 150 lines/mm Czerny–Turner monochromator blazed at 500
nm was used to collect the signal. PLQY and the peak position were
used to calculate the QFLS and the optoelectronic quality (χ).33 PV devices were tested in air using an AAA solar
simulator (Oriel Sol3A) and a Keithley 2400 SMU. A photoconductivity
method was used to determine the mean carrier diffusion length34,35 using a bias of +20 V with a 432 nm blue light-emitting diode at
3.66 × 1021 photons/s m2 flux, which is
2.8 sun equivalent for a 1.8 eV band gap material. Photoconductivity
measurements were made inside a temperature-controlled stage held
at 20 °C.
Supporting Information Available
The Supporting Information is
available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b00813.Additional experimental
details, BiI3 complexation
with DMSO and THF, SEM images, and LambertW fitting of IV curves (PDF)
Supplementary Material
ao8b00813_si_001.pdf
Author Contributions
B.W.W.
and
F.T.E. contributed equally. The manuscript was written through contributions
of all authors. All authors have given approval to the final version
of the manuscript.
The authors
declare no competing financial interest.
Acknowledgments
This
research was supported by the U.S. Department
of Energy SunShot Initiative, Next Generation Photovoltaics 3 program,
Award DE-EE0006710. We also acknowledge partial support from the University
of Washington Molecular Engineering Materials Center (UW MEM-C): an
NSF MRSEC under award number DMR-1719797.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145805610.1021/acsomega.8b01949ArticleCovalently Crosslinked 1,2,3-Triazolium-Containing
Polyester Networks: Thermal, Mechanical, and Conductive Properties Tracy Clayton
A. Adler Abagail M. Nguyen Anh Johnson R. Daniel Miller Kevin M. *Department of Chemistry, Murray State University, 1201 Jesse D. Jones Hall, Murray, Kentucky 42071, United
States* E-mail: kmiller38@murraystate.edu.
Tel: +1 270 809 3543. Fax: +1 270 809 6474.18 10 2018 31 10 2018 3 10 13442 13453 08 08 2018 05 10 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
Azide–alkyne
“click” cyclization was used
to prepare a series of polymerizable acetoacetate monomers containing
a 1,2,3-trizolium ionic liquid group. The monomers were subsequently
polymerized using base-catalyzed Michael addition chemistry, producing
a series of covalently crosslinked 1,2,3-triazolium poly(ionic liquid)
(TPIL) networks. Structure–activity relationships were conducted
to gauge how synthetic variables, such as counteranion ([Br], [NO3], [BF4], [OTf], and [NTf2]), and crosslink
density (acrylate/acetoacetate ratio) effected thermal, mechanical,
and conductive properties. TPIL networks were found to exhibit ionic
conductivities in the range of 10–6–10–9 S/cm (30 °C, 30% relative humidity), as determined
from dielectric relaxation spectroscopy, despite their highly crosslinked
nature. Temperature-dependent conductivities demonstrate a dependence
on polymer glass transition, with free-ion concentrations impacted
by various ions’ Lewis acidity/basicity and ion mobilities
impacted by freely mobile anion size.
document-id-old-9ao8b01949document-id-new-14ao-2018-01949mccc-price
==== Body
Introduction
Poly(ionic liquid)s
(PILs) remain a fascinating and important class
of polyelectrolytes, combining the unique properties of ionic liquids
(ILs) (high thermal and electrochemical stability, variable solubility,
viscosity, and ionic conductivity) with the tunable functionality
and mechanical stability of various macromolecular architectures.1−4 The thermal, mechanical, and conductive properties of PILs are primarily
varied by changing the chemical structure of the cation (ammonium,
phosphonium, imidazolium), anion (halides, inorganic fluorides, perfluoronated
sulfonimides), or both. As a result of their synthetic versatility,
PILs have been targeted for a number of important modern-day applications,
examples of which include actuators,5 batteries,6,7 fuel cells,8,9 and separation membranes.10−13 PILs have been generally prepared through the polymerization monomers
containing ILs, the postpolymerization quaternization of neutral polymers
or quaternization resulting from step-growth polymerization of neutral
monomers.
Contributions from our laboratories to the field of
PILs have centered
on the preparation of covalently crosslinked polyester networks following
either a thiol–ene photopolymerization14 or a base-catalyzed Michael addition polymerization strategy.15−19 Michael addition reactions are extremely useful for forming new
carbon–carbon bonds and readily occur under base-catalyzed
conditions between a Michael donor (an acetoacetate) and an α,β-unsaturated
carbonyl compound, such as an diacrylate ester (the Michael acceptor).15,16 Upon deprotonation of an acetoacetate, the resulting enolate anion
undergoes addition to an acrylate, resulting in a new carbon–carbon
bond after neutralization. Since each acetoacetate contains two acidic
protons, an additional Michael addition will occur in the presence
of excess diacrylate, resulting in covalent crosslinking. The degree
of crosslinking (and thus the thermal and mechanical properties of
the network) can be easily controlled through the manipulation of
the acrylate/acetoacetate ratio.16 Previous
work from our research group has demonstrated the versatility of the
Michael addition polymerization as a method for the preparation of
imidazolium17,18 and 1,2,4-triazolium PIL networks.19 Variations in network architecture (crosslink
density, counteranion, cation) have led to a library of PILs that
display a wide range of thermal and mechanical properties.
Although
the majority of the PIL literature has focused on ammonium,
phosphonium, and imidazolium polycations (with mobile counteranions),
1,2,3-triazolium-based poly(ionic liquid)s (TPILs) have become more
prominent due to the development of the copper(I)-catalyzed azide–alkyne
“click” cycloaddition reaction.20,21 Drockenmuller et al. have pioneered efforts in the synthesis of
a variety of TPILs, several approaches of which have been recently
reviewed.22 Such TPIL synthetic efforts
have ranged from the direct step-growth polyaddition of azides and
alkynes to the chain-growth polymerization of 1,2,3-triazolium-containing
(meth)acrylic monomers. Within their library of TPILs, several covalently
crosslinked networks were prepared and evaluated for various applications.
For example, an epoxy-functionalized IL monomer was reacted with a
poly(propylene glycol)-based diamine, providing TPIL epoxy–amine
networks with relatively high anhydrous ionic conductivities (∼10–7 S/cm at 30 °C).23 In another example, covalently crosslinked polyether-based TPIL
membranes with conductivities of up to 10–6 S/cm
at 30 °C under anhydrous conditions and CO2 permeability
values of 59–110 barrer with CO2/N2 selectivities
of 25–48 were also synthesized.24 TPIL vitrimer networks utilizing thermally reversible C–N
bond transalkylation exchanges have also been reported and were found
to exhibit ionic conductivities up to 10–8 S/cm
(30 °C, anhydrous) as well as reshaping and recycling behavior.25,26
TPIL polyester networks, which contained an asymmetrically
substituted
1,2,3-triazolium group with a limited set of counteranions, were recently
communicated by our laboratory.27 Electrochemical
impedance spectroscopy, utilizing a four-electrode cell, showed that
the resulting TPIL networks exhibited good conductivities between
10–6 and 10–8 S/cm (25 °C,
30% relative humidity (RH)), indicating the promising nature of this
class of PILs. Most notable was the appearance of a common “crossover”
temperature (∼85 °C) in the ionic conductivity curves,
given the same monomer ratio. At temperatures below the crossover
point, Tg/chain dynamics were found to
correlate well to ionic conductivity. Above the crossover temperature,
however, ionic conductivities correlated better to anion size, alluding
to the importance of “free” ion mobility. Though these
correlations are noteworthy, a much more in-depth investigation utilizing
a wider range of counteranions (in terms of size and lipophilicity)
in combination with dielectric relaxation spectroscopy (DRS) is necessary
to further decipher the complex relationships that exist between chain
dynamics, free-ion concentration, and conducting ion mobility.
Toward this end, the synthesis of a more focused series of symmetrically
substituted TPILs is reported herein where DRS has been employed to
determine ionic conductivities (at 30% RH) and to explore chain dynamics
and ion-transport properties. A comparative analysis of these properties
across various anions, crosslink density (acrylate/acetoacetate ratio),
and cations (imidazolium 1,2,4-triazolium, 1,2,3-triazolium) is discussed.
Due to the presumed hydrophilic nature of the TPIL [Br] network, coupled
with a minimum achievable RH of 30%, the effect of relative humidity
on conductivity and water uptake was also explored.
Results and Discussion
Synthesis of the 1,2,3-triazolium acetoacetate monomers began by
first converting commercially available ethyl-6-bromohexanoate to
the azide with sodium azide (Scheme 1). Reaction with trimethylsilylacetylene under Cu-catalyzed
click cyclization conditions resulted in the tetramethylsilane-substituted
triazole ring (not isolated), which was subsequently treated with
a fluoride source (tetrabutylammonium fluoride, TBAF) to provide the
desired 1,2,3-triazole ester 1.21 Reduction of the ester was then accomplished with diisobutylaluminum
hydride (DIBAL-H), resulting in 1-(6′-hydroxyhexyl)-1,2,3-triazole 2. Transesterification with tert-butylacetoacetate,
followed by coupling with 6-bromohexylacetoacetate 4,
resulted in the targeted acetoacetate [Br] monomer 5.
Various anion metathesis reactions (AgNO3, AgBF4, AgOTf, LiNTf2) were then employed to gain access to
other counteranions of interest (monomers 6–9). All of the 1,2,3-triazolium acetoacetate monomers were
clear, room-temperature ionic liquids with varying degrees of yellow
to orange color. 1H and 13C NMR spectroscopies,
as well as elemental analysis, were used to identify the products
and determine purity, respectively, and residual [Br] for PILs 6–9 was found to be <0.1% w/w by ion
chromatography.28
Scheme 1 Preparation of 1,2,3-Triazolium
Acetoacetate Monomers 5–9
Analysis of the thermal properties
of acetoacetate monomers 5–9 was
conducted prior to polymerization.
Differential scanning calorimetry (DSC) Tg values (Table 1, Figure S18) correlated inversely to the size
of the counteranion on the order of [Br] > [NO3] ≈
[BF4] > [OTf] > [NTf2]. Here, assessment
of
the relative anion sizes is based upon molar masses and thermochemical
radii.29 The ability of ionic liquids to
exhibit glass-forming behavior has been previously described using
techniques such as DSC, X-ray diffraction, and Raman spectroscopy.30,31 It is also worth noting that the observed relationship between anion
size and Tg has been observed previously
with imidazolium- and 1,2,4-triazolium-containing acetoacetate monomers.17−19
Table 1 Thermal Properties of 1,2,3-Triazolium-Containing Acetoacetate Monomers
compound anion DSC Tg (°C) TGA Td5% (°C)
5 Br –46.3 188
6 NO3 –54.9 194
7 BF4 –55.4 223
8 OTf –60.5 239
9 NTf2 –67.9 260
Thermal stability, as defined by Td5% (the temperature at which 5% of the material
has decomposed), correlates
inversely to the Lewis basicity of the counteranion on the order of
[NTf2] > [OTf] > [BF4] > [NO3] >
[Br] (Table 1 and Figure S19).32 All
of the acetoacetate monomers exhibited a one-step degradation except
for [BF4] 7 where a two-step process was observed.
Recent work by Clarke et al. using direct insertion mass spectrometry
investigated the decomposition products of 1-alkyl-3-methylimidazolium
[BF4] ILs and found fluoride to be a thermally induced
product of the reaction between tetrafluoroborate and the imidazolium
cation.33 We hypothesize here that as IL
monomer 7 is being heated, fluoride is generated. As
fluoride is a stronger Lewis base (compared to tetrafluoroborate),
the first step results from decomposition of the monomer from [F]
(the exact nature of the decomposition was not determined as part
of this study). The second step would represent decomposition as a
result of [BF4]. To support this hypothesis, the production
of fluoride from [BF4] acetoacetate monomer 7 was observed as a function of time using isothermal thermogravimetric
analysis (TGA) (at 200 °C) followed by analysis of the residue
by ion chromatography. Fluoride content of monomer 7 (determined
from the [F]/[BF4] ratio) was found to be negligible, however,
a 20-fold increase in fluoride concentration was observed during the
first hour at 200 °C. Additional time found the amount of [F]
and [BF4] to decrease, presumably because both anions are
being consumed as part of monomer decomposition. The results from
this study clearly show that fluoride is thermally generated during
the decomposition of [BF4] monomer 7 and thus
could influence the observed decomposition temperature.
1,2,3-Triazolium-containing
acetoacetates 5–9 were polymerized
following a standard Michael addition polymerization
protocol developed by our laboratory. The appropriate amount of acetoacetate
was allowed to react with commercially available 1,4-butanediol diacrylate
in the presence of catalytic 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)
(2 mol %) in a solution of dichloromethane (50 wt %) (Scheme 2).17−19 Each solution
was placed into a poly(tetrafluoroethylene) (PTFE) mold and cured
under ambient conditions for 48 h, followed by 48 h in a 60 °C.
The films were then dried in a vacuum oven at 60 °C for an additional
48 h to ensure removal of trace solvent residue and moisture. Since
conductive properties of the analogous imidazolium and 1,2,4-triazolium
PIL Michael networks had not been previously measured, comparison
networks were prepared fresh, which utilized previously reported imidazolium
and 1,2,4-triazolium [NTf2] acetoacetate monomers (10 and 11, respectively).17,19 For PILs where a variation in cation or anion was of interest, the
acrylate/acetoacetate ratio was held constant at 1.5:1.0. For PILs
in which the cation or monomer ratio was varied, the anion was held
constant at [NTf2].
Scheme 2 Michael Addition Polymerization of
1,2,3-Triazolium-Containing Acetoacetate
Monomers
Gel fraction and %
swelling of the PIL networks were determined
from Soxhlet extraction experiments using dichloromethane (Table 2). High gel fraction
values (>92%) were observed for all of the networks studied here.
Higher swelling values were observed with increasing anion size, presumably
due to an increase in free volume within the network as a result of
anion plasticization, although it is possible that the use of a more
hydrophobic anion ([OTf] and [NTf2]) could result in stronger
polymer–solvent interactions. As expected, an increase in the
acrylate concentration (polymers 16–18) decreased the % swelling due to the increase in covalent crosslinking
and a decrease in free volume within the network. Gel fraction and
% swelling values were similar across the series in which the cation
was varied (networks 16, 19, and 20).
Table 2 Gel Fraction and Thermal Properties
for TPIL Networks
polymer anion (cation) Acr/AcAc ratio gel fraction
(%) % swelling DSC Tg (°C) TGA Td5% (°C)
12 Br 1.5:1.0 97.6 ± 0.4 129.0 ± 0.9 7.7 195
13 NO3 1.5:1.0 95.6 ± 0.1 131.6 ± 1.0 3.9 203
14 BF4 1.5:1.0 97.4 ± 0.2 130.4 ± 3.3 2.9 256
15 OTf 1.5:1.0 95.2 ± 0.3 139.8 ± 0.8 –5.2 302
16 NTf2 1.5:1.0 92.2 ± 0.3 155.1 ± 2.2 –15.6 318
17 NTf2 1.2:1.0 93.1 ± 0.3 151.4 ± 2.5 –22.0 312
18 NTf2 1.8:1.0 93.8 ± 0.8 140.2 ± 3.2 –2.9 318
19 (IM) 1.5:1.0 93.8 ± 0.1 151.5 ± 0.3 –14.4 321
20 (124TRI) 1.5:1.0 95.1 ± 0.4 155.7 ± 0.5 –9.2 315
PIL networks were initially
analyzed by DSC to evaluate Tg and to
correlate to changes in network structure
(Table 2 and Figures S20–S22). An increase in the size
of the counteranion led to a decrease in Tg on the order of [Br] > [NO3] ≈ [BF4] > [OTf] > [NTf2], likely due to a plasticizing
effect
that is often observed in PILs with larger, more hydrophobic anions.
As expected, upon increasing the acrylate concentration and thus the
crosslink density, the Tg increased, given
the same counteranion [NTf2], with the 1.8:1.0 acrylate/acetoacetate
ratio PIL exhibiting the highest value of −2.9 °C. Changing
the cation led to little difference in Tg between the imidazolium and 1,2,3-triazolium PIL networks, however,
the 1,2,4-triazolium [NTf2] PIL was observed to have a
higher Tg value of −9.2 °C,
presumably due to the higher Lewis acidity of the cationic heterocycle,
thereby creating stronger ionic interactions within the network.34,35
TGA was utilized to investigate changes in thermal stabilities
(Td5%) as a function of structural changes
(Table 2 and Figures S23–S25). Analysis of the TPILs
with variable counteranion indicated once again reflected the correlation
between Lewis basicity and relative thermal stability in ILs and PILs.
Overall, [Br] PIL 12 was observed to have the lowest Td5% value (195 °C) than any of the other
counteranion systems due to its relatively high Lewis basicity. In
fact, Td5% values were found to be inversely
related to Lewis basicity on the order of [NTf2] > [OTf]
> [BF4] > [NO3] > [Br]. This trend
is analogous
to the previously discussed acetoacetate monomers, however, it is
worth noting that the PIL networks exhibit higher thermal stabilities
overall. Neither a change in crosslink density (acrylate/acetoacetate
ratio) nor in cation structure appeared to adversely affect thermal
stability, with all of the [NTf2] PIL networks exhibiting Td5% values in excess of 310 °C.
The
mechanical properties of the 1,2,3-triazolium-containing polyester
networks were analyzed using dynamic mechanical analysis (DMA). Networks
which employed different anions were compared initially (Figure 1a) and it was observed
that in general all of the TPILs exhibited similar rubbery plateau
moduli E′ above the Tg (Table 3).
Such a finding was further supported by apparent crosslink density
(ρx) values, which were calculated
from rubbery elasticity theory according to the following equation 1 where E′ is the storage
modulus at a temperature above the Tg (Pa), R is the gas constant (8.314 J mol/K), and T is the temperature (K).36 All ρx values were found to be in the range of
(5.30–6.76) × 10–4 mol/cm3 with no discernible correlation with anion size or Lewis basicity
(Table 3). In line
with the DSC Tg data, the DMA Tg values, as determined from the maximum of
the corresponding tan δ curves (Figure S26), showed a correlation with anion size, with PILs employing
the largest anions [NTf2] 16 and [OTf] 15 resulting in the lowest DMA Tg values (−2.40 and 13.8 °C, respectively) and the network
with the smallest anion, [Br] 12, exhibited the highest
DMA Tg (37.5 °C).
Figure 1 DMA storage modulus (E′) comparison of
TPIL networks: with (a) variation in counteranion; (b) variation in
acrylate/acetoacetate ratio; (c) variation in cation.
Table 3 Mechanical Properties of the TPIL
Networks
polymer anion Acr/AcAc ratio tan δ max Tg (°C) E′@100 °C (MPa) ρx × 10–4 (mol/cm3)
12 Br 1.5:1.0 37.5 6.29 6.76
13 NO3 1.5:1.0 23.7 5.08 5.46
14 BF4 1.5:1.0 24.3 6.18 6.64
15 OTf 1.5:1.0 13.8 5.79 6.22
16 NTf2 1.5:1.0 –2.4 4.93 5.30
17 NTf2 1.2:1.0 –7.6 2.57 2.76
18 NTf2 1.8:1.0 15.7 6.08 6.53
19 (IM) 1.5:1.0 –6.4 4.67 5.02
20 (124TRI) 1.5:1.0 5.6 5.67 6.09
Variation
in acrylate/acetoacetate ratio gave a predictable response
in the corresponding mechanical properties, where an increase in acrylate
concentration led to an increase in crosslink density, an increase
in E′ rubbery plateau modulus (Figure 1b), and an increase in DMA Tg (Figure S27). Interestingly,
a reduction in crosslink density led to an increase in the glassy
plateau modulus. Although additional structural characterization is
necessary, it is speculated that lower crosslinking may increase anion
aggregation resulting from improved ion mobility, leading to a higher
glassy plateau modulus. Variation in cation led to minimal change
in crosslink density or E′ rubbery plateau
modulus (Figure 1c);
however, the 1,2,4-triazolium PIL network 20 was found
to have a higher DMA Tg (Figure S28). As with the previously described DSC Tg data, this trend is presumably due to the
higher Lewis acidity/coordinating ability of the 1,2,4-triazolium
cation.
To evaluate the ionic conductivity of the networks,
frequency-dependent
dielectric spectra were collected on each TPIL over a range of temperatures.
Direct current conductivities (σ) were determined by first converting
dielectric loss spectra (ε″) to the real conductivity
(σ′) domain via the equation σ′ = ε″εoω, where εo is vacuum permittivity
and ω is angular frequency in rad/s. The real conductivity spectra
are characterized by a frequency-independent plateau region, and values
of σ were taken to be the plateau value. Exemplar real dielectric
(ε′), ε″, and σ′ spectra for
TPIL 14 at 80 °C are provided (Figure S29).
Once values were extracted from all spectra,
conductivities were
plotted for each TPIL as a function of temperature. These temperature-dependent
conductivities are shown in Figure 2. Much to our surprise, the TPIL networks exhibited
promising conductivities (10–6–10–9 S/cm at 30 °C, 30% RH) overall despite their crosslinked nature
and were comparable to several previously reported TPILs, including
those from our own laboratories (10–5–10–11 S/cm at 30 °C, 0–30% RH).22−27 Our initial hypothesis is that by anchoring the ionic groups into
a crosslinked network, a more uniform ionic material where ionic aggregation
is severely limited has been created, leading to better than expected
conductivities. The concept of uniform ion distribution (termed “percolated
aggregates”) has been proposed from experimental data37 and theorized in simulations38−40 for PILs where
ionic groups are polymerized into the backbone rather than left pendant
where aggregation is more probable. When comparing the behavior of
PILs having different anions (Figure 2a), it is clear that conductivity depends strongly
on polymer dynamics at lower temperatures. More precisely, lower temperature
conductivities vary inversely with PIL Tg. However, with elevating temperature, the conductivity curves for
various anions converge or crossover, highlighting an increasing dependence
on additional factors. A deeper exploration of the relative contribution
of TPIL properties to conductivity is presented later.
Figure 2 Ionic conductivity curves
(log σ vs 1000/T) for TPIL networks
with (a) variable counteranion; (b) variable
acrylate/acetoacetate ratio; (c) variable cation. The dashed curves
represent Vogel–Fulcher–Tamman (VFT) fitting curves.
When the anion is held constant,
but the acrylate/acetoacetate
ratio is varied (Figure 2b), the highest-Tg TPIL again displays
the lowest conductivity, whereas the lowest Tg PIL’s conductivity is greatest. Unlike the trend observed
with various anions, however, this Tg-dependent
pattern is preserved across the entire measured temperature range.
In addition, the relative differences in conductivities for the three
TPILs at any given temperature are reasonably consistent across all
temperatures. It should be noted that the ordering of the PILs having
different acrylate/acetoacetate ratio also matches what would be expected
based on ion content, i.e., the 1.2:1.0 ratio contains the greatest
ionic monomer content and displays the largest conductivity, whereas
the 1.8:1.0 ratio contains the least ionic monomer and concomitantly
the smallest conductivity. Therefore, the overall ion content of these
three PILs may also be contributing to observed behavior.
Similarly, Figure 2c depicts the temperature-dependent
conductivities of PILs where
the anion and ratio are held constant and the nature of the cation
is changed. As with the previous data, the three PIL’s conductivities
follow the inverse relationship to Tg across
the entire temperature range. The conductivity curve for the imidazolium
PIL does rise more steeply with temperature than either of the triazolium
PILs indicating there may be additional factors that govern ion transport.
For instance, the conductivity trend for cations also follows a pattern
associated to Lewis acidity of the cations (increasing conductivity
with decreasing acidity), which can influence strengths of ionic interactions
and thereby numbers of freely mobile anions in the PIL. All conductivity
curves were fitted to the Vogel–Fulcher–Tamman (VFT)
equation 2 where σ∞ is the infinite
conductivity limit, To is Vogel temperature
where ion motion stops, T is experimental temperature,
and D is the strength parameter, which is inversely
related to the fragility of polymer dynamics.14 The results from this fitting are shown in Table 4, and each dashed curve in Figure 2 depicts the VFT fit.
Table 4 Ionic Conductivity Data and VFT Fitting
Parameters for TPIL Networks
PIL network anion (cation) Acr/AcAc ratio σ at 30 °C (S/cm) σ∞ (S/cm) D To (K)
12 Br 1.5:1.0 6.5 × 10–9 9.0 8.4 217
13 NO3 1.5:1.0 1.3 × 10–7 1.2 7.5 207
14 BF4 1.5:1.0 6.2 × 10–8 10.7 8.1 213
15 OTf 1.5:1.0 2.5 × 10–7 2.8 8.2 202
16 NTf2 1.5:1.0 9.3 × 10–7 0.8 6.8 203
17 NTf2 1.2:1.0 1.7 × 10–6 10.7 11.5 175
18 NTf2 1.8:1.0 2.2 × 10–7 1.5 8.8 195
19 (IM) 1.5:1.0 4.1 × 10–7 5.6 10.8 183
20 (124TRI) 1.5:1.0 2.5 × 10–7 0.6 7.0 206
To elucidate the relative
contributions of Tg versus other factors
to PIL conductivity, each graph from Figure 2 was replotted using
an x-axis of Tg/T; these plots are shown in Figure 3. Such scaling of conductivity and other
transport data has been used to de-emphasize differences in polymer
segmental motion, to more clearly identify the extent to which other
factors impact results. The more strongly that chain dynamics impact
conductivity, the more that the individual conductivity plots will
converge into something akin to a master curve. This convergence is
most apparent with the data presented herein with conductivities for
TPILs in which acrylate/acetoacetate ratio is varied, Figure 3b. So, although those TPILs
vary in percentage of ionic subunits within the polymer, their conductivities
appear to depend primarily on polymer dynamics within the range of
temperatures studied. On the other hand, the conductivity profiles
for anion variation and cation variation, Figure 3a,c, do not converge well indicating that
other factors beyond polymer motion are contributing to observed behaviors.
Figure 3 Tg-normalized ionic conductivity curves
(log σ vs Tg/T) given (a) variable counteranion; (b) variable acrylate/acetoacetate
ratio; (c) variable cation. The dashed curves represent VFT fitting
parameters.
Models of electrode polarization
have been developed that can be
applied to dielectric spectra (both ε′ and ε″)
that allow the relative contributions of free-ion concentration (p) and free-ion mobility (μ) toward conductivity to
be determined. Electrode polarization results from an accumulation
of mobile ions at the electrodes and is most clearly manifested via
the rapid rise then plateau of ε′ when moving toward
the lower frequency end of that spectrum. The region of the spectra
where polarization dominates, then, can be described by modified MacDonald’s
theory using a Debye-type relaxation function 3 where εEP* is the complex dielectric function,
ΔεEP is the relaxation strength, τEP is the relaxation time (or time scale for full polarization),
and n is an exponent dependent upon electrode roughness.41−43 The relaxation time, then, can be correlated to μ and p through the following relationship 4 and relaxation
strength is equivalent to the
following 5 where LD, the
Debye length, is defined as 6 L is sample thickness/electrode
spacing, εs is the static dielectric constant, e is elementary charge, and k is Boltzmann’s
constant. Therefore, simultaneous fitting of temperature-dependent
ε′ and ε″ spectra with eq 3 allows for μ and p to be calculated as a function of temperature from fitting parameters.43
All of the obtained dielectric spectra
were well fit by the modified
Macdonald model except in the case of bromide-containing PIL 12. Example fits are shown in Figure S29 and a plot illustrating τEP as a function of temperature
for the variable cation and variable anion PILs is shown in Figure S30; values of n for
fitting ranged from 0.67 to 0.82. Applying multiplicative shift factors
to ε′ spectra for each PIL resulted in well-converged
master curves except in the case of [Br] 12 (Figure S31), and it appears that its polarization
region should be modeled by a modified or additional relaxation functions.
Attempts to include an interfacial polarization function in the fitting
for [Br] 12 proved unsuccessful in fully describing its
behavior.44,45 It should also be noted that fitting dielectric
spectra with Havriliak–Negami functions at frequencies higher
than the onset of electrode polarization were also attempted to explore
polymer segmental relaxations. However, high-frequency features were
subtle/weak (substantially dominated by electrode polarization) to
nonexistent in the studied frequency range. The inability to observe
such relaxations was confirmed via the use of derivative spectra (εder), which is supposed to aid in such evaluation by eliminating
contributions to the spectra from ion conduction.44
Plots of temperature-dependent free-ion concentration
and ion mobilities
obtained from dielectric fitting are shown in Figure 4. The temperature dependence of free-ion
concentration, or number density of conducting ions, is described
by an Arrhenius function 7 where p∞ is the high-temperature limiting concentration
and Ea is the activation energy for conducting
ions, which
can be thought of as a binding energy for an ion pair. Therefore,
the fitted line in Figure 4a was used to determine log p∞ from the y-intercept and Ea and from the slope. These values are shown in Table 5. The determined values of log p∞ are generally within the 21–22
cm–3 range, which is sensible based on a calculated
value for total possible free ions of approximately 21.1 cm–3 obtained from monomer stoichiometries and molar masses. Furthermore,
the activation energies of PILs 13–16 follow a pattern defined by the Lewis basicity of the anion, with
the most weakly basic [NTf2] forming the weakest ion pairs
and thereby having the lowest Ea, whereas
the most strongly basic [NO3] forms the strongest ion pairs
and requires the largest Ea.32 Similarly, variations in monomer cation (PILs 16, 19, and 20) result in Ea values that trend with the cations’
Lewis acidities, again corresponding to strength of ion pairing interactions.
Figure 4 Temperature-dependent
(a) free-ion concentrations and (b) ion mobilities
calculated from dielectric spectral fitting using the modified Macdonald
model. The dashed lines/curves illustrate the (a) Arrhenius or (b)
VFT fit to each data set.
Table 5 Free-Ion Concentrations and Ion Mobilities
for TPILs
PIL network anion (cation) log p∞ (cm–3) Ea (kJ/mol) log μ∞ (cm2/(V s)) D To (K)
13 NO3 21.59 25.28 –0.13 7.62 190.4
14 BF4 21.62 19.83 1.23 10.88 189.3
15 OTf 21.51 18.92 –1.54 2.98 237.1
16 NTf2 21.66 16.07 –2.57 2.09 242.8
19 (IM) 20.95 17.06 –1.74 2.14 247.4
20 (124TRI) 22.65 29.53 –2.54 1.26 254.0
Temperature-dependent ion mobilities, like conductivities,
are
described by a VFT fitting 8 where the parameters are defined similarly
to eq 2. The data and
VFT fit are shown graphically in Figure 4b, whereas obtained fitting parameters are
listed in Table 5.
With PILs that vary by anion, limiting mobilities increase with decreasing
anion size, except with [BF4] behaving as an outlier. Mobilities
of [BF4]-containing PILs that are 2 orders of magnitude
greater than [NTf2] PILs have been reported in the past,
though no other counteranions were included in that study.46 Furthermore, the [BF4] anion has
demonstrated limited stability in ILs, particularly at elevated temperature
and in the presence of water.47 Since high
temperatures were employed in this study, and measurements were not
made under anhydrous conditions, it is possible that [BF4] decomposition/hydrolysis may contribute to the behavior of TPIL 14, however, such analyses were beyond the scope of this work.
With the PILs where anion is constant, but cation is varied, the limiting
mobilities with [123TRI] and [124TRI] cations are very similar, but
[IM] is nearly an order of magnitude greater. It is likely that this
observed difference is due to crosslink density for [IM] being lower
than with the two triazolium PILs (see Table 3). With higher crosslink density, it is expected
that free ions would be required to take more tortuous paths during
conduction, thereby lowering their apparent mobilities.
Figure 5 shows the
ionic conductivity of TPIL [Br] 12 as a function of temperature
at three different relative humidity values (RH 30, 60, and 90%),
whereas Table 6 summarizes
the water uptake (wt %) of TPIL [Br] 12 at each of these
RH conditions after an overnight (16 h) soak (samples tested in triplicate).
The bromide conductivity increases approximately 4 orders of magnitude
when the RH was increased from 30 to 60%. A further increase of another
order of magnitude was observed when the RH was held at 90%. These
increases can be attributed to a water-assisted ion-transport mechanism,
commonly seen in PILs, which contain hydrophilic ions, such as halides.
Such a transport phenomenon has been likened to water–Nafion
systems and has been observed with other bromide-containing PIL co-polymers,
prepared from acrylic-functionalized imidazolium monomers.48 The strong likelihood of water-assisted bromide
transport is further supported by their noticeably large water uptake
(0.64–27.2 wt %) over the humidity range of interest (Table 6). Such a large increase
in ionic conductivity, as expected, was not observed for the highly
hydrophobic TPIL [NTf2] 16. For the more hydrophobic
PIL [NTf2] 16, ion transport would be more
strongly dictated by segmental motion and polymer dynamics. Although
their conductivities at higher % RH were not examined, it must be
noted that both the [NO3] and [BF4] TPIL networks
did exhibit some water absorption at 30% RH (Table S1), though not nearly to the extent that TPIL [Br] 12 did. Regardless, this small amount of water absorbed could result
in a slight enhancement of ionic conductivity that otherwise might
not be observed under anhydrous conditions.
Figure 5 Ionic conductivity curves
for TPIL [Br] 12, reflecting
the effect of variable relative humidity.
Table 6 Effect of Relative Humidity on Ionic
Conductivity and Water Uptake of the [Br] and [NTf2] TPIL
Networksa
30% RH 60% RH 90% RH
anion σ (S/cm) water uptake
(%) σ (S/cm) water uptake
(%) σ (S/cm) water uptake
(%)
Br 6.46 × 10–9 0.64 ± 0.05 3.16 × 10–5 7.90 ± 0.10 2.45 × 10–4 27.2 ± 0.4
NTf2 9.33 × 10–7 <0.01 9.98 × 10–7 0.05 ± 0.02 1.23 × 10–6 0.67 ± 0.13
a Data were obtained
after a 16 h
soak at 30 °C at the specified RH.
Ion mobility (μ) and free-ion concentration
(p) were investigated at 30 and 60% RH for the [Br]
and [NTf2] TPIL networks (Figure S32). Similarly
to what was noted above, the modified Macdonald model fit all data
well, except for [Br] at 30% RH. For [Br] at 30% RH, an interfacial
polarization function was added and while the addition still did not
fully describe the PIL’s behavior, it did provide enough information
such that reasonable humidity comparisons could be made. When humidity
was increased, ion mobility was found to increase for both TPIL networks,
presumably due to the plasticizing ability of water. Free-ion concentration
for the [Br] TPIL network was found to increase, but decrease for
the [NTf2] networks given an increase in humidity. This
observation is attributed to the ability of water to solvate bromide,
while causing the much more hydrophobic NTf2 anion to aggregate.
Unfortunately, the data acquired at 90% RH were such that these did
not allow for a proper fitting to determine μ and p parameters.
Conclusions
A series of 1,2,3-triazolium-based
bisacetoacetate monomers were
synthesized using an azide–alkyne click cyclization strategy
and subsequently polymerized using base-catalyzed Michael addition.
The resulting TPIL networks were analyzed for their thermal (DSC,
TGA), mechanical (DMA), and electrochemical (DRS) properties. The
counteranion, crosslink density (acetoacetate/acrylate ratio), and
cation were varied to observe changes in these properties.
DSC
thermal analysis of the TPILs indicated an inverse correlation
between Tg and counteranion size, with
[NTf2] TPIL exhibiting the lowest Tg. An increase in the Tg was observed
when the acrylate concentration was increased due to an increase in
covalent crosslinking. An increase in thermal stability (Td5%) was observed with decreasing Lewis basicity of the
anion on the order [NTf2] > [OTf] > [BF4] >
[NO3] > [Br]. Changes in crosslink density brought about
by varying the acrylate/acetoacetate ratio did not appear to affect
thermal stability. Dynamic mechanical analysis indicated that changes
in counteranion did not influence the rubbery plateau storage modulus
(E′) or the apparent crosslink density (ρx) in any discernable way, whereas DMA Tg (tan δ max) was observed to be
inversely related to counteranion size (supporting DSC Tg results). An increase in acrylate concentration did
result in an increase in E′ and crosslink
density. Despite the network nature of the TPILs, obtained conductivities
of 10–6–10–9 S/cm at 30
°C were comparable to a number of previously reported PILs. Ion
conduction demonstrated a reliance on polymer fluidity, especially
at lower measured temperatures. Analysis of dielectric data highlighted
a further dependence of conductivity on both Lewis acidity/basicity
of the employed cations/anions and on free anion size via those properties
influence on free-ion concentration and ion mobility, respectively.
Experimental
Section
Materials
All commercial reagents and solvents were
purchased from either Acros Organics or Sigma-Aldrich and used as
received. Tetrahydrofuran (THF) (99.9%) and N,N-dimethylformamide (DMF) (99.9%) were purchased as anhydrous
from Acros Organics and used as received. Ultrapure water having a
resistivity of 18 MΩ cm was produced using an ELGA Purelab Ultra
filtration device. A JEOL-ECS 400 MHz spectrometer was utilized to
obtain 1H and 13C NMR spectra, and chemical
shift values reported are referenced to residual solvent signals (CDCl3: 1H, 7.24 ppm; 13C, 77.16 ppm; DMSO-d6: 1H, 2.50 ppm; 13C,
39.52 ppm). Elemental analyses were completed by Atlantic Microlab,
Inc. The syntheses of 1-acetoacetoxy-6-bromohexane 4,19 1,4-bis(6′-acetoacetoxyhexyl)-1,2,4-triazolium
bis(trifluoromethylsulfonyl)imide 10,19 and 1,4-bis(6′-acetoacetoxyhexyl)-imidazolium bis(trifluoromethylsulfonyl)imide 11(17) have been previously reported.
Synthesis of Ethyl Ester 1
Ethyl-6-bromohexanoate
(10.0 g, 44.8 mmol), sodium azide (5.83 g, 89.6 mmol), and anhydrous
DMF (100 mL) were charged to a 250 mL round-bottom flask equipped
with a magnetic stir bar. The resulting mixture was stirred for 24
h at 60 °C. The reaction was then cooled to room temperature,
and trimethylsilylacetylene (5.72 g, 58.3 mmol) and copper(I) iodide
(1.11 g) were sequentially added. The reaction was stirred at room
temperature for 2 h, then warmed to 50 °C, and held for 24 h.
The mixture was then cooled to room temperature and poured onto ethyl
ether (300 mL). The organic phase was separated and washed with 150
mL portions of a 3:1 mixture of saturated NH4Cl/NH4OH until the aqueous wash layer was colorless (i.e., no blue
color). The organic phase was then further washed with brine, dried
over a mixture of Na2SO4/MgSO4, filtered,
and the solvent removed under reduced pressure to afford an orange
oil, which was immediately dissolved in anhydrous THF (50 mL). A 1.0
M solution of TBAF in THF (53.8 mL, 53.8 mmol of TBAF) was added,
and the resulting solution was stirred at room temperature overnight.
The residuals were removed under reduced pressure, and the crude oil
was dissolved in ethyl acetate and washed sequentially with 5% NaCl
solution twice and brine. The organic phase was separated, dried over
Na2SO4/MgSO4, filtered, and the solvent
removed to give a brown oil, which was purified by column chromatography
on silica gel with a gradient elution of 0–50% ethyl acetate
in hexanes. Purification resulted in 5.77 g of a light yellow oil
(61%). 1H NMR (400 MHz, CDCl3): δ 1.17
(t, 3H), 1.29 (m, 2H), 1.58 (m, 2H), 1.86 (m, 2H), 2.21 (t, 2H), 4.03
(t, 2H), 4.32 (q, 2H). 13C NMR (100 MHz, CDCl3): δ 14.29, 24.30, 25.96, 30.10, 33.98, 49.99, 60.39, 123.36,
133.81, 173.48. Anal. calcd for C10H17N3O2: C 56.85, H 8.11, N 19.89. Found: C 56.78, H
8.29, N 19.86.
Synthesis of 1-(6′-Hydroxyhexyl)-1,2,3-triazole 2
In a 500 mL, three-necked round-bottom flask was
dissolved the 1,2,3-triazole ester 1 (6.60 g, 31.2 mmol)
in dichloromethane (60 mL). The magnetically stirred solution was
cooled to 0 °C under N2 whereupon DIBAL-H (93.7 mL
of a 1.0 M solution in hexanes, 93.7 mmol) was added dropwise over
a 45 min period, followed by warming to room temperature where stirring
continued for 24 h. The reaction was then slowly quenched with 3.0
M HCl (30 mL), followed by the transfer of the reaction mixture into
a separatory funnel where the organic layer was separated. The aqueous
layer was extracted once with dichloromethane, and the organic layers
were combined, dried over Na2SO4/MgSO4, filtered, and the solvent removed under reduced pressure to afford
4.45 g of a light yellow oil (84%). 1H NMR (400 MHz, DMSO-d6): δ 1.21 (m, 2H), 1.27 (m, 2H), 1.36
(m, 2H), 1.80 (m, 2H), 3.35 (t, 2H), 4.33 (t, 2H), 7.70 (s, 1H), 8.11
(s, 1H). 13C NMR (100 MHz, DMSO-d6): δ 24.86, 24.99, 29.79, 32.28, 49.06, 60.51, 124.53,
133.14. Anal. calcd for C8H15N3O:
C 56.78, H 8.93, N 24.83. Found: C 56.49, H 9.17, N 24.56.
Synthesis
of 1-(6′-Acetoacetoxyhexyl)-1,2,3-triazole 3
1-(6′-Hydroxylhexyl)-1,2,3-triazole 2 (4.29
g, 25.4 mmol) was dissolved in acetonitrile (100 mL)
in a 250 mL round-bottom flask. tert-Butylacetoacetate
(12.03 g, 76.1 mmol) was then added, and the resulting magnetically
stirred solution was warmed to reflux and held for 2 h. Volatiles
were then removed under reduced pressure to afford 5.97 g (93%) of
a light orange oil. 1H NMR (400 MHz, DMSO-d6): δ 1.21 (m, 2H), 1.30 (m, 2H), 1.54 (m, 2H),
1.79 (m, 2H), 2.16 (s, 3H, CH3 on AcAc group), 3.57 (s,
2H, CH2 on AcAc group), 4.01 (t, 2H, J = 6.7 Hz), 4.33 (t, 2H, J = 7.2 Hz), 7.70 (s, 1H),
8.11 (s, 1H). 13C NMR (100 MHz, DMSO-d6): δ 24.63, 25.37, 27.78, 29.58, 30.10, 49.25,
49.55, 64.25, 124.53, 133.14, 167.14, 201.63. Anal. calcd for C12H19N3O3: C 56.90, H 7.56,
N 16.59. Found: C 56.58, H 7.56, N 16.32.
Synthesis of 1,3-Bis(6′-acetoacetoxyhexyl)-1,2,3-triazolium
Bromide 5
1-(6′-Acetoacetoxyhexyl)-1,2,3-triazole 3 (2.96 g, 10.9 mmol) and 1-acetoacetoxy-6-bromohexane 4 (2.97 g, 11.2 mmol) were added to a 25 mL round-bottom flask
and stirred at 60 °C for 48 h under an atmosphere of nitrogen.
The mixture was then cooled to room temperature and washed with ethyl
ether (4 × 20 mL). The product was dried under reduced pressure,
resulting in 4.30 g of an orange oil (91%). 1H NMR (400
MHz, DMSO-d6): δ 1.31 (m, 8H), 1.56
(m, 4H), 1.92 (m, 4H), 2.17 (s, 6H, CH3 on AcAc group),
3.59 (s, 4H, CH2 on AcAc group), 4.04 (t, 2H, J = 6.6 Hz), 4.64 (t, 2H, J = 7.1 Hz), 8.99 (s, 2H). 13C NMR (100 MHz, DMSO-d6): δ
24.50, 24.92, 27.70, 28.47, 30.00, 49.59, 52.95, 64.19, 130.87, 167.15,
201.49. Anal. calcd for C22H36N3O6Br: C 50.97, H 7.00, N 8.11. Found: C 50.85, H 7.03, N 8.02.
Synthesis of 1,3-Bis(6′-acetoacetoxyhexyl)-1,2,3-triazolium
Nitrate 6
To a 50 mL round-bottom flask equipped
with a magnetic stir bar was dissolved 1-(6′-acetoacetoxyhexyl)-1,2,3-triazolium
bromide 5 (1.80 g, 3.47 mmol) in deionized (DI) water
(10 mL). A solution of sliver nitrate (0.62 g, 3.65 mmol) in DI water
(5 mL) was added, and the reaction was stirred at room temperature
overnight in the dark. The mixture was then filtered through Celite
and dried under vacuum, resulting in 1.70 g of a light amber oil (98%). 1H NMR (400 MHz, DMSO-d6): δ
1.32 (m, 8H), 1.54 (m, 4H), 1.91 (m, 4H), 2.17 (s, 6H, CH3 on AcAc group), 3.59 (s, 4H, CH2 on AcAc group), 4.04
(t, 2H, J = 6.6 Hz), 4.62 (t, 2H, J = 7.1 Hz), 8.94 (s, 2H). 13C NMR (100 MHz, DMSO-d6): δ 24.48, 24.91, 27.69, 28.45, 30.06,
49.55, 51.50, 64.17, 130.79, 167.26, 201.62. Anal. calcd for C22H36N4O9: C 52.79, H 7.25,
N 11.19. Found: C 52.55, H 7.13, N 11.04.
Synthesis of 1,3-Bis(6′-acetoacetoxyhexyl)-1,2,3-triazolium
Tetrafluoroborate 7
To a 50 mL round-bottom
flask equipped with a magnetic stir bar was dissolved 1-(6′-acetoacetoxyhexyl)-1,2,3-triazolium
bromide 5 (2.00 g, 3.85 mmol) in DI water (20 mL). A
solution of sliver tetrafluoroborate (0.76 g, 3.89 mmol) in DI water
(5 mL) was added, and the reaction stirred overnight, in the dark,
at room temperature. The mixture was then filtered through Celite
and dried under vacuum, resulting in 1.91 g of a light yellow oil
(94%). 1H NMR (400 MHz, DMSO-d6): δ 1.32 (m, 8H), 1.56 (m, 4H), 1.91 (m, 4H), 2.17 (s, 6H,
CH3 on AcAc group), 3.59 (s, 4H, CH2 on AcAc
group), 4.04 (t, 2H, J = 6.4 Hz), 4.62 (t, 2H, J = 7.1 Hz), 8.92 (s, 2H). 13C NMR (100 MHz,
DMSO-d6): δ 24.47, 24.91, 27.69,
28.45, 30.07, 49.55, 53.02, 61.17, 130.77, 167.27, 201.63. Anal. calcd
for C22H36BF4N3O6: C 50.30, H 6.91, N 8.00. Found: C 50.12, H 6.88, N 7.88.
Synthesis
of 1,3-Bis(6′-acetoacetoxyhexyl)-1,2,3-triazolium
Triflate 8
To a 50 mL round-bottom flask equipped
with a magnetic stir bar was dissolved 1,3-bis(6′-acetoacetoxyhexyl)-1,2,3-triazolium
bromide 5 (1.20 g, 2.31 mmol) in DI water (15 mL). A
solution of silver triflate (0.61 g, 2.36 mmol) in DI water (5 mL)
was added. The mixture was stirred overnight at room temperature in
the dark and then filtered through a short pad of Celite, followed
by solvent removal under reduced pressure to afford 1.21 g (89%) of
a light yellow oil. 1H NMR (400 MHz, DMSO-d6): δ 1.31 (m, 8H), 1.56 (m, 4H), 1.93 (m, 4H),
2.17 (s, 6H, CH3 on AcAc group), 3.59 (s, 4H, CH2 on AcAc group), 4.05 (t, 2H, J = 6.6 Hz), 4.62
(t, 2H, J = 7.1 Hz), 8.92 (s, 2H). 13C
NMR (100 MHz, DMSO-d6): δ 24.47,
24.91, 27.69, 28.45, 30.07, 49.56, 52.98, 64.19, 120.68 (q, J = 322 Hz, −CF3), 130.82, 167.27, 201.61.
Anal. calcd for C23H36F3N3O9S: C 47.01, H 6.18, N 7.15. Found: C 46.98, H 6.14,
N 7.25.
Synthesis of 1,3-Bis(6′-acetoacetoxyhexyl)-1,2,3-triazolium
Bis(trifluoromethylsulfonyl)imide 9
1,3-Bis(6′-acetoacetoxyhexyl)-1,2,3-triazolium
bromide 5 (1.50 g, 2.89 mmol) was added to a 50 mL round-bottom
flask and dissolved in DI water (15 mL). Lithium bis(trifluoromethylsulfonyl)imide
(0.87 g, 3.04 mmol), dissolved in DI water (5 mL), was added to the
reaction, and the resulting mixture was stirred at room temperature
overnight. Dichloromethane (25 mL) was then added and the organic
phase was separated, washed with DI water (3 × 10 mL), and then
the solvent was removed under reduced pressure to afford 2.00 g (96%)
of a light yellow oil. 1H NMR (400 MHz, DMSO-d6): δ 1.32 (m, 8H), 1.56 (m, 4H), 1.91 (m, 4H),
2.17 (s, 6H, CH3 on AcAc group), 3.59 (s, 4H, CH2 on AcAc group), 4.04 (t, 2H, J = 6.4 Hz), 4.62
(t, 2H, J = 7.1 Hz), 8.92 (s, 2H). 13C
NMR (100 MHz, DMSO-d6): δ 24.48,
24.94, 27.71, 28.45, 30.08, 49.57, 53.00, 64.17, 119.43 (q, J = 319 Hz, −CF3), 130.84, 167.25, 201.55.
Anal. calcd for C24H36F6N4O10S2: C 40.11, H 5.05, N 7.80. Found: C 40.09,
H 5.01, N 7.93.
Procedure for Michael Addition Polymerizations
All
of the polymerizations were completed in dichloromethane (50 wt %).
In a typical procedure, 1,3-bis(2′-acetoacetoxyethyl)imidazolium
bis(trifluoromethylsulfonyl)imide 9 (0.90 g, 1.25 mmol)
and 1,4-butanediol diacrylate (0.37 g, 1.88 mmol, 1.5 M equiv) were
dissolved in dichloromethane (1.27 g). DBU catalyst (9.5 mg, 2 mol
%) was then added, and the resulting solution was mixed for 2 min.
The solution was poured into a PTFE mold and cured for 48 h at ambient
temperature, followed by curing in a 60 °C oven for 48 h. Complete
solvent removal and sufficient dryness prior to analysis were ensured
by placing the sample in a vacuum oven (<0.1 mmHg) for 24 h at
50 °C.
Polymer Analysis
All acetoacetate
monomers and PIL
network films were stored in a vacuum oven at 40 °C for 48 h
prior to any analytical testing. Differential scanning calorimetry
(DSC) was performed using a TA Instrument Q200 Differential Scanning
Calorimeter with a heating rate of 5 °C/min on 4–8 mg
samples. Glass transition temperatures (Tg) were determined from the second heating by the inflection point
of the curve observed. A TA Instrument Q500 Thermogravimetric Analyzer
was used to determine Td5%, the temperature
at which 5% weight loss was observed, at a heating rate of 10 °C/min
under an inert nitrogen atmosphere. The mechanical properties of the
TPIL networks were analyzed using a TA Instruments Q800 Dynamic Mechanical
Analyzer (DMA) in film tension mode (single frequency of 1 Hz) at
a heating rate of 5 °C/min. Soxhlet extraction in refluxing CH2Cl2 (24 h) was completed on all TPIL networks in
duplicate. The swollen sample was weighed (mwet) and then placed in a vacuum oven (60 °C, 24 h) to
obtain the dry weight (mdry). Gel fraction
was determined as follows: gel fraction = (mdry/mo) × 100 where mo is the original mass of the sample. Percent
swelling was calculated as follows: % swelling = (mwet/mo) × 100.16 The influence of water absorption was determined
for each TPIL network (in triplicate) by conditioning the sample in
the humidity chamber (Espec BTL-433 benchtop temperature/humidity
oven at 30, 60, 90% RH) for 16 h, followed by conductivity testing.
Water absorption was determined using the following equation: water
absorbed = ((mwet – mdry)/mdry) × 100.
Dielectric
Relaxation Spectroscopy
DRS was performed
with a Metrohm FRA32M frequency response analyzer coupled to an ECI10M
impedance interface and a custom-built (in-house) two-electrode cell
(Figure S17). The cell was placed inside
the aforementioned Espec BTU-433 controlled-temperature/humidity chamber
to maintain constant conditions (between 30 and 150 °C and 30%
RH) during each measurement. Sample membranes of ∼12 mm diameter
and 1 mm thickness were sandwiched between 304L stainless steel electrodes
separated by a 1 mm thick PTFE spacer. Electrodes were polished to
a mirror finish with 8000-, 14 000-, and 60 000-mesh
diamond paste (Sandvik Hyperion; Worthington, OH) prior to use. For
each sample, dielectric/impedance spectra were collected at various
temperatures using a frequency range of 1–107 Hz
and alternating current amplitude of ±0.01 V. The stray admittance
and residual impedance of the test cell were evaluated by open cell
(no sample) and shorted cell measurements, respectively, using the
same experimental conditions outlined above; shorted measurements
were performed using a 12 mm dia by 1 mm thick disk of 99.99% pure
Cu as the sample. Compensations for stray admittance and residual
impedance were applied to all data via Excel, as outlined elsewhere.49 Additionally, all measured values of real dielectric
(ε′) were corrected for contribution from the spacer
according to the method described by Johari.50
Supporting Information Available
The Supporting Information
is available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b01949.1H
and 13C NMR spectra for compounds 1–3 and 5–9 are provided along
with representative DSC and TGA data for each
of the diacetoacetate monomers 5–9; DSC thermograms; TGA traces and DMA tan δ curves for
TPIL networks 12–20; two-electrode
cell used in DRS measurements (PDF)
Supplementary Material
ao8b01949_si_001.pdf
The authors
declare no competing financial interest.
Acknowledgments
Acknowledgment
is made to the donors of the American Chemical
Society Petroleum Research Fund for support of this research (ACS
PRF# 53097-UNI7). Thermal and mechanical analyses were conducted in
the Polymer and Materials Science Laboratory (PMCL) at Murray State
University. DMA support was provided by the Department of Chemistry
at Murray State University as a result of support from the National
Science Foundation (Major Research Instrumentation) under DMR-1427778.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145782610.1021/acsomega.7b00891ArticleSelective Adsorption of Coronene atop the Polycyclic
Aromatic Diimide Monolayer Investigated by STM and DFT Geng Yanfang †§Wang Shuai †§Shen Mengqi †Wang Ranran ‡Yang Xiao ‡Tu Bin *†Zhao Dahui *‡Zeng Qingdao *†† CAS
Key Laboratory of Standardization and Measurement for Nanotechnology,
CAS Center for Excellence in Nanoscience, National Center for Nanoscience and Technology (NCNST), 11 Zhongguancunbeiyitiao, Beijing 100190, P. R. China‡ Beijing
National Laboratory for Molecular Sciences, The Key Laboratory of
Polymer Chemistry and Physics of the Ministry of Education, College
of Chemistry, Peking University, Beijing 100871, P. R. China* E-mail: tub@nanoctr.cn (B.T.).* E-mail: dhzhao@pku.edu.cn (D.Z.).* E-mail: zengqd@nanoctr.cn (Q.Z.).08 09 2017 30 09 2017 2 9 5611 5617 29 06 2017 25 08 2017 Copyright © 2017 American Chemical Society2017American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
The self-assemblies
of polycyclic aromatic diimide (PAI) compounds
on solid surfaces have attracted great interest because of the versatile
and attractive properties for application in organic electronics.
Here, a planar guest species (coronene) selectively adsorbs on the
helicene-typed PAI1 monolayer strongly, depending on the conjugated
cores of these PAIs. PAI1 molecule displays evidently a bowl structure
lying on the highly oriented pyrolytic graphite surface due to the
torsion of the “C”-shaped
fused benzene rings. In combination with density functional theory
calculation, the selective inclusion of coronene atop the backbone
of the PAI1 array might be attributed to the bowl structure, which
provides a groove for immobilizing coronene molecules. On the other
planar densely packed arrays, it is difficult to observe the unstable
adsorption of coronene. The selective addition of coronene molecules
would be a strategic step toward the controllable multicomponent supramolecular
architectures.
document-id-old-9ao7b00891document-id-new-14ao-2017-00891yccc-price
==== Body
Introduction
Two-dimensional (2D)
self-assemblies on a solid surface are an
interesting subject due to the promising perspectives in the nanotechnology
field.1−3 Although the exploitation of controlled supramolecular
chemistry has reached a maturity level where the specific self-assembly
can be predicted to high accuracy, controllable ordering in the multicomponent
architectures at the molecular scale remains a challenge. To obtain
well-defined complex structures, 2D multicomponent nanostructures
through the selective accommodation of many types of guest molecules
in various host template networks have attracted a great deal of attention
over the past decades.4,5 In most cases, the host molecules
formed 2D solid networks with suitable cavities for guest molecules,
and the inclusion of guest molecules cannot disturb the already existing
host network. The shape and size complementarities between the cavity
and guest molecule play an important role in the nanostructure. On
the other hand, there are a few cases of coassembly in which host
nanostructures on the solid surface were tuned by the inclusion of
guest molecules.6,7 The applications of host–guest
systems for the fixation of functional compounds have been hampered
by the inefficient understanding of the behavior of incorporation
of guest species on the host molecules.
Among the most studied
guest molecules, coronene (Cor), with sixfold
symmetry, displayed a stable adsorption structure on unmodified solid
surfaces, including various metal surfaces8,9 and
the highly oriented pyrolytic graphite (HOPG) substrate.10−12 In most reports, a single coronene molecule or clusters were confined
within various networks.13−27 Note that the uses of coronene to transform the self-assembled surface
structures have also been observed.16,17,19 In addition to the location of coronene in the host
cavity, there are some cases in which coronene molecules are partly
or completely located on the host molecules. Horn et al. found an
ordered second coronene layer on top of the first coronene layer due
to the coronene layer and substrate underneath.28,29 Zhang et al. observed a coronene layer on top of HPB-6pa network,
which might be attributed to the electronic interaction and van der
Waals interactions.30 Note that the cavity
of HPB-6a is slightly smaller than the size of the coronene molecule
by around 0.12 nm. Therefore, the adsorption site of coronene might
be attributed to many factors, like the substrate, the cavity of host
network, the host structure, and so on.
In this study, we designed
four polycyclic aromatic diimide (PAI)
derivatives, namely, PAI1 (N,N′-di(2-octyldodecyl)dibenzo[c,g]phenanthrene-1,2,5,6-tetracarboxyldiimide),
PAI2 (N,N′-di(2-octyldodecyl)benzo[k]tetraphene-5,6,12,13-tetracarboxyldiimide), PAI6 (N,N′-di(2-octyldodecyl)benzo[c]picene-7,8,15,16-tetracarboxyldiimide), and PAI8 (N,N′-di(2-octyldodecyl)benzo[c]naphtho[2,1-k]tetraphene-5,6,14,15-tetracarboxyldiimide),
as the target host molecules (Figure 1), which have the same alkyl chains but different backbone
blocks.31 The branched alkyl side chains
attached on the imide nitrogen atoms help in ensuring the stable adsorption
on the solid surface and the recognizable 2D structure. As a powerful
tool to study the molecular systems adsorbed on flat and conductive
solid substrates, scanning tunneling microscopy (STM) showed 2D self-assembled
monolayers formed by PAI derivatives at the 1-phenyloctane/HOPG interface.
Coronene molecules then periodically located on the specific highly
ordered PAI1 host array. In combination with density functional theory
(DFT) calculations, the results showed that coronene can only be immobilized
in the bowl structure, whereas it is unstable on the planar PAI2,
PAI6, and PAI8 monolayers. The formed Cor/PAI1 bilayer structure is
more thermodynamically favorable than that of the PAI1 system. It
is expected that systematic investigations may lead to control the
distribution and dispersion of guest molecules on or in the preformed
arrays on surface.
Figure 1 Chemical structures of four PAI-based compounds.
Results and Discussion
Self-Assembled 2D Structure
of PAIs
First, self-assemblies
of four PAI derivatives were investigated. Figure 2 displays the high-resolution STM images
of 2D molecular organizations. In each STM image, the brighter features
correspond to the conjugated backbone cores of the PAI derivatives,
whereas the darker areas are occupied by the alkyl chains. The orientation
of the backbones is parallel to each other, showing the formation
of striped patterns. It is noteworthy that PAI1 exhibits bright “V”-shaped
protrusion, indicating that the backbone of PAI1 is not parallel with
respect to the substrate surface.31−33 Such nonplanar geometry
might be attributed to the distortion of the C-shaped polycyclic skeletons.
The V-shaped configuration on the HOPG surface might come from the
interaction between the interdigitated alkyl chains as well as the
interaction between alkyl chains and the substrate. For PAI2, PAI6,
and PAI8 molecules, they all exhibit rodlike protrusions in the STM
images, indicating that their backbones are parallel to the HOPG surface.
Therefore, the interactions between adsorbates and the substrate determine
the stable adsorption of molecules on the surface. The unit cells
containing one PAI molecule are superimposed on the STM images, and
the unit-cell parameters are summarized in Table S1.
Figure 2 High-resolution STM images (15 nm × 15 nm) of molecule PAI1
(a), PAI2 (b), PAI6 (c), and PAI8 (d) at the 1-phenyloctane/HOPG interfaces.
The unit cells are inserted on the STM images. Tunneling parameters:
(a) 298.8 pA, 511.2 mV; (b) 299.1 pA, 567.3 mV; (c) 299.1 pA, 601.5
mV; and (d) 299.1 pA, 623.8 mV.
Although the distances between adjacent molecules are slightly
different, there are great changes in the parameter α in the
range of (82–99) ± 2°, indicating that the relative
orientations of these PAI compounds are largely different. The orientation
of the conjugated cores may be due to the hydrogen bond between −C=O
and H–C of the phenyl ring from adjacent two molecules. One
carbonyl group in PAI1 cannot form a hydrogen bond with the other
adjacent PAI1 molecule because the neighboring backbone of PAI1 rotates
out of the substrate surface. Additionally, the elastic alkyl chains
tend to be out of the surface upon the close-packed surface.34 In the cases of PAI2, PAI6, and PAI8, the carbonyl
groups are on the two sides of the conjugated center; therefore, there
might be two hydrogen bonds marked with red circles between two adjacent
molecules. In these STM images, the widths of dark stripes are measured
to be 1.2 ± 0.2 nm, which are consistent with the length of the
alkyl side chains.
The molecular models (Figure 3) corresponding to STM images were obtained
through
DFT calculation, which further confirm the molecular geometry on the
surface. The calculated interaction energies between adsorbates and
interaction energies between adsorbates and the substrate in these
systems are shown in Table 1. In these four systems, the interaction energies between
adsorbates are around 20 kcal mol–1, which result
from the interactions between interdigitated alkyl chains. Compared
with the other three systems, the slightly smaller intermolecular
interaction in PAI1 might be attributed to the curled alkyl chain
induced by the rotation of the backbone. The much larger interaction
energies between adsorbates and substrates of PAI2, PAI6, and PAI8
than those of PAI1 are consistent with the supposed configuration
of PAI1 above. The differences of adsorbate–substrate interaction
energies between PAI2, PAI6, and PAI8 might be due to the backbones.
These results provide evidence that the molecule–substrate
interaction is the predominant factor relative to the molecule–molecule
interaction. The low total energy per unit area in PAI1/HOPG systems
compared to that of other systems supports the only inclusion of coronene
molecules.
Figure 3 Molecular models (a)–(d) of self-assembled monolayers corresponding
to the STM images (a)–(d) in Figure 2, respectively. The unit cells are inserted
on the models.
Table 1 Calculated
Interaction Energies in
the Systems of PAI1/HOPG, PAI1 + Cor/HOPG, PAI2/HOPG, PAI6/HOPG, and
PAI8/HOPGa
interaction energies
between adsorbates (kcal mol–1) interaction energies between adsorbates
and
substrate (kcal mol–1) total energy (kcal mol–1) total
energy per unit area (kcal mol–1 Å–2)
PAI1 –20.121 –56.286 –76.407 –0.237
PAI1 + Cor –34.262 –133.794 –168.056 –0.458
PAI2 –21.712 –291.473 –314.185 –1.006
PAI6 –24.629 –332.837 –357.466 –1.058
PAI8 –23.966 –394.992 –418.958 –1.108
a Note that the more negative energy
means the system is more stable.
Selective Adsorption of Coronene on PAI1 Surface
Next,
the coadsorption behavior of the guest coronene in these self-assembled
patterns of PAI molecules was investigated. Except for the PAI1 monolayer,
STM observation showed no evidence that the coronene molecule can
be immobilized in other monolayers. In the large-scale STM image of
coronene/PAI1, as shown in Figure S1, the
stripes brighter than those of PAI1 were clearly visible, obviously
indicating the localization of coronene molecules. The high-resolution
STM image, as shown in Figure 4, shows that the V-shaped protrusion of PAI1 becomes circular
spots. A unit cell is superimposed upon the STM image with a = 2.9 ± 0.1 nm, b = 1.3 ± 0.1
nm, and α = 99 ± 2°, which is significantly different
from unit parameters of the parent PAI assembly (a = 2.7 ± 0.1 nm, b = 1.1 ± 0.1 nm, and
α = 92 ± 2°). The width of the bright stripe is consistent
with the diameter of the coronene plane parallel to the HOPG surface.
The cross-sectional profiles (Figure 4b) show that the bright stripe is located higher than
the darker stripe by around 0.1 nm in the PAI1 array, whereas the
bright stripe is located higher than the darker stripe by around 0.2
nm after deposition of coronene. Additionally, competitive adsorption
of coronene on the HOPG surface could not happen because there is
no coronene phase, as has been observed. If coronene molecules preferentially
adsorb on the HOPG surface, the structure of the PAI1 monolayer might
be disturbed. From these factors, the adsorbed coronene molecule is
expected to be located on
the PAI1 conjugated cores.
Figure 4 (a) High-resolution STM image of the self-assembled
densely packed
structure of Cor/PAI1/HOPG with the chemical structure of coronene
(15 nm × 15 nm; Iset = 268.8 pA; Vbias = 580.4 mV), (b) line profile of the PAI1
and Cor/API1 monolayer on the HOPG surface corresponding to the STM
images, (c) molecular model in image (a), (d) side view of the molecular
model in (c).
The coronene and conjugated
core of PAI1 cannot be resolved separately
due to the limited resolution. The appropriate position of the coronene
molecules can be identified by DFT calculation. The molecular model,
as shown in Figure 4c, reveals the formation of a two-layer densely packed structure
by specific adsorption of the coronene molecule on the bowl-conjugated
core of PAI1. Coronene displayed parallel configuration to maximize
the interaction between coronene and the substrate.35 The interaction energies, including intermolecular and
molecule–substrate, give more self-assembled information in
the whole system, as summarized in Table 1. The contributions for the stable assembly
of PAI compounds include the intermolecular interaction mainly coming
from the interdigitated alkyl chains and the interaction between PAI1
and the substrate. After addition of coronene molecules, the total
intermolecular interaction energy, including that between PAI1 molecules
and that between coronene and PAI1, was increased to −34.262
kcal mol–1. This might be attributed to the interaction
between the carboxyl oxygen atom and coronene. In other words, the
interaction between coronene and PAI1 contributes to the location
position of coronene. Note that the interaction energies between adsorbates
and the substrate largely increase up to −133.794 kcal mol–1, which indicates that there is a strong interaction
between the coronene/PAI1 system and HOPG substrate. The adsorption
of coronene molecules on PAI1 induced the increased stability of PAI1
on the HOPG substrate, leading to the increased interaction between
PAI1 and the substrate. Therefore, the ordered coronene layer might
be owing to the
PAI1 layer and the HOPG underneath. On the monolayers of PAI2, PAI6,
and PAI8, coronene molecules may tend to move because there is no
groove structure to immobilize the molecules, resulting in that stable
adsorption cannot be observed in STM images. In addition, DFT calculations
showed smaller interaction energies for coronene on these monolayers,
indicating that these are not preferable structures.
The total
energy per unit area obtained through considering all
possible interactions in the system offers an effective factor to
evaluate the thermodynamic stability of different arrays. The selectivity
of immobilization coronene in PAI1 can be explained by smaller total
energy per unit area of PAI1 + Cor/HOPG (−0.458 kcal mol–1 Å–2) system than that of PAI1/HOPG
(−0.237 kcal mol–1 Å–2), indicating the inclusion of coronene make the PAI1 monolayer more
table. This function of stability can be explained by the energy gain.
The resulting interaction between physisorbed host and coronene with
substrate overcomes the instability of the lower density of host matrix.
In presence of coronene guest molecules, the formation of honeycomb
network is thermodynamically favored.6,7 As a result,
the inclusion of coronene molecules in PAI1 monolayer should depend
on the properties of molecular template monolayers.
To study
the electronic interactions between the coronene molecules
and PAI1 monolayer as well as the substrate, we also calculated the
density of states (DOS) to discuss the energy level alignment at the
coronene/PAI1 interface.36,37 In Figure 5, the DOS for PAI1/HOPG and
Cor + PAI1/HOPG are shown. The increased total DOS structures indicate
that strong interaction between coronene molecules and PAI1/HOPG system.
The interaction between PAI1 and coronene molecule is calculated to
be −22.717 kcal mol–1. As shown in the enlarged
DOS diagram, the adsorption of coronene molecules induced the change
of energy-level alignment, which is expected to be used in organic
electronics.
Figure 5 Density of states (DOS) for the HOPG slab and PAI/HOPG
system before
and after adsorption of coronene molecules. Fermi energy is aligned
to 0 eV.
Conclusions
A
series of PAI derivatives assembled into densely packed monolayers,
in which only PAI1 can serve as a template for the immobilization
of coronene molecules. In contrast to the spatial selection in the
cavity, a close-packed coronene molecule atop the PAI1 monolayer has
been observed. The selective incorporation of coronene is explained
by the interaction energy on the basis of the theoretical calculations.
Many systems for further symmetrical studies are needed to study the
structures of templates which can adsorb coronene molecules, and it
is necessary to further explore efficient recipes to distinguish clearly
the specific position of guest molecules in the close-packed monolayer.
Experimental
Section
Materials
The syntheses of PAI derivatives were carried
out according to the previous report.31 Self-assembled PAI monolayers were prepared by directly dropping
the dilute solution of PAI derivative in 1-phenyloctane onto the freshly
stripped HOPG (grade ZYB) surface, which was purchased from Agilent.
The concentration of the solution was prepared to be less than 1.0
× 10–4 M to ensure the formation of highly
ordered structures. The solution of coronene in 1-phenyloctane with
the concentration of 1.0 × 10–2 M was prepared
and then was directly dropped onto the PAI monolayer. After a while,
a drop of 1-phenyloctane solution was deposited onto the preprepared
surface followed by STM record.
Measurement
STM
measurements were performed at the
1-phenyloctane/HOPG interface at room temperature (22–25 °C)
by using a Nanoscope IIIa (Agilent) with tips mechanically formed
from Pt/Ir (80/20). To obtain the topography image, constant-current
STM was performed by continuously adjusting the vertical position
of the STM tip. All of the tunneling conditions were given in the
corresponding figure captions.
Calculations
Theoretical
calculations were performed
using the DFT-D scheme provided by DMol3 code.38 We used the periodic boundary conditions (PBC) to describe
the 2D periodic structure on the graphite in this work. The Perdew–Burke–Ernzerhof
parameterization of the local exchange correlation energy was applied
in local spin density approximation to describe exchange and correlation.
All-electron spin-unrestricted Kohn–Sham wave functions were
expanded on a local atomic orbital basis. For the large system, the
numerical basis set was applied. All calculations were all-electron
ones and performed with the medium mesh. The self-consistent field
procedure was done with a convergence criterion of 10–5 au on the energy and electron density. Combined with the experimental
data, we have optimized the unit-cell parameters and the geometry
of the adsorbates in the unit cell. When the energy and density convergence
criterion are reached, we could obtain the optimized parameters and
the interaction energy between adsorbates. To evaluate the interaction
between the adsorbates and HOPG, we design the model system. In our
work, adsorbates consist of π-conjugated benzene rings. Because
adsorption of benzene on graphite and graphene should be very similar,
we have performed our calculations on infinite graphene monolayers
using PBC. In the superlattice, graphene layers were separated by
35 Å in the normal direction. When modeling the adsorbates on
graphene, we used graphene supercells and sampled the Brillouin zone
by a 1 × 1 × 1 k-point mesh. The interaction
energy Einter of adsorbates with graphite
is given by Einter = Etot(adsorbates/graphene) – Etot(isolated adsorbates in vacuum) – Etot(graphene). For the DOS calculations, k-point samplings for the Brillouin zone were performed
using the 5 × 5 × 1 Monkhorst–Pack k-point mesh.
Supporting Information Available
The Supporting Information
is available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.7b00891.Experimental and
calculated unit-cell parameters, large-scale
STM images of PAI1 and PAI1/coronene structure (PDF)
Supplementary Material
ao7b00891_si_001.pdf
Author Contributions
§ Y.G. and
S.W. equally contributed to this work.
The authors
declare no competing financial interest.
Acknowledgments
The authors
are sincerely thankful to the support from the
National Basic Research Program of China (2016YFA0200700) and National
Natural Science Foundation of China (Nos. 21472029, 21773041, and
51473003).
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145907810.1021/acsomega.8b00934ArticleSuperstructure-Dependent Loading of DNA Origami Nanostructures
with a Groove-Binding Drug Kollmann Fabian †Ramakrishnan Saminathan †Shen Boxuan ‡Grundmeier Guido †Kostiainen Mauri A. ‡Linko Veikko *†‡Keller Adrian *†† Technical
and Macromolecular Chemistry, Paderborn
University, Warburger
Str. 100, 33098 Paderborn, Germany‡ Biohybrid
Materials, Department of Bioproducts and Biosystems, Aalto University, P.O. Box 16100, FI-00076 Aalto, Finland* E-mail: veikko.linko@aalto.fi (V.L.).* E-mail: adrian.keller@uni-paderborn.de (A.K.).20 08 2018 31 08 2018 3 8 9441 9448 08 05 2018 03 08 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under a Creative Commons Non-Commercial No Derivative Works (CC-BY-NC-ND) Attribution License, which permits copying and redistribution of the article, and creation of adaptations, all for non-commercial purposes.
DNA
origami nanostructures are regarded as powerful and versatile
vehicles for targeted drug delivery. So far, DNA origami-based drug
delivery strategies mostly use intercalation of the therapeutic molecules
between the base pairs of the DNA origami’s double helices
for drug loading. The binding of nonintercalating drugs to DNA origami
nanostructures, however, is less studied. Therefore, in this work,
we investigate the interaction of the drug methylene blue (MB) with
different DNA origami nanostructures under conditions that result
in minor groove binding. We observe a noticeable effect of DNA origami
superstructure on the binding affinity of MB. In particular, non-B
topologies as for instance found in designs using the square lattice
with 10.67 bp/turn may result in reduced binding affinity because
groove binding efficiency depends on groove dimensions. Also, mechanically
flexible DNA origami shapes that are prone to structural fluctuations
may exhibit reduced groove binding, even though they are based on
the honeycomb lattice with 10.5 bp/turn. This can be attributed to
the induction of transient over- and underwound DNA topologies by
thermal fluctuations. These issues should thus be considered when
designing DNA origami nanostructures for drug delivery applications
that employ groove-binding drugs.
document-id-old-9ao8b00934document-id-new-14ao-2018-00934fccc-price
==== Body
Introduction
During the last three
decades, the field of structural DNA nanotechnology
has developed a variety of techniques to assemble DNA into increasingly
complex two-dimensional (2D) and three-dimensional (3D) nanostructures.1−3 Currently, DNA nanostructures and especially DNA origami4,5 are widely investigated with regard to their applicability in fields
as diverse as nanoelectronics,6−10 molecular sensing,11−14 and drug delivery.15−26 For the latter application, drug loading of the DNA origami delivery
systems has been achieved mostly via intercalation between the base
pairs of the DNA origami’s double helices.16−19,23,25,26 Intercalation
induces unwinding of the double helices and may therefore lead to
structural distortions of the DNA origami nanostructures.16,27 By employing DNA origami designs with deliberately underwound double
helices, however, intercalator loading of the DNA origami can be enhanced.16,28
The interaction of DNA origami with other chemical species
that
undergo nonintercalative binding to DNA is less studied. Opherden
et al. investigated Mg2+ and Eu3+ coordination
of two different DNA origami nanostructures, that is, 2D triangles
and 3D six-helix bundles (6HBs).29 By employing
a variety of spectroscopic techniques, a superstructure-specific geometry
of Eu3+-binding sites was revealed in the two DNA origami
designs that furthermore deviates from that of genomic double-stranded
DNA (dsDNA).
In this work, we investigate the binding of the
drug methylene
blue (MB) to different 2D and 3D DNA origami nanostructures under
conditions favoring minor groove binding and observe a strong dependence
on DNA origami superstructure. MB is a fluorescent azine dye that
is widely used as an optical and electrochemical probe molecule in
the study of DNA-based systems and reactions.30−33 In clinical practice, MB has
been used extensively as a therapeutic agent to treat numerous diseases,
including malaria and methemoglobinemia.34,35 More recently, MB has been rediscovered as a photosensitizer for
the photodynamic therapy of various viral, bacterial, and fungal infections,
as well as cancers.36−45 Consequently, also the delivery and controlled release of MB by
various carrier systems has received significant attention in recent
years.46−53
Results and Discussion
MB can interact with dsDNA via different
binding modes. At low
salt concentrations, intercalation into the G–C base pairs
is favored, whereas at the high salt concentrations typically
employed in DNA origami experiments, for example, 10 mM MgCl2 as used in the following experiments, a transition to nonintercalative
binding occurs.54−57 Irrespective of the binding mode, however, interaction of MB with
DNA is in general accompanied by a decrease in its absorption at 668
nm.57−59
In order to elucidate the nature of this nonintercalative
binding
mode, UV–vis absorbance spectra of MB with and without
genomic dsDNA from salmon testes were recorded at different ionic
strengths. This dsDNA has a GC content of 41% and is thus
comparable to the fully hybridized M13mp18-based DNA origami scaffold
with a GC content of 42%. As can be seen in the spectra presented
in Figure 1a,
the absorbance at 668 nm clearly decreases upon addition of dsDNA,
both in water and in 1× TAE (Tris base, acetic acid, and ethylenediaminetetraacetic
acid) buffer supplemented with 10 mM MgCl2. In water, this
hypochromicity is accompanied by a significant red shift of the absorbance
peak that results in a crossing of both spectral signatures at a wavelength
of about 680 nm. In TAE/MgCl2 buffer, however, this shift
is absent, indicating the nonintercalative binding of MB, which is
in agreement with previous reports.58,59
Figure 1 (a) UV–vis
absorbance spectra of 20 μM MB with and
without genomic dsDNA from salmon testes in water and MgCl2-containing TAE buffer. DNA concentrations were 13 μM (water)
and 11 μM (TAE + 10 mM MgCl2) in phosphates. In order
to enhance the signal-to-noise ratio and detect even small bathochromic
shifts, the shown spectra have been averaged over 10 individual absorbance
measurements. Individual spectra can be found in the Supporting Information. (b) UV–vis spectra of the competition
between 20 μM MB and 500 μM spermidine (left) and netropsin
(right), respectively, in 1× TAE buffer supplemented with 10
mM MgCl2. The spectra of the spermidine-containing samples
exhibited a broad background which has been subtracted in the above
plot. The concentration of the genomic dsDNA was 308 μM in phosphates.
In order to identify the nonintercalative
binding mode of MB, competition
assays were performed, employing spermidine and netropsin. While spermidine
can bind to both the minor and major grooves,60,61 netropsin is a potent minor groove binder.62,63 Depending on the binding modes of MB and the competing groove binder,
addition of a large excess of these groove binders will result in
its displacement from the minor groove, the major groove, or both,
and thereby reverse the hypochromicity observed upon MB binding to
the dsDNA. Indeed, as can be seen in Figure 1b, addition of both groove binders results
in a drastic increase in MB absorbance, which almost reaches the value
of free MB. This verifies the binding of MB to the minor groove of
dsDNA under the current buffer conditions, which also agrees with
previous theoretical predictions.64
Next, we set out to investigate the interaction of MB with a selection
of representative DNA origami nanostructures (see Figure 2). In particular, we chose
two 3D DNA origami nanostructures, that is, 6HBs65 and 60-helix bundles (60HBs).66 The 6HBs have previously been found to have an extraordinarily high
structural stability under physiological conditions, whereas more
complex 3D structures such as the 60HB are typically less stable.67,68 Furthermore, we also selected three differently shaped 2D DNA origami.
The Z shape69 is also designed on the honeycomb
lattice and features a chiral shape that may serve as an indicator
for visualizing MB-binding-induced structural distortions by atomic
force microscopy (AFM).27 The Rothemund
triangle,4 on the other hand, has previously
been identified as a potent drug delivery vehicle in vivo.18 It is designed on the square lattice and appears
highly strained (see the corresponding CanDo70,71 simulation in Figure 2). In order to evaluate the effect of such strain on MB binding,
we have also evaluated a more relaxed DNA origami structure in the
form of a bow tie that is designed on the same lattice but twist-corrected.69 These DNA origami nanostructures are characterized
by AFM in Figure 2,
both directly after assembly and after subsequent exposure to 20 μM
MB. Obviously, all DNA origami nanostructures remain intact upon MB
exposure. Furthermore, no major structural distortions induced by
MB binding can be observed by AFM. This is in agreement with the minor
groove binding of MB, which does not require any major structural
alterations of the DNA helices.54,55,64,72 Intercalators, on the other hand,
may induce unwinding of the helices and thereby twisting of the DNA
origami.16,27,28 Such a twisting
should be visible at least for the Z-shaped DNA origami.27
Figure 2 CanDo70,71 simulations and AFM images (1
× 1 μm2) of 6HBs (height scales 4.5 nm), 60HBs
(height scales 12
nm), Z-shaped DNA origami (height scales 3 nm), triangles (height
scales 3 nm), and bow ties (height scales 2 nm) before and after exposure
to 20 μM MB. The color coding in the CanDo simulations indicates
the lattice type (red—honeycomb, blue—square).
The binding of MB to these DNA
origami nanostructures was investigated
by UV–vis spectroscopy. In addition to the DNA origami, we
also used synthetic dsDNA (15 bp) with a GC content close to that
of the M13 scaffold (40%) as a reference. All the UV–vis spectra
shown in Figure 3a
were characterized by a decrease in the absorbance of MB at 668 nm
with increasing DNA concentration. As in the case of genomic dsDNA,
no bathochromic shift of the absorption peak is observed, indicating
the binding of MB to the minor groove.
Figure 3 (a) Representative UV–vis
spectra of 20 μM MB in 1×
TAE buffer containing 10 mM MgCl2 and different phosphate
concentrations of dsDNA and different DNA origami nanostructures,
respectively. The spectra are normalized to the absorbance at 668
nm in the absence of any DNA. (b) Representative normalized MB absorbance
at 668 nm as a function of phosphate concentration. (c) Corresponding
binding isotherms. The solid red lines in (c) are linear fits to the
data that have been used for the determination of Kd values. R2 values of the
fits are given in the plots. Error bars in (b,c) represent standard
deviations obtained by averaging over five individual measurements.
For Kd determination, these concentration-dependent
measurements have been repeated at least once (see Methods).
The normalized absorbance values shown in Figure 3b are found to saturate at
high DNA concentrations,
indicating that at these concentrations, all MB in solution is DNA-bound.
For all DNA origami nanostructures investigated here, saturation occurs
at phosphate concentrations between 35 and 55 μM and with different
saturation values of the absorbance. Also, the obtained loading efficiencies
differ significantly for the different DNA origami nanostructures
(see Table S1 for base pair contents) and
range from about 5700 MB molecules per DNA origami for the 60HB to
about 7400 for the bow tie (see Table S1).
The differences in the MB–DNA interaction observed
in Figure 3a,b were
assessed
more quantitatively by converting the concentration-dependent absorbance
values at 668 nm into binding isotherms (see Figure 3c) as described by Zhang and Tang.58 From the linear fits to the data shown in Figure 3c, dissociation constants Kd can be calculated as the ratio of intercept
and slope.58 This approach is frequently
employed for the quantitative investigation of the interaction of
DNA with both intercalators58,73 and groove binders.74,75
All the determined Kd values are
compared
in Figure 4. Obviously,
DNA origami 6HBs present a Kd value virtually
identical to that of synthetic dsDNA with the same GC content. This
is to be expected because the 6HBs have been designed on a honeycomb
lattice with 10.5 bp per helical turn and should thus exhibit a DNA
topology close to the canonical B-form. The same argument of DNA topology
also holds true for the 60HB, which indeed has a similar Kd as the 6HB and the dsDNA. Although in such compact 3D
DNA origami nanostructures, access of MB to the inner helices may
be restricted because of the shielding by the outer helices, this
effect appears to be of minor importance in the 60HB.
Figure 4 Determined Kd values for the investigated
DNA structures. Values are presented as averages over n independent
concentration series with the standard error of the mean as error
bars (see Methods).
Such geometric effects, however, should be entirely absent
in structures
that consist just of a single honeycomb “unit cell”
such as the 6HB or in objects that are purely two-dimensional. The
latter is true for the Z-shaped 2D DNA origami that was constructed
using the honeycomb lattice and is thus designed to exhibit 10.5 bp/turn
just as the 6HB and the 60HB. Surprisingly, however, the Kd determined for the Z-shaped DNA origami is more than
twice as large as those of the 6HB and the dsDNA (see Figure 4). On the basis of the overlap
rule of standard error bars,76 the difference
between the Z shape and the dsDNA is estimated to be statistically
significant with p < 0.05.
In addition to
the honeycomb lattice-based DNA origami, we have
also evaluated MB binding to two 2D DNA origami nanostructures based
on the square lattice.4,69 These structures are designed
with 10.67 bp/turn and thus exhibit DNA topologies different from
the canonical B-form of dsDNA.4 Efficient
minor groove binding of MB64,72 and other molecules77,78 typically requires a tight fit. Therefore, underwinding of the helices
will result not only in an increased spacing of base pairs but also
in a widened minor groove79 and should
thereby reduce the binding affinity of MB. This is in contrast to
the case of intercalation, where underwinding results in lower Kd values because of easier access to the widened
gaps between base pairs.16,28 In agreement with this
hypothesis, both DNA origami triangles and twist-corrected bow-tie
structures show Kd values slightly higher
than that of dsDNA, although the effect is surprisingly small (see Figure 4).
Of all the
DNA origami nanostructures studied in this work, the
Z shape shows the strongest deviation from B-DNA, even though it is
designed on the same honeycomb lattice as the 6HB and the 60HB, both
of which show Kd values similar to dsDNA.
We speculate that the high Kd of the Z-shaped
DNA origami is caused by the presence of DNA topologies different
from the canonical B-form. Despite being based on the honeycomb lattice,
such non-B topologies may occur transiently, that is, resulting from
thermal fluctuations. In the Z-shaped DNA origami, all helices are
aligned parallel to its long axis, including those in the two arms
(see Figure 2). These
arms are therefore comparatively floppy and subject to strong fluctuations.
These fluctuations travel from helix to helix via the crossovers,
thereby inducing an oscillatory over- and underwinding of the helices
in the vicinity of the crossovers (see CanDo70,71 simulations in the Supporting Information). Because groove binding requires a tight fit, both over- and underwinding
will result in reduced binding and in sum to an increased Kd. The bow-tie design also features only parallel
helices and could therefore show a similar behavior as the Z shape.
However, because of the intrinsic underwinding of the helices in the
square lattice, fluctuations in the bow tie may lead even to slightly
improved groove binding because of the occurrence of transient B-form
topologies. Note that in the case of intercalation, such fluctuations
will not lead to different Kd values because
here overwinding and underwinding result in lower and higher binding
affinities, respectively, and thus compensate each other.
Conclusions
In conclusion, we have investigated the interaction of the drug
MB with different DNA origami nanostructures under conditions that
result in binding to the minor groove. The DNA origami superstructure
is found to have a noticeable influence on the binding efficiency
of MB. In particular, non-B topologies as for instance found in designs
using the square lattice with 10.67 bp/turn may result in reduced
binding affinity. Furthermore, also flexible DNA origami shapes that
are prone to structural fluctuations may exhibit reduced groove binding
because of the induction of transient over- and underwound DNA topologies.
These issues should be considered when rationally designing DNA origami
nanostructures for drug delivery applications employing groove-binding
drugs.
Methods
Preparation of dsDNA Samples
For
the initial experiments
addressing the binding mode of MB, lyophilized genomic dsDNA from
salmon testes (Alfa Aesar) was dissolved at the desired concentration
either in high-performance liquid chromatography (HPLC)-grade water
(Carl Roth) or in 1× TAE (Calbiochem) with 10 mM MgCl2 (Sigma-Aldrich). MB, spermidine, and netropsin (all Sigma-Aldrich)
were added to achieve the desired concentrations.
For comparison
with the DNA origami nanostructures, synthetic dsDNA was prepared
by hybridization of two complementary oligonucleotides (Metabion)
with the sequences 5′-TTG GAA CAG CAT TGA-3′ and 5′-TCA
ATG CTG TTC CAA-3′. To this end, the readily mixed sample (100
μM of each strand in 1× TAE with 10 mM MgCl2) was heated to 94 °C in a thermocycler Primus 25 advanced (PEQLAB),
kept at this temperature for 5 min, and cooled down to 20 °C
with a cooling rate of 1.5 °C per minute.
DNA Origami Synthesis and
Purification
All DNA origami
nanostructures were fabricated as previously reported (see below).
All structures are based on the 7249 nt long M13mp18 scaffold (purchased
from Tilibit Nanosystems).Triangle:
the staple sequences (purchased from Metabion)
are taken from the article by Rothemund.4 DNA origami assembly was performed as previously described.80
6HB: the staple
sequences (purchased from Metabion)
are taken from the article by Bui et al.65 DNA origami assembly was performed as previously described.81
60HB: the staple
sequences and the exact fabrication
protocol (20 nM reactions) can be found in the article by Linko et
al.66 Staple strands were purchased from
IDT.
Z shape and bow tie: the staple
sequences and the exact
fabrication protocol (20 nM reactions) can be found in the article
by Shen et al.69 Staple strands were purchased
from IDT.
After assembly, the DNA origami
nanostructures were
purified as described previously80 by spin-filtering
(Amicon Ultra filters from Millipore with 100 kDa molecular weight
cutoff) and washing with 1× TAE supplemented with 10 mM MgCl2.
Determination of DNA Origami Concentrations
The concentrations
of the DNA origami after purification were determined by UV–vis
absorbance measurements using an Implen Nanophotometer P330 operated
in dsDNA mode. Because different DNA origami nanostructures feature
different numbers of base pairs and unpaired nucleotides, the so-determined
concentration values had to be corrected.
The measured concentration cm is a result of the combined absorption the
single-stranded DNA (ssDNA) and the dsDNA fractions in the DNA origami.
Because the extinction of ssDNA is about 1.5 times higher than that
of dsDNA,82 the real concentration creal is given by Here, x is the fraction of
paired bases relative to the total number of nucleotides (paired and
unpaired) in the DNA origami. The numbers of base pairs and nucleotides
of the DNA origami used in this work are given in Table S1.
UV–Vis Spectroscopy
UV–vis
absorbance
spectra with a spectral range from 200 to 800 nm were recorded with
an Implen Nanophotometer P330 equipped with a sub-microliter cell.
The sample volume for each measurement was 2 μL. After each
measurement, the cell was washed at least twice with HPLC-grade water.
To record the UV–vis spectra of samples with different DNA
concentrations, a 20 μM MB solution in 1× TAE with 10 mM
MgCl2 was measured first. Then, a small aliquot of a DNA-containing
solution (80–300 μM in phosphates depending on the DNA
structure, 1× TAE, 10 mM MgCl2, 20 μM MB) was
added to the initial MB solution and mixed well. After recording the
UV–vis spectra of the resulting solution, the addition and
measurement cycle was repeated several times to record a complete
concentration series.
Determination of Kd Values
For the determination of the dissociation constants,
the measured
absorption at 668 nm was averaged over at least five individual measurements
at each DNA concentration in a concentration series, and the resulting
standard deviations were treated as error limits. After transforming
the data according to the protocol of Zhang and Tang,58 the Kd of each concentration
series was determined from a linear fit to the data with instrumental
weighting of the errors (see below). For each DNA origami, this determination
of Kd has been performed for two to three
independent concentration series. The so-obtained Kd values for each DNA origami were averaged, and the error
limits of the individual linear fits were used for determining the
standard error of the mean for each Kd value given in Figure 4 via propagation of error (see Table S3).
The binding constant Kd follows from the relation Here, [Pho] refers
to the molar concentration
of phosphates, which has been used instead of the concentration of
base pairs in order to account for the different fractions of paired
and unpaired nucleotides in the different DNA origami designs. Δεap is the difference between the measured extinction coefficient
of the DNA–MB solution, εa, which features
both DNA-bound and free MB and the extinction coefficient of free
MB in a solution without DNA, εf, with Here, εa and εf are determined
by dividing the measured absorbance values
by the molar MB concentration, which was kept constant at 20 μM
in all experiments.
Δε represents the difference
of the extinction coefficients
of DNA-bound MB, εb, and free MB, εf, that is,
The dissociation constant Kd is
then
determined by plotting versus [Pho] and fitting the data with
a linear function. In this case, the linear fit has a slope of and intercepts the y-axis
at . Therefore, dividing
the intercept by the
slope yields the binding constant Kd.
AFM Imaging
For AFM imaging, a 5 μL droplet of
each DNA origami sample (10 nM in 1× TAE with 10 mM MgCl2) with or without 20 μM MB was deposited on a freshly
cleaved mica substrate. After adding 100 μL of 1× TAE with
10 mM MgCl2 to spread the sample over the whole substrate
surface, the sample was incubated for 5–15 min, subsequently
dipped in HPLC-grade water, and dried in a stream of ultrapure air.
AFM imaging was performed in air using Agilent 5100 AFM in intermittent
contact mode and HQ:NSC18/Al BS cantilevers from MikroMasch.
Supporting Information Available
The Supporting Information is
available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b00934.Individual UV–vis
absorbance spectra of MB–DNA
binding in water and buffer, paired and unpaired bases in the different
DNA origami designs, netropsin competition assay for the different
DNA origami nanostructures, additional independent concentration series
and binding isotherms, loading efficiency of MB, and averaging of Kd values (PDF)
CanDo simulations of the Z-shaped DNA origami
- top
view (AVI)
(AVI) CanDo simulations of
the Z-shaped DNA origami - side view 1 CanDo simulations of the Z-shaped
DNA origami - side view 2
(AVI)
Supplementary Material
ao8b00934_si_001.pdf
ao8b00934_si_002.avi
ao8b00934_si_003.avi
ao8b00934_si_004.avi
Author Contributions
The manuscript
was written through contributions of all authors. All authors have
given approval to the final version of the manuscript.
The authors
declare no competing financial interest.
Acknowledgments
We thank K. Fahmy for many valuable
discussions.
Financial support from the Academy of Finland (grant nos. 286845 and
308578), the Sigrid Jusélius Foundation, and the Jane and Aatos
Erkko Foundation is gratefully acknowledged.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145896010.1021/acsomega.8b01176ArticleHardwood Kraft Lignin-Based Hydrogels: Production
and Performance Zerpa Alyssa Pakzad Leila Fatehi Pedram *Chemical Engineering Department, Lakehead University, 955 Oliver Road, Thunder
Bay, Ontario, Canada P7B 5E1* E-mail: pfatehi@lakeheadu.ca. Tel: 807-343-8697. Fax: 87-346-7943.24 07 2018 31 07 2018 3 7 8233 8242 29 05 2018 16 07 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
In this study, hydrogels
were synthesized through the radical polymerization
of hardwood kraft lignin, N-isopropylacrylamide,
and N,N′-methylenebisacrylamide.
Statistical analyses were employed to produce lignin-based hydrogels
with the highest yield and swelling capacity. The success of the polymerization
reactions was confirmed by NMR and Fourier infrared spectroscopy.
The lignin-based hydrogel was more thermally and rheological stable,
but exhibited less swelling affinity, than synthetic hydrogel. The
rheological studies indicated that the swollen hydrogels were predominantly
elastic and exhibited a critical solution temperature that was between
34 and 37 °C. Compared with the synthetic hydrogel, lignin-based
hydrogel behaved less elastic as temperature increased. In addition
to inducing a green hydrogel, the results confirmed that hardwood
lignin-based hydrogel would have different properties than synthetic-based
hydrogels, which could be beneficial for some applications.
document-id-old-9ao8b01176document-id-new-14ao-2018-011764ccc-price
==== Body
Introduction
Hydrogels are often described as three-dimensional
polymeric networks
formed from cross-linked hydrophilic homopolymers, copolymers, or
macromers.1−4 They are insoluble polymer matrices capable of retaining a large
amount of water in their swollen state; in some cases, up to a thousand
times of their dry weight. Their swelling capability allows them to
obtain the shape of their surroundings when confined.2,5,6
Depending on the source
of polymers, hydrogels may be synthetic,
natural, or hybrid.2 Hydrogels may be degradable
in aqueous environments, making them biocompatible in most cases and
a good carrier for nutrients to cells and their metabolic products.5 They have been deemed to be efficient in the
protection of cells and fragile drugs, such as peptides and proteins.5 Some hydrogels have exhibited stimuli-induced
swelling and deswelling capabilities without disintegration.7−9 The advantage of tunable properties has given hydrogels attention
for biomedical and environmental applications.10,11 Poly (N-isopropylacrylamide) (PNIPAAm) is a thermoresponsive
hydrogel.12−14 However, the applications of PNIPAAm hydrogels are
limited by their fragility.15,16 These applications
can be extended via enhancing their rigidity.
Recently, lignin
(LGN) has been incorporated into the production
of flocculants, dispersants, and hydrogels because lignin is biocompatible
and biodegradable with low toxicity.17−20 At a relatively low production
cost,21 lignin presents the greatest available
aromatic renewable resource worldwide, as well as a primary supplier
of soil’s organic matter.6,22 Lignin provides the
structural strength of plants by nature, which makes it a potential
candidate for PNIPAAm hydrogel modifications.
Previous studies
have been conducted on synthesizing hydrogels
using different types of lignin through free radical polymerization.
Acetic acid lignin was incorporated into N-isopropylacrylamide
(NIPAAm) for hydrogel production.23 The
kinetics studies indicated that the lignin-containing hydrogel retained
7.2% more water than the lignin-free hydrogel over 10 min of swelling.23 In another work, wheat straw alkali lignin was
cross-linked with acrylic acid and N,N′-methylenebisacrylamide (MBAAm) via free radical polymerization.24 The addition of acid hydrolysis lignin was found
to greatly improve the surface morphology and swelling affinity of
the hydrogel.25 Yu et al. developed lignosulfonate-g-acrylic acid hydrogels by grafting acrylic acid onto lignosulfonate
with MBAAm as a cross-linker and lacase/tert-butyl
hydroperoxide as the initiator.26
It is well known that the type of lignin (i.e., hardwood vs softwood
vs nonwood) and its production process (i.e., enzymatic hydrolysis
vs kraft vs sulfite treatment) affect its structure and chemical properties,
which, in turn, affect its polymerization performance and end-use
applications.27−32 There is currently limited research on the use of hardwood kraft
lignin for hydrogel production following free radical polymerization.
As hardwood is vastly available for end-use applications, it is of
great importance to investigate the performance of hardwood lignin
for hydrogel productions.17−21
The first objective of this study was to evaluate the cross-linking
of hardwood-based kraft lignin with NIPAAm as the monomer and MBAAm
as the cross-linker. The second objective of this study was to investigate
the thermal and rheological properties of kraft lignin-based hydrogels,
as well as their swelling performance. The main novelty of this work
was the investigations on the use of hardwood kraft lignin as a commercially
available resource in hydrogel production and on the properties and
performance of the induced hydrogels under different scenarios.
Results
and Discussion
Polymerization
The free radical
polymerization for
producing lignin-based hydrogels is demonstrated in Figure 1. Azobisisobutyronitrile (AIBN)
first undergoes thermal decomposition to generate radicals, which
initiates the polymerization. Figure 1a demonstrates the thermal decomposition of the azo
compounds with heating, which produces two 2-cyanoprop-2-yl radicals
and nitrogen gas.33 In this case, 2-cyanoprop-2-yl
radicals can then be transferred to lignin, NIPAAm, or MBAAm present
in the reaction mixture. When the free radical is transferred to lignin,
it will abstract hydrogen from the hydroxyl group located on lignin’s
aromatic ring generating a phenoxy radical (I in Figure 1b) along with the corresponding
resonance structures (II in Figure 1b).33 The phenoxy radicals
will then attack the carbon double bonds of the NIPAAm monomers and
the cross-linker MBAAm to form the initial propagating chain, which
can then continue further to form the cross-linked structure (Figure 1c). The radical polymerization
is most commonly terminated through the combination of two active
chains.34 In addition, termination may
occur via adjusting pH (i.e., sulfuric acid and sodium hydroxide).
Figure 1 Radical
polymerization reaction for lignin-based hydrogel production:
(a) decomposition of AIBN initiator, (b) formation of phenoxy radicals,
and (c) cross-linking reaction.
Effect of Reaction Conditions
Taguchi L9 orthogonal
design is presented in Table 1. Typically, NIPAAm and MBAAm are used together to form hydrogels,
and only using one of them cannot facilitate hydrogel production.
Generally, the ratio of reactants affects the properties of the induced
products in reactions. Compared with other reactants in this polymerization
reaction system, lignin is more difficult to handle in terms of its
solubility, reactivity, and pH adjustment in solutions. Therefore,
to have a better control over the reactions, we decided to keep the
amount of lignin constant in the reactions but to change the quantity
of other components of the reaction. The range of analysis was optimized
by evaluating the signal-to-noise (SN) ratio to maximize the responses
of the model. The hydrogel sample of 2L was selected as the best hydrogel
sample based on the results achieved. The control sample (2C) was
produced following reaction conditions of 2L but without lignin.
Table 1 Taguchi L9 Orthogonal Design Parameters
run temperature
(°C) time (h) NIPAAm content
(g) pH yield (wt %) maximum swelling
ratio (g/g) S/NLB
1L 65 3 1.2 2.0 76.09 15.41 24.62
2L 65 4 1.8 2.5 77.86 32.59 26.30
3L 65 5 2.4 3.0 80.7 20.19 25.41
4L 75 3 1.8 3.0 49.33 24.08 25.66
5L 75 4 2.4 2.0 84.57 14.00 24.67
6L 75 5 1.2 2.5 91.93 19.03 25.25
7L 85 3 2.4 2.5 65.49 21.76 25.58
8L 85 4 1.2 3.0 83.63 34.39 25.61
9L 85 5 1.8 2.0 90.67 20.91 25.74
Multivariate analysis (MANOVA) was
applied to determine whether
there are differences among the levels and factors. A 95% confidence
interval was selected, implying that the response is deemed significant
if the P-value is smaller than 0.05.35 Furthermore, post hoc analysis was applied to determine
where these significant differences exist when considering multiple
levels.36 Tukey’s test was selected
as an effective post hoc model to compare all the possible pairs of
means and determine where they differ within the data.36−38Table 2 demonstrates
the results of the MANOVA for the responses of lignin-based hydrogels.
It is observable that temperature presents a significant effect on
yield (F = 7.84, p = 0.011, η2 = 0.635) and maximum swelling ratio (F =
14.07, p = 0.002, η2 = 0.076). The
cleavage of the azo compounds may occur more rapidly at higher temperatures,
increasing the concentration of radicals present in the solution and
facilitating the reaction.39 This table
also shows that the reaction time presented a large effect with respect
to yield (F = 222.24, p < 0.001,
η2 = 0.980). This is because the time extension allows
for additional cross-linking to occur in the reaction, resulting in
a higher product yield. A significantly large decrease in yield (F = 43.00, p < 0.001, η2 = 0.905) and swelling capacity (F = 16.67, p = 0.001, η2 = 0.787) with increasing
NIPAAm content was determined between 18 and 24 g/g of lignin. The
higher incorporation of monomer into the hydrogels was found to improve
the hydrogel production. Furthermore, the yield (F = 50.89, p < 0.001, η2 = 0.919)
and the maximum swelling ratio (F = 32.00, p < 0.001, η2 = 0.877) exhibit a significant
effect between pH 2.0 and pH 2.5. This is most likely because concentration
of sulfate ions in the reaction mixture leads to the abstraction of
the terminated polymer chains, which, in turn, reinitiates the propagation
step.40
Table 2 Multivariate Analysis
of the Taguchi
L9 Orthogonal Model for the Lignin-Based Hydrogels
source dependent
variable sum of squares degrees of
freedom mean square F-value P-value η2 observed
power
model yield 2852.78 8 356.60 80.10 0.000 0.986 1.000
swelling ratio 777.82 8 97.23 20.53 0.000 0.948 1.000
temperature
(°C) yield 69.07 2 34.54 7.84 0.011 0.635 0.852
swelling ratio 133.27 2 66.63 14.07 0.002 0.758 0.983
time (h) yield 1956.94 2 978.47 222.24 0.000 0.980 1.000
swelling ratio 183.67 2 91.83 19.39 0.001 0.812 0.998
NIPAAm content
(g) yield 378.66 2 189.33 43.00 0.000 0.905 1.000
swelling ratio 157.85 2 78.92 16.67 0.001 0.787 0.993
pH yield 448.11 2 224.05 50.89 0.000 0.919 1.000
swelling ratio 303.03 2 151.52 32.00 0.000 0.877 1.000
pure error yield 39.62 9 4.40
swelling ratio 42.61 9 4.73
corrected total yield 2892.41 17
swelling
ratio 820.43 17
Table 3 compares
the means and standard deviations for both responses, as well as the
associated coefficients. The responses exhibited a low coefficient
of variation, implying that the obtained data are considered as precise
and repeatable.41
Table 3 Descriptive
Statistics
95% confidence interval
dependent
variable standard
deviation mean lower bound upper bound coefficient
of variation (%)
yield 2.10 77.77 76.65 78.89 2.70
swelling ratio 2.18 22.48 21.32 23.64 9.68
To determine which
lignin-based hydrogel sample exhibited the best
responses, the signal-to-noise (SN) ratio was determined in the Taguchi
analysis. Because the goal for this experiment was to maximize the
response values, the larger-the-better (LB) SN ratio equation, eq 1, was selected42 1 where n is the number of
experiments and yi is
the collected experimental data. The optimal level can then be determined
by selecting the largest SN ratio from each of the performance parameters.42Table 1 lists the signal to noise ratios for selected lignin-based
hydrogel samples, along with their responses (yield and maximum swelling
ratio). The SN values, which maximized both of these responses, were
found to be the highest for 2L. Thus, this sample was selected as
the optimum sample based on the results.
NMR Evaluation
Figure 2 illustrates
the 1H NMR spectrum for the
lignin-based hydrogels. The peak at 1.15 ppm corresponds to two methyl
protons of the N-isopropyl group (A). The proton
of the N-isopropyl group (E) is present at 4.1 ppm.
These large peaks are dominant over the others due to the large content
of NIPAAm within the hydrogels.43,44 The functional groups
for lignin are depicted by a cluster of small peaks from 5 to 8 ppm,
which may be due to the aromatic rings present in kraft lignin. The
peak of dimethyl sulfoxide (DMSO) is observable at 2.6 ppm, which
belongs to dimethyl sulfoxide, DMSO, (D).43
Figure 2 1H NMR spectrum for lignin-based hydrogels (sample 2L).
Fourier Transform Infrared
Spectroscopy (FTIR) Evaluation
The FTIR spectra of the selected
hydrogels with lignin, 2L, and
without lignin, 2C, are shown in Figure 3. The bands located between 1535 and 1639
cm–1 are attributed to the amide groups found in
NIPAAm as well as in N,N′-methylenebiscrylamide.45,46 These compounds also exhibit a broad spectrum between 3400 and 3200
cm–1, indicating the stretching of the N–H
bond.45,47,48 According
to Konduri and Fatehi,49 the presence of
kraft lignin’s aromatic compounds yields a broad peak between
1593 and 1510 cm–1, which is attributed to the benzene
ring vibrations. There are also absorption peaks present at 1130 and
1171 cm–1, which correspond to the stretching of
the C–O bond on the primary alcohol and ether of kraft lignin,
respectively.45 In addition, the C=O
and C=C stretching may be depicted by the bands located at
approximately 1200 and 1500 cm–1, respectively.
The CH stretching of methyl or methylene groups are also shown to
be present in the peaks between 2300 and 2400 cm–1.48 The peaks at 1535 and 1639 cm–1 were intense for both samples, indicating the presence
of NIPAAm. For this reason, the peaks for NIPAAm overshadow the peaks
at 1593 and 1510 cm–1 for aromatic structure of
lignin.
Figure 3 FTIR analysis for hydrogels with lignin, 2L, and without lignin,
2C.
TGA Evaluation
The thermal decomposition behavior of
hydrogels of 2L and 2C are shown in Figure 4. An initial weight loss of 10% is generally
due to moisture removal. Afterward, lignin demonstrates a higher thermal
stability in comparison with the other samples, a desirable property
for additional end-use applications.49 Above
200 °C, lignin exhibits a gradual decrease in weight loss and
levels off at a 55% weight loss above 600 °C. This is because
the thermal breakdown of lignin occurs via two competing reaction
paths of the intramolecular condensation and the thermal depolymerization.50−52
Figure 4 Weight
loss and weight loss rates of control and lignin-based hydrogels:
(a) kraft lignin, (b) 2C, and (c) 2L.
Despite relatively similar trends, sample 2C is shown to
be slightly
less thermally stable than 2L. Sample 2C was found to exhibit a major
weight loss at approximately 415 °C, whereas sample 2L exhibited
a primary weight loss at around 420 °C. Zarzyka and co-workers
described that the use of N,N′-methylenebiscrylamide
allows for a higher cross-linking density, which, in turn, decreases
the chain mobility within the gels.53 Because N,N′-methylenebiscrylamide contributes
to cross-linking, it can be assumed that it was readily consumed during
the thermal decomposition reaction.
Surface Properties and
Swelling Behavior
The surface
area properties of the selected samples are shown in Table 4. The hydrogel without lignin,
2C, was found to have a higher surface area, pore volume, and pore
size compared to the lignin-based hydrogel, 2L. This indicates that
2C hydrogel has a more porous structure.23 Lignin-based hydrogel is expected to become less hydrophilic than
its synthetic form due to the incorporation of a hydrophobic polymer
(lignin). Therefore, this hydrogel (2C) exhibited a better swelling
performance in water, as presumably water molecules could diffuse
into its pores more effectively.
Table 4 Surface and Swelling
Properties of
Hydrogels
sample surface area (m2/g) total pore
volume (cm3/g) average pore
size (A°) maximum swelling
ratio (g/g)
2C 49.62 0.058 24.9 36.22
2L 44.56 0.048 22.1 32.59
Previous studies showed
that the swelling performance of lignin
hydrogels varied in a wide range depending on the hydrogel components
(e.g., lignin types and monomers).6 For
example, lignin-based poly(acrylic acid) (PAA) hydrogels showed relatively
high swelling ratios of 400, 600, and 700 g/g for acid hydrolysis
lignin–PAA, alkali lignin–PAA, and lignosulfonate–PAA
hydrogels, respectively.24,25 The specific surface
area of alkali lignin–PAA hydrogel was reported to be as high
as 122.7 ± 4.51 m2/g.24 On the other hand, hydrogels synthesized by acrylamide and poly(vinyl
alcohol) with alkaline and kraft lignin had a swelling ratio of 8
and 1.5 g/g, respectively.29,52 When cross-linking
with NIPAAm, the hardwood kraft lignin-based hydrogel obtained in
this study exhibited a much higher swelling ratio compared to the
acetic acid lignin-based hydrogel.23
Rheological Behavior
The cross-linked structure of
hydrogels can be further characterized by applying dynamic oscillatory
experiment. A sinusoidal oscillation with a given deformation and
frequency can be applied onto a material to obtain sinusoidal output
for strain.53 Their viscoelastic properties
may be characterized by storage modulus (G′),
which describes the material’s elasticity, and loss modulus
(G″), which is attributed to the viscosity
of materials. The elastic component characterizes a material’s
solid-like ability to store energy (its stiffness), whereas the viscous
component is the liquid-like capability to dissipate energy.54,55
Figure 5 illustrates
the effect of frequency on storage (G′) and
loss (G″) modulus as well as on dynamic viscosity
(η) for both the control and lignin-based hydrogel samples.
Some loss modulus values were unable to be measured accurately at
low frequencies and are thus analyzed from 6.30 rad/s for both samples.56 The storage modulus is greater than that of
the loss modulus for both cases (Figure 5), indicating that the hydrogel samples exhibit
more elastic properties. This behavior is typical for hydrogels as
the solid-like mechanical properties of their cross-linked structure
are more dominant than the viscous properties, which is attributed
to the small amorphous part of the polymer network.53
Figure 5 Frequency sweep of the control and lignin-based hydrogels: (a)
moduli of 2C and 2L and (b) dynamic viscosity of 2C and 2L.
In addition, both storage and
loss modulus were found to increase
with increasing shear frequency, allowing for more energy to be dissipated.
Although frequency is shown to influence the moduli curves, its dependence
is largely insignificant, indicating that the hydrogels have a well-structured
three-dimensional network.57 Furthermore,
the dynamic viscosity is shown to linearly decrease with increasing
frequency, an attribute typical to hydrogels.53 The amount of energy dissipated was found to be slightly greater
for the control samples (2C) than for the lignin-based sample (2L).
This may be due to the incorporation of lignin resulting in a less
cross-linked structure. In other words, the network structure of the
control samples is more tightly cross-linked and is therefore better
able to dissipate energy.
For amplitude sweep test, linear viscoelastic
region (LVR) for
both samples are shown in Figure 6. The strain applied does not exhibit a strong effect
on the moduli, which serves as an indication of the hydrogels’
rigidity.58 In addition, the storage modulus
is shown to exhibit a greater plateau, indicating that the samples’
viscoelastic behavior.59
Figure 6 Strain amplitude sweep
of the control and lignin-based hydrogels:
(a) 2C and (b) 2L.
On the other hand, the
storage modulus is shown to significantly
decrease with increasing strain, indicating a disturbance within the
network structure. The loss modulus slightly increases before rapidly
decreasing to 100% strain. This maximum indicates the microscopic
failure within the hydrogel’s network structure, which indicates
breaking of the interaction present within the polymer matrix.60 At this point, the storage and loss moduli exhibit
a crossover where the hydrogel exhibits a phase change from primarily
elastic to primarily viscous.56 This indicates
the irreversible deformation of the three-dimensional network structure,
which provides the hydrogel its elasticity.54,61
The crossover for the hydrogel 2C was shown to occur at a
lower
strain rate compared to the hydrogel 2L. This increase in rheological
stability with applied strain is most likely due to the incorporation
of lignin.53 In addition, the LVR has a
larger width for the lignin-based sample compared with the control
sample, further supporting that the incorporation of lignin increases
the samples’ rigidity.
Figure 7 shows the
effect of the stress on the modulus resulting from amplitude sweep
tests. The initial plateau designates the LVR, for which the change
in modulus is denoted by the yield point (τy). As
the modulus exhibits a crossover from mainly elastic to mainly viscoelastic,
this crossover is known as the flow point (τf). These
results for both these points are summarized in Table 5. The flow point and yield point for the
lignin-based hydrogel were found to be greater than those for the
control sample, indicating that lignin improved the hydrogels’
rheological performance.
Figure 7 Stress amplitude sweep of the hydrogels of (a)
2C and (b) 2L.
Table 5 Flow Point
and Yield Flow Point for
Control and Lignin-Based Hydrogels (2L and 2C)
sample yield point, τy (Pa) flow point, τf (Pa)
2C 95.1 175.2
2L 216.1 628.9
Figure 8 demonstrates
the rheological properties for both elastic and viscous moduli of
the hydrogel samples at different temperatures. At low temperatures,
the moduli curves dropped with increasing temperature. At approximately
34–37 °C, there is a slight valley in the moduli curves,
which is attributed to the lower critical solution temperature (LCST)
of NIPAAm (32–34 °C). At this temperature, the hydrogels
undergo a reversible phase transition from their swollen state to
a shrunken dehydrated state.23,47 Afterward, the difference
between the elastic and viscous moduli becomes smaller, but does not
reach a crossover temperature. In other words, the hydrogel samples
do not exhibit a phase transition, but rather undergo a plateau with
increasing temperature, indicating their thermal stability.57
Figure 8 Temperature ramp of the control and lignin-based hydrogels:
(a)
2C and (b) 2L.
The control hydrogel
(2C) exhibits a larger modulus than the lignin-based
hydrogel (2L), indicating that the control hydrogel has more elastic
properties even with increasing temperature. In addition, following
the LCST, the gap between the elastic and viscous modulus decreases
more significantly for the lignin-based hydrogels, which suggests
that the lignin-based hydrogels approach the sol–gel temperature
more readily than the control hydrogel.62
Conclusions
Hardwood lignin-based hydrogels were successfully
produced through
radical polymerization of lignin, NIPAAm, and MBAAm, as confirmed
by the NMR and FTIR analyses. Thermogravimetric analysis determined
that the hydrogels exhibited two decomposition stages attributed to
the breakdown of the aliphatic alkenes groups and the remaining carboxylic
and amine groups. Although lignin-based hydrogel had less swelling
affinity, as it possessed smaller surface area and more porous structure
than synthetic one, it was more thermally stable. The slightly greater
energy dissipated for the control hydrogel than for the lignin-based
hydrogel implied that the incorporation of lignin generated less cross-linked
hydrogel. Lignin tended to increase the rigidity and rheological stability
of hydrogel. Compared with the control hydrogel, lignin-based hydrogel
behaved less elastic as temperature increased. These results suggest
that hardwood lignin-based hydrogel can be produced, but its properties
are different from synthetic-based hydrogels.
Methodology
Materials
Mixed hardwood kraft lignin (LGN) was supplied
by FPInnovations’ pilot plant facility located in Thunder Bay,
ON. NIPAAm (97%), MBAAm (99%), azobisisobutyronitrile (AIBN, 98%),
acetone (97%), dimethyl sulfoxide-d6 (DMSO,
99.9% atom D), and tetramethylthionine chloride (methylene blue) were
obtained from Sigma-Aldrich. Sulfuric acid (98%) and sodium hydroxide
(97%) were also obtained from Sigma-Aldrich and diluted with deionized
water to 20 and 10%, respectively.
Reaction
In this
set of experiments, 0.1 g of kraft
lignin, 0.06 g of MBAAm, and varying concentrations of NIPAAm (1.2–2.4
g) were dissolved in round-bottom glass flasks with deionized distilled
water. The pH of the solutions was then adjusted with 20% sulfuric
acid and 10% sodium hydroxide to pH 2.0–3.0 before being purging
with nitrogen gas for 30 min. Water was added into the flasks to generate
the total mass of reaction (40 g), which includes the weight of the
reactants. The flask was placed in a water bath and heated to the
desired temperature before adding 0.08 g of the AIBN initiator. The
reaction was then allowed to proceed at the steady-state temperature
(65–85 °C), with a constant flow of nitrogen gas at 220
rpm. This procedure was repeated for samples with and without lignin.
After completion, the hydrogel samples were extracted from the flasks
and rinsed with acetone to remove unreacted monomers. The hydrogels
were then rinsed with water to prevent further degradation and freeze-dried
at −50 °C for over 24 h in a Labconco FreeZone 1L freeze-dryer.
The yield of the hydrogel production was calculated following eq 2 2 where WHydrogel is the total dry weight of the hydrogel (g) and WLGN, WNIPAAm, WMBAAm, WAIBN are the initial
weights of kraft lignin, NIPAAm, MBAAm, and AIBN, respectively.
The L9 Taguchi orthogonal design was performed with four factors
(each containing three levels) to investigate the effect of reaction
parameters on the responses (i.e., yield of reaction and swelling
ratio) for producing hydrogels.
1H NMR Spectroscopy
The freeze-dried hydrogel
samples were ground to powder before being dissolved in 0.5 g of deuterated
dimethyl sulfoxide (DMSO-d6), and placed
into a 5 mm, 500 MHz glass NMR tube. The sample containing tubes were
inserted into the Varian Unity INOVA 500 MHz NMR machine. The 1H NMR spectra of the samples were acquired at a 15° pulse
flipping angle, a 4.6 μm pulse width, a 2.05 acquisition time,
and 1 s relaxation delay time.
Fourier Transform Infrared
Spectroscopy
Fourier Transform
Infrared Spectroscopy (FTIR) analysis was conducted for the selected
hydrogel samples (0.001 g) using a Bruker Tensor 37 (Germany, ATR
accessory). The IR spectra was recorded in transmittance mode within
the wave number range of 500–4000 cm–1 with
a 4 cm–1 resolution.
Brunauer–Emmett–Teller
(BET) Surface Analysis
The surface area of the hydrogel particles
was determined by using
a Quantachrome surface area analyzer, Nova 2200e, instrument. The
freeze-dried hydrogels were first ground to powder and passed through
multiple sieves. The particles with the size fraction between 150
and 300 μm were selected for analysis. For each test, 0.05 g
of the powder samples were taken into account for specific surface
area analysis according to Brunauer–Emmett–Teller (BET)
method via adsorption–desorption isotherms using nitrogen gas
at −180 °C with the relative pressure range of 0.01–0.99.
Thermogravimetric Analysis (TGA)
The dried powder hydrogel
samples were placed in a desiccator overnight before undergoing thermal
analysis using a thermogravimetric analyzer (TGA i-1000 series, Instrument
Specialist Inc.). Approximately, 8 mg of sample was heated at a constant
flow rate of nitrogen (35 mL/min) from room temperature to 700 °C
at the heating rate of 10 °C/min.
Swelling Performance
The freeze-dried hydrogel samples
were cut and divided into samples weighing approximately 0.2 g. The
dried samples (with a known weight) were immersed into 200 mL of deionized
water for 24 h. The swelling ratio was determined by considering the
swollen weight of the hydrogel samples and the initial weight of dried
hydrogels following eq 3 3 where Wswollen is the
weight of the swollen hydrogel and Wdry is the initial weight of the dry hydrogel.
Rheology
A rheometer,
TA Instruments, Discovery HR-2,
with a Peltier temperature control system was used for analyzing the
viscoelastic properties of hydrogel samples. The upper geometry was
a 40 mm steel parallel plate with a gap of 1 mm and a loading gap
of 60 mm. The dynamic oscillatory measurements were carried out at
a constant temperature of 25 °C, unless stated otherwise. The
hydrogels were prepared for the rheology test according to the method
described elsewhere.53 The hydrogel samples
were saturated in deionized water before testing and were loaded onto
the Peltier plate to cover the surface area of the parallel plate.
Attempts have been made so that the same amount of the hydrogel samples
with similar thickness was loaded on the Peltier plate for each test.
Three tests of frequency sweep, amplitude sweep, and temperature ramp
have been applied on the samples in this set of experiments. The frequency
test was carried out at a shear stress of 0.2 Pa throughout the frequency
range of 0.2–20 Hz (1.267–125.7 rad/s). The amplitude
sweep was obtained at a constant frequency mode of 10 rad/s over a
strain rate range of 0.01–1000%. The temperature ramp was recorded
at a constant strain rate of 2%, with a low frequency of 10 rad/s
over a temperature range of 0–50 °C. The temperature ramp
rate was 5 °C/min.
The
authors
declare no competing financial interest.
Acknowledgments
The authors
would like to thank NSERC, Canada Foundation for
Innovation, Ontario Research Fund, Canada Research Chairs, Northern
Ontario Heritage Fund Corporation for supporting this research.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical
Society 3145882210.1021/acsomega.8b01030ArticleExtent of Helical Induction Caused by Introducing
α-Aminoisobutyric Acid into an Oligovaline Sequence Tsuji Genichiro †Misawa Takashi †Doi Mitsunobu ‡Demizu Yosuke *†† Division
of Organic Chemistry, National Institute
of Health Sciences, Kanagawa 210-9501, Japan‡ Osaka
University of Pharmaceutical Sciences, Osaka 569-1094, Japan* E-mail: demizu@nihs.go.jp. Phone &
Fax: +81-44-270-6578.14 06 2018 30 06 2018 3 6 6395 6399 17 05 2018 05 06 2018 Copyright © 2018 American Chemical
Society2018American Chemical
SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
The preferred conformations of a
dodecapeptide composed of l-valine (l-Val) and α-aminoisobutyric
acid (Aib)
residues, Boc-(l-Val-l-Val-Aib)4-OMe
(3), were analyzed in solution and in the crystalline
state. Peptide 3 predominantly folded into a mixture
of α- and 310-(P) helical structures
in solution and a (P) α helix in the crystalline
state.
document-id-old-9ao8b01030document-id-new-14ao-2018-01030hccc-price
==== Body
1 Introduction
In
proteins, helices are abundant and important secondary structures,
which recognize macromolecules, such as other proteins and DNA. Helical
peptides that mimic proteins are capable of inhibiting protein–protein
interactions, and a variety of helix-stabilizing methods have been
developed to aid the production of such peptides. As representative
techniques, the introduction of α,α-disubstituted α-amino
acids (dAA)1 or cyclic β-amino acids2 into short oligopeptides and side-chain stapling3 can all help to stabilize helical structures.
In particular, α-aminoisobutyric acid (Aib) is the simplest
dAA, and it is commonly used as a helical promoter.4 We have previously reported that the introduction of Aib
residues into natural amino acid sequences stabilized helical structures.
For example, the oligopeptides Boc-(l-Leu-l-Leu-Aib)n-OMe (n = 3 or 4) preferentially
form stable right-handed (P) helical structures.5,6 These peptides are able to act as organocatalysts for asymmetric
reaction, such as enantioselective epoxidation catalysts of α,β-unsaturated
ketones6 and Michael addition of a malonate.7 Furthermore, the amphipathic peptides R-(l-Xaa-l-Xaa-Aib)3-NH2 (R = FAM-β-Ala
and Xaa = Arg or R = H and Xaa = Lys) were also folded into stable
helical structures and were used as antimicrobial peptides8 and cell-penetrating peptides,9 respectively. In addition, we have recently reported that
the azidolysine (Azl)-based peptide Boc-(l-Azl-l-Azl-Aib)3-OMe formed a stable helical structure, and
the azide groups could be replaced with several functional groups
via click reactions without influencing the peptide’s helical
structure.10 Thus, the insertion of Aib
residues into α-amino acid-based oligopeptides is useful for
stabilizing helical structures and providing a variety of functions.
However, there have not been any reports about the secondary structural
changes that occur when Aib residues are introduced into oligopeptides
that form extended β-sheet structures. In general, oligopeptides
composed of β-branched amino acids, such as valine (Val) and
isoleucine (Ile), form β-sheet structures with extended conformations.
In particular, oligovalines have a strong tendency to form β-sheet
conformations.11 In this study, we designed
a dodecapeptide composed of l-Val and Aib residues, Boc-(l-Val-l-Val-Aib)4-OMe (3),
and analyzed its preferred conformations in solution and in the crystalline
state.
2 Results and Discussion
The dodecapeptide
Boc-(l-Val-l-Val-Aib)4-OMe (3) was synthesized using conventional solution-phase
methods according to a fragment condensation strategy, in which 1-(3-dimethylaminopropyl)-3-ethylcarbodiimide
(EDC) hydrochloride and 1-hydroxybenzotriazole (HOBt) hydrate were
used as coupling reagents. Briefly, alkaline hydrolysis of the tripeptide
Boc-l-Val-l-Val-Aib-OMe (1) afforded
the acid 1-COOH, whereas Boc deprotection by trifluoroacetic
acid furnished the amine 1-NH2. The amine 1-NH2 was coupled
with 1-COOH to give the hexapeptide Boc-(l-Val-l-Val-Aib)2-OMe (2). The dodecapeptide 3 was prepared in a manner similar to that used to prepare
the hexapeptide (Scheme 1).
Scheme 1 Synthesis of Peptides 1–3
The dominant conformations of the synthesized
peptides 1–3 in solution were analyzed based on
their Fourier transform infrared
(FT-IR), 1H nuclear magnetic resonance (NMR), and circular
dichroism (CD) spectra. Figure 1 shows the IR spectra of the tri- (1), hexa-
(2), and dodecapeptide (3) in the 3200–3500
cm–1 region (the amide A NH-stretching region) at
a peptide concentration of 5.0 mM in CDCl3 solution. In
the spectra, the weak bands in the 3425–3438 cm–1 region were assigned to free (solvated) peptide NH groups, and the
strong bands in the 3325–3340 cm–1 region
were assigned to peptide NH groups with N–H···O=C
intramolecular hydrogen bonds. These IR spectra are similar to those
of helical peptides containing Aib residues.12
Figure 1 IR
spectra of peptides 1 (green), 2 (blue),
and 3 (red) in CDCl3 solution (peptide concentration:
5.0 mM).
In the 1H NMR spectra
of the dodecapeptide 3, the N-terminal urethane-type
N(1)H proton signal was unambiguously
determined by the high-field position but the remaining eleven peptide
NH protons could not be assigned. Figure 2 shows a solvent perturbation experiment
involving the addition of the strong H-bond acceptor solvent dimethyl
sulfoxide (DMSO-d6) [0–10% (v/v)].
Two NH chemical shifts in the high-field positions were sensitive
to the addition of DMSO-d6. These results
are indicative of a 310- or α-helical structure in
solution.13
Figure 2 Plots of chemical shift
values of the NH protons of peptide 3 as a function of
the concentration of DMSO-d6 (v/v) in
CDCl3 solution (peptide concentration:
5.0 mM).
The CD spectra of the dodecapeptide 3 in 2,2,2-trifluoroethanol
(TFE) showed negative maxima at 207 and 222 nm indicating that 3 formed a right-handed (P) helical structure.
Judging from the R([θ]222/[θ]208) value,14 the secondary structure
of 3 (R = 0.64) was a mixture of α-
and 310-helical structures (Figure 3). This spectrum is similar to that of Boc-(l-Leu-l-Leu-Aib)4-OMe (R = 0.51).15
Figure 3 CD spectra of the dodecapeptide 3 (red) and Boc-(l-Leu-l-Leu-Aib)4-OMe (black) in TFE solution
(peptide concentration: 0.1 mM).
Peptide 3 formed good crystals for X-ray crystallographic
analysis after the slow evaporation of methanol/water at room temperature.
Its crystal and diffraction parameters, selected backbone and side-chain
torsion angles, and intra- and intermolecular hydrogen-bond parameters
are listed in the Supporting Information.16−19 The asymmetric unit in 3 contained two (P) α-helical structures with a flipped C-terminal Aib(12) residue
(Figure 4a). The conformations
of molecules A and B were well-matched,
except for small differences in their side-chain conformations (Figure 4b). The mean ϕ
and ψ torsion angles of the residues (2–11) were −63.1°
and −39.9° for A and −62.6° and
−40.7° for B, which are close to those of
an ideal (P) α-helix (−60° and
−45°, respectively). Regarding the intramolecular hydrogen
bonds in molecules A and B, eight i ← i + 4 type hydrogen bonds were
observed, respectively. In packing mode, molecules A and B were connected by intermolecular hydrogen bonds via methanol
molecules, forming chains with head-to-tail alignments (···A···A···A··· and ···B···B···B···).
Figure 4 (a) X-ray diffraction
structure of 3. The methanol
molecules have been omitted. (b) Superimposed structures of molecules A (green) and B (blue).
3 Conclusions
We designed and synthesized a
dodecapeptide-containing l-Val and Aib residues, Boc-(l-Val-l-Val-Aib)4-OMe (3),
to investigate the influence of the
helical promoter Aib on β-sheet structures. The conformation
of 3 was analyzed based on its FT-IR, 1H NMR,
and CD spectra in solution and X-ray diffraction analysis in the crystalline
state. Peptide 3 predominantly folded into a mixture
of α- and 310-(P) helical structures
in solution and a (P) α helix in the crystalline
state. Although oligopeptides composed of β-branched amino acids
form β-sheet structures with extended conformations, the insertion
of Aib residues into β-sheet-forming peptide sequences could
change the conformations of helical structures. Thus, we revealed
that the insertion of Aib residues into oligopeptides not only stabilized
their helical structures but also markedly altered their secondary
structures (from βsheets to helical structures). Not only helical
but also unique secondary structures will be created by the combination
of natural l- and/or d-amino acids and Aib residues,20 and these findings will be invaluable for the
de novo design of peptide-based organic and bioorganic molecules.
4 Experimental Section
4.1 General
1H and 13C NMR spectra
were recorded at 400 and 100 MHz in CDCl3 (tetramethylsilane
as an internal standard). FT-IR spectra were recorded at 1 cm–1 resolution, with an average of 256 scans used for
the CDCl3 solution method (0.1 mm path length for NaCl
cell). High-resolution mass spectra were recorded with LCMS-IT-TOF
spectrometer. CD spectra were recorded using a 1.0 mm path length
cell in TFE.
4.2 Synthesis of Tripeptide 1
The tripeptide 1 was prepared by conventional
solution-phase peptide synthesis
strategy. Colorless crystals; mp 177–179 °C; [α]D24 = −95.7
(c 0.25, CHCl3); IR (CDCl3,
cm–1): 3437, 2969, 2934, 2875, 1738, 1705, 1671; 1H NMR (400 MHz, CDCl3): δ 6.66 (s, 1H), 6.43
(d, J = 8.0 Hz, 1H), 4.99 (d, J =
7.2 Hz, 1H), 4.21–4.18 (m, 1H), 3.91 (dd, J = 6.8 Hz, 1H), 3.70 (s, 3H), 2.23–2.17 (m, 2H), 1.53 (s,
3H), 1.51 (s, 3H), 1.45 (s, 9H), 0.97 (d, J = 6.8
Hz, 3H), 0.94 (d, J = 6.8 Hz, 3H), 0.92 (d, J = 6.8 Hz, 3H), 0.91 (d, J = 6.8 Hz, 3H); 13C NMR (100 MHz, CDCl3): δ 174.6, 171.6,
167.0, 156.1, 80.4, 60.5, 58.3, 56.4, 52.5, 50.2, 30.3, 30.2, 28.3,
24.8, 24.7, 19.3, 19.2, 17.7, 17.5; [HR-ESI(+)-TOF] m/z: calcd for C20H37N3O6Na [M + Na]+, 438.2575; found, 438.2591.
4.3 Synthesis of Hexapeptide 2
A solution
of the tripeptide Boc-l-Val-l-Val-Aib-OMe (1) (415 mg, 1.0 mmol) and 1 M aqueous NaOH (2.0 mL, 2.0 mmol)
in MeOH (10 mL) was stirred at room temperature for 24 h. The solution
was neutralized with 1 M aqueous HCl and was extracted with AcOEt.
Being dried over Na2SO4 and removing the solvent
afforded the tripeptide-carboxylic acid 1-COOH, which
was used for the next reaction without further purification. Trifluoroacetic
acid (1 mL) was added to a solution of 1 (415 mg, 1.0
mmol) in CH2Cl2 (5 mL), and then the mixture
was stirred at room temperature for 5 h. Removing the solvent afforded
the crude N-terminal free tripeptide 1-NH2, which was used without further purification. A mixture of
EDC (230 mg, 1.2 mmol), HOBt (162 mg, 1.2 mmol), N,N-diisopropylethylamine (418 μL, 2.4 mmol),
the above 1-COOH (1.0 mmol), and the above 1-NH2 (1.0 mmol) in CH2Cl2 (10 mL) was stirred at room temperature for 3 days. The solution
was washed with 3% aqueous HCl, saturated aqueous NaHCO3, and brine, before being dried over Na2SO4. After removing the solvent, the residue was purified by column
chromatography on silica gel (n-hexane/AcOEt = 1:5)
to give the hexapeptide 2 in 46% yield. Colorless crystals;
mp 200–203 °C; [α]D24 = −27.4 (c 0.5, CHCl3); IR (CDCl3, cm–1): 3437, 3340,
2968, 2935, 2875, 1736, 1703, 1665; 1H NMR (400 MHz, CDCl3): δ 7.64 (s, 1H), 7.30 (d, J = 9.2
Hz, 1H), 7.17 (s, 1H), 6.93 (d, J = 6.8 Hz, 1H),
6.44 (d, J = 5.2 Hz, 1H), 5.01 (d, J = 2.6 Hz, 1H), 4.42 (dd, J = 8.8, 5.2 Hz, 1H),
4.18 (dd, J = 6.4, 4.4 Hz, 1H), 3.95 (dd, J = 4.4 Hz, 1H), 3.82 (dd, J = 4.4, 2.6
Hz, 1H), 3.68 (3H, s), 2.50–2.44 (m, 2H), 2.30–2.20
(m, 2H), 1.53 (3H, s), 1.52 (3H, s), 1.50 (9H, s), 1.50 (3H, s), 1.48
(3H, s), 1.06 (d, J = 6.8 Hz, 6H), 1.05–1.04
(m, 3H), 1.01 (d, J = 6.8 Hz, 3H), 1.00 (d, J = 6.8 Hz, 3H), 0.98 (d, J = 6.8 Hz, 3H),
0.95 (d, J = 6.8 Hz, 3H), 0.94 (d, J = 6.8 Hz, 3H); 13C NMR (100 MHz, CDCl3): δ
175.6, 175.2, 172.1, 171.9, 170.9, 170.5, 157.0, 81.8, 62.1, 60.8,
60.0, 58.6, 57.1, 55.8, 52.0, 29.4, 29.2, 28.9, 28.2, 27.5, 25.2,
24.7, 23.7, 19.6, 19.3, 19.2, 18.0, 17.5, 17.4, 17.2; [HR-ESI(+)-TOF] m/z: calcd for C34H62N6O9Na [M + Na]+, 721.4470; found,
721.4502.
4.4 Synthesis of Dodecapeptide 3
The dodecapeptide 3 was prepared using a method similar
to that described for
the preparation of 2. Yield 35%; colorless crystals;
mp 302–304 °C; [α]D24 = −16.9 (c 0.5, CHCl3); IR (CDCl3, cm–1): 3425, 3325,
2967, 2936, 2876, 1734, 1703, 1656; 1H NMR (400 MHz, CDCl3): δ 7.80 (d, J = 4.8 Hz, 1H), 7.77
(s, 1H), 7.73 (s, 1H), 7.67 (d, J = 4.8 Hz, 1H),
7.53–7.51 (m, 3H), 7.21 (d, J = 5.6 Hz, 1H),
7.10 (d, J = 6.0 Hz, 1H), 7.03 (d, J = 7.6 Hz, 1H), 6.72 (br s, 1H), 5.39 (br s, 1H), 4.41 (dd, J = 9.0, 5.8 Hz, 1H), 4.25 (dd, J = 7.2,
5.6 Hz, 1H), 3.89–3.84 (m, 3H), 3.82–3.79 (m, 1H), 3.71–3.62
(m, 2H), 3.67 (s, 3H), 2.47–2.36 (m, 2H), 2.29–2.15
(m, 6H), 1.52–1.48 (m, 33H), 1.12–0.97 (m, 48H); 13C NMR (100 MHz, CDCl3): δ 175.9, 175.9,
175.5, 173.8, 173.8, 173.0, 172.7, 172.6, 172.3, 171.5, 171.0, 157.2,
81.7, 62.9, 62.7, 62.5, 62.3, 60.9, 60.7, 59.2, 57.0, 56.8, 56.6,
55.8, 51.9, 29.8, 29.6, 29.5, 29.2, 29.2, 28.9, 28.3, 27.5, 27.4,
25.2, 24.6, 23.4, 23.3, 23.0, 19.9, 19.7, 19.5, 19.4, 19.4, 19.3,
19.2, 19.1, 19.1, 19.0, 18.9, 18.5, 18.0, 18.0, 17.8; [HR-ESI(+)-TOF] m/z: calcd for C62H112N12O15Na [M + Na]+, 1287.8262; found,
1287.8333.
Supporting Information Available
The Supporting Information is
available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b01030.Crystallographic
data and copies of the 1H NMR and 13C NMR spectra
of the peptides (PDF)
Crystallographic data of peptide 3 (CIF)
Supplementary Material
ao8b01030_si_001.pdf
ao8b01030_si_002.cif
The authors
declare no competing financial interest.
Acknowledgments
This study
was supported, in part, by JSPS KAKENHI
grant number 17k08385 (Y.D.), by a grant from the Takeda Science Foundation
(Y.D.), a grant from the Terumo Life Science Foundation (Y.D.), a
grant from the Suzuken Memorial Foundation (Y.D.), and a grant from
the Naito Foundation (Y.D.).
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145907110.1021/acsomega.8b00825ArticleGraphene/Nickel Oxide-Based Nanocomposite of Polyaniline
with Special Reference to
Ammonia Sensing Ahmad Sharique †Ali khan Mohammad Mujahid ‡Mohammad Faiz *††Department
of Applied Chemistry, Faculty of Engineering and Technology and ‡Applied Science
and Humanities Section, University Polytechnic, Faculty of Engineering
and Technology, Aligarh Muslim University, Aligarh 202002, India* E-mail: faizmohammad54@rediffmail.com (F.M.).17 08 2018 31 08 2018 3 8 9378 9387 26 04 2018 20 06 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
Polyaniline@graphene/nickel
oxide (Pani@GN/NiO), polyaniline/graphene
(Pani/GN), and polyaniline/nickel oxide (Pani/NiO) nanocomposites
and polyaniline (Pani) were successfully synthesized and tested for
ammonia sensing. Pani@GN/NiO, Pani/NiO, Pani/GN, and Pani were characterized
using X-ray diffraction, UV–vis spectroscopy, Raman spectroscopy,
scanning electron microscopy, and transmission electron microscopy.
The as-prepared materials were studied for comparative dc electrical
conductivity and the change in their electrical conductivity on exposure
to ammonia vapors followed by ambient air at room temperature. It
was observed that the incorporation of GN/NiO in Pani showed about
99 times greater amplitude of conductivity change than pure Pani on
exposure to ammonia vapors followed by ambient air. The fast response
and excellent recovery time could probably be ascribed to the relatively
high surface area of the Pani@GN/NiO nanocomposite, proper sensing
channels, and efficaciously available active sites. Pani@GN/NiO was
observed to show better selectivity toward ammonia because of the
comparatively high basic nature of ammonia than other volatile organic
compounds tested. The sensing mechanism was explained on the basis
of the simple acid–base chemistry of Pani.
document-id-old-9ao8b00825document-id-new-14ao-2018-00825xccc-price
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Introduction
A variety of materials
such as carbon nanomaterials, inorganic
semiconductors, and conjugated polymers have been explored to fabricate
gas/vapor sensors.1−7 Conducting polymer-based sensors have high sensitivity because of
the large surface area, fast response, lower power consumption, small
size, and lightweight. Among them, polyaniline (Pani) is considered
to be the most promising and widely applied sensing material because
of its low cost, easy preparation, high environmental stability, tuneable
electrical properties, and unique functions by controlled charge-transfer
processes.8−10 However, its low sensitivity and inadequate thermal
stability still restrict its application in operable sensors. In order
to improve the sensing performance of Pani, many efforts have been
made by loading the noble metals, semiconductors, and other components
to develop composite materials.11−13 Recently, nickel oxide (NiO)
nanoparticles have drawn considerable attention because of their low
price, acceptable sensing properties, and good environmental stability.
Researchers developed gas sensors based on NiO films which have demonstrated
significant sensing properties.14 Because
of its high resistivity, there is still drawback in using NiO in composite
materials for practical sensing applications. To overcome this problem,
many carbonaceous materials with high electrical conductivity have
been introduced to prepare carbon/NiO nanocomposites.15
A number of composites of Pani have been reported
with metal oxides,
metal nanoparticles, graphene (GN), and carbon nanotubes widely used
in gas sensing applications.16
Also,
many other nanocomposites have also been reported as ammonia
sensors.17−21 We have decorated NiO nanoparticles on GN sheets, which increases
the resultant surface area. The material obtained GN/NiO nanocomposite
is also conductive with enhanced surface area, which may be a suitable
material for making conducting nanocomposites with Pani for the purpose
of gas/vapor sensing studies.
In this work, the polyaniline@graphene/nickel
oxide (Pani@GN/NiO)
nanocomposite was selected and studied as an ammonia sensor by examining
the dynamic response of electrical conductivity using a simple four-in-line-probe
dc electrical conductivity measurement setup.
Results and Discussion
X-ray
Diffraction Studies
X-ray diffraction (XRD) spectra
of Pani, polyaniline/nickel oxide (Pani/NiO), polyaniline/graphene
(Pani/GN), and Pani@GN/NiO nanocomposites are shown in Figure 1. Figure 1a exhibits the XRD spectrum of Pani, which
has two characteristic broad peaks at 2θ = 20.31° and 25.23°.
The XRD spectrum of Pani/GN has broad peaks similar to those for Pani
slightly shifted to 2θ = 20.45° and 25.27°, which
is attributed to the presence of GN in the Pani/GN nanocomposite,
as shown in Figure 1b. In Figure 1c, there
are five extra sharp peaks along with characteristic broad peaks of
Pani (at 2θ = 20.25° and 25.34°), which are observed
at 2θ = 37.42°, 43.35°, 62.86°, 75.26°,
and 79.42°, respectively, attributed to the presence of NiO nanoparticles
in the Pani/NiO nanocomposite. The XRD spectrum of the Pani@GN/NiO
nanocomposite is similar to that of the Pani/NiO nanocomposite, as
shown in Figure 1d.
The peaks due to Pani at 2θ = 20.05° and 25.69°, respectively,
shifted from 2θ = 20.31° and 25.23°, which may be
attributed to the interaction of Pani with NiO embedded on GN sheets.
The five intense peaks observed in the Pani@GN/NiO nanocomposite at
2θ = 37.13°, 43.48°, 63.12°, 75.39°, and
79.56° may be ascribed to the (111), (200), (322), (311), and
(222) planes, respectively, due to the reflection of NiO deposited
on GN sheets with a slight shift compared to those in the Pani/NiO
nanocomposite, indicating the successful preparation of the Pani@GN/NiO
nanocomposite.22,23
Figure 1 XRD patterns of (a) Pani, (b) Pani/GN,
(c) Pani/NiO, and (d) Pani@GN/NiO.
Scanning Electron Microscopy Studies
Figure 2 presents the scanning electron
microscopy (SEM) images of Pani, Pani/NiO, Pani/GN, and Pani@GN/NiO
nanocomposites. The SEM images of the Pani@GN/NiO nanocomposite demonstrated
the sheet-type morphology due to the presence of GN/NiO, as shown
in Figure 2a,b. However,
the NiO nanoparticles deposited on GN sheets are not visible here,
which indicates that the NiO nanoparticles deposited on GN sheets
have a nucleating effect on the polymerization of aniline and are
completely covered by the Pani shell. Figure 2c,d presents the SEM images of Pani, which
seems to possess a nanotubelike morphology. Figure 2e presents the SEM image of the Pani/NiO
nanocomposite, in which the polymer matrix is well deposited on NiO
nanoparticles and the Pani is agglomerated by several nanoparticles.
In Figure 2f, it may
clearly be seen that the Pani is well deposited on GN, giving some
sheetlike morphology in the Pani/GN nanocomposite.
Figure 2 SEM micrographs of (a,b)
Pani@GN/NiO nanocomposite, (c,d) Pani,
(e) Pani/NiO, and (f) Pani/GN.
Transmission Electron Microscopy Studies
The morphologies
of Pani@GN/NiO, Pani/NiO, Pani/GN, and Pani were further analyzed
by transmission electron microscopy (TEM), as shown in Figure 3. In this synthesis, we deposited
NiO nanoparticles on GN sheet and then aniline monomers were polymerized
on the surface of GN/NiO. Figure 3a shows that the NiO nanoparticles were deposited on
GN sheets upon which Pani nanotubes are deposited, signifying the
successful incorporation of NiO nanoparticles onto GN sheets for a
nanocomposite with Pani nanotubes. A lattice spacing of 0.818 nm can
be attributed to the lattice spacing of the (200) plane of the NiO
nanoparticles in the Pani@GN/NiO nanocomposite (see the magnified
image of Figure 3a). Figure 3b shows that the
NiO particles are uniformly distributed in the outer shell of the
polymer matrix. In Figure 3c, it can be observed that the short tubes of Pani are precisely
deposited on the GN sheets. We also synthesized Pani using the same
procedure in the absence of the GN and NiO; short tubes of Pani were
obtained, as shown in Figure 3d. In the light of the above observations of TEM analysis,
it can be inferred that the NiO nanoparticles were precisely deposited
on GN sheets and covered by Pani nanotubes. Furthermore, to evaluate
the Brunauer–Emmett–Teller (BET) surface area, the N2 adsorption–desorption isotherms of the Pani@GN/NiO
nanocomposite were measured. The BET surface area of the Pani@GN/NiO
nanocomposite was found to be 275 m2 g–1 (Figure S1).
Figure 3 TEM micrographs of (a)
Pani@GN/NiO nanocomposite, (b) Pani/NiO
nanocomposite, (c) Pani/GN nanocomposite, and (d) Pani.
Optical Studies
The UV–vis
absorption spectra
of Pani@GN/NiO, Pani/NiO, Pani/GN, and Pani are given in Figure 4. In Figure 4a, the band observed at 327
nm for Pani may be attributed to the π–π* electronic
transition of benzenoid rings.24 In the
case of the Pani/GN nanocomposite, the band red-shifted to 332 nm
from 327 nm may be attributed to the interaction of π-electrons
of benzenoid rings with π-bonds of GN, as shown in Figure 4b.25 In Figure 4c, the Pani/NiO nanocomposite illustrates the two bands at 281 and
323 nm, which may be related to the electronic transition from the
valence band to the conduction band in the NiO and due to the π–π*
transition of the benzenoid rings, respectively.26,27 In the case of Pani/NiO, a blue shift is observed in contrast to
that in Pani, which may be attributed to the decrease in the conjugation
of Pani by loading of NiO in Pani, reducing the path of polarons in
Pani. From Figure 4d, it is illustrated that the Pani@GN/NiO nanocomposite reflected
the two maxima at 276 nm, blue-shifted in comparison with Pani/NiO,
and the other at 375 nm, red-shifted in comparison with Pani from
327 nm, which may be attributed to the increase in the extent of conjugation
of Pani by forming an efficient network by electronic transition from
NiO to GN.28 The significant red shift
in the Pani@GN/NiO nanocomposite supports the enhanced dc electrical
conductivity because of the ease in the movement of polarons by extended
conjugation in Pani@GN/NiO.
Figure 4 UV–vis spectra of (a) Pani, (b) Pani/GN
nanocomposite, (c)
Pani/NiO nanocomposite, and (d) Pani@GN/NiO nanocomposite.
Raman Spectroscopy
Figure 5 shows the Raman spectra of
Pani@GN/NiO,
Pani/NiO, Pani/GN, and Pani. In Figure 5a, the different modes of vibration are observed. The
sharp peak at 1410 cm–1 may be associated with the
presence of C–N+ polarons.29 The peaks observed at 1330 and 1570 cm–1 may be
due to the presence of GN sheet bands (D and G), and the bands at
1370 and 1592 cm–1 may be due to two-magnon (2M)
and two-phonon (2P) bands of NiO. In Figure 5b, the Raman spectrum of Pani/NiO displays
two vibrational bands at 1363 and 1574 cm–1, which
may be due to the presence of NiO nanoparticles that correspond to
the 2M and 2P models.30−32Figure 5c displays the Raman spectrum of the Pani/GN nanocomposite, showing
the two bands at 1345(D) cm–1 due to disordered
structures in the GN layers and 1576(G) cm–1 due
to sp2 electronic configuration of graphitic carbon phase
in the Pani/GN nanocomposite.33 In the
Raman spectra of Pani, the bands at 1350 and 1565 cm–1 may be attributed to C–N+ and C=C modes
of vibration, respectively, as shown in Figure 5d. Significant shifts of Raman bands of Pani@GN/NiO
are observed in comparison with the Pani/GN and Pani/NiO nanocomposites.
The D and G bands of GN in the Pani/GN nanocomposite are blue-shifted
from 1345 and 1576 to 1330 and 1570 cm–1, respectively,
in the Pani@GN/NiO nanocomposite, whereas the 2M and 2P bands of NiO
in Pani/NiO are red-shifted from 1363 and 1574 to 1370 and 1592 cm–1, respectively. The substantial band shifts of GN
and nickel oxide constituent in the Pani/GN and Pani/NiO nanocomposites
indicate a strong interaction between NiO and GN sheets, favoring
the charge transfer from NiO to GN sheets28 and forming more holes in Pani. Thus, an increment in the electrical
conductivity of Pani@GN/NiO also strongly supports the interaction
and charge transportation between NiO and GN.
Figure 5 Raman spectra of (a)
Pani@GN/NiO nanocomposite, (b) Pani/NiO nanocomposite,
(c) Pani/GN nanocomposite, and (d) Pani.
Electrical Conductivity
The initial dc electrical conductivities
of Pani, Pani/NiO, Pani/GN, and Pani@GN/NiO nanocomposites were measured
by a standard four-in-line-probe method, as shown in Figure 6a. The electrical conductivity
of Pani was observed to be 1.832 S/cm. The electrical conductivity
of the Pani/NiO nanocomposite prepared by the method mentioned above
was observed to be 0.853 S/cm, which is slightly less than that of
Pani. It may be proposed that the movement of polarons of Pani get
retarded because of the Coulombic interaction between the polarons
of Pani and lone pairs of oxygen of NiO, as shown in Figure 6b. Although, the d-orbitals
of Ni may increase the number of polarons in the Pani chains by accommodating
electrons from Pani, the Coulombic interaction seems to be a dominating
factor. Shambharkar and Umare23 also reported
that the electrical conductivity of the Pani/NiO nanocomposite decreases
with a low NiO content in the nanocomposite.
Figure 6 (a) Initial dc electrical
conductivities of Pani, Pani/NiO, Pani/GN,
and Pani@GN/NiO nanocomposites and the mechanism of conductivity behavior
of (b) Pani/NiO, (c) Pani/GN, and (d) Pani@GN/NiO.
The initial electrical conductivity at room temperature
of the
as-prepared Pani/GN nanocomposite was observed to be 9.2 S/cm, which
was much higher than that of Pani (1.2 S/cm). It may be proposed that
the charge carriers hop from Pani to GN, where they gain high mobility
along the π-conjugated system of GN, as shown in Figure 6c. The overall mobility of
charge carriers thus enhanced because of unobstructed movement along
the GN nanosheets, leading to an increase in the electrical conductivity
of the Pani/GN nanocomposite. Ansari et al.34 also reported that a sulfonated-Pani/GN nanocomposite exhibited
a high electrical conductivity because of π–π interaction
between sulfonated-Pani and GN.
In the case of Pani@GN/NiO,
the electrical conductivity was observed
to be 11.34 S/cm, which was the highest among all samples. It seems
that the NiO acts as a bridge between Pani and GN, which helps in
the movement of charge carriers from Pani to GN and thus increases
electrical conductivity because of a greater mobility of charge carriers
along the π-conjugated system of GN nanosheets, as shown in Figure 6d. Thus, NiO bridges
additionally facilitate the hopping movement of charge carriers between
Pani and GN in the Pani@GN/NiO nanocomposites.
Stability under Isothermal
Ageing Conditions
The isothermal
ageing stabilities of Pani, Pani/NiO, Pani/GN, and Pani@GN/NiO nanocomposites
were calculated, as shown in Figure 7, by using the following equation:13 1 where σt is the electrical conductivity at time t and σ0 is the electrical conductivity
at time zero at experimental
temperature. The as-prepared materials were examined for stability
in terms of dc electrical conductivity retention with respect to time
at different temperatures. The electrical conductivity of each of
the samples was measured at the temperatures 50, 70, 90, 110, and
130 °C versus time at an interval of 5 up to 20 min. From Figure 7a,b, it can be observed
that Pani and Pani/NiO are fairly stable up to 90 °C, whereas
the Pani/GN and Pani@GN/NiO nanocomposites are stable up to 110 °C
in terms dc electrical conductivity, as shown in Figure 7c,d. It may be inferred that
the relative electrical conductivity of Pani@GN/NiO and Pani/GN nanocomposites
showed greater stability than the Pani and Pani/NiO nanocomposite
under isothermal ageing conditions.
Figure 7 Relative electrical conductivity of (a)
Pani, (b) Pani/NiO, (c)
Pani/GN, and (d) Pani@GN/NiO under isothermal ageing conditions.
Stability under Cyclic
Ageing Conditions
The cyclic
ageing stabilities of Pani, Pani/NiO, Pani/GN, and Pani@GN/NiO nanocomposites
were studied, as shown in Figure 8.13 The relative electrical
conductivity (σr) was calculated using the following
equation: 2 where σT is the electrical conductivity (S/cm) at
temperature T (°C) and σ50 is
the electrical conductivity
(S/cm) at 50 °C, that is, at the beginning of each cycle.
Figure 8 Relative electrical
conductivity of (a) Pani, (b) Pani/NiO, (c)
Pani/GN, and (d) Pani@GN/NiO under cyclic ageing conditions.
The electrical conductivity was
recorded for successive cycles
and observed to be increased gradually for each of the cycle with
a regular trend in all of these cases, which may be due to the increment
of the number of charge carriers as polarons or bipolarons at elevated
temperatures. Figure 8a shows the relative electrical conductivity of Pani following the
same trend for each of the cycle with gain in the dc electrical conductivity
as the temperature increases. Also, the relative electrical conductivities
of Pani/NiO, Pani/GN, and Pani@GN/NiO nanocomposites increased as
the temperature increases from 50 to 130 °C, as shown in Figure 8b–d. Among
all of these nanocomposites, the Pani@GN/NiO nanocomposite showed
the lowest gain in conductivity with less deviation. Thus, it may
be inferred that the Pani@GN/NiO nanocomposite is a more stable semiconductor
than Pani and among all of these nanocomposites under cyclic ageing
conditions. The difference observed may be attributed to the removal
of moisture, excess HCl, or low-molecular-weight oligomers of aniline.35
Sensing
The dc electrical conductivity
responses of
the sensors based on Pani, Pani/NiO, Pani/GN, and Pani@GN/NiO were
measured on exposure to ammonia (NH3) at room temperature
(∼25 °C). A four-in-line-probe PID-200 (Scientific Equipment,
Roorkee, India) dc electrical conductivity measuring instrument was
used to study ammonia sensing properties. The pellet fabricated was
in contact with the four probes and placed in a closed chamber of
ammonia vapors (Figure 9).
Figure 9 Instrumental setup of the ammonia sensor and the schematic presentation
of the four-in-line probe.
The electrical conductivity immediately decreases on exposure
to
ammonia for 60 s and rapidly reverts back on exposure to ambient air
in next 60 s in all of the as-prepared materials, as shown in Figure 10a. However, the
greatest change in electrical conductivity was observed in the case
of the Pani@GN/NiO nanocomposite. Therefore, the Pani@GN/NiO nanocomposite
was also tested for different concentrations of ammonia, as shown
in Figure 10b. The
highest change in electrical conductivity was observed for 1703 ppm
of ammonia. As the concentration of ammonia increases from 170 to
1703 ppm, the more polarons of Pani get neutralized by the lone pair
of electrons of ammonia molecules, leading to a decrease of electrical
conductivity. The electrical conductivity change of the Pani@GN/NiO
nanocomposite could be observed on exposure to ammonia as low as 170
ppm concentration.
Figure 10 (a) Effect on the dc electrical conductivity of Pani,
Pani/NiO,
Pani/GN, and Pani@GN/NiO nanocomposites on exposure to (1703 ppm)
ammonia vapors followed by exposure to ambient air with respect to
time, (b) effect on the dc electrical conductivity of the Pani@GN/NiO
nanocomposite on exposure to ammonia vapors at different concentrations,
and (c) steady-state response of dc electrical conductivity of the
Pani@GN/NiO nanocomposite on exposure to 1703 ppm ammonia followed
by exposure to ambient air with respect to time.
The steady-state response of Pani@GN/NiO was determined by
first
keeping the sample in 1703 ppm of ammonia environment for 180 s followed
by 120 s in air for a total duration of 300 s (Figure 10c). It can be observed that the electrical
conductivity immediately decreases on exposure to ammonia for about
65 s and attains saturation for further exposures until exposed to
ambient air. The conductivity reverted in ambient air after 180 s
of exposure to ammonia and became saturated at about 240 s.
Reversibility
The sensitivity and reversibility are
the two important parameters for a gas sensor. Sensitivity may be
defined as the time taken to reach the final value after exposure
to vapors and to reach the initial value on exposure to ambient air,
whereas the reversibility may be considered as the cycling between
the analyte and ambient air without any loss in its sensing ability.
The reversibility of Pani and Pani@GN/NiO nanocomposite was measured
in terms of the dc electrical conductivity. The reversibility of both
the samples was determined by first keeping the sample in 1703 ppm
ammonia vapors for 30 s followed by 30 s in air for a total duration
of 150 s. Figure 11a represents the reversibility response of Pani in terms of the dc
electrical conductivity with a variation range from 1.849 to 1.812
S/cm in ambient air and on exposure to 1703 ppm of ammonia vapors,
respectively. The change in conductivity observed was 0.037 S/cm,
whereas in the case of the Pani@GN/NiO nanocomposite, the reversibility
was observed with an excellent variation range compared to Pani, which
is from 11.146 to 7.489 S/cm in ambient air and on exposure to 1703
ppm of ammonia vapors, respectively, as shown in Figure 11b. In the case of Pani@GN/NiO,
the observed decrease in conductivity by 3.657 S/cm is indicative
of much higher efficiency than that of Pani in terms of reversibility.
There was around about 99 times greater variation observed in the
conductivity of the Pani@GN/NiO nanocomposite than that of Pani.
Figure 11 Variation
in the electrical conductivity of (a) Pani and (b) Pani@GN/NiO
on alternate exposure to (1703 ppm) ammonia vapors and ambient air.
Sensing under Dry and Wet
Atmospheres
The NH3 response properties under
completely dry and wet atmospheres were
also studied. The effect of relative humidity (RH) on ammonia sensing
properties was studied by mixing of humidity and NH3 vapors.
It was seen that the dc electrical conductivity of the Pani@GN/NiO
nanocomposite sharply decreases and reaches its saturation level within
50 s when exposed to 1700 ppm of dry ammonia prepared by heating of
ammonium chloride and slaked lime mixture. Also, the sample Pani@GN/NiO
was tested for pure water vapors, and it was observed that the decrease
in electrical conductivity was not rapid as that it was in the case
of completely dry ammonia, as shown in Figure 12. To confirm the effect of water vapors
on the ammonia sensing properties of the Pani@GN/NiO nanocomposite,
the sample was also exposed to an NH3 atmosphere at 1703
ppm at different humidity levels viz. 20, 30, 40, and 60% RH. The
electrical conductivity of the sample continuously decreases with
time at different RHs. The variations of humidity levels for the same
concentration keep the conductivity stable. The conductivity variations
of Pani@GN/NiO are not much effected at any RH, and the four curves
were almost similar, from which we may conclude that humidity has
only small effect on NH3 sensing properties.
Figure 12 dc electrical
conductivity response as a function of time of Pani@GN/NiO
nanocomposite exposed to 1700 ppm dry ammonia, 20% (1703 ppm ammonia),
30% (1703 ppm ammonia), 40% (1703 ppm ammonia), 60% (1703 ppm ammonia)
RH, and pure water vapors.
Selectivity
For a worthy and applicative gas sensor,
high selectivity is also an important requirement. The conductivity
responses of the Pani@GN/NiO nanocomposite to ammonia and volatile
organic compounds (VOCs) viz. isopropanol, methanol, ethanol, acetone,
acetaldehyde, and formaldehyde at room temperature (25 °C) are
shown in Figure 13. It was observed that the conductivity response of the Pani@GN/NiO
nanocomposite to 1703 ppm ammonia was 9.8, 6.2, 6.6, 7.9, 6.5, and
6.1 times higher than those for isopropanol, methanol, ethanol, acetone,
acetaldehyde, and formaldehyde, respectively. Such a selectivity results
from the difference of their sensing mechanisms, that is, the neutralization
of polarons of Pani that plays an important role in changing electrical
conductivity on exposure to VOCs. The greater the availability of
lone pairs in a vapor/gas, the greater the observed electrical conductivity
change. Ammonia has more electron-donating nature and thus neutralizes
more number of polarons of Pani. On the other hand, in VOCs, there
are interactions of lone pairs of electrons of oxygen of greater −I
effect than that of nitrogen of Pani. Therefore, the lower electron-donating
tendency of VOCs leads to a lower conductivity change. This also infers
the higher selectivity of the Pani@GN/NiO nanocomposite toward NH3.
Figure 13 Selectivity of the Pani@GN/NiO nanocomposite to 1703 ppm of ammonia
and different VOCs (1 M) in water.
The efficient gas sensing properties of Pani@GN/NiO may be
attributed
to the large surface area of Pani which anchored more adsorption and
desorption of gaseous molecules as well as high polarons mobility
due to the presence of GN, essential requirement for rapid response
of any electrical conductivity-based sensor.13 It is expected that the NiO embedded on GN sheets interacts with
lone pairs of nitrogen atoms of Pani, thus increasing the number of
polarons in Pani and creating a more number of active sites at a large
surface area for the interaction of lone pairs of ammonia molecules
to polarons of Pani. However, the detailed understanding on the role
of NiO and GN sheets in the sensing mechanism of the Pani@GN/NiO nanocomposite
requires further investigations on this aspect.
Proposed Mechanism
for Sensing
Sensing by the Pani@GN/NiO
nanocomposite is based on the decrease in electrical conductivity
on exposure to analyte vapors and to revert on exposure to ambient
air. Therefore, the different aspects of emergence of high electrical
conductivity in the nanocomposite have been discussed above in order
to understand the sensing behaviour of the Pani@GN/NiO nanocomposite.
The sensing mechanism of the Pani@GN/NiO nanocomposite was explained
through dc electrical conductivity response by simple adsorption and
desorption mechanism of ammonia vapors at room temperature, as shown
in Scheme 1. In the
Pani@GN/NiO nanocomposite, NiO nanoparticles embedded on GN sheets
interact with lone pairs of nitrogen atoms of Pani; thus, the numbers
of polarons and bipolarons increase in Pani chains. In the presence
of ammonia vapors, the lone pairs of ammonia molecules bind with polarons
of the Pani@GN/NiO nanocomposite, which impedes the mobility of polarons,
leading to a decrease in electrical conductivity. When Pani@GN/NiO
is exposed to ambient air, the ammonia molecules are desorbed from
the surface and thus the electrical conductivity reverts to its initial
value. Thus, the simple adsorption and desorption of ammonia vapors
on the Pani@GN/NiO nanocomposite govern the mobility of polarons.
Scheme 1 Proposed Mechanism of Interaction of Ammonia with the Pani@GN/NiO
Nanocomposite
However, the humidity
present in atmosphere may also interfere
in ammonia adsorption on the Pani@GN/NiO nanocomposite, but the conductivity
changes of Pani@GN/NiO are not much affected at any RH so that humidity
has only small effect on NH3 sensing properties. Therefore,
in competition between ammonia and water molecules, it may be said
that the change in conductivity of Pani@GN/NiO may be mainly due to
ammonia vapors because ammonia has more available electrons than water.
The selective response of the Pani@GN/NiO nanocomposite toward
ammonia may be due to the basic nature of ammonia, which readily interacts
with polarons of Pani, whereas all other VOCs tested are much less
basic than ammonia because they contain an oxygen atom which is more
electronegative than nitrogen, so the electronic interaction with
Pani in these compounds is comparatively poorer.
Conclusions
Pani, Pani/NiO, Pani/GN, and Pani@GN/NiO were successfully prepared
and characterized by XRD, SEM, TEM, UV–vis, and XRD analysis.
The Pani@GN/NiO nanocomposite showed the higher thermal stability
in terms of dc electrical conductivity retention under isothermal
and cyclic ageing conditions than pristine Pani. The results highlighted
that the Pani@GN/NiO nanocomposite was found to be an excellent material
for ammonia sensing with excellent selectivity against VOCs and rapid
response. There was about 99 times greater variation in the electrical
conductivity of Pani@GN/NiO nanocomposite than that of Pani during
sensing. The enhancement of sensing properties in the Pani@GN/NiO
nanocomposite may be attributed to the synergistic effect between
NiO, GN, and Pani. Therefore, the sensor based on the nanocomposite
of GN/NiO with Pani may be useful and efficient while the material
is promising for ammonia vapor sensing.
Experimental Section
Materials
Aniline (99%, E. Merck, India) and commercially
available natural graphite powder (Sigma-Aldrich, USA) were used to
prepare graphene oxide (GO). Sodium dodecylsulfate, ammonium persulfate
(APS), sulfuric acid (H2SO4), hydrated nickel
nitrate (Ni(NO3)26H2O), sodium hydroxide
(NaOH), and hydrazine hydrate (85%) were obtained from the local suppliers
and used as received.
Preparation of Pani, Pani/NiO, Pani/GN, and
Pani@GN/NiO
Pani nanofibers were prepared through the interfacial
polymerization
reaction in which aniline monomers (10 mmol) were dissolved in hexane
(10 mL) under stirring for 30 min. APS (30 mmol) was gently added
to 10 mL of 1 M sulfuric acid solution under constant stirring. The
solution of APS was added dropwise into aniline solution, and the
mixture was allowed to react for 1 h. The final greenish reaction
product was then filtered, washed with double distilled water, and
then dried in an air oven at 70 °C for 10 h.
In a typical
synthesis procedure of the Pani/NiO nanocomposite, 2 mL of aniline
was dissolved in the solution of 2 mL of 1 M H2SO4 in 90 mL of distilled water. A solution of 0.5 g of nickel oxide
(NiO) was prepared in accordance with the existing literature36 and was then added to aniline solution. APS
(5 g) dissolved in 10 mL of 1 M H2SO4 was added
to the aniline solution, and the reaction mixture was stirred for
24 h at room temperature. The final reaction product was then filtered
and washed thoroughly with distilled water and acetone until the filtrate
became colorless. The resulting product was dried at 70 °C for
10 h.
To prepare the Pani/GN nanocomposite, GO (20 mg) was prepared
in
accordance with the existing literature37 and was then dissolved in 10 mL of 1 M H2SO4 with constant stirring for 1 h. Subsequently, aniline solution (10
mmol) prepared in 1 M H2SO4 was mixed to the
GO solution and stirred for another 1 h. The APS (30 mmol) solution
prepared in 1 M H2SO4 was then added to the
above solution. The final reaction mixture was kept under constant
stirring, followed by a conventional microwave treatment at 300 W
for 30 min. The resulting suspension was separated by centrifugation
and washed with double distilled water and ethanol. The final product
was dried at 70 °C under vacuum for 12 h.
In the synthesis
of GN/NiO, the as-prepared GO (25 mg) was ultrasonically
dispersed in 10 mL of double distilled water for 1 h and 0.5 g of
Ni(NO3)2·6H2O in 25 mL of distilled
water was added into the above dispersion. After constant stirring
for 6 h, 10 mL of 1 M NaOH aqueous solution was added into the above
reaction mixture drop by drop. The pH value was adjusted to ∼10
by 10% aqueous ammonia. After that, 10 mL of hydrazine hydrate (85%)
was added to it. The reaction mixture was stirred for several minutes
before being treated with microwave at 300 W for 30 min. The product
was separated by centrifuging and washed with double distilled water
followed by ethanol. The product was dried in a vacuum oven at 50 °C
for 24 h. The dried sample was heated in a N2 atmosphere
at 300 °C for 3 h to obtain GN/NiO. The Pani@GN/NiO nanocomposite
was prepared by mixing GN/NiO to aniline monomer in a weight ratio
of 5:1. GN/NiO was dispersed in ethanol and water (1:1 weight ratio)
by stirring for 60 min and then added to the aniline solution prepared
in 1 M H2SO4. An aqueous solution of APS (10
mL) prepared in 1 M H2SO4 was added dropwise
to the mixture of aniline and GN/NiO at 5–10 °C and kept
under constant stirring for 24 h. The resultant product was washed
several times by vacuum filtration using ethanol and double distilled
water. The final product was dried at 50 °C for 12 h.
Characterization
The morphology, structure, and chemical
composition of Pani, Pani/NiO, Pani/GN, and Pani@GN/NiO were investigated
by a variety of methods. XRD pattern were recorded by a Bruker D8
diffractometer with Cu Kα radiation at 1.5418 Å. SEM studies
were carried out by JEOL, JSM, 6510-LV (Japan). TEM studies were carried
out by using JEM 2100, JEOL (Japan). The Raman spectra were taken
using a Varian FT-Raman spectrometer. UV–vis spectra were recorded
at room temperature using a Shimadzu UV–vis spectrophotometer
(model 1601). dc electrical conductivity measurements were performed
by using a four-in-line probe electrical conductivity retention measuring
instrument with a PID controlled oven (Scientific Equipment, Roorkee,
India). The thermal stability of all as-prepared materials in terms
of dc electrical conductivity under isothermal and cyclic ageing conditions
was also studied. The equation used in the calculation of dc electrical
conductivity was 3 where I, V, W, and S are the current (A),
voltage (V), thickness of the pellet (cm), and probe spacing (cm),
respectively, and σ is the conductivity (S/cm).11,38 In thee testing of isothermal stability, the pellets were heated
at 50, 70, 90, 110, and 130 °C in an air oven, and the dc electrical
conductivity was measured at particular temperatures at an interval
of 5 min in the accelerated ageing experiments. In the testing of
the stability under cyclic ageing conditions, dc conductivity measurements
were taken five times within the temperature range of 50–130
°C.
Supporting Information Available
The Supporting Information is
available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b00825.Nitrogen adsorption–desorption
isotherms of the
Pani@GN/NiO nanocomposite (PDF)
Supplementary Material
ao8b00825_si_001.pdf
The authors
declare no competing financial interest.
Acknowledgments
The authors
are extremely grateful to Mohd Shoeb
for supporting and helpful discussion.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145893910.1021/acsomega.8b00962ArticleStatistics of the Auger Recombination of Electrons and Holes via
Defect Levels in the Band Gap—Application to Lead-Halide Perovskites Staub Florian †Rau Uwe †Kirchartz Thomas *†‡† IEK5-Photovoltaik, Forschungszentrum Jülich, 52425 Jülich, Germany‡ Faculty of Engineering and CENIDE, University of Duisburg-Essen, Carl-Benz-Str. 199, 47057 Duisburg, Germany* E-mail: t.kirchartz@fz-juelich.de.18 07 2018 31 07 2018 3 7 8009 8016 10 05 2018 05 07 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under a Creative Commons Non-Commercial No Derivative Works (CC-BY-NC-ND) Attribution License, which permits copying and redistribution of the article, and creation of adaptations, all for non-commercial purposes.
Recent evidence for
bimolecular nonradiative recombination in lead-halide perovskites
poses the question for a mechanistic origin of such a recombination
term. A possible mechanism is Auger recombination involving two free
charge carriers and a trapped charge-carrier. To study the influence
of trap-assisted Auger recombination on bimolecular recombination
in lead-halide perovskites, we combine estimates of the transition
rates with a detailed balance compatible approach of calculating the
occupation statistics of defect levels using a similar approach as
for the well-known Shockley–Read–Hall recombination
statistics. We find that the kinetics resulting from trap-assisted
Auger recombination encompasses three different regimes: low injection,
high injection, and saturation. Although the saturation regime with
a recombination rate proportional to the square of free carrier concentration
might explain the nonradiative bimolecular recombination in general,
we show that the necessary trap density is higher than reported. Thus,
we conclude that Auger recombination via traps is most likely not
the explanation for the observed nonradiative bimolecular recombination
in CH3NH3PbI3 and related materials.
document-id-old-9ao8b00962document-id-new-14ao-2018-009626ccc-price
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Introduction
One of the key prerequisites
for optoelectronic materials are long nonradiative lifetimes1−7 for recombination via defects as compared to the recombination coefficients
for direct radiative band-to-band transitions.8−13 Recombination via defects14,15 is usually assumed
to be mediated by the emission of multiple phonons,16−21 whereas band-to-band recombination via multiphonon emission is thought
to be extremely unlikely in inorganic semiconductors.22 Because the transition rates are strongly reduced for an
increasing number of phonons17,22 involved in a single
transition at low-to-moderate strength of electron–phonon coupling,
direct band-to-band recombination is typically assumed to be entirely
radiative in inorganic semiconductors. This is different in organic
semiconductors due to the higher energy associated with molecular
vibrations in organic molecules relative to the energy of phonons
in inorganic semiconductors.23 Given that
lead-halide perovskites due to the high atomic mass of Pb and I have
particularly low phonon energies,24,25 it is initially
rather surprising that there is evidence26,27 for recombination terms that are quadratic in charge-carrier density
(like radiative recombination in high-level injection) and are nonradiative.
In addition to multiphonon recombination, Auger recombination is the
second archetypal nonradiative recombination mechanism.13,28−30 Auger recombination involving two free electrons
and one hole or two free holes and one electron, respectively, should
be cubic in charge-carrier density in the high-level injection and
would therefore not be able to explain the observed features. However,
Auger recombination involving trapped charge carriers could in principle
explain the observed quadratic behavior.26
Thus far, trap-assisted Auger recombination has been mainly
discussed for the case of highly doped semiconductors29−31 where this mechanism is most efficient because of the high density
of free charge carriers. This implies that only the limiting linear
case of low injection (with respect to the doping level) is usually
considered. In addition, it has been discussed in the context of determining
limiting efficiencies for Si solar cells, but recently also for perovskite
solar cells.13,28,30,32 To study the potential effect of trap-assisted
Auger recombination on bimolecular recombination in lead-halide perovskites
close to the radiative limit, a model for the full recombination statistics
is required. Therefore, we develop a detailed balance compatible rate
equation model in analogy to the Shockley–Read–Hall
(SRH) recombination statistics.14,15 Subsequently, we use
known material properties of the lead-halide perovskites and previously
derived equations33 for the transition
rates to estimate the Auger coefficients for trap-assisted Auger recombination
in perovskites. Finally, we derive the necessary trap density for
trap-assisted Auger recombination to explain the observed nonradiative
contribution to bimolecular recombination. The necessary defect density
is at least on the order of 1017 cm–3 for midgap defects and increases for more shallow defects. This
defect density is about 1 order of magnitude higher than the defect
densities that have so far been observed in the experiment.34,35 Thus, we conclude that the trap-assisted Auger recombination is
unlikely to be the reason for the observed nonradiative bimolecular
recombination and probably does not pose a fundamental limitation
to the efficiency of the lead-halide perovskites.
Results and Discussion
Recombination
Statistics
The complete picture of the Auger processes involving
traps as outlined in ref (33) is illustrated in Figure 1. In total, four processes can be summarized by four
transition coefficients T1...T4:(1) two electrons e and an empty trap ht transform into an
electron e* (at nonthermal energy) and a trapped electron et according to the reaction scheme: 2e + ht ↔ e*
+ et.
(2) an
electron, a hole h, and an empty trap transform into a hole h* (at
nonthermal energy) and a trapped electron: e + h + ht ↔
h* + et.
(3) an electron, a hole, and a trapped electron transform into an electron
(at nonthermal energy) and an empty trap: e + h + et ↔
e* + ht.
(4) two holes and a trapped electron transform into a hole (at nonthermal
energy) and an empty trap: 2h + et ↔ h* + ht.
Figure 1 Illustration of various interactions between
free charge carriers and defect states resulting in electron capture
(with coefficients T1, T2) and hole capture (T3, T4), respectively. Please note that the processes
2 and 3 consist of two possible interactions each. The energy levels
of the valence and conduction bands are here denoted as EV and EC, respectively. Furthermore, Et marks the imperfection level (trap depth).
Thus, processes 1 and 2 result
in electron capture and processes 3 and 4 in hole capture such that
a net recombination of an electron–hole pair requires a combination
of steps 1 or 2 with 3 or 4.
To fulfill the requirements of
detailed balance, we also have to consider the back reactions, i.e.,
impact ionization of trapped electrons or holes via hot electrons
or holes. The rates R1...4,b for the back
reactions are determined by the Auger coefficients C1...4* such
that we have, e.g., for back 1R1,b = C1*n*N, where n* denotes the concentration of hot electrons and N the concentration of filled traps. If we assume that the
thermalization of charge carriers is faster than the Auger processes
or their inverses, the ratio between n* and the overall
concentration n of electrons is constant and corresponds
to the ratio n0*/n0 between both
concentrations at thermal equilibrium. Thus, we define the coefficient C1 = C1*n0*/n0 and, analogously, C2 = C2*p0*/p0, C3 = C3*n0*/n0, and C4 = C4*p0*/p0 using p0*, p0, p*, and p as the analogous variables for the holes. Then, the rates
for the four transitions can be written as 1 2 3 and 4 Here, we
use the abbreviations 5 and 6 where n0 and p0 are the
equilibrium concentrations of the electrons and the holes. The concentrations n1 and p1 correspond
to the values of n and p, when the
Fermi level lies at the trap depth ET.
We eliminate the parameters C1,...,C4 in eqs 1–4 by using the principle of
detailed balance36 and expressing them
as a product of T1,...,T4 multiplied with either n1 or p1 in analogy to the derivation of
Shockley–Read–Hall statistics. By assuming steady-state
conditions dN/dt = 0, we may eliminate
the concentration N of filled traps by writing 7 We then obtain for the (normalized) density of occupied
trap states 8 The final
recombination rate RTA is subsequently
given by inserting eq 8 into RTA = R1 + R2 = R3 + R4 and is given by 9
Simulation
Results
Figure 2a illustrates eq 9 as
a function of the excess charge-carrier concentration Δn = n – n0 using the parameters given in Table 1. The rate of Auger recombination involving interactions
with defect states exhibits three regimes with different dependencies
of RTA on the excess charge-carrier concentration
Δn. We assume the semiconductor to be p-type
(n0 ≪ p0) in this example (doping density NA =
3 × 1015 cm–3),37 thus, for Δn ≪ NA, we are in low-level injection conditions. In addition,
we assume the defect to be close to the conduction band, i.e., n1 ≫ p ≫ p1. In this case, eq 9 simplifies to 10 i.e., the recombination
rate scales linearly with Δn = n. This linear scaling is independent of the position of the trap
and would also happen for a midgap trap, in which case, the rate would
be 11 For higher excess charge densities, Δn > NA, we enter high-level
injection conditions, where we may simplify eq 9 using the conditions n1 ≫ n = p = Δn ≫ p1 (for a trap close
to the conduction band edge). Then, we obtain 12 i.e., a cubic relation between the rate and the excess carrier concentration.
Only in the saturation regime, where n = p = Δn ≫ n1 ≫ p1, the recombination
rate 13 starts to scale
quadratically with Δn. Thus, the three regimes
visible in Figure 2a differ from the situation encountered for Auger recombination of
free charge carriers. Here, also three regimes are visible, but the
order for the Auger recombination rate RA (for free carriers) is RA ∼ Δn (for low-level injection), RA ∼ Δn2 (for n ≈ p), and RA ∼ Δn3 for high-level injection.
In contrast, the Auger recombination via traps features an intermediate
cubic scaling law as long as the doping concentration is smaller than
either n1 or p1. To estimate the magnitude of trap-assisted Auger recombination
for the specific case of lead-halide perovskites, we use equations
for the transition coefficients T1,...,T4 derived by Landsberg et al.,33 which are given by 14 where Table 2 provides the values for the abbreviations Ni, di, and bi for i = 1,...,4.
Figure 2 (a, c) Recombination rate and (b, d) effective
lifetime as a function of charge-carrier concentration. (a) The situation
of a shallow trap (ET = 0.1 eV) with the
solid gray line indicating the total trap-assisted Auger recombination
and the dotted lines illustrate the approximations given by eqs 10, 12, and 13 valid in three different injection
regimes. (c) The equivalent plot for the case of a midgap trap, which
only shows a linear regime at low Δn and a
quadratic regime at high Δn. (b) The effective
lifetime τeff for Auger recombination via traps assuming
a trap density NT = 1018 cm–3 and the radiative lifetime τrad =
Δn/Rrad assuming Rrad = kradnp, with krad = 10–10 cm3/s. (d) The effective lifetime for a deep trap. For
comparison, we also added the values for SRH recombination using capture
coefficients determined as discussed in ref (22) and using different trap
densities that are lower than the one for trap-assisted Auger recombination.
Table 1 Input Parameters
Used for the Calculations Presented in Figures 2 and 3 if Not Otherwise
Stateda
band gap Eg 1.6 eV
effective mass of electrons me 0.2m0
effective mass
of holes mh 0.2m0
relative permittivity εr 33.524
a There are various reported values for the effective mass of electrons
and holes in the literature that are ranging from ∼0.1 to ∼0.3.37,49−53 Here, we use a value of 0.2m0 for simplicity,
where m0 is the electron rest mass.
Table 2 Definition of the
Abbreviations Used To Determine the Trap-Assisted Auger Recombination
Coefficients Ti Using Equation 15a
i Ni di1 di2 bi
1 13 –260
2 0.5(33 – 15σL) 0.5(33 – 15σL)
3
4
a Here, Eg is the band
gap, Et is the trap depth with respect
to the conduction band, σ = mh/me is the ratio of the hole and electron effective
mass, and σL = 1/σ. In this form, the notation
is valid for free electrons in the conduction band interacting with
defect states. For free holes in the valence band, Et, σ, and σL have to be adjusted
accordingly.
Figure 2b shows the resulting effective
lifetime τeff for the trap-assisted Auger recombination
assuming a high trap density of 1018 cm–3. We define the effective lifetime for a given process as τeff = Δn/R, where R is the recombination rate for a certain recombination
mechanism. The effective lifetime τTA for the trap-assisted
Auger recombination is therefore defined as τTA =
Δn/RTA, whereas
the effective radiative lifetime is τrad = Δn/Rrad. Here, Rrad is the radiative recombination rate. We note that
for low-excess charge-carrier concentrations Δn, both the trap-assisted Auger recombination and radiative recombination
lead to a constant effective lifetime, consistent with the recombination
rate increasing linearly with Δn in both cases.
Once Δn exceeds the doping concentration assumed
to be NA = 3 × 1015 cm–3, the Auger lifetime drops drastically until Δn ≈ n1, at which point
the slope gets flatter again. This is the logical consequence of the
three regimes for RTA seen in Figure 2a. We also note that
even for such a high trap density of NT = 1018 cm–3, the radiative lifetime
is lower for all values of Δn.
Figure 2c,d show the situation
of a deep trap first for the recombination rate (c) and subsequently
for the effective lifetime (d). For deep traps, n1 is very small (n1 ≪ NA), thus there exist only two regimes (low injection
and high injection), but no saturation regime. In consequence, the
effective lifetimes for radiative and trap-assisted Auger recombination
have the same shape. For the assumed values of krad and NT, the values for τTA and τrad are quite similar. In Figure 2d, we also show for
comparison the effective Shockley–Read–Hall lifetime
via a deep trap. We do these calculations based on the theory of multiphonon
recombination discussed in ref (22) and based on refs (17) and (18). Here, we observe that for trap densities already much lower than
used for Auger recombination via traps, the SRH lifetime dominates
over a wide range of Δn values.
Having
established the general features of the recombination statistics of
Auger recombination involving traps, we now want to investigate more
closely under which circumstances the recombination rate is comparable
to the radiative recombination rate. In particular, we are interested
in the case described by eq 13, where the scaling is quadratic. In this scenario, we may
define the total bimolecular recombination rate Rbm as 15 i.e., the sum of radiative recombination
(kradn2),
minus the amount of light that is reabsorbed and contributes to the
internal generation (prkradn2, with pr being the probability of reabsorption37,38) plus the trap-assisted Auger recombination. Figure 3a illustrates the effective Auger coefficient CT ≡ kTA/NT as a function of trap depth ET. As it is the case for Shockley–Read–Hall
statistics, also the Auger recombination rate via defects shows its
maximum for midgap traps, when detrapping of captured charge carries
is least likely. The vertical dashed lines represent intrinsic defect
levels according to the density functional theory calculations as
reported in ref (39). In the next step, we evaluate the defect density NT, which has to be present in the samples to cause a certain
nonradiative bimolecular recombination coefficient knon. Table 3 shows the experimental data from various groups on the total, radiative,
and nonradiative bimolecular recombination coefficient. The values
for the nonradiative recombination coefficient vary quite strongly.
Therefore, we vary knon in the range between
10–12 and 10–10 cm3/s and show the necessary trap density as a function of trap position
in Figure 3b. In comparison,
we show the necessary trap depth to achieve a monomolecular Shockley–Read–Hall
type lifetime τSRH = 1 μs assuming the multiphonon
transitions as discussed in ref (22). We judge from Figure 3b that deep trap densities >1017 cm–3 are needed for midgap traps and higher for
shallower traps. Although such trap densities at midgap would lead
to very short SRH lifetimes that are not consistent with experiment,
such trap densities may explain the experimental data if the trap
is not midgap but at a trap depth of around 0.5–0.6 eV away
from either the conduction or valence band. To put these densities
into context, Table 4 compares the trap densities that have been measured on CH3NH3PbI3 in the literature. Table 4 suggests that so far most experimentally
observed trap densities are in the range of 1015–1016 cm–3, i.e., in a range that would not
lead to substantial trap-assisted Auger recombination.
Figure 3 (a) Coefficient CT of trap-assisted Auger recombination as a
function of the trap depth ET with respect
to the conduction band edge EC. Vertical
dashed lines represent trap depths of various intrinsic defects according
to ref (39). (b) Trap
density NT as a function of trap depths ET that would be needed to cause a nonradiative
bimolecular recombination coefficient of 10–11 and
10–10 cm3/s (light blue and dark blue
curves, respectively). In addition, we added the trap density needed
to achieve a 1 μs monomolecular lifetime as calculated in ref (22) based on the theory of
multiphonon Shockley–Read–Hall recombination.
Table 3 Values for the Bimolecular
Recombination Coefficients in Units of cm3/s of CH3NH3PbI3 from Literature
references kext (cm3/s) krad (cm3/s) knon (cm3/s)
(37) 4.78 × 10–11 8.7 × 10–10 neglected
(27, 37)a 4.78 × 10–11 8.4 × 10–11 4.4 × 10–11
(54)b 1.4 × 10–10 to 2 × 10–11 6.8 × 10–10 0
(26)c 8.1 × 10–11 7.1 × 10–11 7.2 × 10–11
(26)d 7.9 × 10–11 1.8 × 10–10 5.6 × 10–11
a Data from ref (37) corrected using the evidence from ref (27) that only 66% of the bimolecular recombination
is radiative.
b Measurements
done at different thicknesses.
c Samples with PbI2 precursor.
d Samples made from PbCl2 precursor.
Table 4 Trap Densities Reported
for CH3NH3PbI3 Thin Films in the
Literature
reference method trap density
(cm–3) trap depth ET (eV)
(34) thermally stimulated current (TSC) >1015 ∼0.5
(55) noise spectroscopy 4 × 1015 ∼0.8
(56) deep level transient spectroscopy (DLTS) ∼1015 0.62
∼1015 0.75
(57) steady state photocarrier grating >1016 recombination center
(58) TSC 9 × 1016 0.18
5 × 1016 0.49
(59) admittance spectroscopy ∼1016 cm–3 0.16
(60) admittance spectroscopy ∼1016 cm–3 a 0.27
∼1017 cm–3 b 0.28
(35) DLTS 9 × 1013 to 5 × 1014 cm–3 0.78
a Dimethylformamide as solvent with hydroiodic acid as additive.
b Dimethyl sulfoxide as solvent.
Discussion and Outlook
Having established that Auger recombination via traps is not likely
to explain the observed nonradiative contributions to bimolecular
recombination, it is useful to discuss the implications of this result
and consider alternative explanations for the observed trends. First,
we want to state that most experimental approaches to study bimolecular
recombination would not be sensitive to whether bimolecular recombination
is radiative or nonradiative. In most cases, the transient decay is
fitted with a model that accounts for bimolecular recombination. In
the case of transient photoluminescence experiments, it is clear that
some of this recombination has to be radiative to generate a signal,
but the determination of how much of this bimolecular recombination
is radiative would require additional information. This information
can either be another experiment that determines the total recombination
as done by Richter et al.26 or some experimental
circumstances that would distinguish radiative from nonradiative such
as the sensitivity of radiative recombination to parasitic absorption
via the modulation of the photon recycling probability as done previously
by us.27 Certainly, two sets of experimental
evidence we are aware of are not very much and future will tell whether
these results are reproduced by others or are a peculiar feature of
the samples or the data analysis in these articles. However, assuming
that the data are representative, we want to briefly explore what
other explanations there might be.
In a simple zero-dimensional
picture, the authors are not aware of any recombination mechanism
that would be quadratic in charge-carrier density and still be nonradiative
other than the one discussed here. Thus, it is logical to explore
effects requiring more dimensions. There are essentially two options
in our opinion: (i) diffusion of carriers at high-level injection
inside the films leads to a decrease in signal that could be interpreted
as a recombination but is not or (ii) lateral inhomogeneous lifetimes
lead to a distribution of decay times that creates a decay that appears
quadratic in the charge-carrier density but is not related to locally
quadratic recombination mechanisms. Let us briefly look into the two
options in more detail. After the excitation of a sample with a laser
pulse, electrons and holes are created based on the generation profile
of the sample. Disregarding interferences, it is clear that more electrons
and holes would be created close to the front surface of the sample
and less toward the back. As long as the electron and hole concentrations
are roughly equal, the luminescence is higher than after equilibration
of the charge-carrier distribution. This leads to a decay in the luminescence
that requires no recombination to happen. Diffusion of charge carriers
during a transient photoluminescence experiment has been taken into
account in the classical theory articles on transient photoluminescence
experiments,40,41 in first experiments on perovskite
films with contact layers,42 and in the
case of transient experiments on perovskite crystals.43,44 However, given the range of mobilities that is commonly reported,45,46 diffusion and equilibration of charge carriers in a film of few
hundreds of nanometer thickness should happen in the sub-nanosecond
range (e.g., ∼300 ps for a 300 nm film and a mobility of 20
cm2/(V s)). Thus, for this explanation to affect the experiments,
there have to be at least some charge carriers with a substantially
lower mobility to see an effect on the time scale where bimolecular
recombination is typically observed.
The second option is laterally
inhomogeneous lifetimes that have been reported and studied in a range
of publications.47,48 If by averaging over a certain
area, the macroscopic decay curve does not capture one lifetime but
a broad distribution of lifetimes, the tail of this distribution toward
shorter lifetimes could influence the shorter time scales of a transient
photoluminescence experiment and thereby affect the way we interpret
the data. Future work of modeling the photoluminescence in two or
three dimensions will have to show whether this is a likely explanation
for the observed data in refs (26, 27). Both of these alternative approaches to explain the experimental
data would not be a unique feature of every MAPI sample, but instead
could vary from sample to sample. They would therefore not contradict
reports6,7 of extremely high photoluminescence quantum
efficiencies that leave little room for additional nonradiative pathways.
Conclusions
In summary, we have developed a rate model for
the full recombination statistic of electrons and holes via trap-assisted
Auger recombination. The model covers the linear low injection case
with a recombination rate RTA ∝
Δn proportional to the density of excess charge
carriers Δn, as well as two nonlinear situations,
namely, high-level injection with RTA ∝
Δn3 and the saturation situation
with RTA ∝ Δn2. The latter case represents the bimolecular recombination
that directly competes with radiative recombination. As an example,
our calculations following the theory of ref (33) yield the actual rates
for the case of CH3NH3PbI3. The coefficients
for this specific case are however relatively small. Therefore, we
conclude that this mechanism is not likely to be the origin of the
experimentally measured nonradiative bimolecular recombination coefficients.
The authors declare no competing financial interest.
Acknowledgments
T.K. and U.R. acknowledge support from the DFG (Grant Nos. KI-1571/2-1
and RA 473/7-1) and from the Helmholtz Association via the PEROSEED
project. T.K. thanks Igal Levine (Weizmann, Rehovot) for sharing most
of the references for Table 4.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145782310.1021/acsomega.7b00928ArticleDesign of Polyproline-Based
Catalysts for Ester Hydrolysis Hung Pei-Yu †Chen Yu-Han †Huang Kuei-Yen †Yu Chi-Ching †Horng Jia-Cherng *†‡†Department
of Chemistry and ‡Frontier Research Center on Fundamental and
Applied Science of Matters, National Tsing
Hua University, 101 Sec. 2 Kuang-Fu Rd., Hsinchu, Taiwan 30013, ROC* E-mail: jchorng@mx.nthu.edu.tw. Phone: +886-3-5715131
ext. 35635. Fax: +886-3-5711082 (J.-C.H.).07 09 2017 30 09 2017 2 9 5574 5581 05 07 2017 24 08 2017 Copyright © 2017 American Chemical Society2017American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
A number of simple
oligopeptides have been recently developed as
minimalistic catalysts for mimicking the activity and selectivity
of natural proteases. Although the arrangement of amino acid residues
in natural enzymes provides a strategy for designing artificial enzymes,
creating catalysts with efficient binding and catalytic activity is
still challenging. In this study, we used the polyproline scaffold
and designed a series of 13-residue peptides with a catalytic dyad
or triad incorporated to serve as artificial enzymes. Their catalytic
efficiency on ester hydrolysis was evaluated by ultraviolet–visible
spectroscopy using the p-nitrophenyl acetate assay,
and their secondary structures were also characterized by circular
dichroism spectroscopy. The results indicate that a well-formed polyproline
II structure may result in a much higher catalytic efficiency. This
is the first report to show that a functional dyad or triad engineered
into a polyproline helix framework can enhance the catalytic activity
on ester hydrolysis. Our study has also revealed the necessity of
maintaining an ordered structure and a well-organized catalytic site
for effective biocatalysts.
document-id-old-9ao7b00928document-id-new-14ao-2017-009288ccc-price
==== Body
Introduction
Natural enzymes, exhibiting
powerful efficiency and remarkable
selectivity because of their unique folded structures, are usually
involved in biochemical reactions. They play a major part in maintaining
the functions in organisms. For instance, proteases are capable of
accelerating the digestion of proteins into shorter fragments by hydrolyzing
the peptide bonds. However, restricted to their length and complexity,
most enzymes are difficult to acquire and vulnerable to environmental
conditions, such as pH and temperature. Thus, artificial enzymes have
received much attention in recent years because of their great stability
and easy accessibility. Baker et al. and Korendovych et al. explored
the efficient catalysts with rigid protein scaffolds by computational
design.1,2 Ulijn et al. conducted phage display as
a discovery technique for selecting active sequences.3 To demonstrate more details on the importance of three-dimensional
structures, many artificial enzymes using various scaffolds, such
as α-helical-coiled coils and barrels,4−6 β3-peptide bundles,7 short helices,8 and β-hairpins,9,10 were
reported. Moreover, nanomaterials11,12 and self-assembled
structures including membranes,13 amyloid
fibers,14−17 and hydrogels18 were implemented for
mimicking similar protein structures; yet, the activity of these supramolecular
frameworks is still limited compared to natural enzymes.
In
natural enzymes, their active site is frequently composed of
several residues, taking responsibility for specific binding and chemical
catalysis. For example, chymotrypsin, a serine protease, possesses
a hydrophobic pocket for binding to aromatic substrates and a catalytic
site composed of His57, Asp102, and Ser195 residues.19 It is generally accepted that more than two amino acid
residues that operate together at the active site of enzymes are regarded
as a catalytic dyad or triad. Mechanically, nucleophilic residues
(cysteine and serine) play a role of attacking the substrate; histidine
acts as a general base to deprotonate the nucleophile; and acidic
residues (aspartic acid and glutamine acid) function to polarize and
align the base (Figure 1A).20,21 Additionally, it is well-documented that
the guanidyl group in the arginine residue22 and the backbone NH group1,23,24 can aid in stabilizing the transition state of the substrate. These
functional residues were initially applied to the primary sequence
design25 and subsequently considered in
the coassembly system.15,16,22
Figure 1 (A)
Schematic diagram of the catalytic triad in a protease. (B)
Cartoon representation of a PPII helix with His incorporated into
the i position.
Inspired by the previous reports, here we chose polyproline
peptides
as the scaffold and introduced a catalytic dyad or triad into the
peptides. It was found that proline-rich sequences in proteins often
form a polyproline II (PPII) structure, a left-handed helix with all
trans peptide bonds, and three residues in each turn. On account of
their structural stability and rigidity, oligoproline peptides were
widely used as rulers and scaffolds for various studies.26,27 Hence, we designed and synthesized a series of 13-residue polyproline
peptides containing a histidine residue at the i position
and other residues with a functional side chain, such as Asp, Ser,
and Cys, at the i + 3 or i –
3 position, as minimalistic biocatalysts (Figure 1B). According to the structure of a PPII
helix, these positions would be located on the same side, and we predicted
that the imidazole side chain of His could place an appropriate orientation
and form strong interactions with the functional groups at position i – 3 or i + 3 to form a dyad or
triad active site. Additionally, (2S,4R)-hydroxyproline (Hyp) and (2S,4R)-methoxyproline (Mop), 4-substituted proline derivatives, were found
to have a high propensity to form PPII conformation because of the
stereoelectronic effects.28,29 Therefore, they were
also used to replace the regular proline residues for understanding
the correlation between PPII structure and enzyme activity. The results
showed that the interactions between different functional groups significantly
contributed to the catalytic ability and that a well-formed PPII structure
could lead to a higher catalytic efficiency.
Results and Discussion
To explore the activity of polyproline-based catalysts on ester
hydrolysis, we chose (Pro)11 as the control peptide (free P11) and designed a series of peptides in which the specific
position was substituted with His and the residues frequently found
in the active sites of natural enzymes. For a single His-incorporated
peptide (H6), the His residue was placed in the middle
(position 6) of the peptide because the conformation of His might
be fixed by the proline-rich sequence. In the multiple substitution
peptides, His residues were incorporated into position 6, whereas
nucleophilic (Cys, Ser, and His), neutral (Trp), and acidic (Asp)
residues were placed at positions 3 and 9 to mimic the triad or dyad
in natural enzymes. These peptides were designated as H3H6, W3H6, S3H6, S3H6D9, and C3H6D9. In addition, the peptides with Pro replaced by Hyp
(Hyp-H3H6 and Hyp-C3H6D9) or Mop (Mop-H3H6) were applied to investigate the relationship between
PPII-forming propensity and catalytic efficiency. A Gly–Tyr
dipeptide was attached to the C-terminus of each peptide for concentration
determination. Furthermore, all peptides except for free P11 have capped ends because a previous study found that the removal
of the capping groups would reduce the catalytic activity.14 The sequences of designed peptides are shown
in Table 1.
Table 1 Peptide Sequences Used in This Study
peptide sequencea
free P11 NH-PPPPPPPPPPPGY-OH
H6 Ac-PPPPPHPPPPPGY-NH2
W3H6 Ac-PPWPPHPPPPPGY-NH2
H3H6 Ac-PPHPPHPPPPPGY-NH2
S3H6 Ac-PPSPPHPPPPPGY-NH2
S3H6D9 Ac-PPSPPHPPDPPGY-NH2
C3H6D9 Ac-PPCPPHPPDPPGY-NH2
Hyp-H3H6 Ac-OOHOOHOOOOOGY-NH2
Hyp-C3H6D9 Ac-OOCOOHOODOOGY-NH2
Mop-H3H6 Ac-O′O′HO′O′HO′O′O′O′O′GY-NH2
a Ac indicates an acetylated N-terminus
and NH2 indicates an amidated C-terminus; Hyp and O are
the abbreviations for (2S,4R)-hydroxyproline;
and Mop and O′ are the abbreviations for (2S,4R)-methoxyproline.
After synthesis of the peptides, circular dichroism
(CD) spectroscopy
was utilized to characterize their secondary structures. As shown
in Figure 2, all peptides
exhibit a similar far-UV spectrum with a positive band between 220
and 230 nm and a negative peak near 205 nm, indicating the presence
of PPII conformation. We used the maximal molar ellipticity at the
positive band to evaluate their PPII-forming propensity and content.
As shown in Figure 2 and Table 2, the
replacement of proline to nonproline residues causes the decrease
in the PPII structure. Compared to free P11, all peptides
with Pro replaced by other residues display a much weaker positive
band, and the multiple substitutions impose an even greater effect
on PPII conformation than does the single substitution. Although the
peptides with double- and triple-substituted nonproline residues show
a much weaker characteristic CD signal of the PPII structure, W3H6 displays a stronger positive band around 230 nm due to
the electronic absorption of aromatic residues.30,31 Therefore, the PPII propensity of W3H6 could not be
evaluated solely by its ellipticity at the positive band. As expected, Hyp-H3H6, Hyp-C3H6D9, and Mop-H3H6 form a relatively intense PPII structure, and their molar ellipticity
in the positive band is close to or even higher than that of free P11 (Figure 2B and Table 2), which can be attributed to that Hyp and Mop prefer a Cγ-exo pucker and a trans peptide bond to enhance PPII-forming propensity.28,29
Figure 2 Far-UV
CD spectra for the designed peptides: (A) H6, W3H6, S3H6, and S3H6D9 and
(B) H3H6, C3H6D9, Hyp-H3H6, Hyp-C3H6D9, and Mop-H3H6 at pH 7.4 and 25 °C.
The spectrum of free P11 is included for comparison.
Table 2 CD Parameters for
the Peptides at
25 °C
peptide λmax (nm) [θ]max (103 deg cm2 dmol–1)
free P11 228 3.37
H6 228 1.66
W3H6 229 2.75
H3H6 229 0.86
S3H6 229 0.75
S3H6D9 231 0.43
C3H6D9 231 –0.18
Hyp-H3H6 226 6.00
Hyp-C3H6D9 226 4.62
Mop-H3H6 226 3.12
To evaluate the catalytic
efficiency of our designed peptides and
compare the results with the previous hydrolase designs, we chose p-nitrophenyl acetate (p-NPA) as a simple
chromogenic substrate to monitor the catalytic reaction. The catalytic
reaction is as follows:
The initial hydrolytic rate (V0) was
determined by monitoring the production of 4-nitrophenol at 405 nm
and pH 7.4 with ultraviolet–visible (UV–vis) spectroscopy.
As shown in Figure 3A,B, the dependence of the initial hydrolytic rate on the substrate
concentration for each peptide is consistent with the Michaelis–Menten
model, and the kinetic parameters can be obtained and calculated by
fitting the curves to the model. The determined parameters are listed
in Table 3. The reaction
in the presence of free histidine residues was also monitored and
used as a control. Figure S3 in the Supporting Information indicates that the rate of hydrolysis of p-NPA in the presence of free P11 was extremely
low and close to that without any peptides or amino acids present
in solution, suggesting that the polyproline backbone was unable to
catalyze the reaction. This is likely attributed to the fact that free P11 does not contain nucleophiles to accelerate the reaction,
and the proline residues lack NH groups on the backbone to stabilize
the oxyanion intermediate of ester hydrolysis as suggested by previous
studies.1,23,24
Figure 3 (A–C)
Esterase activity for the designed peptides at pH
7.4 and 25 °C, with solid lines showing the fits to the Michaelis–Menten
equation. (D) Esterase activity for the selected peptides under different
pH conditions, with solid lines showing the fits to the modified Henderson–Hasselbalch
equation (eq 1).
Table 3 Kinetic Parametersa for p-NPA Hydrolysis by Designed
Peptides
at 25 °C and pH 7.4
peptide kcat (10–3 s–1) KM (mM) kcat/KM (M–1 s–1)
free His (H-His-OH) 0.78 ± 0.16 1.73 ± 0.49 0.45 ± 0.16
free P11 0.28 ± 0.06 0.88 ± 0.32 0.31 ± 0.13
H6 0.70 ± 0.05 1.81 ± 0.17 0.39 ± 0.05
W3H6 1.15 ± 0.38 1.92 ± 0.85 0.60 ± 0.33
H3H6 2.44 ± 0.73 4.38 ± 1.50 0.56 ± 0.25
S3H6 0.86 ± 0.33 1.52 ± 0.82 0.56 ± 0.37
S3H6D9 0.97 ± 0.24 2.12 ± 0.69 0.46 ± 0.19
C3H6D9 1.05 ± 0.27 2.44 ± 0.78 0.43 ± 0.18
Hyp-H3H6 1.76 ± 0.16 1.42 ± 0.19 1.23 ± 0.20
Hyp-C3H6D9 1.73 ± 0.15 1.75 ± 0.20 0.99 ± 0.14
Mop-H3H6 1.88 ± 0.67 3.02 ± 1.30 0.62 ± 0.35
a Deviations of kcat and KM were the standard
errors of fitting and were used to calculate the deviation of kcat/KM by the equation .
To prevent the electrostatic
repulsions and extra charges from
affecting the catalytic efficiency, we introduced end caps by acetylating
the N-terminus and amidating the C-terminus on the following peptides: H6, W3H6, H3H6, S3H6, S3H6D9, and C3H6D9. Of the designed peptides,
His, Trp, Ser, Asp, or Cys was incorporated in the multiple substitution
peptides for the purpose of forming catalytic dyads or triads. As
shown in Table 3, the
catalytic efficiency of the H6 peptide (kcat/KM is 0.39 M–1 s–1) is lower than that of free His (kcat/KM is 0.45 M–1 s–1), indicating
that the single His incorporation in a polyproline peptide could not
induce an effective electron transfer to catalyze the reaction. By
contrast, the polyproline peptides with double substitutions (H3H6, S3H6, and W3H6) are 1.5-fold
more active in comparison with H6, suggesting that the
residues (His, Ser, and Trp) at position 3 of H3H6, S3H6, and W3H6 could interact with His at position
6 to facilitate the electron transfer and enhance the catalytic properties.
Therefore, it could be inferred that all peptides with double substitutions
may form a catalytic dyad in their active site. As detailed in Table 3, W3H6 is more efficient than H3H6 and S3H6 and
has a kcat/KM value of 0.60 M–1 s–1. It could
be explained by an increased nucleophilicity of His because of the
histidine–aromatic interaction provided by Trp at position
3, which was also observed in barnase, a natural hydrolase.32 To validate our assumption that the PPII structure
can facilitate a proper orientation between the side chains of His
and Trp and generate strong interactions to enhance the catalytic
activity, we prepared a dipeptide Trp–His (WH)
and measured its catalytic efficiency. As shown in Figure S4 of the Supporting Information, its catalytic efficiency
(kcat/KM is
0.52 M–1 s–1) is lower than that
of W3H6, providing a piece of evidence that the PPII
framework does play a positive role to increase its catalytic activity.
Surprisingly, the catalytic activity of the peptides with triple substitutions
slightly decreased compared with those with double substitutions.
Their catalytic activity of the hydrolyzing p-NPA
is around 0.45 M–1 s–1. It seems
that introducing more residues into the PPII structure could not always
benefit their catalytic abilities. As shown in Table 2, the peptides with triple substitutions
(S3H6D9 and C3H6D9) dramatically reduce
the propensity of forming a PPII structure, which may lead to an increased
distance between the i and i + 3/i – 3 positions. Thus, it could be assumed that the
catalytic triad may not be successfully formed in S3H6D9 and C3H6D9, and Asp cannot play a role as orienting
the His residue and neutralizing the intermediates.
To demonstrate
more structure–activity relationships, we
replaced the proline residues of H3H6 and C3H6D9 with Hyp and used Mop to substitute for the proline of H3H6 as well to form a more robust PPII structure. Interestingly, as
shown in Figure 3B,
we found that both Hyp-H3H6 and Hyp-C3H6D9 remarkably accelerated the hydrolysis of p-NPA.
An approximately threefold increase in catalytic efficiency was observed
for Hyp-H3H6 compared with free His residue. Both of
the Hyp-H3H6 (kcat/KM is 1.23 M–1 s–1) and Hyp-C3H6D9 (kcat/KM is 0.99 M–1 s–1) exhibited a twofold higher efficiency than that of their corresponding
peptides H3H6 (kcat/KM is 0.56 M–1 s–1) and C3H6D9 (kcat/KM is 0.43 M–1 s–1), respectively. As shown in Table 3, the peptides with Hyp-rich sequences show a relatively
stronger binding affinity (lower KM) for
the substrate than do their Pro-rich counterparts, leading to a much
higher catalytic efficiency. It is likely that Hyp residues provide
extra interactions and result in a stronger binding to the substrates.
As reported in a few natural active sites, an oxyanion hole could
stabilize the transition state of the substrate.1,23,24 Therefore, we believe that the OH group
on the Hyp side chain could potentially serve as a hydrogen bond donor
to stabilize the reaction intermediate and increase the reaction rate.
This argument may also be supported by the observation that Mop-H3H6 exhibits a slightly higher activity (kcat/KM is 0.62) than H3H6 but a much lower activity than Hyp-H3H6 (Figure 3C). Because the OMe
group on the Mop side chain cannot be a hydrogen bond donor, Mop cannot
form similar hydrogen bonding interactions as Hyp does during the
reaction, leading to a lower catalytic efficiency. In addition, the
fact that Hyp-H3H6, Hyp-C3H6D9, and Mop-H3H6 have a higher catalytic efficiency than their corresponding
peptides (H3H6 and C3H6D9) demonstrates
the important role of a PPII structure. As aforementioned, the peptides
containing Hyp or Mop residues favor the formation of a stable PPII
structure, which may bring about a closer distance between the i and i + 3/i –
3 positions. As a result, it could be speculated that the PPII helix-forming
propensity of our designed peptides also has a great impact on their
catalytic activity. Although the efficiency of our designed peptides
is not comparable to that of natural enzymes in catalyzing such an
ester hydrolysis reaction, most of our designed polyproline-based
peptides still exhibited a greater catalytic activity than some reported
peptide-based nanostructures whose kcat/KM ranges from 0.09 to 0.62 M–1 s–1 at pH 7.5.12,15,16 Most notably, even as a short peptide, the activity
of Hyp-H3H6 is better or comparable to the previously
reported metal-based esterases (kcat/KM is 0.33–1.38 M–1 s–1 at pH 7.5).5
Because
the protonated and deprotonated state of an active site
would affect its catalytic activity, we investigated the hydrolysis
reaction under different pH conditions for the selected peptides: W3H6, H3H6, S3H6D9, and Hyp-H3H6. As illustrated in Figure 3D, while the efficiency of these peptides remained low below
pH 8.0, a noticeable increase could be observed as the pH values rose
beyond 8.0. The catalytic efficiency (kcat/KM) of each selected peptide at pH 10.0
is in the range of 23–30 M–1 s–1, which is 30-fold greater than that at pH 7.4 (Table S3 in the Supporting Information). Using eq 1, a pair of kinetic pKa could be determined for each selected peptide (Table 4). As the typical
pKa of a His imidazole ring is about 6,
it is likely that the obtained pKa values
around 6.5 represented deprotonation of a His side chain. Besides,
we would suggest that the higher pKa reflected
deprotonation of the Tyr side chain because its pKa is approximately 10.3 in the free form. We further used 1H NMR spectroscopy to measure the pKa of a His side chain in S3H6D9. A series of high-resolution
one-dimensional (1D) 1H NMR spectra for S3H6D9 were acquired at pH values ranging from 4 to 8 (Figures 4A and S5 in the Supporting Information), whereas a titration
curve was obtained by plotting the chemical shifts of His C2H versus pH (Figure 4B). By fitting the titration curve into the Henderson–Hasselbalch
equation (eq 2), a pKa value of 6.64 and a Hill coefficient of 1.6
could be determined for S3H6D9. The pKa value measured by NMR is in good agreement with the
pKa value derived by the kinetic hydrolysis
assay, reflecting that the deprotonation of the His imidazole group
could significantly increase the catalytic efficiency.
Figure 4 (A) Representative high-resolution
1D 1H NMR spectra
of peptide S3H6D9, with the C2H peak of His
labeled with an “*”. (B) Titration curve for the peptide S3H6D9 produced from 1D 1H NMR titration experiments,
with a solid line showing the fit to the Henderson–Hasselbalch
equation (eq 2).
Table 4 Kinetic pKa and Maximal Efficiency for p-NPA Hydrolysis by
Selected Peptides
peptide pKa1 pKa2 kcat/KM(max)1 (M–1 s–1) kcat/KM(max)2 (M–1 s–1)
W3H6 6.73 ± 0.18 9.83 ± 0.01 0.50 ± 0.06 47.93 ± 0.49
H3H6 6.30 ± 0.43 9.74 ± 0.01 0.32 ± 0.07 42.36 ± 0.49
S3H6D9 6.27 ± 0.44 9.91 ± 0.03 0.29 ± 0.09 42.46 ± 1.39
Hyp-H3H6 6.74 ± 0.93 9.92 ± 0.11 0.81 ± 0.46 53.78 ± 5.93
Furthermore, to have more insights into the
structure of designed
peptides, we conducted Hartree–Fock (HF) calculations on the
conformation of oligopeptides. As it was found that Ac-(Pro)5-OMe is the simplest peptide model to form a stable PPII structure,33 we used the seven-residue oligopeptide models,
Ac-(Pro)2Ser(Pro)2HisPro-OMe, Ac-Cys(Pro)2His(Pro)2Asp-OMe, and Ac-(Pro)7-OMe,
to simplify the computational studies, in which Ac-(Pro)2Ser(Pro)2HisPro-OMe was used to mimic S3H6, whereas Ac-Cys(Pro)2His(Pro)2Asp-OMe was
utilized as a model to mimic C3H6D9. In the energy-minimized
structure, the dihedral angles of Ac-(Pro)2Ser(Pro)2HisPro-OMe and Ac-Cys(Pro)2His(Pro)2Asp-OMe are similar to those of Ac-(Pro)7-OMe and an idealized
PPII helix, indicating that this peptide could form a PPII-like helix
(Table S4 in the Supporting Information). For an ideal PPII helix, every third residue is about 9 Å
apart, suggesting that the distance between the two side chains at
positions i and i + 3 should be
less than 9 Å to form possible interactions. As shown in Figure
S6 of the Supporting Information, the distance
between the side chains of Ser and His in the energy-minimized structure
of Ac-(Pro)2Ser(Pro)2HisPro-OMe is 5.4 Å,
which is significantly shorter than 9 Å, suggesting that the
functional groups of Ser and His might interact and form a reaction
dyad to catalyze ester hydrolysis. This finding may in part explain
why S3H6 exhibits a better activity than H6. For the optimized structure of Ac-Cys(Pro)2His(Pro)2Asp-OMe (Figure 5), the distance between Cys and His is 2.90 Å, whereas the distance
between His and Asp is up to 6.7 Å. In comparison, the distances
within the catalytic triad of chymotrypsin, a serine protease, are
shorter than 3 Å,19 which facilitates
the proton transfer between them. It could be inferred that the functional
groups in the triple substitution peptide, C3H6D9, might
not form a catalytic triad because the long distance between His and
Asp could hinder them from forming an appropriate orientation between
the functional groups. Therefore, the observation in the computational
structure may rationalize why the triple substitution peptides exhibited
a less catalytic efficiency than did the double substitution peptides.
Figure 5 Energy-minimized
structure model for Ac-Cys(Pro)2His(Pro)2Asp-OMe
representing the peptide C3H6D9. The
distances between the side chains of Cys, His, and Asp are indicated
in the diagram.
Conclusions
In
the current work, a series of polyproline peptides were designed
and prepared to form PPII helices and serve as a scaffold to catalyze
ester hydrolysis. We found that introducing a pair of residues containing
His into the PPII structure could successfully imitate a catalytic
dyad and improve the catalytic efficiency. However, introducing more
than two nonproline residues could dramatically perturb the PPII structure
and failed to form a catalytic triad in the polyproline-based scaffold.
Surprisingly, the replacement of Pro to Hyp in the peptide not only
favors forming a stable PPII helix but also provides additional interactions
to accelerate the hydrolysis of ester. In addition, the deprotonation
of histidine side chains could enhance the catalytic activity of peptides.
Our results provide compelling lines of evidence that the secondary
structure of the peptide-based enzymes could have substantial impacts
on their catalytic activity for ester hydrolysis and demonstrate new
insights into the structure–activity relationship of polyproline-based
catalysts. This work also reveals valuable information for the design
of potentially useful peptide-based enzymes. With a view to develop
remarkable artificial enzymes, the studies of organizing suitable
secondary and tertiary structures to improve their catalytic activity
are currently on the way in our laboratory.
Materials and Methods
General
Chemical reagents and [(9-fluorenylmethyl)oxy]carbonyl
(Fmoc) amino acids were purchased from Advanced ChemTech, Alfa Aesar,
ECHO, JT Baker, and Sigma-Aldrich and used without further purification.
Fmoc-(2S,4R)-Mop was synthesized
by the method previously described.29 Preloaded
Tyr resin was prepared by attaching Fmoc-Tyr-OH to 2-chlorotrityl
resin using the procedure previously described.31 The loading capacity of Fmoc-Tyr resin was determined according
to the previously reported method (Applied Biosystems Technical Note
123485, Rev. 2, http://www3.appliedbiosystems.com/cms/groups/psm_marketing/documents/generaldocuments/cms_040640.pdf). Matrix-assisted laser desorption/ionization time-of-flight (MALDI-TOF)
spectra were obtained using an Autoflex III SmartBeam LRF200-CID spectrometer
(Bruker Daltonics).
Peptide Synthesis and Purification
All peptides were
synthesized on a 0.05 mmol scale by standard solid-phase methods and
Fmoc chemistry protocols. HBTU-mediated coupling reactions were carried
out on a Discover SPS microwave peptide synthesizer (CEM Corp.). Preloaded
2-chlorotrityl resin was used to produce a free C-terminus, whereas
the use of the Rink amide resin generated an amidated C-terminus upon
cleavage. Cleavage of the peptides from the resin and side-chain deprotection
was performed using a solution of 95% trifluoroacetic acid (TFA)/2.5%
triisopropylsilane (TIS)/2.5% H2O (v/v) or 94% TFA/1% TIS/2.5%
H2O/2.5% 1,2-ethanedithiol (v/v) to treat the peptide-resin
product for 3 h at ambient temperature. The filtrate was then precipitated
and washed with ice-cold methyl t-butyl ether and
purified by reverse-phase HPLC with a semipreparative C18 column.
H2O/acetonitrile gradients with 0.1% (w/v) TFA were used
as the eluting solvent system to purify the peptides. The purified
products were identified by MALDI-TOF-mass spectrometry (Table S1
and Figure S2 in the Supporting Information). All peptides were more than 90% pure according to the HPLC analysis
as shown in Figure S1 of the Supporting Information.
Preparation of Peptide Stock Solutions
Purified and
lyophilized peptides were dissolved in 25 mM buffer solution [MES
(pH 6.0–6.5), HEPES (pH 7.0), Tris (pH 7.4–9.0), and
CAPS (pH 10.0)] to make a 0.5 mM peptide stock solution. The concentration
of peptides was determined by the UV absorbance at 280 nm in 6 M guanidine
hydrochloride at pH 6.5, using an extinction coefficient of 1420 M–1 cm–1 for Tyr and 5500 M–1 cm–1 for Trp.
CD Spectroscopy
CD spectra were recorded on an Aviv
model 410 CD spectrometer with a 1 mm path-length-quartz cuvette.
The measurements were performed in pH 7.4 and 25 mM Tris buffer with
a peptide concentration of 100 μM. The far-UV CD spectra were
taken from 190 to 260 nm with an averaging time of 10.0 s and a wavelength
step of 1 nm at 25 °C.
Kinetic Assays
The catalytic activities
of the peptides
were determined using p-NPA as the substrate. The
kinetic measurements were performed on a JASCO V-630 spectrophotometer
associated with an STR-773 water thermostatic cell holder and stirrer
by monitoring the absorbance of the hydrolysis product (p-nitrophenol) at 348 nm or 405 nm at 25 °C. A volume of 100
μL of the freshly prepared peptide stock solution was added
to 1900 – x μL of buffer solution. After
having recorded the initial absorbance (blank), a volume of x μL of 20 mM p-NPA stock in acetonitrile
was subsequently added to obtain a final p-NPA concentration
of 100–1600 μM (the final acetonitrile content was less
than 5% in all reaction mixtures). The reaction mixture was stirred
for 60 s before collecting the data, and the absorbance was recorded
every 10 s for 150–1200 s (as shown in Table S2 of the Supporting Information). Initial rates were determined
from linear fits of the plots of absorbance versus time, and the values
were from averaging duplicate measurements. The extinction coefficients
of the hydrolysis product at different pH values were experimentally
determined by measuring the absorbance of p-nitrophenol
in the specified buffers and by taking the average of at least three
repeats. The reported kinetic parameters (kcat and KM) were derived by fitting the
data to the Michaelis–Menten equation, and the pH-dependent
curves were fit to the following modified Henderson–Hasselbalch
equation 1
Determination of pKa by NMR
A series of S3H6D9 (1.2 mM) peptide samples were prepared
in 90% H2O/10% D2O-containing sodium 3-(trimethylsilyl)-1-propanesulfonate
in solution as the chemical shift reference. Their pH values in the
range of 4–8 were adjusted by adding NaOD or DCl directly into
the samples. High-resolution 1D 1H NMR spectra were acquired
at 25 °C using a Varian VNMRS-700 NMR spectrometer (Varian, Inc.)
at National Tsing Hua University Instrumentation Center. The spectra
were analyzed using Bruker Topspin (v.2.1) software, and the pKa values were determined by fitting a plot of
the chemical shift (δ) of His C2H versus pH into
the modified Henderson–Hasselbalch equation 2 where δ is the observed chemical shift,
δd is the chemical shift for the fully deprotonated
species, δp is the chemical shift for the fully protonated
species, and n is the Hill coefficient, which is
1 for a residue that follows ideal Henderson–Hasselbalch behaviors.
Structure Modeling
Geometry optimization for the model
peptide in the aqueous phase was carried out using the HF/6-31+g(d)
and CPCM-SCRF solvation method, conducted by the Gaussian 09 software.34 The initial structure was generated with idealized
torsion angles for the PPII backbones based on the reported structural
data.35
Supporting Information Available
The Supporting Information is
available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.7b00928.Measured molecular
weights of the peptides, detailed
experimental conditions for pH-dependent kinetic assays, pH-dependent
kinetic parameters for ester hydrolysis, dihedral angles of energy-minimized
structural models, HPLC chromatograms, MALDI-TOF spectra, UV–vis-monitored
ester hydrolysis reaction curves, additional esterase activity plots,
additional pH-dependent 1H NMR spectra, and energy-minimized
structure model for Ac-(Pro)2Ser(Pro)2HisPro-OMe
(PDF)
Supplementary Material
ao7b00928_si_001.pdf
The authors
declare no competing financial interest.
Acknowledgments
We are thankful to the financial support from the
Ministry of Science and Technology of Taiwan (MOST 105-2113-M-007-018
& MOST 106-2113-M-007-016) and National Tsing Hua University (106N501CE1).
We are also grateful to the National Center for High-Performance Computing
(NCHC) for computer time and facilities.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145805410.1021/acsomega.8b02002ArticleFabrication of Ordered 2D Colloidal Crystals on Flat
and Patterned Substrates by Spin Coating Banik Meneka Mukherjee Rabibrata *Instability and Soft Patterning Laboratory,
Department of Chemical Engineering, Indian
Institute of Technology Kharagpur, Kharagpur, West Bengal 721302, India* E-mail: rabibrata@che.iitkgp.ac.in (R.M.).17 10 2018 31 10 2018 3 10 13422 13432 12 08 2018 05 10 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
Spin
coating is a simple and rapid method for fabricating ordered
monolayer colloidal crystals on flat as well as patterned substrates.
In this article, we show how a combination of factors, particularly
concentration of the dispensed colloidal solution (Cn) and spin-coating speed, influences the ordering process.
We have performed systematic experiments on different types of substrates
with two types of colloidal particles (polystyrene and silica). We
also show that even when perfect ordering is achieved at some locations,
there might be a significant spatial variation in the deposit morphology
over different areas of the sample. Our experiments reveal that higher Cn is required for obtaining perfect arrays,
as the diameter of the colloids (dD) increases.
Interestingly, a combination of higher Cn and rotational speed (expressed as revolutions per minute) is required
to achieve perfect ordering on a topographically patterned substrate,
as compared to that on a flat surface, because of loss of inertia
of the particles during outward flow because of impact on the substrate
features. Finally, we also identify the relation between the particle
diameter and the height of the pattern features to achieve topography-mediated
particle ordering.
document-id-old-9ao8b02002document-id-new-14ao-2018-02002eccc-price
==== Body
Introduction
It
is well-known that monodispersed colloidal particles self-assemble
into hexagonal close-packed (HCP) structures, under appropriate conditions,
which are also known as two-dimensional (2D) colloidal crystals, and
find wide applications in fabrication of optical chips,1 photonic band gap materials and photonic crystals,2−4 data storage,5 chromatography,6 sensors,7 masks for
nanosphere lithography,8 etc. Various interfacial
self-assembly techniques, such as sedimentation,9 confined convective self-assembly,10 dip coating,11 drop casting and evaporative
drying,12 deposition during retraction
of liquid meniscus within a microfluidic chamber,13 electrophoretic deposition,14,15 self-assembly
at the gas–liquid interface,16,17 Langmuir–Blodgett
(LB) technique,18 inkjet printing,19 spray coating,20 spin
coating,21−41 and so forth, have been utilized to fabricate monolayer colloidal
crystals with HCP ordering. Almost all methods rely on the convective
assembly of particles engendered by lateral capillary forces, which
cause an attractive interaction between the particles that push them
together, favoring the nucleation of a close-packed ordered monolayer.
Surface stabilization of the particles is important to prevent uncontrolled
aggregation in the early stage of self-assembly.11 Methods such as sedimentation or electrophoretic deposition
are well suited for three-dimensional assembly, as they easily form
multilayers. Although dip coating and LB-based techniques are capable
of producing high-quality 2D crystals, they are inherently slow, require
large volume of colloidal solution, and are difficult to scale up.
It turns out that spin coating, which is widely used for coating polymer
thin films over large areas, is also well suited for creating 2D colloidal
crystals. Major advantages of spin coating include rapid formation
(∼few minutes), high-throughput, extremely low amount of colloidal
solution requirement (∼microliter), high degree of reproducibility,
scalability, and direct integration with standard microfabrication
approaches.
The possibility of creating a 2D monolayer array
of latex particles
[polystyrene (PS) beads] on a rigid substrate by spin coating was
first demonstrated by Deckman and Dunsmuir in early 80s.21,22 Subsequently, on the basis of this concept, Van Duyne pioneered
the concept of nanosphere lithography, which is widely used as a physical
mask for subsequent additive deposition of various types of materials.8,23 Monolayer arrays of many other types of colloids such as silica,
titania, core–shell particles, hollow titania spheres, and
nanoparticles of gold, silver, cobalt, etc. have been fabricated by
spin coating.24−26 Jiang and McFarland spin-coated a colloidal sol comprising
a mixture of a tri-acrylate monomer and a photoinitiator to fabricate
a well-ordered nonclose-packed hexagonal array. The monomer, which
acts as a spacer, is subsequently photopolymerized to form either
a polymer nanocomposite36 or a macroporous
polymer with reverse opal structure (in conjugation with etching),37 spanning over large areas.38 However, it is important to point out that as the spin-coating
process is radially symmetric about the center of rotation, it is
not possible to arrange all the particles in the form of a single
defect-free crystal spanning over the entire substrate.29 It has been shown by Yethiraj and co-workers
that under idealized conditions, it becomes possible to obtain crack-free
orientationally correlated polycrystal (OCP) structures,29,31 which comprise defect-free single-crystal domains radially arranged
with respect to the center of the film. While each single crystalline
domain laterally spans about 10 μm (represented with the correlation
length, lR), their orientation undergoes
continuous macroscopic rotation on length scales much larger than
the diameter of the colloidal particles.31 Application of an external magnetic field has been shown to be a
promising approach that enhances the uniformity of the deposited colloidal
particles, provided the colloids are magnetic in nature.39−41
Apart from monolayer arrays with HCP ordering, colloidal particles
arranged in a nonhexagonal manner also find applications in many exotic
areas such as optics and photonics and as sensing materials.42,43 Such arrays are typically created by depositing the colloids on
a chemically or a topographically patterned substrate, which acts
as a template. The possible formation of a topography-directed non-HCP
colloidal array was first reported by van Blaaderen et al. based on
gravity settling of silica particles, which was referred to as colloidal
epitaxy.44,45 Subsequently, several other techniques such
as micromoulding,46,47 electrostatic assembly,48 flow inside the microfluidic cell,49 dip coating,50 LB
technique,51 spin coating,52−57 and so forth have been used to obtain pattern-directed particle
arrays with a nonhexagonal geometry. A spin-coated pattern-directed
particle array was first demonstrated by Ozin and Yang where they
obtained non-HCP arrays of silica microspheres into anisotropically
etched square pyramid pits,52 based on
a combination of gravity-driven sedimentation and evaporation-induced
capillary forces, which lead to rapid settling, self-assembly, and
crystallization within the pits. Brueck and co-workers reported the
self-assembled array formation of sub-100 nm silica particles inside
line gratings and circular holes. They highlighted the critical role
of pH of the casting solution and showed that good ordering was possible
only when pH was 7.53 The same group showed
the possible fabrication of aligned multilayer particle arrays inside
deeper trenches, where the layer thickness could be controlled by
multiple spin-coating steps. Varghese et al. obtained size selective
array of particles within the pattern grooves from a mixture of particles
of different sizes.56
From the above
discussion, it is clear that spin coating is a simple
method, which can be used to fabricate monolayer colloidal crystals
with both HCP and non-HCP ordering on flat and patterned substrates,
respectively. However, in spin coating, particle array formation depends
on a combination of capillary, gravitational, centrifugal, and electrostatic
forces. The situation gets further complicated on a topographically
patterned substrate where the solution layer undergoes topography-mediated
rupture during spin coating.57−59 Further, because of symmetry
issues discussed already,29 as well as
nonplanarization of colloidal suspensions during spin coating from
a volatile medium,40 it becomes impossible
to achieve perfect ordering with the particles over a large area,
and at best crack-free OCP structures can be obtained.31 Colson et al. approached this complex parameter
optimization problem from the concept of Experimental Design and predicted
the optimum condition for obtaining a defect-free array over ASA ≈ 200 μm2 area.60 Most experimental papers
only report the optimized condition that offers a near perfect array,
and there are not too many systematic experimental studies that show
how the morphology varies with change in various input parameters.
Lack of such a study often renders it difficult to identify the conditions
for perfect ordering, particularly over large areas.
In this
article, we show the conditions under which perfect colloidal
arrays can form on flat as well as patterned surfaces of a variety
of materials based on systematic experimental investigations. Our
results show that a uniform array is formed within a narrow parameter
window spanning over large areas. The best structures we obtained
exhibit correlation length lR ≈
15 ± 2.5 μm and ASA ≈ 210 ± 12 μm2 in each single crystalline
domain comprising HCP monolayer arrays of the colloidal particles,
with no crack between adjacent domains over the entire sample surface
(15 mm × 15 mm). Such a structure will be referred to as “perfectly
ordered structure” in the subsequent section of the paper.
We show that such perfect ordering is achieved within a very narrow
parameter window that depends strongly on the diameter of the colloidal
particles (dD). We also show that there
can be a significant spatial variation in the morphology of the structures
and extent of ordering primarily because of nonplanarization of the
colloidal suspension,30 and therefore,
care must be taken to examine the structure at different locations
of the sample. We hope the reported results will act as a guide, particularly
for beginners to identify the actual optimized condition based on
a first trial that may lead to nonuniform deposition. Further, on
a patterned surface comprising grating geometry, we show how the morphology
of the ordered particles within the grooves depend on relative commensuration
between the particle diameter (dD) and
the groove width (lP), in addition to
the concentration of the particles in the colloidal solution (Cn). Finally, by coating the colloidal solution
on grating patterned substrates with the same periodicity (λP) and lP, but a different groove
depth (hP), we identify the minimum height
of the features necessary to successfully align the particles.
Results
and Discussion
Self-Assembly of PS Colloids on the Sylgard
184 Substrate
As discussed in the Introduction section,
the objective of the work is to identify the condition at which perfect
monolayer arrays of colloidal particles can be achieved. We performed
systematic experiments for each size and types of colloids on different
substrates by casting the sols with different colloidal concentrations
(Cn) at different revolutions per minute
(rpm), to find out the condition that leads to perfect ordering. Figure 1 highlights one such
optimization attempt, showing various degrees of ordering with PS
colloids having dD = 600 nm, as a function
of Cn and rpm on the UVO-exposed Sylgard
184 substrate. A UVO-exposed poly(dimethyl siloxane) (PDMS) substrate
is deliberately chosen as it is hydrophobic in nature (θE-W ≈ 109.5°). We show that it becomes possible
to create a perfect array even on a hydrophobic surface using methanol
as the solvent. However, it must be highlighted that because of UVO
exposure, the PDMS surface becomes almost completely wetted by methanol,
and therefore, ordered array formation gets favored.
Figure 1 Morphology of the colloidal
deposit at different Cn–rpm combinations,
when PS colloids with dD = 600 nm are
spin-coated on a flat UVO-exposed
PDMS substrate. The location is 4 mm away from the center of the substrate.
It may be noted that in all cases,
the surfactant used is sodium
dodecyl sulfate (SDS) and its concentration is 0.025 wt %. The presence
of surfactant molecules in the colloidal suspension in appropriate
quantity is essential for achieving perfect ordering, as they get
adsorbed on the particle surface and control the interaction between
the particles and surrounding. Self-assembly of colloidal particles
into monolayer colloidal crystals require repulsive interactions between
the particles, as strong attraction leads to the formation of highly
disordered structures.61 Though a detailed
analysis on how ordering is influenced by the surfactant concentration
is beyond the scope of the present study (and will be taken up separately),
we observed that disordered structures form both when the surfactant
concentration is very low (or absent) or higher than 0.1 wt %, when
micelles start to form. Apart from SDS, we could also obtain perfect
ordering using a nonionic surfactant (Triton-X). However, no ordering
could be achieved when a cationic surfactant [hexadecyltrimethylammonium
bromide (HTAB)] was used. This is attributed to the Coulombic binding
of the positively charged head group of HTAB onto PS and silica particles,
both of which have negative surface charge, as verified by dynamic
light scattering measurements (data shown in Figure S1 of online Supporting Information). As the head group of
the cationic surfactant molecules adsorbs on the particle surface,
their hydrophobic tail orients outward and adjacent surfactant-covered
particles experience strong attraction in the presence of alcohol
because of hydration pressure. This leads to agglomeration and consequent
suppression of ordered crystal formation.
Before presenting
the experimental results, we feel it will be
appropriate to highlight the key theoretical results related to spin
coating,62−64 particularly some of the recent theoretical papers
which are specific to spin coating of colloidal dispersions.39−41 This will help us in qualitatively explaining some of the experimental
findings reported in this paper. It is well-known that in the initial
stage of spin coating, the dispensed solution flows radially outward
because of centripetal forces and the advancing solution meniscus
reaches the edge of the sample. The excess solution (including the
particles) is subsequently thrown out, which is known as splash drainage.
Spin coating of simple fluids has been modeled based on lubrication approximation ever since
the pioneering work of Emslie et al.,62 where the primary focus was to find out how film thickness (h) varies as a function of spinning time (t) and radial distance from the center of spinning (r). However, the model neglected the role of evaporation, and thinning
was considered only because of centrifugal forces. Meyerhofer subsequently
improved the model by incorporating the effect of evaporation by considering
spin coating to be a two-step process comprising two different stages:
(a) initial phase dominated by the radially outward flow and (b) evaporation-dominated
later stage where there is virtually no flow. The model considered
rate of evaporation (e) to depend on rpm as e ∝ (rpm)1/2.63 Subsequent improvement on spin-coating modeling was proposed by
Cregan and O’Brien,64 based on the
argument that solvent evaporation starts almost instantaneously with
deposition of the solution and therefore cannot be neglected even
in the initial phase. Although the model is based on lubrication approximation
and utilizes matched asymptotic expansion techniques, it considers
a constant rate of evaporation and predicts the deposited layer thickness
of the solute (not colloids) h∞(s) rather accurately and
is given as64 1 where C0 is the
initial solute concentration, γ is the kinetic viscosity, ω
is the angular velocity, and E is the rate of evaporation
of the solvent. Equation 1 can be simplified as 2 where is constant for a specific
experimental
condition and β = 2/3.
The Cregan model was extended specifically
for colloids by González-Viñas
and co-workers, who argued that for a particulate system the film
thickness h∞(s) should be replaced by a term “compact-equivalent
height”, which depends on the kind of deposited structure and
can be calculated as the product of packing fraction and Vornoi cell
volume.65 Aslam et al. proposed that the
term h∞(s) in eq 1 for a simple solute should be replaced by compact-equivalent
height (CEH) for colloidal deposition, which gives 3 where the contact A1 can be obtained by simply replacing the solute
concentration C0 with the initial colloid
concentration (Cn) in the expression of A mentioned above. Further, for the submonolayer
deposit with a hexagonal structure, the expression of CEH is given
as41 4 where ϵ2 is the local occupation
factor, which is defined as the area occupied by the colloidal clusters
relative to the total area. In this paper, the term fractional surface
coverage (Fs) can be considered identical
to the occupation factor (ϵ2) used by Pichumani and
González-Viñas.39 It may
also be noted that we have written eq 4 in terms of dD, the diameter
of the colloidal particles, rather than the particle radius as in
refs (40) and (41).
Figure 1 shows the
morphology of the colloidal deposit obtained for various Cn–rpm combinations. At low rpm, the centripetal
force remains weak and therefore fails to spread the particles uniformly.
Thus, the evolution is dominated by viscous shear forces, which in
turn results in the particles getting arranged in a disordered fashion
(series A, Figure 1). As the rpm increases, the centripetal force becomes stronger,
resulting in uniform spreading. This also enhances the evaporation
rate up to a point where the forces acting on the colloidal particles
get balanced. Under this condition, the particles move on the substrate
surface easily and self-assemble into a monolayer with HCP ordering
that spans over a large area (frames B22, C33, and D44 of Figure 1). It also becomes
clear that the balance between the shear force and the drying rate
can only be maintained when Cn is increased
along with an increase in rpm. However, increase of Cn to much higher values leads to a sharp enhancement in
the viscosity of the remnant colloidal suspension during the late
stage of spinning. This hinders the mobility of the particles on the
substrate surface, and HCP ordering gets suppressed in favor of random
disorganized structures (frames B25 and C35, Figure 1). When the speed of rotation is increased
further, the radial outflow of the particles increases and consequently,
a larger amount of particles are thrown out of the substrate because
of splash drainage. Consequently, the remnant suspension rotating
on the substrate becomes very dilute. Consequently, the remaining
PS particles fail to form monolayer coverage on the substrate, though
they may show localized HCP ordering (series E, Figure 1).
The gradual morphology transition
along each column and row of Figure 1 highlights the influence
of enhanced rpm and Cn on the ordering
process, respectively. It can be clearly seen that the fractional
coverage of the surface (Fs) reduces with
an increase of rpm, for a given Cn, as
the proportion of splash drainage increases at higher rpm. On the
other hand, Fs gradually increases with
an increase in Cn for a constant rpm,
as more number of particles are initially dispensed on the substrate.
In fact, in most cases, the morphology gradually transforms from monolayer
with partial coverage to scattered multilayers with an increase in Cn, where the drying front fails to drag the
particles over the initially assembled particles.
Important
observation in Figure 1 is the formation of a perfectly ordered monolayer
with HCP ordering in frames B22, C33, and D44 (Fs ≈ 1.0). This means that a perfect monolayer coverage
is possible for different combinations of Cn and rpm. At this point, it is worth highlighting that all the images
in Figure 1 are captured
at a location which is approximately 4 mm away from the center of
the substrate. However, in order to claim that a specific coating
condition is optimum for achieving perfect crystalline ordering, it
is important to check the structure uniformity over the entire sample
substrate. We checked this by performing careful atomic force microscopy
(AFM) scan of the samples at different radial distances (rD) from the center of the sample at 1 mm intervals. The
samples chosen for this study include the ones which are seen to give
perfect ordering in Figure 1. In addition, few samples corresponding to different Cn–rpm combinations were also explored,
the details of which are mentioned in the legend of Figure 2A. We note that at an rpm of
200 as well as at a higher rpm (=2500), perfect ordering is not achieved
anywhere on the sample surface. For the low rpm case, the morphology
comprises a scattered multilayer over major portion of the substrate
(rD > 2 mm), indicating weak action
of
the centripetal force, which fails to drag the particles. On the other
hand, at higher rpm, the centripetal force is much higher than the
shear force and a large amount of particles are lost because of splashing.
Consequently, Fs never exceeds 50% over
the entire substrate. For the sample with Cn = 0.52% rotated at 400 rpm, we observe a slight undercoverage till rD ≈ 2 mm but a very high degree of multilayer
formation beyond rD > 5 mm. An opposite
trend is observed in the sample with Cn ≈ 1.2%, rotated at rpm = 1000. Here, a near perfect array
with Fs ≈ 1.0 is obtained in the
outer section of the sample (rD ≥
4 mm). However, the areas close to the center show a significant undercoverage
(Fs down to ≈0.75%). As can be
seen in Figure 2A,
the most uniform coverage is observed in the sample with Cn = 0.67%, rotated at rpm = 600. Thus, for PS colloids
with dD ≈ 600 nm, we identify a
combination of Cn = 0.67% and rpm = 600
to be optimum.
Figure 2 Variation of fractional coverage Fs as a function of distance from center (rD) for different Cn–rpm
combinations.
AFM images in insets (A1–A3) show perfectly ordered HCP morphology
at rD = 2, 5, and 7 mm. In all cases,
PS colloids with dD = 600 nm have been
used.
The trend in Figure 2A highlights the critical role
of solvent evaporation time on the
array formation. Unlike water, which has a vapor pressure = 3.17 kPa,
methanol has a much higher vapor pressure (13.02 kPa), which means
methanol evaporates much faster. Therefore, particle spreading can
take place only till the adequate amount of solvent is present. This
means at low rpm (200 and 400), even before major part of the particles
can reach the sample periphery, the solution starts to dry up, which
is also associated with the enhancement of viscosity, and therefore,
multilayers are formed toward the outer areas of the sample. Thus,
for an organic solvent, the balance of shear force and centripetal
force must be established within a very narrow time window, before
major part of the solvent evaporates away. This in turn allows perfect
array formation at Cn which is typically
much lower than that reported in the literature with an aqueous colloidal
sol, which also implies much reduced splash drainage of the colloidal
particles. Further, Figures 1 and 2 clearly highlight the success
of our work in obtaining a neat and perfect array on a hydrophobic
surface (θE-W ≈ 109°) of the cross-linked
PDMS substrate, UVO-exposed for 30 min (Table 1). In fact, Choi et al. have clearly mentioned
that it is nearly impossible to obtain a perfect array on a hydrophobic
surface.32 We show that this limitation
can be circumvented by using methanol as the solvent. The only requirement
is methanol must wet the surface, which is achieved by 30 min UVO
exposure, despite the substrate remaining hydrophobic.
Table 1 Details of the Flat Substrates Used
sl. no. substrate RMS roughness
(nm) water contact
angle (θE-W°) methanol
contact angle (θE-M°) surface energy (mJ/m2)
1 glass 0.429 ± 0.043 17.3 8.2 56.4
2 silicon wafer 0.305 ± 0.039 11.1 2.3 59.17
3 PS film coated on glass 0.486 ± 0.044 91.5 5.1 38.3
4 PMMA film coated on glass 0.493 ± 0.038 73.2 3.2 41.8
5 cross-linked PDMS film on
glass 0.505 ± 0.042 114.5 35.8 24.2
5A UVO-exposed PDMS
film on glass 0.514 ± 0.023 109.5 2.4 28.3
Self-Assembly of PS and Silica Colloids on
Different Substrates
In Table 2, we show
the optimized conditions for obtaining HCP arrays on different substrates
with colloids of different sizes and of different materials. The optimized Cn–rpm combination is obtained by performing
experiments in line with Figures 1 and 2 for particles of each
diameter on each type of substrate. The corresponding images of the
ordered arrays are shown in Figures S2–S5 of online Supporting Information
Table 2 Optimized
Conditions for Perfect Ordering
on Flat Substrates
material
of particle dD (nm) substrate Cn (wt/vol %) rpm figure number
in online Supporting Information
PS 300 glass 0.25 wt % 1000 rpm, 120 s S2A
silicon wafer 0.2 wt % 1000 rpm, 120 s S2B
PS film 0.3 wt % 800 rpm, 120 s S2C
PMMA film 0.25 wt % 800 rpm, 120 s S2D
UVO-exposed PDMS film 0.4 wt % 800 rpm, 120 s S2E
PS 600 glass 0.5 wt % 800 rpm, 120 s S3A
silicon wafer 0.4 wt % 800 rpm, 120 s S3B
PS film 0.6 wt % 600 rpm, 120 s S3C
PMMA film 0.5 wt % 600 rpm, 120 s S3D
UVO-exposed PDMS film 0.67 wt % 600 rpm, 120 s S3E
PS 800 glass 0.8 wt % 600 rpm, 120 s S4A
silicon wafer 0.75 wt % 800 rpm, 120 s S4B
PS film 0.85 wt % 500 rpm, 120 s S4C
PMMA film 0.8 wt % 500 rpm, 120 s S4D
UVO-exposed PDMS film 0.9 wt % 500 rpm, 120 s S4E
silica 350 glass 0.4 wt % 800 rpm, 120 s S5A
silicon wafer 0.3 wt % 1000 rpm, 120 s S5B
PS film 0.47 wt % 600 rpm, 120 s S5C
PMMA film 0.4 wt % 600 rpm, 120 s S5D
UVO-exposed PDMS film 0.5 wt % 600 rpm, 120 s S5E
In order
to highlight the dependence of the optimum condition on
simultaneous variation of several parameters, we construct morphology
phase diagrams. Two types of morphology phase diagram can be constructed,
which are shown in Figure 3. The phase diagram shown in Figure 3A can be constructed for each particle with
a specific dD—substrate combination
to identify the optimum condition. The diagram shown in Figure 3B is obtained by plotting each
of the optimum points obtained for different dD—substrate combinations. To generate a plot like the
one shown in Figure 3A, which is specific to PS particles with dD = 600 nm on UVO-exposed PDMS substrates at a location that
is 4 mm away from the center of the substrate, we classify the morphology
obtained at different Cn–rpm combinations
into three subcategories, which are perfectly ordered, underfilled,
and overfilled, as has been discussed in the context of Figure 1. The three distinct morphologies
are represented with different symbols. The information in Figure 2 is further used
to identify the Cn = 0.67% and rpm = 600
as the optimum condition which is marked with a square. It can further
be seen that the Cn at which transition
from underfilled to overfilled structures take places varies linearly
with rpm.
Figure 3 Morphology phase diagram (A) for PS colloids having dD = 600 nm on a UVO-exposed flat PDMS substrate and (B)
for colloids of different sizes on different types of flat substrates.
While each color represents colloid of a specific type and dD, each symbol represents a type of substrate,
as per legend provided in the figure.
Figure 3B
represents
the global morphology phase diagram which is constructed by using
the data reported in Table 2, each one of which has been obtained by constructing a particle
and substrate specific morphology phase diagram similar to that shown
in Figure 4A. Representing
data with simultaneous variation of four parameters (Cn, rpm, dD, and substrate
type) on a single plot was itself challenging, and therefore, the
logic adopted for representation needs to be mentioned. In the plot,
a particular color of the symbols represents particles of a specific dD. In contrast, different types of substrates
have been represented with different shapes of the symbols. The figure
highlights that for a particular type of particle, perfect ordering
is achieved on three polymeric substrates [PS, polymethylmethacrylate
(PMMA), and UVO-exposed PDMS] at nearly identical conditions. In contrast,
it emerges out from Figure 3B that a higher rpm is required to obtain perfect ordering
on glass and silicon substrates. This probably is a signature of slippage
of the solvent on a polymeric substrate and needs to be explored in
greater detail. Also, it becomes evident from both Figure 3B and Table 2 that for obtaining perfect ordering, Cn increases with an increase in dD, a trend that is counterintuitive, as lesser number
of larger particles are required to cover the same surface area, when dD is larger. It may however be explained rather
easily from eq 4, which
suggests that to achieve constant surface coverage (Fs) or occupation factor (ϵ2), is proportional to dD.41 As Cn is very dilute, one may further argue that 1 – Cn ≈ 1, and hence, Cn exhibits direct proportionality with dD.
Figure 4 Morphology of the colloidal deposit at different Cn–rpm combinations, when PS colloids with dD = 600 nm are spin coated on the patterned
UVO-exposed PDMS substrate with type 2 geometry (λP = 1.5 μm).
Table 2 also reveals
that for a particular dD, the optimum Cn increases slightly, with lowering of the substrate
surface energy. This can be attributed to the reduced strength of
the particle–substrate interaction with lowering of γ.
However, how exactly the surfactant molecules adsorb on the substrate
and thus influence the ordering process is not fully clear and will
be analyzed separately. It can be seen that there is no monotonic
correlation of Cn and rpm with the substrate
surface energy for the formation of a perfect array, though the parameters
are quite close on various substrates. This observation is an indirect
evidence that the surface has a much lower role on the assembly, apart
from its wettability. We argue this happens because of the presence
of the surfactant molecules, which favor wetting of solution on the
substrate, which is the necessary condition for achieving ordering.
Template-Directed Assembly of Colloids
Particle Diameter Approximately
Equal to Pattern Line Width
(dD ≈ lP)
It is well-known that physical confinement provided by
the patterned substrate effectively traps the colloidal particles
during spin coating.51 The grooves act
as the preferred location for the deposition of the particles, as
the solvent layer ruptures over the substrate pattern protrusions.57 Consequently, the remaining liquid flows in
the grooves, localizing the colloids there. Subsequently, the lateral
capillary forces between the particles drive them to form closely
packed structures aligned along the grooves. It has also been recently
shown by Aslam et al. that a patterned substrate also eliminates axial
symmetry by spin coating and therefore suppresses the formation of
OCP structures.57
In this section,
we show how the morphology of the particle deposit varies as a combination
of Cn and rpm. As a test case, we examine
the ordering of dD = 600 nm PS particles
on the type 2 grating patterned substrate of the UVO-exposed cross-linked
PDMS. For a type 2 substrate, the groove width is lP ≈ 750 nm, the groove depth is hP ≈ 250 nm, and the periodicity is λP ≈ 1.5 μm. Using a substrate of the same material
as that in Figure 1 allows direct comparison between the conditions that leads to a
perfect ordering on a flat substrate and a patterned substrate. As dD and lP are comparable,
we consider that the particle and the patterned substrate are commensurate.
Figure 4 shows various
deposition morphologies of dD = 600 nm
PS particles on type 2 substrate, obtained at different Cn–rpm combinations. The trend is similar to that
observed on a flat surface; for a particular Cn, Fs-P (surface coverage
or fill fraction on a patterned substrate) gradually reduces with
an increase in rpm because of higher splash drainage. On the other
hand, increase of Cn at a constant rpm
leads to the deposition of more particles, leading to disorder, as
particles get deposited on top of the stripes, after filling the grooves
(frames A14, A15, B24, and B25 of Figure 4). Among all the frames of Figure 4, perfect ordering is observed
in frame B23 for a parameter combination of Cn = 0.75% and rpm = 1000. It is interesting to note that perfect
ordering on a patterned substrate requires higher Cn as well as higher rpm for particles with the same dD as compared to the flat substrate of the same
material. This means that on a patterned substrate, more number of
particles are required for perfect ordering. This is counterintuitive
as perfect ordering on a grating patterned substrate implies that
particles align only inside the grooves, and therefore, only about
50% of the number of particles is required to achieve the same, in
comparison to a perfect HCP structure on a flat surface (Fs ≈ 1.0). The observation can be explained well
with the help of eq 4 (modified Cregan model).41 As Fs (or ϵ2) is almost half on
a grating patterned substrate, as compared to that on a flat substrate,
CEH on a patterned substrate is also approximately half than that
on a flat substrate. From eq 3, we note that CEH = A1ω–β. Figure 4 shows that Cn = 0.75% for perfect ordering on a patterned substrate, which is
compared to a value of Cn = 0.67% on a
flat surface (Figure 2). As the values of Cn are rather close
to each other, the values of are also rather close on a flat and a patterned
substrate. Thus, from eq 4, lower CEH becomes possible on a patterned substrate only when ω
is higher as compared to that on a flat substrate.
We summarize
the optimized conditions for obtaining perfectly ordered
structures (Fs-P ≈ 1.0)
on type 1 and type 2 substrates of different materials, with both
silica and PS colloids of different sizes, as presented in Table 3, by performing experiments
in line with Figure 4 for particles of each dD on each type
of patterned substrate. Figure 5A shows the perfectly ordered structure obtained with silica
colloids having dD = 350 nm on a patterned
type 1 PMMA substrate, under conditions mentioned in Table 3. Interestingly, on patterned
substrates, we find that the rpm at which perfect ordering is obtained
for a particular colloid is independent of the substrate material,
though Cn differs slightly from substrate
to substrate. This clearly highlights the critical role of colloidal
spreading on the formation of perfect structures, rather than the
particle–substrate interaction, which seems to influence the
ordering process weakly. The results imply that the evolution during
spinning up to the stage of topography-mediated rupture of the solvent
layer is not much influenced by the substrate. Also, as already discussed,
in all cases higher rpm is required for obtaining a perfect array,
as compared to that on a flat substrate of the same material.
Figure 5 (A) Perfectly
ordered structure with Fs-P ≈
1.0 obtained by spin coating silica colloids having dD = 350 nm on type 1 patterned PMMA substrate.
(B) Unique ordered structures with PS colloids having dD = 600 nm on type 2 patterned PMMA substrate, where the
particles fully cover the patterned substrate. Inset (B1) shows the
cross-sectional AFM line profile and (B2) represents a schematic highlighting
the particle arrangement. The overall pattern is HCP, but particles
rest at two different elevations.
Table 3 Optimized Conditions for Perfect Ordering
on Patterned Substrates
material
of particle dD (nm) substrate substrate
type Cn (wt %) rpm
PS 300 patterned PS film type 1 0.45 1400 rpm, 120 s
patterned PMMA film type 1 0.45 1400 rpm, 120 s
UVO-exposed patterned PDMS
film type 1 0.5 1400 rpm, 120 s
PS 600 patterned PS film type 2 0.67 1000 rpm, 120 s
patterned PMMA
film type 2 0.65 1000 rpm, 120 s
UVO-exposed patterned PDMS
film type 2 0.75 1000 rpm, 120 s
silica 350 patterned PS film type 1 0.55 1200 rpm, 120 s
patterned PMMA
film type 1 0.5 1200 rpm, 120 s
UVO-exposed patterned PDMS
film type 1 0.6 1200 rpm, 120 s
Until this point, we
have considered a perfectly ordered structure
to be one where only the grooves are completely filled up by the colloids
in an uninterrupted threadlike manner (Fs-P ≈ 1.0). However, Figure 5B shows another interesting morphology where the entire
patterned substrate is covered in a near HCP manner by PS colloids
(dD = 600 nm). The section B1—B1
in the inset of Figure 5B shows that some particles are at a lower level as compared to others.
This happens when Cn is adequately high
and they start depositing covering the entire patterned substrate.
The particles which lead to within the grooves arrange themselves
in a zigzag threadlike manner. The remaining particles, which deposit
over the substrate stripes, align themselves in an interesting arrangement
of alternate single and double particles along the length of the stripes,
alongside the particle thread formed within the groove. The arrangement
is schematically shown in inset (B2) of Figure 5B. This structure forms when Cn ≈ 2.5% and rpm = 1000. Because lP is higher than dD, the particles
align in a zigzag fashion inside the grooves, allowing more particles
to pack themselves side by side over the stripes. As larger number
of particles are dispensed (Cn for optimum
coverage = 0.75%, as per Table 3) on the surface, the applied centripetal force fails to splash
out significant fraction of the excess particles that are available
after filling of the grooves. The morphology is novel and highlights
that the hexagonal arrangement still leads to minimum energy configuration
even if the particles remain at multiple levels.
Effect of Template
Height on Pattern-Directed Assembly
In this section, we show
how the feature height (hP) of the substrate
patterns influences the pattern-directed
ordering. For this purpose, type 2 substrates of different hP were used. The experiments were performed
with dD = 600 nm PS colloids so that the dD and λP remain commensurate.
The initial Cn–rpm combination
chosen was the same as that which is seen to give perfect ordering
in Figure 4, frame
B23. It can be seen that perfect pattern-directed ordering is obtained
till hP ≈ 150 nm, when the Cn–rpm combination was kept unaltered.
It can be seen in Figure 6B that the ordering is lost when hP ≈ 125 nm. The uniqueness of Figure 6B can be understood by comparing it with
frames A13–A15 and B24–B25 of Figure 4 which also shows distorted arrays on patterned
substrates. However, in all those frames of Figure 4, the grooves are totally filled and the
excess particles are seen to get localized over the stripes, resulting
in disorder. In contrast, in Figure 6B, the particles are seen to accumulate over the stripe
tops, despite some grooves remaining vacant. This means that during
the radial outward flow, the hP of the
features is too low to intercept the flow and guide the particles
within the grooves. When we performed similar experiments with dD = 300 nm on type 1 substrates of different hP, we observed that ordering gets lost below hP ≈ 75 nm. The trend, including the critical hP below which topography-guided ordering is
lost, is nearly similar for all substrates having identical pattern
topography. It can be seen that the limiting value of hP/dD lies between 0.2 and
0.25 below which the topography of the substrate patterns fails to
provide confinement to the particle organization process. On the basis
of the first results reported in this article, a detailed investigation
on this problem will be taken up separately. Similar transition from
order to disordered structures with gradual reduction of hP has been observed earlier in the context of pattern-directed
dewetting of thin polymer films.66 A detailed
investigation on this topic is underway. It will be particularly interesting
to explore if there is a critical hP around
which there will be a transition from OCP structures to purely template-guided
ordered structures, which is likely to depend on dD of the colloids as well.
Figure 6 Morphological variation
in template-guided assembly of PS colloids
(dD = 600 nm) on type 2 gratings of height
(A) 150 and (B) 125 nm.
Particle Diameter Smaller Than Pattern Line Width (dD < lP)
In Figure 7, we show how the
morphology of the deposit depends when dD is much smaller than the groove width of the patterned substrate.
Unlike all the earlier cases, where perfect ordering means a single
thread of particles aligned along the substrate groove, more complex
ordering is possible when dD and lP are noncommensurate. We produce one such example
with dD = 300 nm PS particles coated on
type 2 PMMA substrate, which has lP =
750 nm. While we obtained a variety of morphologies depending on the
combination of Cn and rpm, we report the
morphology which can be considered as the perfectly ordered structure
and can be considered analogous to Figure 4, frame B23. In Figure 7, the laterally coexisting particles are
seen to arrange in a hexagonal manner, though they are aligned along
the groove.
Figure 7 Particle doublet obtained with PS colloids having dD = 300 nm on type 1 substrate, obtained with Cn = 05% and rpm = 1000.
Conclusions
In this article, we have systematically
demonstrated the conditions
under which perfect arrays of monodispersed colloids can be obtained
on both defect-free flat and topographically patterned substrates
of different materials, using spin coating. On the flat surface, we
obtained structures that exhibit correlation length lR ≈ 15 ± 2.5 μm and ASA ≈ 210 ± 12 μm2 in
each single crystalline domain comprising HCP monolayer array of the
colloidal particles, with no crack between adjacent domains over the
entire sample surface (15 mm × 15 mm). We have shown in details
the optimization process, and the role of individual parameters, particularly Cn and rpm on the extent of ordering process
and constructed a morphology phase diagram to highlight the collective
role of Cn and rpm on perfect ordering
with particles of different sizes on different surfaces. We have also
highlighted the need to check the spatial variation of the as-cast
morphology, as there can be a significant variation in the extent
of ordering and Fs over the surface. Our
results also highlight the critical role of surfactants added on the
formation of uniform particle arrays, which might eventually open
up a new route to overcome the nonplanarization effect in spin coating,
particularly from a volatile organic solvent. Our intention is that
the report will significantly help beginners in the area to quickly
optimize the parameters by identifying the nature of the defect in
the structure and appropriately modulating either rpm or Cn. To facilitate this, we have highlighted the likely
types of defects that may result when Cn and/or rpm is low or high. We also show that higher Cn is required for obtaining perfect arrays with larger dD particles, which is in line with the recent
theoretical predictions on the spin coating of colloidal particles
by Aslam et al.41
On a patterned
surface, we note that both higher rpm and Cn are required for obtaining perfect ordering,
which can be attributed to lower Fs as
compared to that on a flat surface and has been explained well from
the theory. We also explored how the ratio of dD and hP can influence the ordering
process. If the features are shallower than 20% of the particle diameter,
then the patterns fail to confine the particles. Or in other words,
a grating much shallower than the particle diameter is sufficient
for confining the particles. We also report the formation of novel
multielevation structures under certain conditions when the topographically
patterned substrate is fully covered with particles at high Cn, as well as interesting structure comprising
an array of particle doublets when dD is
nearly 50% of lP.
As a final summary,
we understand that 2D monolayer colloidal array
formation on both flat and patterned substrates by spin coating is
a complex problem because of its multiparameter nature. While we have
carefully examined the dependence of Cn and rpm on the ordering process, various other parameters such as
effect of surfactant type and concentration, relative commensuration
between particle size and pattern geometry, and so forth also influence
the ordering process, which needs detailed investigation.
Materials and
Methods
Substrates
Glass slides, silicon wafer, films of cross-linked
PDMS, PS (molecular weight: 280 kDa, Sigma-Aldrich USA), and PMMA
(molecular weight: 120 kDa, Sigma-Aldrich USA) were used as different
substrates. The size of the substrates was 15 mm × 15 mm. The
glass and silicon substrates were cut from glass slides and silicon
wafer (test grade, Wafer World Inc.) respectively. They were subsequently
cleaned following a standard procedure. All polymer films were spin-coated
on cleaned glass pieces. The thickness of the PDMS film was ∼10
μm, which was obtained by spin-coating a degassed mixture of
part A to part B (1:10 wt/wt) of Sylgard 184 (a thermo curable, PDMS-based
elastomer, Dow Corning, USA) in n-hexane (SRL, India)
at 2500 rpm for 1 min. The coated film was cured at 120 °C for
12 h in an air oven for complete cross-linking. The thickness of the
PS and PMMA films was ∼500 nm, which was obtained by coating
dilute solutions [10% (w/v) PS and PMMA] in toluene on the glass slides
at 2500 rpm for 1 min. After coating, the PS and PMA films were annealed
at 60 °C for 3 h in a vacuum oven to remove the remnant solvent.
All the flat substrates were characterized using an atomic force microscope.
Contact angle goniometry (ramé-hart Instrument Co.) was used
to measure the water and methanol contact angle on each of the substrates,
which along with the substrates surface energy are listed in Table 1.
All the substrates
were used as it is, except cross-linked PDMS substrates which were
not wetted by the solvent (methanol). To make it wettable, the cross-linked
PDMS substrates were exposed to UVO (PSD Pro UV–O, NovaScan,
USA). UV irradiation at 185 nm wavelength leads to the production
of ozone from atmospheric oxygen. The ozone molecules, in turn, dissociate
into oxygen at 254 nm irradiation.67 The
reactive oxygen radicals, thus created, attack the methyl groups present
in Sylgard 184 (Si–CH3) and replace them with silanol
groups (Si–O–H), hence generating a superficial oxide
layer of higher surface energy and leads to enhanced wetting of the
samples. The drastic drop in methanol contact angle on the UVO-cured
PDMS substrate can be observed in Table 1.
Patterned Substrates
Some PS, PMMA,
and PDMS films
were patterned using topographically patterned stamps, which were
obtained from peeling the foils of commercially available optical
data storage disks such as DVD and CD.68 The PS and the PMMA films were patterned using capillary force lithography.69,70 The cross-linked PDMS films were patterned using a UVO-mediated
soft embossing technique reported elsewhere.68 The morphology of all three films patterned using the same stamps
was identical, implying the formation of a perfect negative replica
of the stamp pattern, which was verified using an atomic force microscope.
While the grating patterns obtained with a DVD foil has the periodicity
λP ≈ 750 nm, groove width lP ≈ 350 nm, and groove depth hP ≈ 100 nm (Figure S6, online Supporting Information, marked as type 1 patterns), the films
patterned with a CD foil has λP ≈ 1.5 μm,
groove width lP ≈ 750 nm, and groove
depth hP ≈ 250 nm (Figure S7, online Supporting Information, marked as type 2 patterns).
Grating patterns with the same λP but different hP was obtained following stress relaxation-associated
imprinting of partially precured PDMS films, which is reported in
detail elsewhere.71,72 In short, PDMS films of different
viscoelasticities were created by precuring the films for different
durations before embossing. These films, once imprinted with flexible
foils, underwent stress relaxation, which resulted in films with different hP. Figure 8A shows the hP of different
PDMS substrates used in our study, created as a function of precuring
time (tP) of the PDMS film. Figure 8B1,B2 shows the cross-sectional
line profiles of the type 1 and type 2 patterns having different hP.
Figure 8 (A) Variation of pattern feature height (hP) with precuring time (tP). (B)
AFM cross-sectional profile of patterns with different features hP, as a function of tP.
Colloidal Particles
Monodispersed colloids of PS with
diameters dD ≈ 300, 600, and 800
nm were purchased from Sigma, UK. Monodisperse silica particles of
diameter (dP) ≈ 350 nm were synthesized
following Stöber’s method by the hydrolysis of tetraethyl
orthosilicate (99.99%, Sigma-Aldrich) in ethanol (99.99%, Sigma-Aldrich)
medium in the presence of ammonium hydroxide (28%, Sigma-Aldrich)
as a catalyst.73 The details about the
reaction can be found in the online Supporting Information (Section S4.0).
Prior to spin coating, dilute
solution of PS and silica colloids in methanol was mixed with 0.025
wt % (unit of Cn is in terms of wt/vol
%) solution of SDS (purest grade purchased from Merck, India) in methanol
to stabilize the colloidal dispersion and was sonicated in a water
bath for 1 h. All the results reported in this paper are with SDS.
However, in some cases, a nonionic surfactant (Triton-X) or a cationic
surfactant (HTAB) was also used. It is quite clear that the presence
of surfactants favors better ordering, and therefore, surfactant concentration
is going to be an important factor influencing the morphology of the
deposits. A detailed analysis on how the nature and concentration
of the surfactant influence the ordering process will be analyzed
separately.
Spin-Coated Array Fabrication
For
spin coating, the
bare substrate (mounted onto the chuck) was first started to rotate
and allowed to attain the final rotational velocity. Subsequently,
100 μL of the stabilized colloidal dispersion was dispensed
on the rotating substrate using a micropipette. This protocol of dispensing
the colloidal suspension was adopted to minimize the effects of acceleration
on the sample. Coating over all the samples was performed at a room
temperature of 25 °C and a relative humidity of 30%. The rpm
and the colloid concentration (Cn) vary
from sample to sample and are mentioned in the appropriate sections.
The morphology of the colloidal arrays was investigated using an atomic
force microscope (Agilent Technologies, AFM 5100) in intermittent
contact mode using a silicon nitride cantilever (PPP-NCL, Nanosensors
Inc., USA) and a field emission scanning electron microscope (JSM7610F,
JEOL, Japan). For every AFM image, the fractional coverage (Fs) was calculated using the “slice”
feature of Pico Image Basic (Version 5.1), an integrated AFM imaging
and analysis software package. Details about the calculation procedure
of Fs can be found in Section S5.0 of
the online Supporting Information
Supporting Information Available
The Supporting Information
is
available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b02002.Surface charge
of PS and silica colloids; HCP array
formation by PS and silica colloids on different surfaces; details
of the different patterns used; synthesis of silica colloids; and
fractional coverage calculation procedure (PDF)
Supplementary Material
ao8b02002_si_001.pdf
The authors
declare no competing financial interest.
Acknowledgments
R.M. acknowledges DST, Government
of India, for
funding under its SERI initiative, grant number: DST/TM/SERI/DSS/361(G).
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145886910.1021/acsomega.8b01061ArticleEfficient Perovskite Solar Cells with Reduced Photocurrent
Hysteresis through Tuned Crystallinity of Hybrid Perovskite Thin Films Qi Jun †§Yao Xiang †§Xu Wenzhan †Wu Xiao †Jiang Xiaofang †Gong Xiong *†‡Cao Yong †† Institute
of Polymer Optoelectronic Materials and Devices, State Key Laboratory
of Luminescent Materials & Devices, South China University of Technology, Guangzhou 510640, P. R. China‡ Department
of Polymer Engineering, College of Polymer Science and Polymer Engineering, The University of Akron, Akron, Ohio 44325, United States* E-mail: xgong@uakron.edu. Fax: (330) 972 3406.28 06 2018 30 06 2018 3 6 7069 7076 19 05 2018 19 06 2018 Copyright © 2018 American Chemical
Society2018American Chemical
SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
Hybrid perovskite materials used
for realization of efficient perovskite
solar cells have drawn great attention in both academic and industrial
sectors. It was reported that the crystallinity of hybrid thin-film
perovskite materials plays an important role in device performance.
In this study, we report a novel and simple method to tune the crystallinity
of CH3NH3PbI3 thin film for device
performance of perovskite solar cells. By employing tetraphenylphosphonium
chloride on the top of PbI2 thin layer in the two-step
perovskite deposition processes, the crystallinity of the resultant
CH3NH3PbI3 thin film was tuned. As
a result, perovskite solar cells by the CH3NH3PbI3 thin film with tuned crystallinity exhibit an enlarged
open-circuit voltage and enhanced short-circuit current, thus boosted
efficiency as well as reduced photocurrent hysteresis compared to
pristine CH3NH3PbI3 thin film. These
results indicate that our study provides a new simple way to boost
device performance of perovskite solar cells through tuning the crystallinity
of CH3NH3PbI3 thin film.
document-id-old-9ao8b01061document-id-new-14ao-2018-01061pccc-price
==== Body
1 Introduction
In the past years, hybrid
perovskite materials used for realization
of efficient perovskite solar cells (PSCs) have drawn great attention
in both academic and industrial sectors due to their advanced features,
such as large absorption coefficient,1,2 high charge-carrier
mobility,3,4 and long charge-carrier diffusion lengths.5,6 Power conversion efficiencies (PCEs) of more than 22% have been
reported from PSCs fabricated by CH3NH3PbI3 with large crystal and generic interfacial engineering in
PSCs device structure.7−10 However, there is still a gap to realize 31% PCE, a theoretical
value, from CH3NH3PbI3-based PSCs.11 Toward the end, device performance parameters,
short-circuit current (JSC), open-circuit
voltage (VOC), and fill factors (FFs)
are required to be enhanced for boosting PCE. In the case of PSCs
fabricated by CH3NH3PbI3 thin film, VOC is estimated to be 1.3 V.11 But the reported VOC always
exhibited unavoidable optical and electrical losses,12,13 which were induced by interfacial states.14−16 Toward the
end, passivating the charge defects and improving the energy disorder
at the electron extraction layer have been utilized to realize large VOC.16−22 On the other hand, many effects have been also devoted to enhance JSC PSCs.11,23−25 Han et al. reported a solvent-annealing process to control the crystal
orientation transformation to improve charge-carrier collection and
prolong charge-carrier lifetime, thus boosting JSC.26 Recently, Leblebici et al.
have found that different crystal facets of individual grains have
a direct impact on both VOC and JSC.27 Thus, optimization
of microscopic facet orientation of CH3NH3PbI3 crystals in polycrystalline perovskite thin film could boost
both VOC and JSC.26−29
In this study, we report a novel and simple method to tune
the
crystallinity of CH3NH3PbI3 thin
film for boosting PSCs device performance. By employing tetraphenylphosphonium
chloride (TPPCl) on the top of PbI2 thin layer in the two-step
perovskite deposition processes, the crystallinity of the resultant
CH3NH3PbI3 thin film was tuned. As
a result, the PSCs fabricated by the CH3NH3PbI3 thin film pretreated with the TPPCl ultrathin layer exhibit
a VOC of 1.12 V, a JSC of 21.71 mA/cm2, an FF of 74.43, and a corresponding
PCE of 18.04%, with dramatically reduced hysteresis, compared to the
PSCs fabricated by pristine CH3NH3PbI3 thin film, which exhibit a VOC of 1.04
V, a JSC of 21.08 mA/cm2, an
FF of 74.41, and a corresponding PCE of 16.34%, with serious hysteresis.
2 Results and Discussion
TPPCl is selected to tune the
crystallinity of CH3NH3PbI3 thin
film through modification of PbI2 thin-layer surface originated
from the Cl– anion, which probably chelated with
the Pb2+ cations
and altered the kinetics of thin-film formation.29 The molecular structure of TPPCl is shown in Scheme 1a. Figure 1a–e presents the scanning electron
microscopy (SEM) images of pristine PbI2 thin film and
PbI2 thin films treated with the TPPCl ultrathin layers.
It is found that pristine PbI2 thin film possesses layered
crystals with sizes of tens of nanometers and many voids. Such observation
is in good agreement with the morphologies of PbI2 thin
film reported by others.30,31 After the PbI2 thin films are treated with different TPPCl ultrathin layers cast
from different concentrations of TPPCl solutions, PbI2 thin
films still possess layered crystals with sizes of tens of nanometers
and many voids, but a mass of interlaced particles like strip is adhered
to the surfaces of PbI2 thin films. As the TPPCl solution
is at 1 mg/mL, several well-distributed large TPPCl particles are
formed on the surface of PbI2 thin film. As the TPPCl solution
is further increased to 1.5 mg/mL, large TPPCl nanoparticles are aggregated
on the surface of PbI2 thin film.
Figure 1 Top view of SEM images
of pristine PbI2 thin film and
PbI2 thin film treated with the TPPCl ultrathin layers
cast from TPPCl solutions with concentrations of (a) 0 mg/mL, (b)
0.25 mg/mL, (c) 0.5 mg/mL, (d) 1 mg/mL, and (e) 1.5 mg/mL. Top view
of SEM images of pristine CH3NH3PbI3 thin film and CH3NH3PbI3 thin film
pretreated with the TPPCl ultrathin layers cast from TPPCl solutions
with concentrations of (f) 0 mg/mL, (g) 0.25 mg/mL, (h) 0.50 mg/mL,
(i) 1 mg/mL, and (j) 1.5 mg/mL.
Scheme 1 (a) Molecular Structure of TPPCl and (b) the Device Structure
of
Perovskite Solar Cells
Figure 1f–j
presents the SEM images of pristine CH3NH3PbI3 thin film and CH3NH3PbI3 thin films pretreated with TPPCl ultrathin layers. Compared to pristine
CH3NH3PbI3 thin film, no significant
change in the film morphology is observed in the CH3NH3PbI3 thin film pretreated with the TPPCl ultrathin
layer cast from TPPCl solution with a concentration of 0.25 mg/mL.
However, the CH3NH3PbI3 thin film
pretreated with the TPPCl ultrathin layer cast from TPPCl solution
with a concentration of 0.5 mg/mL, displays larger and more inerratic
grains. The CH3NH3PbI3 thin film
pretreated with the TPPCl ultrathin layer cast from TPPCl solution
with a concentration of 1.0 mg/mL, shows larger gains and higher gains
continuity with distinctly less grain boundaries. The CH3NH3PbI3 thin film pretreated with the TPPCl
ultrathin layer cast from TPPCl solution with a concentration of 1.5
mg/mL, possesses very fine grain with flatness feature of grain boundary.
Thus, these results demonstrate that the TPPCl ultrathin layers affect
the qualities of resultant CH3NH3PbI3 thin films.
Figure 2 presents
the X-ray diffraction (XRD) patterns of pristine CH3NH3PbI3 thin film and CH3NH3PbI3 thin films pretreated with TPPCl ultrathin layers.
No XRD patterns assigned to TPPCl ultrathin layer are found in all
CH3NH3PbI3 thin films, indicating
that TPPCl is evaporated during the thermal annealing for the formation
of CH3NH3PbI3 thin films. All CH3NH3PbI3 thin films exhibit the same
diffraction peaks located at 14.1, 28.5, and 31.9°, corresponding
to the (110), (220), and (114) crystal planes. No XRD patterns assigned
to TPPCl ultrathin layer are found in all. These results indicate
that all CH3NH3PbI3 thin films possess
the tetragonal crystal phase.29,32 However, the peak intensities
are different. The highest peak intensity (the (110) plane) is observed
from the CH3NH3PbI3 film pretreated
with the TPPCl ultrathin layer cast from a 1.0 mg/mL concentration
of TPPCl solution, indicating that the CH3NH3PbI3 thin film pretreated with the TPPCl ultrathin layer
possesses the best crystallinity, which is in good agreement with
the SEM results. All of these results imply that the CH3NH3PbI3 film pretreated with the TPPCl ultrathin
layer cast from a 1.0 mg/mL concentration of TPPCl solution, possesses
optimal photovoltaic properties.
Figure 2 XRD patterns of pristine CH3NH3PbI3 film and CH3NH3PbI3 thin films
pretreated with the TPPCl ultralayers cast from TPPCl solutions with
concentrations of 0, 0.25, 0.50, 1, and 1.5 mg/mL.
Figure 3 depicts
the UV–vis absorption spectra of pristine CH3NH3PbI3 thin film and CH3NH3PbI3 film pretreated with the TPPCl ultrathin layers.
All CH3NH3PbI3 thin films have identical
absorption spectrum with the same onset of absorption, indicating
that the TPPCl ultrathin layers do not have any influence on the band
gap of the CH3NH3PbI3 thin film.
However, the CH3NH3PbI3 thin film
pretreated with the TPPCl ultrathin layers possesses gradually enhanced
absorbance ranging from 380 to 770 nm along with the TPPCl ultrathin
layers cast from increased concentrations of TPPCl solutions. The
CH3NH3PbI3 thin film pretreated with
the TPPCl ultrathin layer cast from a 1.0 mg/mL concentration of TPPCl
solution possesses the highest absorbance. Such high absorbance indicates
that more light will be absorbed by the CH3NH3PbI3 thin film, implying that more photocurrent could
be generated.
Figure 3 UV–vis spectra of pristine CH3NH3PbI3 film and CH3NH3PbI3 films
pretreated with the TPPCl ultrathin layers cast from TPPCl solutions
with concentrations of 0, 0.25, 0.50, 1, and 1.5 mg/mL.
The photovoltaic properties of pristine CH3NH3PbI3 thin film and CH3NH3PbI3 thin films pretreated with TPPCl ultrathin
layers are evaluated
through investigation of device performance of PSCs with a device
structure of ITO/PTAA/CH3NH3PbI3/PC61BM/BCP/Ag, as shown in Scheme 1b, where ITO is indium tin oxide, which acts as the
anode; PTAA is poly[bis(4-phenyl)(2,4,6-trimethylphenyl)amine], which
acts as the hole extraction layer; PC61BM is 6,6-phenyl-C61-butyric acid methyl ester, which acts as the electron extraction
layer; BCP is bathocuproine, which acts as the hole blocking layer;
and Ag is sliver, which acts as the cathode. The current density versus
voltage (J–V) characteristics
of PSCs are shown in Figure 4a. The device performance parameters are summarized in Table 1. The PSCs fabricated
by the pristine CH3NH3PbI3 thin film
exhibit a VOC of 1.04 V, a JSC of 21.08 mA/cm2, an FF of 74.41, and a corresponding
PCE of 16.34%. These device performance parameters are consistent
with reported values from PSCs with the same device structure.7−9 The PSCs fabricated by the CH3NH3PbI3 thin film pretreated with TPPCl ultrathin layers exhibit enlarged VOC, enhanced JSC, and thus boosted PCEs. The best device performance (VOC of 1.12 V, JSC of 21.71
mA/cm2, FF of 74.43, and the corresponding PCE of 18.04%),
is observed from the PSCs fabricated by the CH3NH3PbI3 thin film pretreated with the TPPCl ultrathin layer
cast from a 1.0 mg/mL concentration of TPPCl solution.
Figure 4 (a) J–V characteristics
and (b) external quantum efficiency (EQE) spectra of PSCs fabricated
by pristine CH3NH3PbI3 film and CH3NH3PbI3 films pretreated with the TPPCl
ultrathin layers cast from TPPCl solutions with concentrations of
0, 0.25, 0.50, 1, and 1.5 mg/mL.
Table 1 Device Performance Parameters of PSCs
solution
concentrations for deposition of the TPPCl ultrathin layer (mg/mL) VOC (V) JSC (mA/cm2) FF (%) PCE (%) HI (%)
0 1.04 21.08 74.41 16.34 3.74
0.25 1.06 21.32 75.17 17.04 1.73
0.5 1.08 21.77 74.84 17.51 1.11
1 1.12 21.71 74.43 18.04 1.12
1.5 1.08 21.38 65.75 15.26 –3.11
Figure 4b presents
the external quantum efficiencies (EQE) of PSCs fabricated by either
pristine CH3NH3PbI3 thin film or
CH3NH3PbI3 thin films pretreated
with TPPCl ultrathin layers. Enhanced EQE values are observed from
the PSCs fabricated by the CH3NH3PbI3 thin films pretreated with TPPCl ultrathin layers compared to those
by pristine CH3NH3PbI3 thin film.
The integrated JSC values are 20.16 mA/cm2 for the PSCs fabricated by pristine CH3NH3PbI3 thin film, and 20.42, 20.83, 20.80, and 20.46
mA/cm2 for the PSCs fabricated by CH3NH3PbI3 thin films pretreated with the TPPCl ultrathin
layers cast from the TPPCl solutions with concentrations of 0.25,
0.5, 1.0, and 1.5 mg/mL, respectively. These JSC values are consistent with the JSC extracted from J–V characteristics,
as shown in Figure 4a.
The increased JSC is attributed
to
the enlarged grain size (Figure 2) and stronger light-harvesting ability of CH3NH3PbI3 thin films pretreated with TPPCl ultrathin
layers (Figure 3).33,34 To further understand enhanced JSC,
transient photocurrent (TPC) and transient photovoltage (TPV) measurements
are conducted to assess the intrinsic properties of charge-carrier
extraction and charge-carriers recombination in PSCs.35,36Figure 5a presents
the normalized TPC of the PSCs fabricated by either pristine CH3NH3PbI3 thin film or CH3NH3PbI3 thin films pretreated with TPPCl ultrathin
layers. The PSCs fabricated by CH3NH3PbI3 thin films pretreated with TPPCl ultrathin layers possess
slightly shorter charge extraction lifetimes (0.17, 0.24, and 0.23
μs) compared to that (0.29 μs) by the PSCs fabricated
the pristine CH3NH3PbI3 thin film,
indicating that reduced trap-assisted charge recombination and better
charge extraction efficiencies have taken place in these PSCs. However,
the longest charge extraction lifetime (0.43 μs) is observed
in the PSCs fabricated by CH3NH3PbI3 thin film pretreated with the TPPCl ultrathin layers cast from a
1.5 mg/mL concentration of the TPPCl solution, indicating that PSCs
fabricated by such thin film exhibit the poorest device performance.
Figure 5 (a) Transient
photocurrent and (b) transient photovoltage decays
of PSCs fabricated by pristine CH3NH3PbI3 thin film and CH3NH3PbI3 thin films pretreated with the TPPCl ultrathin layers cast from
TPPCl solutions with concentrations of 0, 0.25, 0.50, 1, and 1.5 mg/mL.
Figure 5b shows
the normalized TPV of the PSCs fabricated by either pristine CH3NH3PbI3 thin film or CH3NH3PbI3 thin films pretreated with TPPCl ultrathin
layers. The PSCs fabricated by CH3NH3PbI3 thin films pretreated with TPPCl ultrathin layers possess
longer charge recombination lifetimes to reach the same TPV compared
to those fabricated by pristine CH3NH3PbI3 thin film. The longest charge recombination lifetime is observed
in the PSCs fabricated by CH3NH3PbI3 thin film pretreated with the TPPCl ultrathin layer cast from a
1 mg/mL concentration of the TPPCl solution. The longer charge recombination
lifetime demonstrates the more suppressed charge recombination in
PSCs. Thus, the PSCs fabricated by CH3NH3PbI3 thin film pretreated with TPPCl ultrathin layers possess
larger JSC values compared to those fabricated
by pristine CH3NH3PbI3 thin film.
The light intensity dependence on VOC is further investigated to illustrate the charge-carrier recombination
in PSCs. Figure 6a
displays the light intensity dependence on VOC for the PSCs fabricated by either pristine CH3NH3PbI3 thin film or CH3NH3PbI3 thin films pretreated with TPPCl ultrathin layers.
According to VOC ∝ S In(I)37 (where S is the slope and I is the light intensity),
the smallest S (0.038) is observed in the PSCs fabricated
by the CH3NH3PbI3 thin film pretreated
with the TPPCl ultrathin layer cast from a 1 mg/mL concentration of
the TPPCl solution, indicating that suppressed trap-assisted charge
recombination occurred in PSCs.38 Therefore,
the PSCs fabricated by the CH3NH3PbI3 thin film pretreated with the TPPCl ultrathin layer cast from a
1 mg/mL concentration of the TPPCl solution exhibit the highest JSC value among all PSCs.
Figure 6 (a) VOC dependence on different light
intensities and (b) J–V characteristics,
in the dark, of the PSCs fabricated by pristine CH3NH3PbI3 thin film and CH3NH3PbI3 thin films pretreated with the TPPCl ultrathin layers
cast from TPPCl solutions with concentrations of 0, 0.25, 0.50, 1,
and 1.5 mg/mL.
To understand the underlying
physics of enlarged VOC, the J–V characteristics
of PSCs are measured in the dark, and the results are shown in Figure 6b. According to the
Shockley–Queisser model,39 the relationship
between J and VOC is
described as where J0 is the
reverse dark current density, q is the electron charge, n is the diode ideality factor, k is the
Boltzmann constant, and T is the temperature. Thus,
it concludes that a large VOC is anticipated
from the PSCs with a low value of J0.
As shown in Figure 6b, the PSCs fabricated by the CH3NH3PbI3 thin film pretreated with TPPCl ultrathin layers possess
low J0 values compared to those fabricated
by the pristine CH3NH3PbI3 thin film.
In particular, the PSCs fabricated by the CH3NH3PbI3 thin film pretreated with the TPPCl ultrathin layer
cast from a 1 mg/mL concentration of the TPPCl solution possess the
lowest J0. Thus, the PSCs fabricated by
the CH3NH3PbI3 thin film pretreated
with the TPPCl ultrathin layer cast from a 1 mg/mL concentration of
the TPPCl solution exhibit the largest VOC value.
The hysteresis behaviors of PSCs are further investigated. Figure 7a–e presents
the J–V characteristics of
the PSCs fabricated by either pristine CH3NH3PbI3 thin film or the CH3NH3PbI3 thin film pretreated with TPPCl ultrathin layers under either
forward scan direction (from the negative voltage to the positive
voltage) or reserved scan direction (from the positive voltage to
the negative voltage). The hysteresis index (HI) is defined as .40Table 1 summarizes PCEs and
the corresponding HI values of PSCs under different scan directions.
Clearly, the PSCs fabricated by pristine CH3NH3PbI3 thin film exhibit PCEs of 17.00 and 17.66% under
forward and reversed scan directions, respectively, which reveal an
HI value of 3.74%. A stable PCE and the smallest HI are observed from
the PSCs fabricated by the CH3NH3PbI3 thin film pretreated with TPPCl ultrathin layer cast from a 1 mg/mL
concentration of the TPPCl solution. Thus, the PSCs fabricated by
the CH3NH3PbI3 thin film pretreated
with the TPPCl ultrathin layers possess reduced photocurrent hysteresis.
Such reduced photocurrent hysteresis behavior probably originated
from suppressed charge recombination due to the improved crystallinity
of CH3NH3PbI3 thin films.
Figure 7 J–V characteristics of
the PSCs fabricated by pristine CH3NH3PbI3 thin film and the CH3NH3PbI3 thin films pretreated with the TPPCl ultrathin layers cast from
TPPCl solutions with concentrations of 0, 0.25, 0.50, 1, and 1.5 mg/mL
and measured under forward and reverse scan directions.
3 Conclusions
In summary,
we reported a simple method to tune the crystallinity
of CH3NH3PbI3 thin film in a two-step
process. Compared to pristine CH3NH3PbI3 thin film, large and inerratic grains have been observed
in the CH3NH3PbI3 thin film pretreated
with the TPPCl ultrathin layer. As a result, the PSCs fabricated by
CH3NH3PbI3 thin film pretreated with
TPPCl ultrathin layer exhibit a VOC of
1.12 V, a JSC of 21.71 mA/cm2, an FF of 74.43, and a corresponding PCE of 18.04%, with dramatically
reduced hysteresis compared to the PSCs fabricated by pristine CH3NH3PbI3 thin film, which exhibit a VOC of 1.04 V, a JSC of 21.08 mA/cm2, an FF of 74.41, and a corresponding
PCE of 16.34%, with serious hysteresis. Our results provide a new
strategy to boost device performance through tuning the crystallinity
of perovskite thin films.
4 Experimental Section
4.1 Materials
Bathocuproine (BCP), tetraphenylphosphonium
chloride (TPPCl), n-butyl alcohol, anhydrous N,N-dimethylformamide (DMF), and ethanol
were purchased from Sigma-Aldrich. Lead(II) iodide (PbI2) was purchased from Alfa Aesar. Phenyl-C61-butyric acid
methyl ester (PC61BM) was purchased from 1-Material Inc.
Poly[bis(4-phenyl)(2,4,6-trimethylphenyl)amine] (PTAA) and methylammonium
iodide (MAI) were purchased from Xi’an Polymer Light Technology
Corp. All materials were used as received without further purification.
4.2 Solution Preparation
PbI2 was
first dissolved in DMF at a concentration of 400 mg/mL and then
stirred at 60 °C for 12 h to form a PbI2 solution.
Afterward, the PbI2 solution was filtered using a filter
of size 0.45 mm to obtain a transparent yellow solution. The MAI was
dissolved in ethanol to form an MAI solution with a concentration
of 35 mg/mL. TPPCl was dissolved in n-butyl alcohol
with concentrations of 0.25, 0.5, 1, and 1.5 mg/mL.
4.3 Preparation of CH3NH3PbI3 Thin
Film
The CH3NH3PbI3 thin
films were prepared by a two-step deposition
method. PbI2 solution was first spin-cast on the top of
the PTAA layer, which was cast from the corresponding solution, and
thermally annealed at 80 °C for 5 min. After PbI2 thin
film was cooled to room temperature, the TPPCl ultrathin layer was
coated on the top of PbI2 thin film from TPPCl solution
at 4000 rpm for 30 s. Afterward, the MAI thin layer was spin-coated
on the top of either pristine PbI2 thin film or the PbI2/TPPCl thin film and thermally annealed at 100 °C for
2 h for converting PbI2 and CH3NH3I into CH3NH3PbI3 thin film.
4.4 Characterization of CH3NH3PbI3 Thin Film
The surface profilometer (Tencor,
Alpha-500) was used to measure the film thickness. UV–vis absorption
spectra of CH3NH3PbI3 thin films
were recorded on an HP 8453 spectrophotometer. Top-view images of
CH3NH3PbI3 thin films were obtained
using a field-emission scanning electron microscope (Zeiss Merlin).
4.5 Fabrication of Perovskite Solar Cells
Precleaned
indium tin oxide (ITO) glass substrates were first treated
by oxygen plasma for 3 min. Afterward, ∼10 nm of the PTAA film
was spin-cast on the top of the ITO substrates from PTAA solution
and then thermally annealed at 100 °C for 10 min. The CH3NH3PbI3 thin films were prepared by
the two-step deposition method described above. Then, an ∼40
nm thick PC61BM layer was spin-cast on the top of the CH3NH3PbI3 thin film. Afterward, an ∼10
nm BCP thin film was spin-cast on the top of the PC61BM
layer. Finally, an ∼100 nm silver (Ag) electrode was thermally
evaporated on the top of the BCP layer in vacuum with a base pressure
of 2 × 10–6 mbar. The device area was measured
to be 5.7 mm2.
4.6 Characterization of Perovskite
Solar Cells
The current density–voltage (J–V) characteristics of PSCs were measured
under 1 sun from
an AM 1.5 G solar simulator (Japan, SAN-EI, XES-40S1), where light
intensity was calibrated using a standard silicon solar cell with
a KG5 visible filter. The photocurrent hysteresis properties of PSCs
were assessed by testing the PSCs at both forward (from −1.2
to 0.2 V) and reverse (from 0.2 to −1.2 V) directions at a
scan rate of 3 V/s. The external quantum efficiency (EQE) spectra
of PSCs were recorded on a DSR100UV-B spectrometer with an SR830 lock-in
amplifier, a bromine tungsten light source, and a calibrated Si detector.
4.6.1 Transient Photovoltage and Transient Photocurrent
Measurements
A digital oscilloscope (Tektronix TDS 3052C)
with input impedances of 1 MΩ and 50 Ω was used to monitor
the charge density decay and charge extraction time of PSCs. The transient
photovoltage of PSCs was measured under 0.03 sun illumination with
a small perturbation by an attenuated laser pulse (500 nm). The laser-pulse-induced
photovoltage variation (ΔV) was smaller than
5% of the VOC produced by the background
illumination. The transient photocurrent of PSCs was measured by applying
laser pulses to the short-circuited devices in the dark with an excitation
wavelength of 500 nm, a pulse width of 120 fs, and a repetition rate
of 1 kHz.
Author Contributions
§ J.Q. and
X.Y. contributed to this work equally.
The authors
declare no competing financial interest.
Acknowledgments
This study was
financially supported by NSFC (51329301).
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145892110.1021/acsomega.8b01188ArticleRationalizing the Formation of Activity Cliffs in
Different Compound Data Sets Hu Huabin Stumpfe Dagmar Bajorath Jürgen *Department of Life Science Informatics,
B-IT, LIMES Program Unit Chemical Biology and Medicinal Chemistry, Rheinische Friedrich-Wilhelms-Universität, Endenicher Allee 19c, D-53115 Bonn, Germany* E-mail: bajorath@bit.uni-bonn.de.
Phone: 49-228-73-69100.11 07 2018 31 07 2018 3 7 7736 7744 30 05 2018 26 06 2018 Copyright © 2018 American Chemical
Society2018American Chemical
SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
Activity cliffs are formed by structurally
analogous compounds
with large potency variations and are highly relevant for the exploration
of discontinuous structure–activity relationships and compound
optimization. So far, activity cliffs have mostly been studied on
a case-by-case basis or assessed by global statistical analysis. Different
from previous investigations, we report a large-scale analysis of
activity cliff formation with a strong focus on individual compound
activity classes (target sets). Compound potency distributions were
systematically analyzed and categorized, and structural relationships
were dissected and visualized on a per-set basis. Our study uncovered
target set-dependent interplay of potency distributions and structural
relationships and revealed the presence of activity cliffs and origins
of cliff formation in different structure–activity relationship
environments.
document-id-old-9ao8b01188document-id-new-14ao-2018-01188zccc-price
==== Body
1 Introduction
Activity cliffs are formed by structurally similar (analogous)
active compounds with large differences in potency.1−4 Because activity cliffs represent
small chemical changes having large biological activity effects, they
embody the pinnacle of structure–activity relationship (SAR)
discontinuity,3 which is detrimental for
quantitative SAR predictions.2 However,
discontinuous SARs and activity cliffs often reveal SAR determinants,
especially when encountered during early stages of compound optimization,
and thus provide viable information for medicinal chemistry.3,4
For a consistent assessment of activity cliffs, similarity
and
potency difference criteria must be clearly defined.3 On the basis of globally assessed potency range distributions
of pairs of active analogues, an at least 100-fold difference in potency
(on the basis of equilibrium constants, if available) has been proposed
and frequently been used as an activity cliff criterion.4,5 The definition of activity cliffs also depends on the molecular
representations and similarity measures that are used.4,6 Compound similarity for activity cliff definition can be quantified
in different ways, for example, by calculating Tanimoto similarity
on the basis of molecular fingerprint representations or by applying
substructure-based similarity criteria.3,4 Numerical similarity
measures, such as the Tanimoto coefficient, yield a continuum of values,
and a threshold must be set for defining activity cliffs. By contrast,
substructure-based methods produce a binary readout, for example,
two compounds share the same core structure—and are classified
as similar—or they do not. In addition to comparing molecular
graph-based (two-dimensional) representations, activity cliffs have
also been determined in three dimensions by calculating the similarity
of experimental compound binding modes taken from complex X-ray structures.7
For graph-based activity cliff definition,
substructure similarity
assessment is—in our experience—generally more consistent
than numerical similarity calculations and often easier to interpret
from a chemical perspective.4 Among substructure-based
approaches, the matched molecular pair (MMP) concept8,9 is particularly attractive for activity cliff definition. An MMP
is defined as a pair of compounds that are only distinguished by a
chemical modification at a single site.8 This modification corresponds to the exchange of a pair of substructures,8,9 which is termed a chemical transformation.9 By introducing appropriate transformation size restrictions, the
formation of MMPs can be limited to structural analogues typically
generated during compound optimization.10 Applying this similarity criterion yields a structurally conservative
and chemically intuitive definition of activity cliffs.4,10 Moreover, transformation size-restricted MMPs can be efficiently
generated algorithmically,9,10 hence enabling large-scale
analysis of activity cliff populations.
In light of these considerations,
our preferred activity cliff
definition encompasses the formation of a transformation size-restricted
MMP by two compounds sharing the same biological activity that have
an at least 100-fold difference in potency.4,10 Whenever
possible, potency differences are determined on the basis of (assay-independent)
equilibrium constants. The so-defined activity cliffs have been termed
MMP-cliffs.10
The definition of activity
cliffs is focused on compound pairs
and hence accounts for pairwise relationships. However, activity cliffs
in compound data sets are mostly not formed by isolated compound pairs
(i.e., pairs without structural neighbors forming additional activity
cliffs). Rather, the vast majority of activity cliffs are formed in
a coordinated manner by groups of structurally related compounds with
large potency variations, meaning that individual compounds are involved
in the formation of multiple activity cliffs with different analogues.11,12 In activity cliff networks where nodes represent compounds and edges
pairwise activity cliffs, compound subsets forming coordinated cliffs
give rise to the formation of disjoint clusters.12 These activity cliff clusters are a rich source of SAR
information and much more informative than cliffs considered as isolated.13 More than 95% of MMP-cliffs detected across
different data sets were formed in a coordinated manner.14 In activity cliff networks, clusters often include
“hubs,” that are, nodes representing molecules that
are centers of local activity cliff formation with multiple partner
compounds. Such molecules have also been termed “activity cliff
generators.”15,16
In addition to activity
cliff coordination, the frequency with
which activity cliffs occur across different data sets has been determined.5,14 There has been substantial growth in activity cliff information
over time. For example, from June 2011 until January 2015, the number
of MMP-cliffs originating from the ChEMBL database,17 the major public repository of compounds and activity data
from medicinal chemistry sources, nearly doubled; with a total of
more than 17 000 MMP-cliffs available at the beginning of 2015.14 In addition, the target coverage of MMP-cliffs
increased from about 200 to 300 individual target proteins over this
period of time. However, despite this strong growth, the proportion
of bioactive compounds involved in the formation of MMP-cliffs across
different compound data sets remained essentially constant at close
to 23%.14
So far, activity cliffs
have been studied in exemplary compound
sets on a case-by-case basis or surveyed by global statistical analysis.5,14 In addition, cliff populations have been organized and visualized
in network representations.12,13 However, what has not
been attempted thus far is systematically exploring and comparing
activity cliff formation in different compound activity classes (also
called target sets). To these ends, we have analyzed in detail potency
distributions and structural relationships between compounds in many
different target sets, studied how activity cliffs were formed, and
determined the differences between sets. Hence, the focus of our current
study has been on details of activity cliff arrangements in individual
compound sets rather than on global statistical exploration. Our analysis
revealed many characteristic differences in activity cliff formation
between target sets.
2 Materials and Methods
2.1 Activity Cliff Definition
For our
current analysis, we introduced a modification of our preferred MMP-cliff
definition stated above.4,10 For MMP generation,
standard random fragmentation of exocyclic single bonds9 was replaced by fragmentation according to retrosynthetic
(RECAP) rules,18 yielding (transformation
size-restricted) RECAP-MMPs (RMMPs).19 Retrosynthetic
MMPs were generated to further increase the chemical relevance (synthetic
accessibility) of compound pairs, forming cliffs. Accordingly, the
formation of an RMMP was used as a similarity criterion for activity
cliffs, and an at least 100-fold difference in potency between RMMP
compounds was required, as before. The so-defined activity cliffs
are referred to as RMMP-cliffs.
2.2 Compounds
and Activity Data
Bioactive
compounds with high-confidence activity data were assembled from ChEMBL
version 23.17 The following selection criteria
were applied: First, only compounds involved in direct interactions
(type “D”) with human targets at the highest confidence
level (assay confidence score 9) were selected. Second, only numerically
specified equilibrium constants (Ki values)
were considered as potency measurements. Equilibrium constants were
reported as pKi values. On the basis of
these selection criteria, a total of 71 967 unique compounds were
obtained with activity against a total of 904 targets. Accordingly,
these compounds were organized into 904 target sets.
2.3 RMMP Analysis
RMMPs were systematically
generated for all target sets, yielding 354 094 target set-based RMMPs
(243 110 unique RMMPs) that were formed by 46 977 compounds from 574
target sets. For the subsequent analysis, only target sets that contained
at least 100 RMMPs were retained, which resulted in 237 sets yielding
a total of 347 025 target-based RMMPs (238 795 unique RMMPs) formed
by 44 451 compounds.
For each
target set, an RMMP network was generated in which nodes represented
compounds and edges pairwise RMMP relationships. In this network,
each separate RMMP cluster represented a unique series of analogues.
RMMP networks were also used to represent RMMP-cliffs by highlighting
edges that represented both RMMP and activity cliff relationships.
All network representations were drawn with Cytoscape.20
2.4 Potency Distributions
For the 237
qualifying target sets, compound potency distributions were monitored
in boxplots. On the basis of the interquartile range (IQR), that is,
the range between quartile 1 (Q1) and 3 (Q3), target sets were assigned
to three different categories, as shown in Figure 1: category 1 (CAT 1), IQR was smaller than
1 order of magnitude (<10-fold difference in potency); CAT 2, IQR
fell between 1 and less than 2 orders of magnitude (10- to 100-fold
difference); and CAT 3, IQR no smaller than 2 orders of magnitude
(≥100-fold difference in potency). By definition, the IQR represented
the potency range of ∼50% of the compounds in each target set.
Figure 1 Potency
distribution in target sets and categorization. The compound
potency distributions of all 237 target sets were analyzed in a boxplot
and the IQR, that is, the difference between quartile 3 and 1, was
determined. On the basis of the IQR, target sets were divided into
three different categories (CAT 1: IQR < 1; CAT 2: 1 ≤ IQR
< 2; CAT 3: IQR ≥ 2).
3 Results and Discussion
3.1 Study
Concept
Activity cliffs have
so far mostly been studied on the basis of individual compound series
or by global statistical analysis.3−5 Our current study was
designed to systematically investigate, for the first time, the differences
in activity cliff formation and frequency between different target
sets by relating compound potency distributions and structural relationships
to each other. Therefore, potency distributions were determined for
many different target sets, categorized, compared, and related to
intra-set analogue relationships, which were systematically determined.
Primary goals of the analysis included the assessment of differences
in activity cliff formation and frequency between different target
sets and the rationalization of such differences on the basis of potency
and structural criteria, as defined in the following. To better understand
target set-dependent activity cliff distributions, they were visualized
in network representations. Taken together, these features set our
current analysis apart from previous studies of activity cliffs in
computational and medicinal chemistry.3,4
3.2 Structural Relationships
Close structural
relationships between active compounds are one of the two major determinants
of activity cliffs, in addition to potency differences. RMMP (or MMP)
calculations reveal close structural relationships and identify pairs
of analogues. Importantly, however, the number of RMMPs produced by
a given target set cannot be reliably used as an indicator of structural
homogeneity. Rather, the presence or absence of multiple subsets of
analogues comprising different series strongly influences structural
heterogeneity or homogeneity, which is reflected by the cluster structure
of RMMP networks, as illustrated in Figure 2. Here, two target sets with similar numbers
of RMMP-forming compounds are compared. The target set on the left
was dominated by a large cluster of analogues and was thus structurally
homogeneous, whereas the set on the right contained 20 different small
clusters and 1 larger cluster and was structurally heterogeneous.
It follows that the cluster structure of RMMP networks must be carefully
considered as a prerequisite for RMMP-cliff formation.
Figure 2 Structural similarity
in target sets. For two exemplary target
sets, RMMP networks are shown in which blue nodes represent compounds
and edges pairwise RMMP relationships. Separate clusters represent
a unique series of analogues. Although the number of RMMP-forming
compounds (CPDs) was similar for both target sets, the number of clusters
differed significantly.
3.3 Potency Distributions and Profiles
The likelihood of large potency differences between similar compounds
can be estimated by monitoring the potency distributions of target
sets. For our analysis, we assigned potency distributions to three
different categories (CAT 1–3) on the basis of boxplot-derived
IQR values, as shown in Figure 1. CAT 1, 2, and 3 comprised 25, 169, and 43 target sets, respectively.
Hence, the majority of target sets fell into CAT 2 whose IQR spanned
1 to 2 orders of magnitude in potency and thus delineated an activity
cliff-relevant range, which was further expanded by CAT 3. These observations
supported our categorization of potency distributions. Accordingly,
potency distributions became increasingly variable from CAT 1 to 3,
as revealed by the potency distribution profiles in Figure 3. The CAT 1 profiles in Figure 3a reflect narrow
potency distributions on the basis of which activity cliff formation
is unlikely. By contrast, the CAT 2 profiles in Figure 3b and, especially, CAT 3 profiles in Figure 3c reveal large potency
variations between structural analogues, resulting in a principally
high propensity of activity cliffs.
Figure 3 Potency distribution profiles. Shown are
exemplary potency distribution
profiles for target sets belonging to different categories [(a), CAT
1; (b), CAT 2; (c), CAT 3] according to Figure 1. Black dots represent RMMP compounds and
red dots singletons not participating in RMMPs.
3.4 RMMP-Cliffs
In 207 of the 237 qualifying
targets sets, RMMP-cliffs were identified, amounting to a total of
11 834 cliffs. Table 1 reports that the number of RMMP-cliffs increased over target sets
of CAT 1, 2, and 3, with on average 2, 52, and 69 cliffs per set,
respectively. Thus, there was a general trend of increasing number
of RMMP-cliffs with increasing variability of potency distributions.
The very small number of RMMP-cliffs for CAT 1 sets was directly attributable
to the narrow potency distributions characterizing this category. Table 2 reports that the
48 target sets containing 50 to a maximum of 820 RMMP-cliffs exclusively
belonged to CAT 2 and CAT 3 that had activity cliff-relevant IQR values.
By contrast, target sets with less than 50 RMMP-cliffs were found
in all 3 categories. Figure 4 shows that the majority of target sets with large number
of 100 or more RMMP-cliffs belonged to CAT 2, which was due to the
large number of 169 target sets in this category compared to only
43 sets in CAT 3. A systematic increase in the number of activity
cliffs with increasing IQR values was not observed.
Figure 4 RMMP-cliffs vs IQR values.
For each of the 237 target sets, the
number of RMMP-cliffs (y-axis) is plotted against
increasing IQR values (x-axis). Red vertical lines
separate target sets belonging to CAT 1, 2, and 3.
Table 1 Target Set Statisticsa
CAT # target sets # clusters (mean) # RMMP-cliffs (mean)
1 25 10 2
2 169 54 52
3 43 37 69
a For each target set category (CAT),
the number (#) of target sets, mean number of RMMP clusters per set,
[# clusters (mean)], and mean number of RMMP-cliffs are reported.
Table 2 RMMP-Cliff Distributiona
# RMMP-cliffs (range) # target sets CATs
0 30 1, 2, 3
[1, 10) 77 1, 2, 3
[10, 20) 33 1, 2, 3
[20, 50) 49 1, 2, 3
[50, 100) 20 2, 3
[100, 500) 25 2, 3
[500, 820] 3 2, 3
a For different ranges of RMMP-cliffs,
the number of target sets (# targets) and categories (CATs) they belong
to are reported.
However,
despite these general trends, the propensity to form RMMP-cliffs
could not solely be attributed to the variability and spread of potency
distributions. Rather, as further discussed below, potency distributions
in target sets must be viewed in combination with RMMP networks and
their cluster structure. Table 1 also reports that target sets in CAT 1, 2, and 3 contained
on average 10, 54, and 37 RMMP clusters, respectively. Thus, CAT 2
and CAT 3 sets contained large number of clusters (analogue series)
whose local potency distributions strongly influenced RMMP-cliff formation.
3.5 Interplay of Potency Patterns and Structural
Relationships
The 207 target sets containing RMMP-cliffs
were individually examined to evaluate potency distribution profiles
and RMMP networks in context and rationalize why RMMP-cliffs were
formed with different frequencies. The analysis revealed a number
of characteristic features determining cliff formation that are summarized
in Figure 5 by comparing
exemplary target sets. Figure 5a (top) shows a set of phosphodiesterase 3A inhibitors with
a flat CAT 1 potency distribution profile, which prohibited RMMP-cliff
formation, despite the presence of two analogue series with in-part
extensive RMMP relationships. In addition, Figure 5a (bottom) displays somatostatin receptor
5 ligands with a variable CAT 2 distribution and more than 100 RMMP-forming
compounds. Although cliff formation was more likely in this case,
the target set did not contain any RMMP-cliffs either. This was a
direct consequence of a heterogeneous cluster structure and local
potency distributions over different subsets of analogues forming
16 clusters, as revealed by the RMMP network of this set.
Figure 5 Differences
in RMMP-cliff formation. In (a–c), exemplary
target sets with characteristic differences in activity cliff formation
are compared, as described in the text. For each set, its potency
distribution profile and RMMP network are shown and RMMP statistics
are reported. Network nodes are colored by potency using a continuous
color spectrum from red (lowest potency in the target set) over yellow
(intermediate) to green (highest potency). If available, compounds
forming exemplary RMMP-cliffs are shown and consistently labeled in
all display items.
Figure 5b shows
two different sets of kinase inhibitors with similar CAT 2 potency
distributions but different RMMP cluster structures that yielded 40
(top) and 27 (bottom) RMMP-cliffs, respectively. Exemplary RMMP-cliffs
are displayed. In both instances, the target sets were structurally
heterogeneous but RMMP-cliffs were formed across different clusters,
revealing high degrees of SAR discontinuity.
In Figure 5c, sets
of anandamide amidohydrolase (top) and Bcl-X (bottom) inhibitors are
compared having CAT 2 (top) and CAT 3 (bottom) distributions, respectively.
The anandamide amidohydrolase inhibitors contained only 49 RMMP-forming
compounds. The RMMP network was dominated by a densely connected cluster
of 19 analogues that formed 79 coordinated RMMP-cliffs (exemplary
cliffs are shown). Thus, in this case, the number of RMMP-cliffs was
much larger than the number of participating analogues because of
extensive coordination of cliffs. Hence, this cluster represented
an SAR hotspot. By contrast, the Bcl-X inhibitors contained a much
larger number of 119 RMMP-forming compounds that were distributed
over 20 clusters. Although the CAT 3 potency distribution of this
target set was highly variable, the majority of compounds in individual
clusters had comparable potency, whereas the potency levels of clusters
significantly differed, giving rise to the presence of only three
RMMP-cliffs.
Taken together, the results in Figure 5 were representative of many
target sets
we studied. Analyzing the potency distribution profiles and in combination
with RMMP networks revealed the characteristic features of target
sets and clearly rationalized differences in RMMP-cliff frequency
across target sets.
4 Conclusions
Herein,
we have reported a systematic analysis of RMMP-cliffs in
more than 200 target sets to investigate and better understand the
origins of cliff formation and differences in the frequency of cliffs.
Our study was strongly focused on individual target sets and their
comparison. Potency distributions were determined and categorized,
and structural relationships were analyzed at the level of RMMPs and
organized in networks. Structural homogeneity of target sets and potency
distributions of increasing variability generally supported the formation
of RMMP-cliffs. However, the interplay of structural and potency relationships
determined the frequency with which RMMP-cliffs were formed, as revealed
by relating potency profiles and RMMP networks to each other and studying
local potency distributions across different RMMP clusters.
The analysis scheme introduced herein reveals target set-dependent
formation of activity cliffs, provides immediate visual access to
characteristic activity cliff-relevant features of target sets, and
rationalizes differences in the frequency of cliffs across sets.
Author Contributions
The study
was carried out by all authors, and the manuscript was written with
contributions of all authors. All authors have approved the final
version of the manuscript.
The authors
declare no competing financial interest.
Acknowledgments
H.H. is supported by the China
Scholarship Council
(CSC).
==== Refs
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==== Front
ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145808010.1021/acsomega.8b01942ArticleTailoring the Emission of Fluorinated Bipyridine-Chelated
Iridium Complexes Zhang Guang †§∥Baumgarten Martin *†Schollmeyer Dieter ‡Müllen Klaus *†† Max
Planck Institute for Polymer Research, Ackermannweg 10, Mainz D-55128, Germany‡ Institute
für Organische Chemie, Johannes-Gutenberg
Universität, Mainz D-55128, Germany§ Jiangsu
Key Laboratory for Carbon-Based Functional Materials & Devices,
Institute of Functional Nano & Soft Materials (FUNSOM), Joint
International Research Laboratory of Carbon-Based Functional Materials
and Devices, Soochow University, Suzhou 215123, China* E-mail: baumgart@mpip-mainz.mpg.de (M.B.).* E-mail: muellen@mpip-mainz.mpg.de (K.M.).22 10 2018 31 10 2018 3 10 13808 13816 08 08 2018 25 09 2018 Copyright © 2018 American Chemical
Society2018American Chemical
SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
New functionalized tris(2′,6′-difluoro-2,3′-bipyridinato-N,C4′)iridium(III) ((dfpypy)3Irs) complexes,
including small molecules and their dendrimer embedded analogoues,
were synthesized and characterized. It is demonstrated that both the fac-(dfpypy)3Ir-based polyphenylene dendrimers
and (triisopropylsilyl)ethynyl (TIPSE)-substituted (dfpypy)3Ir complexes induce large bathochromic shifts (∼50 nm) of
emission bands compared with fac-(dfpypy)3Ir. This is due to the pronounced 3π–π*
character of emissive excited states and the extended conjugation.
A further remarkable feature is the small bathochromic shift of the
emissions of fac-tris(2-phenylpyridine)iridium (fac-(ppy)3Ir)-based polyphenylene dendrimers
when compared to those of the iridium (Ir) complex core. Obviously,
the triplet metal-to-ligand charge transfer makes emission less sensitive
to extended conjugation than the 3π–π*
transition. This finding suggests new concepts for designing blue
phosphorescent dendrimer emitters. Both the dendrimers and the TIPSE-substituted
(dfpypy)3Ir complexes represent new green and the trimethylsilyl-functionalized
(dfpypy)3Ir new blue phosphorescent emitters. Incorporation
of TIPSE moieties into the ligands of iridium complex gives rise to
enhanced phosphorescence.
document-id-old-9ao8b01942document-id-new-14ao-2018-019422ccc-price
==== Body
Introduction
Phosphorescent emitters
(PEs) such as iridium (Ir) and platinum
(Pt) complexes have been intensively investigated since the first
report on PE-based organic light emitting diodes (OLED) by Baldo et
al. in 1998.1−5 PEs could provide much higher efficiencies than conventional organic
singlet fluorophores because the former generates both singlet and
triplet excitons in devices (corresponding to 100% internal quantum
efficiency and around 20% external quantum efficiency (EQE) theoretically).1−8 Significant improvements of red,9 green,10 blue,11−13 and white14 OLEDs based on small-molecule PEs have been achieved so
far and all have reached or passed 20% EQEs. PEs have also received
attention in applications such as photocatalysis,15−17 chemical sensors,18,19 solar cells,20,21 and biolabeling,22 due to their intriguing photophysical properties.
The neat films of PEs are prone to undergo severe self-quenching.23−27 Therefore, the emitters (also called dopants) are usually incorporated
into a matrix to ensure high photoluminescence quantum yields (PLQYs).
The matrix composed of host materials, e.g., 4,4′-bis(N-carbazolyl)-1,1′-biphenyl, serves as medium for
charge transport and energy transfer to the dopants.6,28−30 However, these devices based on small molecules still
suffer from expensive ultra high vacuum fabrication and inhomogeneous
distribution of the dopants in the matrix. Dendrimers can overcome
these problems because of their good film formation and generation-by-generation
site-specific functionalization.31−35 In a rigid and structurally well-defined dendritic
molecule, the core can be a phosphorescent emitter while the surface
is functionalized with host moieties. Thus, the ratio between the
hosts and dopants and their positions are accurately controlled in
a dendritic structure.32,33 There have been many studies
on dendrimer-based phosphorescent emitters, especially green and red
ones, since the pioneering work of Samuel and Burn et al. in 2001.35−43 So far, very few blue PEs were reported and they all suffered from
poor color purity and/or low efficiencies.44−48 Accordingly, it is worthwhile to develop high-performance,
dendrimer-based blue PEs.
Shape-persistent polyphenylene dendrimers
(PPDs) as emitters have
been widely studied.49−54 Core and surface-functionalized, first-generation PPDs were shown
to improve OLED performance through the shielding effect and appropriate
choice of surface moieties. The latter were thought to bring about
efficient surface-to-core energy transfer and charge transport.50,51 PPDs were also employed as phosphorescent green and red emitters.49,53 Interestingly, the peak emission of fac-(ppy)3Ir-based PPDs (G1–G4) (Figure 1) in solution was located at 516 nm, i.e.,
very close to that of fac-(ppy)3Ir (λem: ∼508 nm).55 It follows
that the attachment of polyphenylene dendrons on fac-(ppy)3Ir does not change the emission wavelength notably.
Figure 1 Molecular
structures of fac-(ppy)3Ir,
G1, fac-(dfpypy)3Ir, and the targeted
iridium complexes.
fac-Tris(2′,6′-difluoro-2,3′-bipyridinato-N,C4′)iridium(III) (fac-(dfpypy)3Ir) (Figure 1) was described as a pure blue PE (λmax: 438 and
463 nm) with high PLQY (∼0.71) and thermal stability (5% loss
at 452 °C from thermogravimetric analysis).56 We thus chose this chromophore as the core of a PPD, en
route to unprecedented blue phosphorescent dendrimer emitters. In
this contribution, as depicted in Figure 1, several (dfpypy)3Ir-based small
molecules and a first-generation PPD with carbazoles in the periphery
(1) are introduced, whereby carbazoles act as charge
transport and energy transfer moieties.
Results and Discussion
Synthesis
A trimethylsilyl (TMS)-substituted Ir complex 4 was
considered as the initial candidate because TMS groups
could be transformed into iodo substituents later.57 As depicted in Scheme 1, 2-bromo-5-trimethylsilylpyridine (8)
was synthesized from 2,5-dibromo-pyridine (10) and trimethylsilylchloride
(TMSCl) in high yield (82%). Then, compound 8 was reacted
with 2,6-difluoropyridinyl-3-boronic acid (9) obtained
from commercial 2,6-difluoropyridine (11) to furnish
the functionalized bipyridine ligand (7) by Suzuki coupling
in moderate yield (50%). Subsequently, the one-step reaction between
bipyridine 7 and iridium(III) acetylacetonate (Ir(acac)3) to the iridium complex (4 and 5) failed.56,58−60 A two-step
method was therefore applied by refluxing the bipyridine ligand 7 with IrCl3, providing a dichloro-bridged dimer
(6) as a yellow solid in moderate yield (48%). Then,
the dimer (6) and the ligand (7) were heated
under basic conditions,47 leading to a
yellow solid (5). Attempted substitution of the TMS group
with iodine remained unsuccessful.
Scheme 1 Synthetic Routes for TMS-Functionalized
(dfpypy)3Ir
(a) (1) n-BuLi,
Et2O, −78 °C, 1 h, (2) TMSCl, room temperature
(rt), 12 h, 82%; (b) (2,6-difluoro-3-pyridinyl)boronic acid 9, Pd(PPh3)4, K2CO3, tetrahydrofuran (THF), water, 85 °C, 24 h, 50%; (c) IrCl3·nH2O, 2-ethoxyethanol, 140
°C, 24 h, 48%; (d) compound 7, AgSO3CF3, K2CO3, mesitylene, 170 °C, 24
h, 53%; (e) UV light, THF, 12 h, 90%; (f) (1) isopropylamine, THF, n-BuLi, 0 °C, 30 min for making fresh lithiumdiisopropylamide
(LDA), (2) LDA, THF, −78 °C, 1 h, (3) triisopropylborate,
rt, 12 h, 1 M HCl (aq), 100%; (g) ICl, CCl4, 80 °C,
12 h; (h) Ir(acac)3, ethylene glycol, 200 °C.
Tri-cyclometalated iridium(III) complexes usually
exist in two
configurations, i.e., a facial and meridional, with C3 and C1 symmetry, respectively.60−62 The obtained
TMS-functionalized Ir complex 5 possesses meridional
configuration, as demonstrated by its 1H and 19F NMR spectra (Supporting Information).
The facial isomer 4 was easily obtained by stirring a
THF solution of 5 under UV light for 12 h in high yield
(90%) (Scheme 1e).60−62 For Ir complex 4, only 4 proton signals are present
in the low-field region of its 1H NMR spectra, corresponding
to the 4 protons of the bipyridine ligand; in addition, two peaks
in the 19F NMR spectra represent the two fluorine atoms
in one ligand, thus demonstrating a C3 symmetry of
complex 4. On the other hand, the number of corresponding
NMR signals for molecule 5 was tripled in comparison.
Single crystals of both complexes 4 and 5, suitable for X-ray diffraction, were obtained by slow addition
of methanol to a dichloromethane (DCM) solution. As shown in Table S2 and Figure 2, the facial configuration possesses nearly
identical Ir–N bonds (∼2.12 Å) and Ir–C
bonds (∼2.00Å), similar to those in fac-(dfpypy)3Ir56 and consistent
with its C3 symmetry. For the meridional one, however,
the Ir–N2 bond has a notably longer length (∼0.1 Å)
than that of others. This suggests that these bonds can break and
reorganize to form the facial isomer 4, which is in accord
with the successful meridional-to-facial transformation upon photochemical
treatment.60−62 Moreover, several short intermolecular contacts exist
for both materials (e.g., F···H–C, F···C,
C···C, N···H–C, and face-to-face
π···π interactions) (Supporting Information), similar to those in fac-(dfpypy)3Ir.56
Figure 2 Crystal structure views
of Ir complexes 4 and 5 with ellipsoids
at 50% probability (proton atoms were hidden
for clarity).
With the successful synthesis
of the TMS-substituted Ir complexes,
the preparation of (dfpypy)3Ir-based PPDs became possible.
In view of the Diels–Alder reaction with carbazole-functionalized
tetraphenylcyclopentadienone (21), ethynyl units had
to be introduced (Scheme 2), yielding TIPSE-functionalized ligands (14 and 15). The first step involved generating the bromo-functionalized
bipyridines (16 and 17) from 2,6-difluoro-pyridine-5-boronic
acid (9) and 2-iodo-4-bromopyridine (19)
or 2-iodo-5-bromopyridine (18) by Suzuki coupling in
which the iodo reacted much faster than the bromo groups. Then, (triisoprypylsilyl)acetylene
was allowed to react with compounds 16 and 17 by Sonogashira coupling to afford the TIPSE-functionalized bipyridine
ligands 14 or 15 in high yields (85 and
96%).
Scheme 2 Synthetic Routes for TIPSE-Functionalized Ir Complexes
(a) Pd(PPh3)4, K2CO3, THF, water, 80 °C, 24 h, 39%
for 16, 34% for 17; (b) Pd(PPh3)2Cl2, PPh3, CuI, triethylamine,
(triisopropylsilyl)acetylene, 80 °C, 24 h, 85% for 14 and 96% for 15; (c) IrCl3·nH2O, 2-ethoxylethanol, 140 °C, 24 h, 57% for 12, 24% for 13; (d) TIPSE-substituted bipyridine 14 or 15, K2CO3, AgSO3CF3, 1,3,5-trimethylbenzene, 170 °C, 24 h,
25% for 2, 20% for 3.
For iridium complex formation, the functionalized bipyridines 14 or 15 were treated with IrCl3·nH2O to furnish the dichloro-bridged dimers 12 and 13 in moderate yields (57 and 24%) (Scheme 2). Thereafter, TIPSE-functionalized
Ir complexes 2 and 3 were obtained by a
reaction between the dimer and TIPSE-substituted bipyridine 14 or 15 under basic conditions. The low yields
(25 and 20%) are similar to those commonly reported for Ir complexes.47 The collected iridium complexes 2 and 3 were in meridional configurations, as confirmed
by 1H and 19F NMR measurements (Supporting Information).
Compound 2 could not be transformed into its facial
isomer by photochemical treatment, probably due to decomposition upon
prolonged UV light irradiation. Finally, dendrimers 20 and 1 were obtained starting from the TIPSE-substituted
molecule 2. As depicted in Scheme 3, first, the TIPS fragments were removed
by treatment with tetrabutylammonium fluoride (TBAF).12 With the ethynyl-substituted Ir complex 22 available, dendrimer 20 was obtained by a Diels–Alder
reaction between 22 and molecule 21 in moderate
yield (55%). The resulting product is meridional, as confirmed by
the 1H NMR and 19F NMR spectra (Supporting Information). As the facial isomer
usually displays a higher PLQY than that of the meridional one,60,63 the former was successfully prepared by photolysis in 83% yield.
The facial dendrimer 1 was comprehensively characterized
by 1H and 19F NMR spectroscopy, matrix-assisted
laser desorption ionization time-of-flight (MALDI-TOF) mass, and high-resolution
mass spectrometry (HRMS).
Scheme 3 Synthetic Routes for Iridium Complex-Based
Dendrimers
(a) TBAF, THF, rt, 46%; (b) o-xylene, 150 °C, 48 h, 55%; (c) UV light, THF, 12
h, rt, 83%.
In the 1H NMR spectra
of dendrimer 1 (Figure 3) proton Ha ortho to the fluorine atom appears
as a singlet peak at around 5.90
ppm. Protons Hb and Hc occur at 8.13 and 7.52
ppm, respectively. The carbazole protons at 4,5-positions (Hf) are found at 8.05 ppm, and the tert-butyl group
protons at 1.33 ppm are clearly assigned. Moreover, there are only
two peaks present in the 19F NMR spectra, corresponding
to the two fluorine atoms in one ligand of the molecule.
Figure 3 1H NMR and 19F NMR (inset) spectra of dendrimer 1 (solvent: CD2Cl2).
The MALDI-TOF mass spectra of dendrimer 1 exhibits
a single peak of the molecular ion, in good agreement with the molecular
mass of the dendrimer (Figure S3). The
HRMS spectra show clear isotope patterns of the molecular ion, which
is consistent with the calculated result (Figure S3).
Photophysical Characterization
As
depicted in Figure 4a, both TMS-substituted
Ir complexes 4 and 5 exhibit strong absorptions
between 250 and 300 nm due to the ligand-based π–π*
transitions.56 The relatively weak bands
between 350–400 nm are attributed to the singlet metal-to-ligand
charge transfer (1MLCT).56,60 In addition,
as shown in the inset of Figure 4a, a shoulder between 400 and 450 nm is tentatively
assigned to a mixture of spin–orbital coupling-enhanced ligand
(L)-centered 3π–π* (3LC)
and triplet MLCT (3MLCT) transitions, which is based on
a comparison with fac-(dfpypy)3Ir.56 This is consistent with the two absorption bands
of molecule 4, in which one centered at 412 nm is presumably
ascribed to 3LC and the other (λmax: 438
nm) to 3MLCT according to the proposed orbital diagram
of the Ir complexes (Figure 6, top left). The facial one appears as a stronger and
deeper blue emitter than the meridional one (Figure 4b), which is similar to the situation prevailing
in other reported Ir complexes,60,63 such as fac-(ppy)3Ir and mer-(ppy)3Ir.60 Both emission spectra are structured, resembling fac-(dfpypy)3Ir.56 The small bathochromic shift of the emission of compound 4 against that of fac-(dfpypy)3Ir56 is due to the electron-donating effect of the
TMS groups (Table 1). In line with that, the emission is essentially attributed to ligand-based 3π–π* transitions rather than 3MLCT because electron-donating moieties lead to a blue-shifted emission
for a 3MLCT-type phosphorescence.64 As indicated in Figure 6, TMS-substituted bipyridine (7) has a higher
highest occupied molecular orbital (HOMO) but about the same lowest
unoccupied molecular orbital (LUMO) level compared to those of difluoro-substituted
bipyridine 26. With the new orbital formation between
Ir and ligand, it shows that the transition energy of MLCT and LC
of material 4 increases and decreases respectively, compared
with those of fac-(dfpypy)3Ir and consequently
causes blue- and red-shifted emissions individually. This is consistent
with the conclusion from Lee et al., that the emission of fac-(dfpypy)3Ir is mainly attributed to a 3LC nature of the emissive excited states, even though their
calculated results support 3MLCT.56
Figure 4 UV–vis
absorption (a) and photoluminescence spectra (b)
of compound 4 and 5 in 10–4 M DCM solution (excited at 330 nm).
Figure 5 UV–vis absorption (a) and emission spectra (b) of compounds 3, 2, 20, and 1 (10–5 M in DCM, ex: 385 nm for 3 and 2 and 348 nm for 20 and 1, measured
at room temperature).
Figure 6 Molecular orbital distributions and energy levels of Frontier molecular
orbitals (FMOs) of the ligands (calculated using DFT, B3LYP, 6.31G
method).
Table 1 Photophysical and
Electrochemical
Properties of Ir Complexes
λab (nm) λem (nm)
Sol (rt) Sol (rt) Sol (77 K) ETb PLQYc HOMO (ev)d LUMO (ev)d Ega
fac-(dfpypy)3Ir 375e 438, 463e 0.71e
5 259, 370, 436, 441 448, 475 446, 475 2.78 –6.03 –2.60 3.43
4 262, 334, 370, 411, 438 444, 472 440, 469 2.82 0.58 –6.01 –2.57 3.44
3 270, 329, 376 508 479, 509 2.59 0.73
2 289, 349, 383 489, 525 486, 521 2.55 0.30 –5.68 –2.83 2.85
1 297, 334, 348 515 486, 517 2.55 0.31 –5.55 –2.11
a Calculated
from the energy difference
between HOMO and LUMO.
b Calculated
from the highest energy
peak of emission spectra (77 K) (Figure S5), which is 1240/λem.
c Measured in toluene solution with
quinine sulfate in 0.5 M H2SO4 solution as the
standard.
d Calculated from
cyclic voltammetry
(CV) by comparing the first redox onset of the compounds and the oxidation
onset of ferrocene.
e Obtained
from ref (56).
For the absorption of Ir complexes 2 and 3 (Figure 5), the first
two bands between 270 and 350 nm are due to the π–π*
transitions of the ligands. The weaker one (370–400 nm) is
likely attributed to the 1MLCTs.56,60 The little shoulders above 400 nm are assigned to a mixed state
of spin–orbital coupling-enhanced 3π–π*
and 3MLCT, referring to fac-(dfpypy)3Ir.56 Both are green emitters with
pronounced bathochromic shifts (∼45 nm for compound 3) in contrast to fac-(dfpypy)3Ir (Figure 5b), which should
relate to the extended conjugations. This also suggests that the emissive
excited states exhibit dominant 3π–π*
rather than 3MLCT nature because the former induces bigger
bathochromic shift than the latter when the conjugation is extended.
As shown in Figure 6, for Ir complex 2, due to the
smaller energy gap of ligand 14 than that of difluoro-substituted
bipyridine (26), the reduction of transition energy is
considerable for LL but is much less notable for MLCT, compared to
that for fac-(dfpypy)3Ir. This is consistent
with the 3LC nature of the emissive excited states of materials 4 and 5.
Additionally, both the bathochromically
shifted absorption and
emission of Ir complex 2 compared with molecule 3 is ascribed to the bigger band gap of 4-TIPSE-substituted
bipyridine 15 than that of ligand 14, which
indicates that conjugation at 5 position is more effective (Figure 6). Moreover, Ir complex 3 appears as a stronger emitter than phosphore 2 (Figure 5b), owing
to very high extinction coefficient between 400 and 500 nm (ε
≤ 6000 M/cm) of lumiphore 3, which corresponds
to 3LC and 3MLCT transitions. This is comparable
to that of highly emissive fac-(ppy)3Ir
(ε ≤ 6000 M/cm) in the same region.65 This is also consistent with the higher PLQY of Ir complex 3 than that of 2 (Table 1). The Ir complex 3 is a rare
case of a strongly emitting cyclometalated Ir complex with alkynyl
groups in the ligand.49,53
As to the absorption of
dendrimers, a strong band at around 297
nm is characteristic for carbazole absorptions.66 The band between 320 and 350 nm and the one ranging from
370 to 400 nm are due to electronic transitions of the ligands50 and 1MLCTs, respectively. The less
notable shoulders (400–450 nm) stem from a mixed state of spin–orbit
coupling-enhanced 3π–π* and 3MLCT.56 Both dendrimers are green emitters
(Table 1), similar
to materials 2 and 3. Consequently, dendrimer 1 exhibits a bathochromically shifted emission of 50 nm compared
to that of fac-(dfpypy)3Ir. This strong
shift is correlated to 3π–π* rather
than 3MLCT, similar to complex 2. This feature
is quite different from fac-(ppy)3Ir-based
PPDs bearing very small redshifts (∼8 nm) in emissions as compared
with parent fac-(ppy)3Ir.53 Lo et al. argued that this is due to the lack of conjugation
between dendron and ligand.67 We rather
propose that this is due to the dominant 3MLCT nature of
emissions of fac-(ppy)3Ir-based PPDs (Figure S6).
As shown in Figure 6, for molecule 25, polyphenylene dendrons indeed significantly
decrease the band gap of the ligand compared with bipyridine 26 (4.25 vs 5.05 eV calculated). The close band gaps between
TIPSE-substituted bipyridine 14 and ligand 25 and the similar emission colors of Ir complexes 2 and 1 further manifest that their luminescence has primary 3LC nature. The facial dendrimer displays slightly stronger
emission than that of the meridional one, similar to other Ir complexes,
e.g., materials 5 and 4, but the emission
intensity of both are much lower than that of compound 3. This is consistent with the much weaker absorptions of 3LC and 3MLCT of the dendrimers than those of compound 3. Extending the conjugation of the ligand is an effective
way to tune the color of emission of metal–organic complexes,68 which has been reported for dendrimer-based
blue PEs as well.44
Electrochemistry
The redox properties of some of the
prepared Ir complexes were studied by cyclic voltammetry (CV). Compound 4 and 5 exhibit two oxidation processes, starting
above 1.5 V (Figure S7), which indicates
their relatively low HOMOs (∼−6.00 eV) (Table 1), similar to that in fac-(dfpypy)3Ir.56 Both of them present three reversible reduction couples (LUMO: ∼−2.60
eV). Going to Ir complex 2, due to the extended conjugations,
the HOMO (−5.68 eV) is raised and the LUMO (−2.83 eV)
is decreased compared with molecules 4 and 5. As to dendrimer 1, the HOMO and LUMO were calculated
to be −5.55 and −2.11 eV, respectively. This is consistent
with the FMOs of the peripheral carbazoles,66 probably owing to the big ratio between the number of carbazole
groups and Ir complex segment within one molecule (6:1).
Conclusions
We find that the TMS-functionalized and TIPSE-substituted (dfpypy)3Irs and (dfpypy)3Ir-based polyphenylene dendrimers
exhibit bathochromically shifted emissions, when compared with parent fac-(dfpypy)3Irs due to the dominant 3LC nature of their emissive excited states. This demonstrates that
strong red-shifted emission occurs when both extended conjugations
and significant 3LC character are involved in a phosphore.
It is also found that when both extended conjugations and primary 3MLCT nature are present in an Ir complex, the bathochromic
shift is less notable or much weaker, as seen, for example, in fac-(ppy)3Ir-based polyphenylene dendrimers.
Therefore, this work provides useful insights into the design of new
blue phosphorescent dendrimer emitters besides the most commonly utilized
method of breaking the conjugation between the PE core and the dendron
with alkyl segments.45 Appropriate steps
are: (i) to select the core of a dendrimer with a blue PE with dominant 3MLCT nature of its emissive excited state or (ii) to utilize
a UV PE with major 3LC nature of its emissive excited states
as the core of the dendrimer to push the emission of the dendrimer
into pure blue region by extended conjugations.
Experimental Section
Materials
and Methods
All chemicals and solvents were
purchased from commercial sources and used as received except where
noted. Reactions were all conducted under argon atmosphere. 1H NMR and 13C NMR spectra were recorded on Bruker AMX
250, AC 300, and AMX 500 NMR spectrometers. The solvents for NMRs
were CD2Cl2 with the reference peak at 5.32
ppm (1H) and 53.84 ppm (13C) and DMSO-d6 with the reference peak at 2.50 ppm (1H). Field desorption mass spectra were recorded on a VG-Instruments
ZAB 2-SE-FDP using 8 kV accelerating voltage. MALDI-TOF mass spectra
were recorded by a Bruker Reflex II spectrometer with fullerene as
the reference and dithranol as the matrix. HR-MALDI-TOF mass spectra
were recorded by a SYNAPT G2-Si time-of-flight instrument equipped
with a MALDI source (Waters Corp. Manchester, U.K.). UV–vis
absorption spectra were measured by a Varian Cary 4000 UV–vis
spectrometer (Varian Inc. Palo Alto) using quartz cells with path
length of 1 cm. Fluorescence spectra were recorded with a SPEX Fluorolog
2 spectrometer. Cyclic voltammetry (CV) measurements were conducted
on a computer-controlled GSTAT12 workstation using a three-electrode
system in which a Pt wire, a silver wire (or a saturated calomel electrode),
and a glassy carbon electrode were used as counter, reference, and
working electrode, respectively. The measurements were conducted in
0.1 M tetrabutylammonium hexafluorophosphate (TBAPF6) solution
under argon environment with a scan rate of 100 mV/s at room temperature.
The solvents were DCM for the oxidation part and acetonitrile for
the reduction part. Ferrocene/ferrocenium (Fc/Fc+) worked
as the internal reference throughout the measurements. The calculations
of HOMO and LUMO using CV were based on the following equations, HOMO
(eV) = −Eoxonset + EFconset – 4.80 and LUMO (eV)
= −Eredonset + EFconset – 4.80, where Eoxonset, EFc/Fc+onset, and Eredonset mean the onset oxidation potential of
the targeted molecule, the onset oxidation potential of ferrocene,
and the onset reduction potential of the targeted molecule compared
with the reference electrode. The calculated isotope distributions
of the molecular mass of the dendrimer were conducted with mMass software.
The X-ray intensity data for 4 was measured on a STOE
IPDS-2T X-ray diffractometer system equipped with a Mo-target X-ray
tube. The data frames were collected using the program X-Area and
processed using the program Integrate routine within X-Area. The reflection
intensities were corrected for absorption on the basis of the crystal
faces using XRED-32. The X-ray intensity data for 5 was
measured on a Bruker SMART APEX2 CCD-based X-ray diffractometer system
equipped with a Mo-target X-ray tube. The data frames were collected
using the program APEX2 and processed using the program SAINT routine
within APEX2. The data were corrected for absorption on the basis
of the multiscan technique, as implemented in SADABS. Structure solution
and refinement were performed using SHELT-2014. Crystal of compound 4 contains one molecule of CH2Cl2.
The density functional theory calculations for ground-state geometry
optimizations were performed using PC controlled Gaussian software.
Supporting Information Available
The
Supporting Information
is available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b01942.Synthetic procedures
and characterization data of the
targeted molecules: 1H NMR, 13C NMR, X-ray single-crystal
diffraction, low-temperature photoluminescence, and cyclic voltammetry
(PDF)
Crystallographic
data (CIF)
Supplementary Material
ao8b01942_si_001.cif
ao8b01942_si_002.pdf
Author Present Address
∥ Institute of Functional Nano & Soft Materials, Soochow University,
Suzhou, 215123, China (G.Z.).
The authors
declare no competing financial interest.
Acknowledgments
The authors
gratefully thank the Deutsche Forschungsgemeinschaft
(SFB625) for providing financial support for this research. The authors
also gratefully thank Dr Wen Zhang for MALDI-TOF mass characterizations.
G.Z. also thanks the financial support from Collaborative Innovation
Center of Suzhou Nano Science & Technology, the Priority Academic
Program Development of Jiangsu Higher Education Institutions (PAPD),
and the 111 Project.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145880710.1021/acsomega.8b00574ArticlePorous Organic Polymer-Derived Carbon Composite as
a Bimodal Catalyst for Oxygen Evolution Reaction and Nitrophenol Reduction Gopi Sivalingam †Giribabu Krishnan ‡Kathiresan Murugavel *††Electro
Organic Division and ‡Electrodics and Electrocatalysis Division, CSIR-Central Electrochemical Research Institute, Karaikudi 630003, TamilNadu, India* E-mail: kathiresan@cecri.res.in. Tel: 04565-241312.11 06 2018 30 06 2018 3 6 6251 6258 26 03 2018 31 05 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
Ethylene
diamine-based porous organic polymer (EPOP) was synthesized,
carbonized at different temperatures, and characterized. The successful
formation of the triazine polymer was confirmed by Fourier-transform
infrared spectroscopy, 13C, and 15N cross-polarization
magic angle spinning solid-state NMR. The two-dimensional layered
architecture and graphitic nature of the samples resembled that of
nitrogen-doped amorphous carbon, as confirmed by Raman, powder X-ray
diffraction, and transmission electron microscopy measurements. The
catalytic activity of these materials toward nitrophenol reduction
and electrocatalytic activity toward oxygen evolution reaction (OER)
were systematically evaluated in detail. Electrocatalytic activity
toward oxygen evolution reaction was systematically evaluated by chronoamperometry
and linear sweep voltammetry. Results clearly demonstrate that all
of these catalysts exhibit good OER activity and excellent stability.
Among all catalysts, EPOP-700 showed better OER activity, as reflected
by its onset potential and current density, comparable with that of
the metal-based OER catalysts and better than that of metal-free catalysts.
Further, their catalytic activity toward the reduction of 4-nitrophenol
to 4-aminophenol was tested with NaBH4; although all of
these catalysts showed good catalytic activity; EPOP-800 displayed
better catalytic activity.
document-id-old-9ao8b00574document-id-new-14ao-2018-005743ccc-price
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Introduction
Porous
organic polymers (POPs), a subclass of organic polymers/organic
materials, show great advantage over conventional polymers in the
area of catalysis due to their high surface area.1,2 They
are highly cross-linked and are amorphous in nature.1,3 Proper tuning of the porosity in these materials can be achieved
with desired functional groups or linking units. It is anticipated
that porous organic polymers with high nitrogen content are desirable
for catalytic applications.4 It is also
advantageous that the “N” atom can coordinate to metal
atoms;5 hence, their surface can be modified
with desired metals to further improve their catalytic properties.6 Among the porous organic polymers, covalent triazine
frameworks constitute an important class because of their high nitrogen
content, high surface area, high thermal and chemical stability, easy
preparation on a large scale, and use in catalytic applications.6−9 Thomas and co-workers developed a novel ionothermal process for
the synthesis of covalent triazine frameworks from aromatic nitriles
using ZnCl2 at elevated temperatures (≥400 °C)
in molten state.10 Such a high-temperature
procedure usually yields highly porous framework due to the partial
decomposition of organic moiety, although it was reported that nitrile
trimers are stable up to 400 °C.6,10,11 POPs can also be synthesized from melamine3 and cyanuric chloride (C-Cl) under mild conditions;8,12,13 however, POPs prepared under
mild conditions exhibit very low surface area.14,15 It is further shown that these syntheses are solvent dependent.
The condensation reaction in dimethylacetamide and N-methyl pyrrolidine yielded 4 times high surface area material than
the one obtained using dioxane as a solvent, indicating the impact
of solvent on porosity in such reactions. Fifteen POPs are electron
rich and they exhibit good π-electron mobility along the triazine
ring and if conjugated with an aromatic linker, they exhibit good
electronic conductivity, which enhances their chemical, electrochemical,
and photocatalytic activity.16 Altogether,
POPs find application in energy storage devices, gas storage/separation,
photocatalysis, etc. wherein the triazine nitrogen is shown to play
a dominant role.16−21 Recent applications of POPs focus on the heteroatom doping, multilayer
assembling, and metal cocatalysts aimed toward further enhancement
of their catalytic properties.22−25
Oxygen evolution reaction (OER) is one of the
most promising sustainable
systems to generate clean and effective energy. OER is a complex multistep
reaction as it involves several surface-adsorbed intermediates, and
this reaction usually requires large overpotential for the actual
process, which distinctly reduces the process efficiency even if the
benchmark catalysts are applied.26 Numerous
electrocatalysts have been developed till date to improve the efficiency
of oxygen evolution.27 Ru- and Ir-based
noble metal catalysts were frequently employed as benchmark catalysts
due to their efficiency in oxygen evolution reaction. Further, nanoscale
catalysts with reduced noble metal content and high surface area were
developed to reduce the cost. Later, metal nanocatalysts on carbon
matrices were developed. In this scenario, metal-free catalysts have
attracted wide attention owing to their analogous performance with
noble metal catalysts. Frequently studied metal-free catalysts include
graphene-based materials, carbon nanotubes (CNTs), and so on, which
are usually expensive. Metal-free catalysts were also developed from
inexpensive carbon-based materials by high-temperature treatment under
inert conditions.
On the other hand, 4-nitrophenol (4-NP) is
an important organic
pollutant obtained from agricultural and industrial sources.28 Metal-catalyzed reduction of 4-NP with excess
NaBH4 yields 4-aminophenol (4-AP), a key intermediate in
the production of paracetamol and dyeing industry. Hence, development
of an efficient catalyst for the reduction of 4-NP to 4-AP will be
of broad interest owing to its industrial value. In general, metal
or metal-based nanocatalysts were employed for the catalytic reduction
of 4-NP to 4-AP with excess NaBH4. Till date, very few
metal-free catalysts based on graphene materials are known for the
reduction of 4-NP to 4-AP, which are usually expensive.28,29 In this context, development of a catalyst with dual performance
in OER and nitrophenol reduction would be interesting, provided they
display excellent catalytic activities in both the reactions, as they
follow a different pathway.
Recently, we reported on the synthesis
of phenylenediamine-based
POP network and its electrocatalytic activity toward the nitrobenzene
reduction and oxygen evolution reaction (OER).14 Further, the carbonized sample was tested for its energy
storage performance.30 There are very few
reports available on OER and nitrophenol reduction using metal-free
catalysts derived from POPs.
Herein, we report the synthesis,
carbonization, and characterization
of ethylene diamine-based porous organic polymer (EPOP) and their
catalytic activity toward oxygen evolution reaction and nitrophenol
reduction.
Results and Discussion
The reported procedure was followed
to obtain EPOP (Scheme 1).14 EPOP-600, EPOP-700, and EPOP-800
were obtained by the carbonization
of EPOP sample at 600, 700, and 800 °C under inert atmosphere
(3 h) in a tubular furnace, respectively.
Scheme 1 Synthesis of EPOP
and Its Carbon Composites
The successful formation of the porous organic polymer
is confirmed
by Fourier-transform infrared spectroscopy (FT-IR) analysis. The absence
of cyanuric chloride (C-Cl) stretching vibration at 850 cm–1 and a broad peak at 3400 cm–1 corresponding to
“NH2” of ethylene diamine confirms the absence
of both the starting materials (Figure S1). Apart from this, key peaks such as the stretching frequencies
of triazine rings were observed at 1347 and 1571 cm–1, bending and stretching vibration of sp3 “CH2” moiety were observed at 1447 and 2940 cm–1 respectively. The peak at 804 cm–1 corresponds
to the breathing mode of vibration of triazine unit (Figure S2). All of these characteristic peaks indicate the
successful formation of triazine polymer, which is further confirmed
by solid-state 13C and 15N cross-polarization
magic angle spinning (CP-MAS) spectroscopy. The FT-IR of the carbonized
sample (EPOP-800) showed key features of the triazine ring to some
extent; however, the characteristic peaks corresponding to CH2 group were absent and the pattern looked very similar to
that of the nitrogen-doped graphene.31
The successful formation and the nature of the formed porous organic
polymers can be confirmed by cross-polarization magic angle spinning
(CP-MAS) solid-state 13C and 15N NMR spectroscopy. 13C CP-MAS measurement of EPOP sample (Figure S3a) confirmed the coexistence of triazine and ethylene
diamine moieties in the polymer; the aromatic sp2 carbon
of triazine was observed at δ 166 ppm, and the aliphatic sp3 carbon of ethylene diamine was observed at δ 41 ppm,
indicating that these two individual moieties are covalently linked
during the synthesis [starting materials are soluble in organic solvents;
upon completion of the reaction, the product EPOP was washed several
times with organic solvents to remove unreacted starting materials].
Similarly, 15N CP-MAS measurement of EPOP sample (Figure S3b) showed two broad peaks at δ
−172 and −90 ppm, corresponding to the triazine N and
linker ethylene diamine N, respectively. This confirms the presence
of two different N (triazine N and ethylene diamine N) atoms in the
sample.
Raman spectroscopy is an important tool that specifies
the defects
and disorderly nature of carbon materials. Figure 1 shows the Raman spectra of carbon composites
of EPOP, and the Raman spectra of EPOP is given in Figure S4a. It is clear that after carbonization at different
temperatures, we observe only two peaks at 1330 (D-band) and 1600
cm–1 (G-band). This clearly proves that EPOP has
undergone chemical and structural changes. The observed peaks lie
in the D- and G-band region; usually, D-band arises due to the disorders
and imperfection present in the carbon lattice. G-band is assigned
to one of the two E2g modes corresponding to stretching
vibrations in the basal-plane (sp2 domains) of carbon lattice.
The D- and G-band peaks were observed at 1346, 1358, and 1342 cm–1 and 1542, 1550, and 1567 cm–1,
EPOP-600, 700, 800 respectively. The G peaks of all samples shift
to higher frequencies as the pyrolyzing temperature increased. The
quantitative amount of blueshift for EPOP-700 and EPOP-800 is 8 and
25 cm–1, respectively, when compared to that of
EPOP-600. It is obvious that the shift in Raman peaks may be attributed
to the effect of doping and strain. Usually, the doping of nitrogen
in carbon-based materials, such as graphene and CNTs, the blueshift
of G peak is apparent, which we observed in our case. Typically, it
is known that the compressive/tensile strain in carbon materials (graphene
and CNTs) may induce a blue/redshift of Raman peaks. Doping of nitrogen
atoms in carbon lattice may lead to the defect pinning and distortion
of lattice. The doping may be associated with bond formation and this
produces deformation and stress fields. The formation of pyrrolic
nitrogen by doping of nitrogen will have a C–N bond length
of 1.37 Å, which shortens compared to that of C–C bond
(1.42 Å). The extent of structural disorder present in the carbonized
POP can be considered from the ID/IG ratio.32 The ID/IG ratios of all
three carbonized samples were found to be 1.47 (EPOP-600), 1.41 (EPOP-700),
and 0.87 (EPOP-800). The increase in ID/IG ratio indicates more structural disorder;
if the value is high, it indicates a low degree of graphitization.
The order of graphitization for all three carbonized samples can be
given as EPOP-800 > EPOP-700 > EPOP-600.
Figure 1 Raman spectrum of carbon
composites of EPOP.
Figure 2a–d
shows the powder X-ray diffraction (PXRD) pattern of EPOP and its
carbon composites. All samples displayed a broad peak, and hence deduction
of any structural information of the POP becomes feeble. EPOP showed
a broad peak around the 2θ value of 23.7°, ascribed to
the graphitic carbon like structure, with a d-spacing
of 3.72 Å,32 whereas EPOP-600 and
EPOP-800 showed a broad peak with a spacing of 3.68 and 3.59 Å,
respectively, suggesting the presence of graphitic structure.32,33 EPOP-700 showed a broad peak around the 2θ value of 26.1°
close to that of graphitic carbon with d-spacing
of 3.47 Å.33 From the PXRD, we infer
that all samples were found to resemble graphitic carbon. The reason
for the resemblance to graphitic carbon could be attributed to the
carbonization process; a similar kind of observation was made for
room-temperature analogues.6 Further, these
results were supported by Transmission electron microscopy (TEM) analysis.
Figure 2 XRD profile
of (a) EPOP, (b) EPOP-600, (c) EPOP-700, and (d) EPOP-800.
TEM image of the EPOP showed stacked sheetlike
network, whereas
the high-resolution transmission electron microscopy (HR-TEM) images
of the carbonized samples EPOP-600 and EPOP-700 showed exfoliated
sheetlike structure. EPOP-800 displayed carbon sheetlike morphology,
which was crumpled to spherelike morphology on the topographical view34 (Figure 3). Selected area electron diffraction patterns of all of
these samples showed amorphous nature of the material (Figures S5–S8). These results are highly
consistent with XRD analyses.
Figure 3 (a) TEM image of EPOP, HR-TEM images of (b)
EPOP-600, (c) EPOP-700,
and (d) EPOP-800.
Field emission scanning
electron microscopy (FE-SEM) images of
EPOP and the carbonized samples were shown in Figures S9–S12. EPOP sample exhibited irregularly agglomerated
particle-like morphology. In the case of carbonized samples, change
in morphology was observed. As the carbonization temperature increased
from 600 to 800 °C, the morphology changed from irregularly agglomerated
network to highly agglomerated network, which could be attributed
to the high pyrolysis temperature.4
The oxygen evolution activities of the prepared carbon sample (EPOP,
EPOP-600, EPOP-700, and EPOP-800) were studied in 1 M KOH using linear
sweep voltammetry (LSV). The prepared samples were coated on carbon
paper and used as working electrode. Figure 4 shows the polarization curves of the prepared
carbon sample. Among these samples, EPOP-700 showed an onset potential
of 1.527 V, which is lower than that of the other carbon samples (EPOP:
1.673 V, EPOP-600: 1.70 V, EPOP-800: 1.65 V). EPOP-700 sample exhibited
overpotential of 297 mV to attain a current density of 10 mA/cm2; however, other carbon samples showed relatively high overpotential,
as shown in Table 1. Also, at high current density of 300 mA/cm2, the EPOP-700
sample showed a low overpotential of 580 mV, whereas other samples
exhibited high overpotential. The obtained results with high current
density are found to be better than the metal-based OER catalysts.35 The influence of pH on the OER activity has
been studied for EPOP-700 sample (Figure S21). Among the four catalysts used in this study, EPOP-700 showed high
electrocatalytic activity, which could be ascribed to the presence
of nitrogen atoms present on the surface/edges of the sample. It is
evident from the elemental
analysis that the N content in the sample EPOP-700 has relatively
high nitrogen content than other samples as a result of high nitrogen
atom doping during carbonization process (Supporting Information (SI), Table 1). From N %, it may
possibly be concluded that 700 °C is the ideal temperature to
attain high nitrogen doping with respect to EPOP samples. The presence
of nitrogen atoms on the surface impacts the polarity and hydrophilicity
of the sample, which is known to improve mass transfer properties
at the electrode–electrolyte interface. The OER kinetics of
the samples EPOP, EPOP-600, EPOP-700, and EPOP-800 were examined using
a Tafel plot. From figure 4b, it is apparent that favorable reaction kinetics and a small
Tafel slope of 76 mV/dec was found for EPOP-700 among all studied
catalysts (SI, Table 2). The Tafel slope
value implies that a lower electrochemical polarization occurred at
the interface. The enhanced OER activity of EPOP-700 sample can be
explained on the basis of N % (SI, Table 1). A high N % of 16.87 was obtained for EPOP-700 in comparison to
other samples. The morphology analysis of EPOP-700 reveals the high
stability of the carbon after prolonged OER for 10 h (Figure S19). EPOP-700 sample displayed better
electrocatalytic performance among the studied catalysts (EPOP, EPOP-600,
and EPOP-800), and this improved performance might be related to the
increased electron transfer at the electrode interface accompanied
by high ionic conductivity. To elucidate this, electrochemical impedance
spectroscopy (EIS) measurements for all four catalysts were carried
out (Figure S17). Nyquist plots obtained
from the EIS measurement showed a lower resistance of 90 Ω for
EPOP-700 compared to that of other catalysts (EPOP = 293 Ω,
EPOP-600 = 238 Ω, EPOP-800 = 102 Ω). This lower charge-transfer
resistance arises from the efficient interfacial contact of porous
carbon network with electrolyte. EPOP-700 catalyst holds a smaller Rct, which facilitates the faster charge-transfer
rate and hence better OER performance. Also, we anticipate that such
OER performance might be concomitantly related to the intrinsic activity
of the catalyst, high electrochemical surface area (ECSA), and efficient
charge-transfer kinetics prevailing at the electrode surface. The
mechanistic aspect of the EPOP-700 can be explained as follows: the
nitrogen atom present in the network of EPOP-700 might be negatively
charged because of the electron withdrawing nature, and hence the
adjacent carbon atoms might become positively charged (Figure S20). The positively charged carbon adsorbs
OH– from the electrolyte, which leads to the accumulation
of OH– on the surface of the catalyst, and this
may have positive influence on the catalytic reaction. For the rate-determining
step of OER, the adjacent positively charged carbon atoms should undergo
facile recombination of the two adsorbed species. The electron density
localized on the nitrogen atoms in the carbon network may reside near
the Fermi level, and so they can participate in the electrocatalytic
reaction.36
Figure 4 Electrochemical performance
of EPOP and its carbon composites toward
OER. (a) LSV; (b) Tafel plots in 0.1 M KOH solution at 2 mV/s.
Table 1 Electrochemical Data
of the Catalysts
s. no catalyst onset (V) current density (mA) Tafel slope (mV/dec) overpotential (mV) active
surface area ECSA (cm–2)
1 EPOP 1.673 53 169 440 0.0568
2 EPOP-600 1.70 22 177 470 0.0016
3 EPOP-700 1.527 322 76 297 0.233
4 EPOP-800 1.65 37 106 420 0.0598
To evaluate the catalytic performance of EPOP and
its carbon composites
toward the reduction of nitro group to amino group, the catalytic
reduction of 4-NP was carried out in excess NaBH4 in aqueous
medium. The decrease and increase in absorption intensity of 4-NP
or 4-AP is measured in the presence of different catalysts as a function
of time, as shown in Figure 5a–d. As the time increases, absorbance at 400 nm corresponding
to 4-nitrophenolate anion decreases and the absorbance at 298 nm corresponding
to 4-aminophenolate anion increases, indicating the catalytic activity
of all four catalysts. An identical experiment was carried out with
excess NaBH4 without catalyst. It is remarkable that even
after a day, no change in intensity of 4-nitrophenolate peak was observed,
indicating that the catalyst is necessary for this conversion. The
difference in the degree of catalytic activity can be correlated with
the complete disappearance of the peak at 400 nm vs function of time.
Although all catalysts displayed good catalytic activity toward the
reduction of 4-NP to 4-AP, the time taken for the complete reduction
of 4-NP to 4-AP varied. It is evident that EPOP-800 sample took 35
min for the complete conversion of 4-NP to 4-AP, displaying the best
catalytic activity among all. The order of catalytic activity can
be derived as EPOP-800 > EPOP-700 > EPOP-600 > EPOP. From
these observations,
it can be concluded that the catalyst with a high degree of graphitization
showed better catalytic activity in 4-NP reduction, whereas the same
is not in the case of OER catalysis that follows a different mechanism.
The reaction followed pseudo first-order kinetics. The improved catalytic
performance of EPOP-800 can be ascribed to the facile adsorption of
4-NP on the catalyst’s surface. The concept of facile adsorption
of 4-NP on the carbon surface has been reported using density functional
theory calculation in the literature.37 The rate constant for 4-NP reduction of all catalysts was tabulated
(SI, Table 3), and the activity factors
for all catalysts were found to be 63.3, 90, 113, 150 min–1/g, respectively. The observed rate constant and activity factor
values are better than those of the reported nonmetallic catalysts.29,37
Figure 5 UV–vis
absorption spectra for the catalytic reduction of
4-nitrophenol by NaBH4 over (a) EPOP, (b) EPOP-600, (c)
EPOP-700, and (d) EPOP-800.
Conclusions
In conclusion, porous organic polymers based
on ethylene diamine
and triazine were successfully synthesized, carbonized at different
temperatures, and characterized. The as-synthesized materials were
studied for the catalytic activity toward OER and nitrophenol reduction.
Among the catalysts employed in this study, EPOP-700 sample displayed
excellent OER activity with an overpotential of 580 mV at a current
density of 300 mA/cm2, with a prolonged stability over
10 h. These results were further complimented by Tafel slope and EIS
measurements. A small Tafel slope of 76 mV/dec and lower resistance
of 90 Ω were obtained for EPOP-700 compared to that of other
catalysts employed in this study. The excellent activity of EPOP-700
could be attributed to high N doping, as apparent from elemental analysis.
The obtained results were found to be better than those of the metal-free
catalysts and are comparable with those of metal-based OER catalysts.
In addition, these catalysts showed excellent catalytic activity toward
the reduction of 4-NP to 4-AP. EPOP-800 sample displayed excellent
catalytic activity by reducing 4-NP to 4-AP in 35 min, whereas other
catalysts took relatively longer times. The observed rate constant
and activity factor values are better than those of the reported nonmetallic
catalysts.
Experimental Section
Materials and Methods
All reagents
and solvents were
purchased from Sigma-Aldrich/Alfa Aesar and used without further purification.
13C and 15N CP-MAS measurements were carried
out on a Bruker Avance 400 spectrometer, operating at 100.6 MHz for 13C and 40.53 MHz for 15N using a Bruker 4 mm double
resonance probe-head at a spinning rate of 10 kHz. The X-ray diffraction
(XRD) patterns were measured at room temperature (RT) using a Bruker
D8 ADVANCE instrument using Cu Kα radiation with a wavelength
of 1.5418 Å. The powder diffraction covered the angle ranges
from 5–65°, with a step angle of 0.02°/min. The morphological
structures of the prepared samples were captured using a scanning
electron microscope (SEM) of TESCAN, VEGA 3 with Bruker detector.
Thermogravimetric analysis (TGA) was used to study the thermal degradation
of synthesized materials using a TGA/SDT Q600, TA instruments at a
scanning rate of 5 °C/min, from room temperature to 1000 °C
under nitrogen atmosphere. FT-IR analysis was carried out on a Bruker
Tensor 27 (Optik GmbH) using RT DLaTGS (Varian) detector. Transmission
electron microscope (Tecnai 20 G2 (FEI make), Netherlands) was used
to analyze the surface morphology. Brunauer–Emmett–Teller
surface area and porosity analysis was carried out on an Accelerated
Surface Area and Porosimetry system (ASAP-2020 V4.03 (V4.03 H)) at
77 K. Raman spectra were recorded using a high-resolution Renishaw
Raman microscope employing a He–Ne laser of 18 mW at 633 nm.
Cyclic voltammetry was carried on an autolab PGSTAT 302N workstation
at room temperature in a standard three-electrode cell. The working
electrode was a carbon paper (area = 1 cm2, mass loading
of 2 mg/cm2) and modified glassy carbon, and the counter
electrode was a Pt wire. The reference electrode was Ag/AgCl/KCl (3
M) electrode. The oxygen evolution reaction was studied by using linear
sweep voltammetry carried out at room temperature using 1 M KOH as
the electrolyte at a scan rate of 1 mV/s. For the ease of comparison
of results, the potentials were converted to the reversible hydrogen
electrode scale.
Ink Preparation
The ink was prepared
by equimolar preparation
1:1:1 (water/isopropyl alcohol/Nafion), and the solution was sonicated
for 3 h. A small volume (100 μL) of this solution was added
to 5 mg of the catalyst to prepare the slurry and was sonicated for
30 min. The catalyst ink was coated on the surface of tory carbon
by manual brush coating. The modified tory carbon was allowed to dry
at room temperature.
Nitrophenol Reduction
Reduction
of 4-NP to 4-AP was
carried out in the presence of excess NaBH4, which is an
important organic catalytic reaction. This reaction was carried out
to evaluate the catalytic performance of EPOP catalyst. Two milligrams
of 4-NP was dissolved in 40 mL of deionized water and sonicated for
half an hour; the solution was light yellow. Then, NaBH4 (120 mg) was added to the 4-NP solution. In the absence of EPOP
catalysts, a small amount of bubbles was observed because of the hydrogen
generation by the reduction reaction between NaBH4 and
water. However, in the presence of EPOP (3 mg) catalysts, a large
amount of bubbles was observed and the gas release rate became much
faster.
Synthesis of EPOP
Under inert conditions, ethylene
diamine (1.4 g, 24.4 mmol) was dissolved in anhydrous 1,4-dioxane
(100 mL) under constant stirring at RT. To this solution, K2CO3 (4.5 g, 32.5 mmol) was added and stirred for 30 min.
Then, the solution was cooled to 10 °C and cyanuric chloride
(3 g, 16.27 mmol) dissolved in 100 mL anhydrous 1,4-dioxane was added
dropwise over 8 h. The mixture was allowed to warm to RT and refluxed
for 3 days (during the course of the reaction, color changed from
dark brown to pale brown). The solution was cooled to RT; the mixture
was filtered, washed with 1,4-dioxane and methanol to remove unreacted
SM, and dried under vacuum to yield EPOP (yield = 90%).
Supporting Information Available
The Supporting
Information
is available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b00574.FT-IR, 13C and 15N NMR, HR-TEM,
FE-SEM, TGA, electrochemical active surface area calculation, SEM
image of EPOP-700 modified electrode after OER measurements, EIS,
chronoamperometry, XPS (PDF)
Supplementary Material
ao8b00574_si_001.pdf
The authors
declare no competing financial interest.
Acknowledgments
Dr. M.K.
thanks DST-INSPIRE for the faculty award and DST-SERB
Start-up Research grant for research funding. Director and support
staffs of CSIR-CECRI are gratefully acknowledged for their constant
encouragement and support.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145902610.1021/acsomega.8b01137ArticleUnusual Nucleophilic Addition of Grignard Reagents
in the Synthesis of 4-Amino-pyrimidines Tinson Ryan A.
J. Hughes David L. Ward Leanne Stephenson G. Richard *School of Chemistry, University
of East Anglia, Norwich Research Park, Norwich, Norfolk NR4 7TJ, U.K.* E-mail: g.r.stephenson@uea.ac.uk.10 08 2018 31 08 2018 3 8 8937 8944 25 05 2018 18 07 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
Pyrimidines have
always received considerable attention because
of their importance in synthesis and elucidation of biochemical
roles, in particular that of vitamin B1. Herein, we describe a reaction
pathway in a Grignard reagent-based synthesis of substituted pyrimidines.
A general synthesis of α-keto-2-methyl-4-amino pyrimidines and
their C6-substituted analogues from 4-amino-5-cyano-2-methylpyrimidine
is reported. The presence of the nitrile substituent in the starting
material also results in an unusual reaction pathway leading to C6-substituted
1,2-dihydropyrimidines. Grignard reagents that give normal pyrimidine
products under standard reaction conditions can be switched to give
dihydropyrimidines by holding the reaction at 0 °C before quenching.
document-id-old-9ao8b01137document-id-new-14ao-2018-011378ccc-price
==== Body
Introduction
The synthesis of pyrimidines
has always been a priority topic for
investigation because of their widespread use as scaffolds in medicinal,
pharmaceutical, and academic chemistries. Recently, there has been
a marked return to prominence of these structures, particularly in
the functionalized amino pyrimidine series,1 as synthetic targets. Although a majority of these examples are
2-amino pyrimidines, examples of 4-2 and
6-aminopyrimidines3 are also notable features.
These vital building blocks of life are found in many biologically
significant molecules, including structures like DNA 1, drugs such as zidovudine 2,4,5 and
barbiturate sodium thiopental 3 (Figure 1). Pyrimidines are also investigated for
the treatment of the neurological disorders Beriberi and Korsakoff
syndrome and as a recognition motif for binding in thiamine diphosphate-dependent
enzymes (compound 4, Figure 1).6,7
Figure 1 (a) DNA fragment, HIV
drug zidovudine, sodium thiopental, and vitamin
B1.
Because of their versatile
hydrogen-bonding interactions, these
small fragments have been intensively investigated by medicinal chemists
during the past decade. Their applications in GSK’s antimalaria
drug trimethoprim 5,8 antibiotic
bacimethrin 6,9 and in the
treatments of thiamine deficiency,10−12 are well-documented
(Figure 2).
Figure 2 Aminopyrimidines
in GSK’s trimethoprim and antibiotic bacimethrin.
Commonly, the synthesis of pyrimidine rings utilizes
a sodium alkoxide-catalyzed
condensation reaction between urea, an aldehyde, and a malonic ester.
Most methodologies to form these rings utilize this process, now called
the Biginelli reaction.13−15 Assembly of the core aromatic
structure permits further functionalization with a range of reactive
groups. The initial synthetic strategies to access the valuable 4-amino-2-methyl
pyrimidine substitution pattern were originally developed by Williams16 (Scheme 1). The reported procedure is outlined below and was subsequently
modified by others for the development and production scale-up of
vitamin B1 synthesis.
Scheme 1 Williams’ Synthesis of 4-Amino-2-methyl
Pyrimidine
Although the 4-amino-2-methyl
pyrimidines have been investigated
with many differing structural modifications,17−19 there are very
few examples for the synthesis of α-keto-4-amino-2-methyl pyrimidines
and their analogues.20 As the core pyrimidine
ring is observed widely throughout nature, it was surprising to find
such a lack of examples because these α-keto structural analogues
could be good candidates for inhibitor mimics and for potential structural
manipulations in structure–activity relationship studies. To
address this issue, we have devised a new synthetic route, which uses
cheap and readily available starting materials, to construct α-keto-4-amino-2-methyl
pyrimidines.
Results and Discussion
Our approach
to α-keto-4-amino-2-methyl pyrimidines is based
on the inclusion of a nitrile substituent at the 5-position to enable
the introduction of a wide variety of R groups. This allows us to
exploit the easy availability of 2-methyl-4-amino-5-cyano-pyrimidines
(Scheme 2).17
Scheme 2 Synthetic Approach to Access α-Keto-4-amino-2-methyl
Pyrimidines
with a Wide Variety of R Groups
Thus, our synthesis of a range of differently substituted
α-keto-2-methyl-4-amino
pyrimidines began by employing the established condensation reaction
of cheap and accessible reagents, acetamidine hydrochloride 14 and ethoxymethylenemalonitrile 15, which after
recrystallization of the crude product from ethanol gave the required
nitrile 13 in a 78% yield (Scheme 3, step 1).17
Scheme 3 New Synthesis of the Pyrimidyl Ketones
We now turned to a series of preliminary experiments to
assess
the optimum temperature for addition of the Grignard reagent to the
nitrile. Addition of the Grignard reagent at 0 °C and warming
to 40 °C gave total consumption of the starting material after
16 h. Lower temperatures resulted in incomplete consumption and required
longer reaction times. Addition of the appropriate Grignard reagent
produced the desired keto products 12 with various R
groups after simple column chromatography in yields of 16–68%
(see Scheme 4 and Table 1, product type A). The infrared spectra of the products showed an unusually
low position for the C=O stretching vibration of the ketones
at about 1650 cm–1. In the 1H nuclear
magnetic resonance (NMR) spectra, the signals for the NH2 protons came at two separate chemical shifts, presumably because
of H-bonding to the adjacent carbonyl oxygen by one of the protons
of the amino substituent. This strong intramolecular hydrogen bonding
also accounts for the unusual position of the C=O stretching
vibration for these compounds and is consistent with the data reported
for 1-(2-aminophenyl)ethanone.21 During
the purification of our ketone products, it became apparent that other
byproducts had been formed during the Grignard reaction. Characterization
of these byproducts allowed us to identify some unexpected structures,
which reveal an unusual alternative pathway for the addition of the
Grignard reagent at the C-6 position of the pyrimidine ring (Scheme 4, product types B and C).
Scheme 4 Surprising Range of Products Isolated
from the Addition of Grignard
Reagents to the Nitrile-Substituted Aminopyrimidine
Table 1 Product Structures and Yields of Grignard
Addition Products A, B, or C
entry R temp, °C % yield (type A) % yield (type B) % yield (type C)
1 Me 0–40a 18 (50%)b
2 Me 40c 17 (85%)
3 Et 0–40a 19 (68%)b 20 (27%)d
4 Et 40c 21 (80%)
5 Pr 0–40a 22 (16%)b 23 (20%)d
6 Pr 0–25e 24 (67%)
7 Pr 40c 22 (22%)
8 Bu 0–40a 25 (18%)d
9 Bu 0–25e 26 (87%)
10 i-Pr 0–25e 27 (56%)
11 t-Bu 40c 28 (42%)
12 phenyl 0–40a 29 (25%)b 30 (40%)d
13 phenyl 0–25e 31 (81%)
14 vinyl 40c 32 (76%)
15 HC≡C 40c
16 HC≡C 0–25e
a Grignard reagent was added at 0
°C, and the reaction mixture was then warmed to 40 °C and
then left to cool and stirred at rt overnight.
b By procedure I.
c By procedure III (Grignard reagent
was added at 40 °C).
d By procedure II (like procedure
I but neutralized with aqueous NaHCO3, before extraction).
e By procedure IV in which the
reaction
temperature was maintained at 0 °C for 3 h before being allowed
to warm to rt overnight.
The formation of these unexpected substitution patterns (see Scheme 4) was apparent from
the lack of the C6 aromatic proton at ∼8.0 ppm in the 1H NMR spectrum and the retained strong C≡N stretching
vibration at 2100 cm–1 in the infrared spectrum.
After adjusting the reaction conditions, addition of the methyl and
ethyl Grignard reagents at 40 °C instead of 0 °C gave the
[1,2]-dihydropyrimidine analogues of type C in good yields
(80–85%). These structures were identified by the presence
of the methyl signal as a doublet with 3J coupling (6.0 Hz) to the CH proton (q, 3J = 6.0 Hz) located at 4.1 ppm (e.g., see Figure 3). The assignment of these spectral features
was confirmed by the analysis of 1H correlation spectroscopy
data. The [1,2]-dihydro products also retained the distinctive nitrile
stretch at 2100 cm–1 in their infrared spectra.
The key features discussed above allow the characterization data for
the products of type B/C and the anticipated
product of type A to be easily distinguished. Remarkably,
these [1,2]-dihydro compounds remained stable at room temperature
over a period of weeks, despite the loss of aromaticity following
the addition of the Grignard reagent. Some aryl-22 and ferrocenyl-substituted23 examples appear to share the same stability shown by our nitrile-substituted
structures, whereas Lyle24 has reported
instability in the cyano-substituted dihydropyridine analogues.
Figure 3 Structure of
racemic 17 with the CHMe feature that
gives a characteristic C6 quartet and C7 doublet in the 1H NMR spectrum.
A plausible mechanism
for the synthesis of side products of types B/C could arise as a consequence of the Schlenk
equilibrium25 between the Grignard reagent
RMgX, R2Mg, and MgX2. Coordination of the Lewis
acidic MgX2 to the N1 nitrogen of the pyrimidine to form 16 would make the C6 position more electrophilic and hence
promote attack by the Grignard reagent (Scheme 5). Moreover, an electron-withdrawing group
adjacent to this position would further increase the electrophilicity
of the C6 position providing an explanation for why, in the 5-cyano
series, this side-reaction is far more favored. An alternative possibility,
however, would be a radical mechanism for the transfer of the R group,
followed by loss of H• by an oxidative step to form 17.
Scheme 5 Proposed Mechanism of the formation of [1,2]-Dihydropyrimidine 17
Examples of reactions
that are capable of forming stereogenic centers
from an aromatic system using Grignard reagents are rare, but a notable
precedent for this type of transformation has been described in the
synthesis of antifungal agent Voriconazole by Pfizer.26 The methyl and ethyl C6-substituted analogues have been
reported previously in the synthesis of vitamin B1 analogues,
but were acquired by condensation chemistry as described by Todd et
al.27,28 This condensation approach has not been
applied to the synthesis of other analogues containing modifications
at this position, so the new examples described here, which are obtained
by the Grignard approach, will open up a general access to this class
of structures.
Interestingly, the Schlenk equilibrium is often
controlled by changes
to the Grignard reagent, solvent, or temperature. To assess the optimum
conditions, a range of temperatures from (−78 to 40 °C)
were tested, but this served only to increase the consumption of the
starting nitrile 13 and did not affect the product outcome.
It was noticeable that addition of the Grignard at 0 °C followed
by warming to 40 °C gave a mixture of products, so some Grignard
additions at 40 °C were attempted. As the Schlenk equilibrium
should favor formation of the R1MgX species at higher temperatures
and in a polar aprotic solvent, the involvement of Lewis acidic MgX2 could be reduced, and therefore C-6 addition should be decreased.
This, however, with our initial choice of methyl and ethyl Grignard
reagents, gave 17 and 21 as the sole products
(Table 1, entries 2
and 4).
A range of solvents were then examined to assess their
affect upon
product distribution. As tetrahydrofuran (THF) had already been used
for the preliminary experiments, we sought to decrease the solvent
polarity. Diethyl ether was tested under the same conditions, and
from the analysis of the 1H NMR spectra, it was obvious
that only methyl ketone and the unreacted starting material were present.
Attempts using 1,4-dioxane resulted in the precipitation of the MgX2 salts. Removal of these MgX2 salts by filtration
was expected to improve the selectivity for the formation of the ketone
compound; however, this proved not to be the case, and the under these
conditions, the attempted reaction gave only the recovered unreacted
starting material.
On the basis of the mechanism proposed in Scheme 5, it seemed probable
that the products that
retained the nitrile group originated by initial addition of the nucleophile
to the heteroaromatic ring (producing the [1,2]-dihydro product of
type C) and that oxidation under the reaction conditions
later resulted in rearomatization to give 5-cyano-6-alkyl-2-methylpyrimidine
products of type B. This hypothesis was tested for Grignard
reagents (R1 = Et, Pr, Bu, and Ph; Table 1 entries 3, 5, 8, and 12) that tended to
give low yields and only products of types A and B. By avoiding the high temperature of 40 °C and keeping
the reaction mixture at 0 °C for 3 h, more time was allowed for
the addition at C6 to go to completion before the reaction was quenched.
Under these conditions (Table 1, entries 6, 9, 10, and 13), the [1,2]-dihydro products
of type C were isolated at moderate to good yields. Bulky
Grignard reagents (branched R1 groups such as i-Pr and t-Bu) give poorer results (56 and 42%, respectively).
In the other cases, (R1 = Me, Et, Pr, and Bu), the yields
of the [1,2]-dihydro products ranged from 67 to 87%. Extending the
study to phenyl- and vinylmagnesium bromide, we were able to show
that the low temperature conditions worked well to improve the yields
with phenylmagnesium bromide, giving [1,2]-dihydro product 31 in an 81% yield (compare entries 12 and 13), and our original 40
°C reaction conditions were suitable with vinylmagnesium bromide,
giving 32 in a 76% yield.
On the basis of these
trends, it appears that the unexpected formation
of [1,2]-dihydropyrimidine is in fact the preferred addition pathway
and proceeds efficiently, albeit slowly, at 0 °C. At higher temperatures,
the addition at the nitrile begins to become significant, so that
reactions that are allowed to warm up before all of the Grignard reagent
has been consumed can produce substantial amounts of the ketones (type A products). Type B products in many cases arise
by rearomatization of [1,2]-dihydropyrimidines, accounting for the
failure to isolate type C products in these cases. In
other cases, however, the addition of the Grignard reagent can be
performed at 40 °C to give methyl- and ethyl-substituted [1,2]-dihydropyrimidines
in a high yield. We proposed that this difference arises from the
differences in stability of type C products under strong
acid (HCl; entries 1, 3, 5, 8, and 12) conditions used in the quench,
compared to the weak acid (ammonium chloride) used for entries 2,
4, 6, 7, 9, 10, 11, 13, and 14. Steric bulk in the nucleophile (e.g.,
entry 8) seems to block addition at the nitrile, and type A products were not formed with butylmagnesium bromide. Alkynyl Grignard
reagents are less reactive and HC≡CMgBr failed to add to 13, even at 40 °C.
Crystallization and X-ray analysis
of the simple methyl substituted
example 17 confirmed the [1,2]-dihydro structure and
the presence of the stereogenic center at C6 (Figure 4). C6 is displaced 0.078(2) Å from the
good mean plane of the rest of the heterocyclic ring, which supports
the presence of extended π-overlap into the nitrile substituent.
The shorter bond length of C1–C2 [1.379(2) Å] when compared
to the C1–C6 bond of the C–CHMe [1.510(2) Å] suggests
the presence of the alkene π bond in conjugation with the nitrile
substituent within the aromatic π-system.
Figure 4 diagram for the crystal
structure of 4-amino-2-methyl-5-cyano-6-methyl-[1,2]-dihydropyrimid-ine 17. Thermal ellipsoids are drawn at the 50% probability level.
Measurement of the CN bond length
C11–N12 [1.158(2) Å]
indicates a typical length for this group, although the C1–C11
C–CN [1.402(2) Å] bond length lies between a normal C–C
bond (1.5 Å) and an sp2 C=C (1.3 Å), thereby
suggesting the presence of a partial sp2 bond character
between the aromatic π-system and the nitrile bond. At C6, the
CHMe position adopts the classic tetrahedral geometry with a bond
angle for the atom group N5–C6–H6 at 109.0(9)°
and the bond length for C1–C6 at 1.510(2) Å, whereas the
shorter bonds between the sp2 centers of C1–C2 and
C4–N3 have lengths of 1.379(2) and 1.312(2) Å, respectively.
Interestingly, these structures form a hydrogen-bonded dimer pair
(racemic, with R and S configurations)
around a center of symmetry, forming a binding pattern similar to
that observed in DNA base pairs (Figure 4), which becomes extended through further
pairs of hydrogen bonds (see the Supporting Information).
This paper identifies three competing pathways for the addition
of Grignard reagents to the readily available 4-amino-2-methyl-5-cyanopyrimidine
starting material, giving access to either the sought after α-keto-4-amino-2-methyl
pyrimidines or alternative products arising from substitution of the
pyrimidine ring itself. Especially in the cases where the exclusive
formation of a single product has been identified, the results presented
here should open the way for the exploitation of these substitution
patterns in future research. Furthermore, studies are now in progress
to extend the range of examples that give exclusively the unusual
chiral 1,2-dihydropyrimidines to introduce alternative reactive functional
groups at the C6 position (e.g., alkynes) to prepare the way for the
development of an enantioselective version of the procedure.
Ideally, this research would facilitate a wider range of ongoing
synthetic modifications such as Diels–Alder cycloaddition chemistry
and metal-catalyzed cross-coupling reactions, which could utilize
the vinyl adduct 32. Each in their own way, the intended
α-keto products and the unusual ring-substituted products are
ideal structures to access a wide range of pyrimidine-derived compounds
that will be of value in medicinal and bioorganic chemistry. Our procedure
avoids the need for extensive purification steps and so provides a
potential “gateway compound” suited for easy functionalization
in future studies. It also offers potential access to key intermediates
in the substantial quantities needed for sustained biochemical/pharmaceutical
research projects and scale-up processes.29 Furthermore, the ketones made available in this way would be suitable
prochiral candidates for reductions to provide useful intermediates
for the chiral synthetic pool and/or enzymatic studies.30,31
Experimental Section
General Considerations
All reactions
were carried out
in dry solvents, unless otherwise stated. Anhydrous THF, diethyl ether,
and toluene were distilled over sodium following literature methods.
All solvents and chemicals were purchased from appropriate suppliers
including Sigma-Aldrich, Acros, TCI, Fluorochem, Alfa Aesar, and Fisher.
Infrared spectra were obtained on a PerkinElmer spectrum 100 Fourier
transform infrared spectrometer, with most compounds dissolved in
dichloromethane and measured as a film on a NaCl disc. In cases where
compounds were not soluble in this solvent, the infrared spectrum
was obtained using an attenuation total reflection plate. 1H and 13C NMR spectra were obtained using a Bruker (Ascend)
500 MHz spectrometer and a sample express autosampler. Mass spectra
were measured by the EPSRC UK National Mass Spectrometry Facility,
Swansea, UK using an LTQ Orbitrap XL spectrometer. Melting points
were recorded on a BUCHI melting point apparatus B545. X-ray diffraction
data were recorded at the UEA on an Oxford Diffraction Xcalibur-3/Sapphire3
CCD diffractometer. The data were then processed with the CrysAlisPro-CCD
and -RED programs.32,33 The structure was determined
by the direct method routines in the SHELXS program34 and refined by full-matrix least-squares methods on F2’s in SHELXL34 using WinGX.35 Scattering factors for
neutral atoms were taken from the International Tables for X-ray Crystallography.36
Preparation of 4-Amino-5-cyano-2-methylpyrimidine
(13)17
Sodium (0.19
g) was added
in small pieces to ethanol (4.0 mL) to produce a 2 M solution of sodium
ethoxide. Then, acetamide hydrochloride (0.80 g, 8.50 mmol) was added.
Filtration through celite gave a clear solution, which upon addition
of ethoxymethylene malonitrile (0.50 g, 4.10 mmol) produced a yellow
precipitate that was collected by filtration and recrystallized from
ethanol to give the title compound as fine yellow needles (1.10 g,
70%). mp 245–247 °C [lit.17 mp 246–248 °C]. 1H NMR (500 MHz, DMSO-d6): δ 8.52 (s, 1H), 7.77 (s, 2H), 2.40
(s, 3H) ppm. 13C NMR (126 MHz, DMSO-d6): δ 170.6, 162.8, 161.6, 116.2, 87.1, 26.4 ppm. IR
νmax: 3378, 3334 (NH2), 2223 (sp CN),
1672, 1584, 1542 (C–H, sp2 stretch) cm–1.
Preparation of tert-Butylmagnesium Bromide
2-Methyl-2-bromopropane (1.0 mL, 8.9 mmol, 1 equiv) in dry THF
(9.0 mL) was added dropwise to a predried round-bottom flask containing
magnesium turnings (427 mg, 17.8 mmol, 2.0 equiv) in anhydrous THF
(20 mL). After activation with a small amount of iodine, addition
was maintained to keep a gentle reflux. The reaction was then stirred
at room temperature (rt) for 3 h. The Grignard reagent was titrated
against 1,10-phenanthroline and isopropyl alcohol.
Typical Procedure
I for the Synthesis of α-Keto-4-amino-2-methylpyrimidines
(Products of Type A)
5-(4-Amino-2-methylpyrimidinyl)propan-1-one
(19)
To 4-amino-5-cyano-2-methylpyrimidine 13 (200
mg, 1.5 mmol) in THF (5 mL) was added ethylmagnesium bromide in THF
(3 M, 5.3 mmol, 1.74 mL, 3.5 equiv) dropwise at 0 °C. The reaction
mixture was warmed to 40 °C and left to stir overnight. The reaction
was then quenched with 1 M HCl (10 mL), stirred for a further 24 h,
and then extracted with EtOAc (3 × 10 mL). The combined organic
layers were washed with brine (10 mL), dried over MgSO4, filtered, and evaporated under pressure to leave a fine powder.
Column chromatography on silica eluting with EtOAc/hexanes (1:3 v/v)
gave the product as a white solid (168 mg 68%). Rf = 0.6 EtOAc/hexanes
1:3 v/v. mp 160–162 °C. 1H NMR (500 MHz, CDCl3): δ 8.73 (s, 1H), 8.62 (s, 1H), 5.67 (s, 2H), 2.87
(q, 3J = 7.3 Hz, 2H, H-4), 2.47 (s, 3H,
H-1), 1.15 (t, 3J = 7.3 Hz, 3H, H-5) ppm. 13C NMR (126 MHz, CDCl3): δ 201.4, 171.1,
161.9, 158.9, 109.2, 29.5, 26.4, 8.1 ppm. IR νmax: 3385, 3263, 3109, 2980 (sp3 C–H stretch), 1657,
1625, 1528 (sp2 C–H stretch) cm–1. HRMS (ESI-LTQ Orbitrap XL) m/z: [M + H]+ calcd for C8H12N3O, 166.0975; found, 166.0972.
Typical Procedure II for
the Synthesis of 4-Amino-5-cyano-2-alkyl-
or 2-Arylpyrimidines (Products of Type B)
4-Amino-5-cyano-2-methyl-6-phenylpyrimidine
(30)32
To 4-amino-5-cyano-2-methylpyrimidine 13 (200 mg, 1.5 mmol) in THF (5 mL) was added phenylmagnesium
bromide in THF (3 M, 5.2 mmol, 1.74 mL, 3.5 equiv) dropwise at 0 °C.
The reaction was warmed to 40 °C and left to stir overnight,
then quenched with 1 M HCl (10 mL), and stirred for a further 24 h.
The reaction was then neutralized with aqueous NaHCO3 and
extracted with EtOAc (3 × 10 mL). The combined organic layers
were washed with brine (10 mL), dried over MgSO4, filtered,
and evaporated under reduced pressure to leave a fine powder. Column
chromatography on silica eluting with EtOAc/hexanes (gradient, 5:1
v/v to pure EtOAc) gave the product as a white powder (315 mg, 40%).
Rf = 0.2 EtOAc/hexanes 5:1. v/v. 1H NMR (500 MHz, DMSO-d6): δ 7.87–7.82 (m, 2H), 7.63–7.51
(m, 3H), 2.47 (s, 3H) ppm (this compound would only dissolve in DMSO-d6; signals for the NH2 protons were
not observed because of exchange with H2O in the solvent). 13C NMR (126 MHz, DMSO-d6): δ
169.7, 168.4, 164.7, 136.8, 131.3, 129.4, 129.0, 116.7, 84.2, 26.4
ppm. IR νmax: 3379, 3330 (NH2), 2168 (sp
CN), 1680, 1626, 1561 cm–1. HRMS (ESI-LTQ Orbitrap
XL) m/z: [M + H]+ calcd
for C12H11N4, 211.0978; found, 211.0978.
Typical Procedure III for the Synthesis of 4-Amino-5-cyano-2-methyl-6-alkyl-
or 6-Alkenyl-[1,2]-dihydropyrimidines at 40 °C (Products of Type
C)
4-Amino-5-cyano-2-methyl-6-vinyl-[1,2]-dihydropyrimidine (32)
To 4-amino-5-cyano-2-methylpyrimidine 13 (2.5
g, 19 mmol, 1 equiv) in THF (50 mL) was added vinylmagnesium
bromide in THF (3 M, 65 mmol, 21.8 mL, 3.5 equiv) dropwise at 40 °C.
The reaction mixture was left to stir overnight and then quenched
with saturated aqueous ammonium chloride (20 mL) at 0 °C and
stirred for further 48 h and extracted with EtOAc (3 × 10 mL).
The combined organic layers were washed with brine (10 mL), dried
over MgSO4, filtered, and evaporated under reduced pressure
to give the product as a fine yellow powder (2.24 g, 76%). mp 171–173
°C. 1H NMR (500 MHz, DMSO-d6): δ 8.47 (br s, 1H), 5.88 (s, 2H), 5.76 (ddd, 3J = 16.9, 9.9, 6.9 Hz, 1H), 5.07–5.00 (m,
2H), 4.49 (d, 3J = 6.9 Hz, 1H), 1.88 (s,
3H) ppm. 13C NMR (126 MHz, DMSO-d6): δ 160.8, 159.4, 139.9, 122.1, 114.3, 52.5, 51.4,
21.8 ppm. IR νmax: 3316, 3302 (NH2), 2171
(sp CN), 1734 (sp2 CO), 1683, 1638, 1601 (sp2 C–H stretch) cm–1. HRMS (ESI-LTQ Orbitrap
XL) m/z: [M + H]+ calcd
for C8H11N4, 163.0978; found, 163.0975.
Typical Procedure IV for the Synthesis of 4-Amino-5-cyano-2-methyl-6-alkyl-
or 6-Alkenyl-[1,2]-dihydropyrim-idines from 0 °C to rt (Products
of Type C)
4-Amino-5-cyano-2-methyl-6-propyl-[1,2]-dihydropyrimidine (24)
To 4-amino-5-cyano-2-methylpyrimidine 13 (200 mg, 1.5 mmol) in anhydrous THF (5 mL) at 0 °C was added
propylmagnesium chloride (2 M, 5.2 mmol, 2.6 mL, 3.5 equiv) dropwise
at 0 °C. The reaction mixture was stirred at 0 °C for 3
h and then left to warm to rt overnight. The reaction mixture was
cooled to 0 °C and quenched with saturated aqueous ammonium chloride
(10 mL) and left to stand for 3 h. The product was extracted with
EtOAc (3 × 10 mL), washed with brine (10 mL), dried over MgSO4, filtered, and evaporated to dryness to give the title compound
as a fine yellow powder (180 mg, 67%). mp 163–165 °C. 1H NMR (400 MHz, DMSO-d6): δ
8.21 (s, 1H), 5.74 (s, 2H), 4.04 (dd, J = 18.8, 4.6
Hz, 1H), 1.84 (s, 3H), 1.46–1.23 (m, 4H), 0.92–0.88
(m, 3H) ppm. 13C NMR (101 MHz, DMSO-d6): δ 161.4, 160.1, 122.6, 51.7, 49.3, 41.4, 22.2, 16.9,
14.2 ppm. IR νmax: 3310, 3252 (NH2), 2100
(CN), 1650, 1617, 1538 (sp2 C–H stretch) cm–1. HRMS (ESI-LTQ Orbitrap XL) m/z: [M + H]+ calcd for C9H15N4, 179.1291; found, 179.1291.
Synthesis of
α-Keto-4-amino-2-methylpyrimidines
5-(4-Amino-2-methylpyrimidinyl)ethanone
(18)
Following procedure I, using methylmagnesium
bromide followed by
column chromatography on silica eluting with ethyl acetate/hexanes
(1:3 v/v) gave the title compound as a white solid (470 mg, 50%).
mp 170–172 °C. 1H NMR (500 MHz, CDCl3): δ 8.70 (s, 1H), 8.57 (s, 1H), 5.72 (s, 1H), 2.50 (s, 3H),
2.48 (s, 3H) ppm. 13C NMR (126 MHz, CDCl3):
δ 198.2, 171.4, 161.8, 159.8, 109.8, 26.6, 26.1 ppm. IR νmax: 3372, 3114, 1651 (sp2 C=O), 1590, 1520
(sp2 C–H aromatic stretch) cm–1. HRMS (ESI-LTQ Orbitrap XL) m/z: [M + H]+ calcd for C7H10N3O, 152.0818; found, 152.0815.
5-(4-Amino-2-methylpyrimidinyl)butan-1-one
(22)
Following procedure I, using n-propylmagnesium
bromide followed by column chromatography on silica eluting with EtOAc/hexanes
(2:1 v/v) gave the title compound as a white solid (43 mg, 16%). Rf
= 0.3 EtOAc/hexanes 2:1 v/v. mp 147–149 °C. 1H NMR (500 MHz, CDCl3): δ 8.73 (s, 1H), 2.81 (t, 3J = 7.4 Hz, 3H), 2.50 (s, 3H), 1.73–1.64
(m, 2H, H-5), 0.94 (t, 3J = 7.4 Hz, 3H,
H-6) ppm. 13C NMR (126 MHz, CDCl3): δ
200.6, 170.5, 162.0, 158.2, 109.3, 40.3, 25.8, 17.9, 13.8 ppm. IR
νmax: 3373, 3265 (NH2) 1653, 1629, 1534
(sp2 C–H stretch) cm–1. HRMS (ESI-LTQ
Orbitrap XL) m/z: [M + H]+ calcd for C9H14N3O, 180.1131; found,
180.1129.
This product was also obtained following procedure
III; using n-propylmagnesium bromide followed by
column chromatography on silica eluting with EtOAc/hexanes (2:1 v/v)
gave the title compound as a white solid (60 mg, 22%).
5-(4-Amino-2-methylpyrimidinyl)phenone
(29)
Following procedure I, using phenylmagnesium
bromide followed by
column chromatography on silica eluting with EtOAc/hexanes (gradient,
5:1 v/v to pure EtOAc) gave the title compound as a white powder (200
mg, 25%), Rf = 0.5 EtOAc/hexanes 5:1 v/v. mp 182–184 °C. 1H NMR (500 MHz, DMSO-d6): δ
8.33 (s, 1H), 8.12 (s, 2H), 7.68–7.63 (m, 3H), 7.61–7.54
(m, 2H), 2.45 (s, 3H) ppm. 13C NMR (126 MHz, DMSO-d6): δ 196.2, 170.63, 162.8, 161.8, 138.6,
132.5, 129.4, 129.0, 108.9, 26.3 ppm. IR νmax: 3381,
2925, 1627, 1577, 1598 (sp2 C–H stretch) cm–1. HRMS (ESI-LTQ Orbitrap XL) m/z: [M + H]+ calcd for C12H12N3O, 214.0975; found, 214.0973.
Synthesis of
4-Amino-5-cyano-2-alkyl- or 2-Arylpyrimidines
4-Amino-5-cyano-6-ethyl-2-methylpyrimidine
(20)27
Following
procedure II, using methylmagnesium
bromide followed by column chromatography on silica eluting with EtOAc/hexanes
(gradient, 1:1 v/v to pure EtOAc) gave the title compound as a white
powder (66 mg, 27%). Rf = 0.7 EtOAc/hexanes 1:1 v/v. mp 197–199
°C [lit.27 mp 193–194 °C]. 1H NMR (500 MHz, CDCl3): δ 5.42 (s, 2H), 2.66
(q, 3J = 7.6 Hz, 2H), 2.38 (s, 3H), 1.16
(t, 3J = 7.6 Hz, 3H) ppm. 13C NMR (126 MHz, CDCl3): δ 175.5, 170.4, 163.3, 115.3,
86.3, 30.6, 26.4, 12.8 ppm. IR νmax: 3377, 3340 (NH2), 2223 (CN), 1682, 1553, 1577 (sp2 C–H
stretch) cm–1. HRMS (ESI-LTQ Orbitrap XL) m/z: [M + H]+ calcd for C8H11N4, 163.0978; found, 163.0974.
4-Amino-5-cyano-2-methyl-6-propylpyrimidine (23)
Following procedure II, using n-propylmagnesium
bromide followed by column chromatography on silica eluting with EtOAc/hexanes
(2:1 v/v) gave the title compound as a yellow/white powder (53 mg,
20%). Rf = 0.6 EtOAc/hexanes 2:1 v/v. mp 176–177 °C. 1H NMR (500 MHz, CDCl3): δ 5.50 (s, 2H), 2.71
(t, 3J = 10 Hz, 2H), 2.47 (s, 3H), 1.75–1.66
(m, 2H), 0.94 (t, 3J = 7.4 Hz, 3H) ppm. 13C NMR (126 MHz, CDCl3): δ 173.0, 169.1,
162.1, 114.1, 85.6, 37.5, 25.1, 21.2, 12.4 ppm. IR νmax: 3368, 3338 (NH2) 1653, 1629, 224 (CN), 1678, 1553, 1417
(sp2 C–H stretch) cm–1. HRMS (ESI-LTQ
Orbitrap XL) m/z: [M + H]+ calcd for C9H13N4, 177.1135; found,
177.1133.
4-Amino-6-butyl-5-cyano-2-methylpyrimidine
(25)
Following procedure II, using n-butylmagnesium
bromide followed by column chromatography on silica eluting with EtOAc/hexanes
(gradient, 1:1 v/v to pure EtOAc) gave the title compound as a white
solid (50 mg, 18%). Rf = 0.6 EtOAc/hexanes 1:1 v/v. mp 180–182
°C. 1H NMR (500 MHz, CDCl3): δ 5.69
(s, 2H), 2.72 (t, 3J = 10 Hz, 2H), 2.46
(s, 3H), 1.68–1.60 (m, 2H), 1.40–1.31 (m, 2H), 0.88
(t, 3J = 7.4 Hz, 3H) ppm. 13C NMR (126 MHz, CDCl3): δ 175.2, 170.4, 163.6, 116.0,
87.1, 37.0, 31.6, 26.8, 23.1, 14.2 ppm. IR νmax:
3339, 3379, 2227 (sp CN), 1687, 1559, 1461 (sp2 C–H
stretch) cm–1. HRMS (ESI-LTQ Orbitrap XL) m/z: [M + H]+ calcd for C10H15N4, 191.1291; found, 191.1289.
Synthesis of 4-Amino-5-cyano-2-methyl-6-alkyl- or -6-Phenyl-
or 6-Alkenyl-[1,2]-dihydropyrimdines
4-Amino-5-cyano-2,6-dimethyl-[1,2]-dihydropyrimidine
(17)
Following procedure III, using methylmagnesium
bromide gave the title compound as a fine yellow powder (2.4 g, 85%).
mp 221–222 °C. 1H NMR (500 MHz, DMSO-d6): δ 8.27 (s, 1H), 5.77 (s, 2H), 4.17
(q, 3J = 6.0 Hz, 1H), 1.84 (s, 3H), 1.18
(d, 3J = 6.0 Hz, 3H) ppm. 13C NMR (126 MHz, DMSO-d6): δ 161.0,
159.7, 122.4, 53.6, 45.5, 25.5, 22.1 ppm. IR νmax: 3399, 3304, 2152 (sp CN), 1658, 1608, 1563 (sp2 C–H
stretch) cm–1. HRMS (ESI-LTQ Orbitrap XL) m/z: [M + H]+ calcd for C7H11N4, 151.0978; found, 151.0975.
4-Amino-5-cyano-6-ethyl-2-methyl-[1,2]-dihydropyrimidine (21)
Following procedure III, using ethylmagnesium
bromide gave the title compound as a fine yellow powder (2.1 g, 80%).
mp 213–215 °C. 1H NMR (500 MHz, DMSO-d6): δ 8.19 (s, 1H, H-6), 5.75 (s, 2H,
H-2), 4.09 (td, 3J = 4.6, 2.3 Hz, 1H),
1.86 (s, 3H), 1.50–1.38 (m, 2H), 0.86 (t, 3J = 7.4 Hz, 3H) ppm. 13C NMR (126 MHz, DMSO-d6): δ 161.5, 160.3, 122.7, 51.0, 50.6,
31.2, 21.7, 8.1 ppm. IR νmax: 3372, 3326 (NH2), 2180, 2149 (sp CN), 1659, 1600, 1565 (sp2 C–H
stretch) cm–1. HRMS (ESI-LTQ Orbitrap XL) m/z: [M + H]+ calcd for C8H13N4, 165.1135; found, 165.1135.
4-Amino-6-butyl-5-cyano-2-methyl-[1,2]-dihydropyrimidine (26)
Following procedure IV, using n-butylmagnesium
bromide gave the title compound as a fine yellow
powder (250 mg, 87%). 1H NMR (500 MHz, DMSO-d6): δ 8.22 (s, 1H), 5.74 (s, 2H), 4.08 (td, J = 4.8, 2.4 Hz, 1H), 1.86 (s, 3H), 1.45–1.40 (m,
2H), 1.34–1.25 (m, 4H), 0.90 (t, J = 6.9 Hz,
3H) ppm. 13C NMR (126 MHz, DMSO): δ 161.1, 160.2,
122.3, 51.3, 49.6, 38.4, 25.4, 22.8, 21.9, 14.5 ppm. IR νmax: 2159 (sp CN), 1631, 1588, 1520 cm–1.
HRMS (ESI-LTQ Orbitrap XL) m/z:
[M + H]+ calcd for C10H17N4, 193.1448; found, 193.1447.
4-Amino-5-cyano-2-methyl-6-iso-propyl-[1,2]-dihydropyrimidine
(27)
Following procedure IV, using iso-propylmagnesium bromide gave the title compound as a fine yellow
powder (150 mg, 56%) mp 170–171 °C. 1H NMR
(400 MHz, DMSO-d6): δ 8.14 (s, 1H),
5.75 (s, 2H), 3.89 (d, J = 2.6 Hz, 1H), 1.87 (s,
3H), 1.57 (s, 1H), 0.86 (d, 3H), 0.82 (d, 3H) ppm. 13C
NMR (101 MHz, DMSO-d6): δ 162.1,
160.8, 123.0, 55.4, 49.9, 36.7, 21.7, 17.3, 16.4 ppm. IR νmax: 3368, 3321 (NH2), 2175 (CN), 1652, 1601, 1565
(sp2 C–H stretch) cm–1. HRMS (ESI-LTQ
Orbitrap XL) m/z: [M + H]+ calcd for C9H15N4, 179.1291; found,
179.1290.
4-Amino-5-cyano-2-methyl-6-tert-butyl-[1,2]-dihydropyrimidine
(28)
Following procedure III, using tert-butylmagnesium bromide gave the title compound as a
fine yellow powder (120 mg, 42%). mp 217–219 °C. 1H NMR (500 MHz, DMSO-d6): δ
8.38 (s, 1H), 5.82 (s, 2H), 3.61 (s, 1H), 1.96 (s, 3H), 0.85 (s, 9H)
ppm. 13C NMR (126 MHz, DMSO-d6): δ 161.9, 161.6, 124.2, 58.9, 48.9, 40.8, 25.0, 21.9 ppm.
IR νmax: 2159 (sp CN), 1637, 1598, 1562 cm–1. HRMS (ESI-LTQ Orbitrap XL) m/z: [M + H]+ calcd for C10H17N4, 193.1448; found, 193.1445.
4-Amino-5-cyano-2-methyl-6-phenyl-[1,2]-dihydropyrimidine
(31)
Following procedure IV, using phenylmagnesium
bromide gave the title compound as a fine yellow powder (256 mg, 81%). 1H NMR (400 MHz, DMSO-d6): δ
8.79 (br s, 1H), 7.4–7.37 (m, 2H), 7.31–7.27 (m, 3H),
5.91 (s, 2H), 5.11 (s, 1H), 1.92 (s, 3H) ppm. 13C NMR (101
MHz, DMSO-d6): δ 145.9, 129.4, 129.0,
128.2, 127.9, 127.2, 127.0, 122.4, 53.8, 22.1. IR νmax: 3345, 3317 (NH2), 2123 (CN), 1646, 1601, 1550 (sp2 C–H stretch) cm–1 HRMS (ESI-LTQ
Orbitrap XL) m/z: [M + H]+ calcd for C12H13N4, 213.1135; found,
213.1137.
Supporting Information Available
The Supporting Information is
available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b01137.Copies of 1H and 13C NMR spectra
for all new compounds and X-ray structure details for compound 17 (PDF)
Crystallographic data for compound 17 (CIF)
Supplementary Material
ao8b01137_si_001.pdf
ao8b01137_si_003.cif
Author Contributions
The manuscript
was written through contributions of all authors. All authors have
given approval to the final version of the manuscript, and all authors
have contributed equally.
The authors
declare no competing financial interest.
Acknowledgments
We thank
the EU Interreg Trans Manche/Channel cross-border
project “Academy-Industry Chemistry Channel” (AIcc:
ref 4196) for the financial support and the EPSRC mass spectrometry
facility at the University of Swansea for HRMS data.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145879710.1021/acsomega.8b00818ArticleIn Situ Shape Change of Au Nanoparticles on TiO2 by CdS
Photodeposition:
Its Near-Field Enhancement Effect on Photoinduced Electron Injection
from CdS to TiO2 Fujishima Musashi †Ikeda Takuya ‡Akashi Ryo ‡Tada Hiroaki *‡†Faculty
of Science and Engineering and ‡Graduate School of Science and
Engineering, Kindai University, 3-4-1 Kowakae, Higashi-Osaka, Osaka 577-8502, Japan* E-mail: h-tada@apch.kindai.ac.jp.06 06 2018 30 06 2018 3 6 6104 6112 25 04 2018 25 05 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
Hemisphere-like
gold nanoparticles (NPs) were loaded on TiO2 (Au/TiO2) by the deposition–precipitation
method. Subsequent photodeposition of CdS on the Au surface of Au/TiO2 at 50 °C yields Au(core)–CdS(shell) hybrid quantum
dots with a heteroepitaxial (HEPI) junction on TiO2 (Au@#CdS/TiO2), whereas nonHEPI Au@CdS/TiO2 was formed by CdS
photodeposition at 25 °C. In the HEPI system, the shape of the
Au core changes to an angular shape, whereas it remains in a hemisphere-like
shape in the nonHEPI system. The hot photodeposition technique was
applied to the Au NP-loaded mesoporous TiO2 nanocrystalline
film (Au/mp-TiO2). Using Au@CdS/mp-TiO2 and
Au@#CdS/mp-TiO2 as the photoanodes, two-electrode quantum
dot-sensitized photoelectrochemical cells were fabricated for hydrogen
(H2) generation from water, and the performances of the
cells were evaluated under illumination of simulated sunlight. In
the photocurrent and the rate of H2 evolution, the Au@#CdS/mp-TiO2 photoanode cell surpasses the CdS/mp-TiO2 and
Au@CdS/mp-TiO2 ones. Three-dimensional finite-difference
time-domain calculations for the model systems indicated that the
angular shape Au core generates an intense electric field at the corners
and edges, extending the electric field distribution over the Au core–CdS
shell interface. The striking shape effect on the cell performances
can originate from the promotion of the CdS excitation and charge
separation due to the near-field enhancement by the deformed Au core.
document-id-old-9ao8b00818document-id-new-14ao-2018-00818pccc-price
==== Body
1 Introduction
Plasmonic
photocatalysts consisting of metals and semiconductors
have recently attracted much interest as the key materials for solar-to-chemical
transformations.1−3 The optoelectric properties of the plasmonic metals
such as Au nanoparticles (NPs) strongly depend on the shape in addition
to the size and loading amount.4,5 Periodic arrays of Au
nanorods (NRs) were formed on a TiO2 single crystal electrode
(Au NR/TiO2) by electron beam lithography, and the plasmonic
activity for photoelectrochemical water splitting was studied under
external biased conditions.6 Also, TiO2-capped Au NR array with redox catalysts electrochemically
prepared using porous alumina templates shows photocatalytic activity
for water splitting without external wiring.7 In both the systems, two peaks corresponding to the transverse and
longitudinal modes of the localized surface plasmon resonance (LSPR)
unique to the Au NRs were observed in the action spectrum of incident
photon-to-current efficiency (IPCE), and the hot-electron transfer
mechanism is proposed for the reaction.8 However, the study on the effect of the shape on the plasmonic photocatalytic
activity is limited because the synthesis of such catalysts usually
needs expensive experimental equipment and elaborated techniques.
On the other hand, a large contact area and a high-quality interface
between the metal and semiconductor are crucial for the efficient
interfacial electron transfer enhancing photocatalytic activity of
plasmonic photocatalysts.9,10 Colloidal solutions
of Au and CdS NRs were separately synthesized, and Au-NR/CdS-NR hybrids
were prepared by mixing them.11 The authors
showed that the Au-NR/CdS-NR exhibits high visible-light activities
for the oxidation of salicylic acid and reduction of p-nitrophenol due to the large contact area between Au- and CdS-NRs.
This colloid-based method is convenient and versatile for the preparation
of various metal–semiconductor nanohybrids; however, organic
modifiers are necessary as the shape-controlling agents contaminating
the interface between the components. Whereas postheating at high
temperatures improves the interface quality by removing the organic
modifiers, and may cause aggregation of metal NPs, and further, damage
of the components. Consequently, if a low temperature technique can
be developed for changing the shape of the components in metal–semiconductor
nanohybrids with a large contact area and high-quality interfaces,
it could provide basic and useful information about the shape effect
on the activity of the plasmonic photocatalysts. Here, we report in
situ shape change in the Au NP on TiO2 with the selective
photodeposition of the CdS shell on the Au NP at 50 °C, and the
mechanism on the low temperature formation of the heteroepitaxial
(HEPI) junction between the Au(core) and CdS(shell) (Au@CdS). Furthermore,
Au@CdS/TiO2 is applied as the photoanode of quantum dot-sensitized
photoelectrochemical cells (QD-SPECs) for H2 generation
from water, and the shape effect of the Au core on the cell performances
is discussed on the basis of the results of three-dimensional finite-difference
time-domain (3D-FDTD) calculations.
2 Results
and Discussion
2.1 Hot Photodeposition of
CdS on Au/TiO2
The morphology of the samples was
checked by transmission
electron microscopy (TEM). The loading amount of Au on TiO2 was determined to be 0.0190 ± 0.002 g TiO2 g–1 by inductively coupled plasma spectroscopy (ICPS).
Au NPs with a hemisphere-like form and a mean diameter (dAu) of 8.0 nm (standard deviation = 1.8 nm) were deposited
on TiO2 by the deposition–precipitation method.12Figure 1A shows the TEM image for the sample with CdS photodeposited
on Au/TiO2 at 50 °C. A CdS shell is formed on the
surface of every Au NP to yield Au@CdS/TiO2. Similar TEM
images were observed for the samples prepared at 25 °C (Figure S1),13 where
the mean shell thickness of 7.7 nm (standard deviation = 2.3 nm) was
confirmed.12 The selective photodeposition
of CdS on Au was explainable in terms of the electron pool effect
of Au NP and the strong affinity of Au and sulfur.14 The amounts of CdS photodeposited on Au/TiO2 at 25 and 50 °C were comparable to 0.025 ± 0.003 g TiO2 g–1. Figure 1B shows X-ray diffraction (XRD) patterns for the samples
prepared at 25 and 50 °C. The former has several diffraction
peaks of anatase TiO2 with a shoulder at 27 < 2θ
< 30°. In the pattern for the latter, two weak peaks are present
at 2θ = 26.62 and 28.42° assignable to the diffraction
from the (002) and (101) planes of hexagonal CdS. Figure 1C,D show Cd 3d- and Au 4f-X-ray
photoelectron (XP) spectra for Au@CdS/mp-TiO2, prepared
by varying photodeposition time (tPD),
respectively. In spectrum C, two signals are observed at binding energy
(EB) = 411.9 and 405.2 eV due to the emission
from the Cd 3d3/2 and Cd 3d5/2 orbitals, respectively,
intensifying with an increase in tPD.
In spectrum D, Au/TiO2 has emissions from the Au 4f5/2 orbital at EB = 86.4 eV and
the Au 4f7/2 orbital at EB =
82.8 eV, which disappear at tPD > 0.5
h. Evidently, the present photodeposition technique yields a hexagonal
CdS shell completely covering the Au core, and the rise in the deposition
temperature from 25 to 50 °C somewhat increases the CdS crystallinity.
Figure 1 (A) TEM
image of Au@CdS/mp-TiO2 prepared by photodeposition
at 50 °C. (B) XRD patterns for Au@CdS/mp-TiO2 prepared
by photodeposition at 25 and 50 °C. Cd 3d (C) and Au 4f (D)-XP
spectra for Au@CdS/TiO2 prepared by photodeposition at
25 °C.
To gain information about
the junction between the Au core and
the CdS shell, high-resolution (HR) TEM observation and analysis were
carried out. Figure 2A,B compare the typical HR-TEM images for Au@CdS/TiO2 prepared
at 25 and 50 °C. As shown in image A, the CdS photodeposition
at 25 °C yields nonHEPI Au@CdS hybrids on TiO2 (Au@CdS/TiO2) and the shape of the Au core remained to be in a hemisphere-like
shape. In image B, the CdS shell formation induces the Au(111) facets
with the d-spacing of 0.236 nm. The d-spacing of 0.335 nm for the CdS shell agrees with the value for
the hexagonal CdS(0002) plane. The CdS shell grows on the Au(111)
surface with a HEPI relation of CdS{0001}/Au{111} (Au@#CdS/TiO2): the symbol # denotes the HEPI junction between the Au core
and the CdS shell below. Figure 2C,D show the side view and top view of a model for
the CdS/Au NP interface, respectively. The interface consists of the
Au(111) plane and the S plane perpendicular to the c-axis of CdS. Importantly, the photodeposition of CdS on Au/TiO2 at 50 °C simultaneously changes the shape of the Au
core from a hemisphere-like shape to an angular shape with edges and
corners. A similar shape change in the Au core was also observed in
the CdS photodeposition on Au/ZnO.10
Figure 2 HR-TEM images
for Au@CdS/TiO2 prepared by photodeposition
at 25 °C (A) and 50 °C (B). The side view (C) and top view
(D) of a model for the CdS/Au NP interface of the sample prepared
at 50 °C (d1 = 0.7172 nm, and d2 = 0.7493 nm, d3 = 0.8651 nm, d4 = 0.8274 nm).
So far, several Au NP-metal chalcogenide
heteronanostructures with
the HEPI junction have been synthesized at temperatures in the range
from 170 to 300 °C.15−18 The basic mechanism on the low temperature formation
of Au@#CdS/TiO2 in the present system is discussed. The
general requirements to form the HEPI junction are small lattice mismatch
<15% for core–shell structures15 and slow crystal growth near the equilibrium conditions.19 Upon UV-light irradiation of Au/TiO2 in ethanol containing Cd2+ ions and S8, the
excited electrons in the conduction band (CB) of TiO2 are
transferred to the Au NPs. Simultaneous excitation of the Au NP-LSPR
can lead to the hot-electron transfer from the Au NPs to the CB of
TiO2,8 which is overwhelmed
by the electron transfer in the opposite direction under these conditions.20 The accumulation of the electrons in Au NPs
rises its Fermi energy (EF) to approach
the CB minimum of TiO2. S8 is selectively adsorbed
on Au NPs due to the strong S-Au bond (∼184 kJ mol–1),21 gradually reduced to S2– ions by the electrons accumulated in Au NPs with the concentration
being maintained low near the Au surface to react with Cd2+ ions. Consequently, the CdS shell slowly grows on the surface of
Au NP. The CdS deposition induces the Au(111) facet so as to generate
the maximum S-Au interfacial bonds stabilizing the interface between
the Au(111) with the largest surface Au-atom density and the S plane
of CdS(0001). Both the Au(111) and CdS(0001) planes have hexagonal
symmetry, and the three unit cells in the Au(111) plane (0.8651 nm)
fit with the two unit cells in the CdS(0001) plane (0.8274 nm) with
a lattice mismatch degree of −4.36%. The fact that the HEPI
junction between the Au core and the CdS shell can be induced by an
increase in the photodeposition temperature from 25 to 50 °C
indicates that the activation of the mobility of the Au surface atoms
is important for the formation of high-quality junction. The melting
point of transition metals is known to dramatically decrease with
increasing electron occupancy in the d-band above half filling or
increasing EF. Recent full-multiple scattering
calculations indicated that the bulk-state Au has 6.9% vacancy in
the d-band due to the hybridization of the 5d orbitals with 6s and
6p orbitals.22 The EF upward shift in Au NPs by the photoinduced electron transfer
from TiO2 may cause the surface phonon softening of Au
NPs. The enhancement of the vibrational amplitude on the surface atoms
can assist to reconstruct and relax the lattice mismatch at the interface.
Thus, the present photodeposition technique, satisfying the requirements
for the formation of HEPI, enables its low temperature formation.
2.2 Application to the QD-SPEC Cells
Au@#CdS/TiO2 is very promising as the photoanode for the
QD-SPEC cell for H2 generation from water,23−25 where the optical properties are fundamental to the application. Figure 3A compares UV–visible
absorption spectra for Au/mp-TiO2, CdS/mp-TiO2, Au@CdS/mp-TiO2, and Au@#CdS/mp-TiO2. The
absorption edge for the pristine mp-TiO2 composed of anatase
TiO2 nanocrystals is located at ∼390 nm. In the
spectrum for Au/mp-TiO2, the LSPR of Au NPs appears around
550 nm, and CdS/mp-TiO2 has absorption at λ <
510 nm due to the CdS interband transition. Although Au@CdS/mp-TiO2 possesses both the features of Au/mp-TiO2 and
CdS/mp-TiO2, the CdS shell formation induces significant
broadening and redshift in the LSPR peak from 550 to 640 nm. This
remarkable redshift and broadening in the LSPR peak would be due to
the large refractive index of the CdS shell (2.32)26 and the potent interaction between the Au core and the
CdS shell. The absorption spectrum for Au@#CdS/mp-TiO2 is
similar to that for Au@CdS/mp-TiO2, but the former has
a significantly stronger LSPR than the latter at λ < 730
nm.
Figure 3 (A) UV–visible absorption spectra for Au/mp-TiO2 (green line), CdS/mp-TiO2 (black line), Au@CdS/mp-TiO2 (blue line), and Au@#CdS/mp-TiO2 (red line), and
IPCE action spectra for the QD-SPEC cells using CdS/mp-TiO2 (black circle), Au@CdS/mp-TiO2 (blue circle), and Au@#CdS/mp-TiO2 (red circle). (B) solar-to-current efficiency (STCE) as a
function of applied voltage (Eapp) for
the CdS/mp-TiO2 (black), Au@CdS/mp-TiO2 (blue),
and Au@#CdS/mp-TiO2 (red) photoanode cells.
Two-electrode QD-SPEC cells were fabricated using
Au/mp-TiO2, CdS/mp-TiO2, Au@CdS/mp-TiO2, and Au@#CdS/mp-TiO2 as the photoanode and Pt cathode,
and the photocurrents were
measured under illumination of simulated sunlight (λ > 430
nm,
AM 1.5, one sun). The STCE was calculated from the photocurrent (Jph) using 1 1 where Erev (V)
and I are the standard state reversible potential
for the overall cell reaction and the light intensity (100 mW cm–2), respectively. The Erev was calculated to be +0.23 V from the standard reaction Gibbs energy
of +44.3 kJ mol–1 for the present overall cell reaction.26Figure 3B shows STCEs for the QD-SPEC cells as a function of applied
bias (Eapp). The photocurrent for the
Au/mp-TiO2 photoanode cell was very small. This is probably
because of the poisoning of the Au NP surface by the oxidized S2– ions. The CdS/mp-TiO2 photoanode cell
shows a volcano-shaped one with a maximum of 0.0095% at Eapp = 0.125 V. The presence of the Au core greatly increases
the STCE, decreasing the Eapp, where the
STCE reaches maximum. Strikingly, the Au@#CdS/mp-TiO2 photoanode
cell provides a maximum STCE of 0.037% at Eapp = 0.025 V, which is substantially larger than the value of 0.028%
at Eapp = 0 for Au@CdS/mp-TiO2.
To elucidate the origin for the Au core effect, three-electrode
PEC cells with the structure of a working electrode|0.25 M Na2S, 0.35 M Na2SO3|Ag/AgCl (reference
electrode)|counter electrode were constructed. A stable photocurrent
was observed for each cell (Figure S2).
Furthermore, the photocurrent was measured for the PEC cells with
CdS/mp-TiO2, Au@CdS/mp-TiO2, and Au@#CdS/mp-TiO2 as the working electrodes under irradiation of monochromatic
light by varying its wavelength. In Figure 3A, the IPCE action spectra for the cells
are also shown. The onset wavelength for the photocurrent (λon) ranges from 560 to 600 nm, and the order of the IPCE value
at 430 < λ < 600 nm is CdS/mp-TiO2 < Au@CdS/mp-TiO2 < Au@#CdS/mp-TiO2. The discrepancy between
the λon and the CdS absorption edge (∼510
nm) indicates that the interfacial electron transfer from CdS to TiO2 occurs via the transition from the valence band (VB) of CdS
to the CB of TiO2 (path 2)27 besides the injection from the CB of CdS to the CB of TiO2 (path 1).14 In the Au@CdS/mp-TiO2 and Au@#CdS/mp-TiO2 photoanodes, not the Au NP
core but the CdS shell acts as the photosensitizer, because the photocurrent
hardly flows around the LSPR peak of the Au core. Also, the Au core
and further, the high-quality junction between the Au core and the
CdS shell enhances the electron injection from CdS to TiO2.
Figure 4A
compares
the rate of H2 evolution under simulated sunlight illumination
(λ > 430 nm, AM 1.5, one sun) of the QD-SPEC cells with different
photoanodes. In the Au@CdS/mp-TiO2 and Au@#CdS/mp-TiO2 photoanode cells, the amount of H2 increases proportionately
to irradiation time, while good linearity in the plot has also recently
been confirmed for the CdS/mp-TiO2 photoanode cell.28 These results indicate that every photoanode
stably works under these conditions. The rate of H2 evolution
is in the order of CdS/mp-TiO2 (0.03 mL h–1 cm–2) ≪ Au@CdS/mp-TiO2 (0.18
mL h–1 cm–2) < Au@#CdS/mp-TiO2 (0.20 mL h–1 cm–2). The
mean lifetime of the electrons injected into the CB of TiO2 (τn) can be estimated by analyzing
the potential decay curve in the three-electrode QD-SPEC cell by 2 2 where kB and q are the Boltzmann constant and the elementary
charge of
electron, respectively, and Voc is obtained
from the subtraction of the electrode potential in the dark (Edark) from the electrode potential under light
illumination (Eph).29Figure 4B shows plots of log(τn/s) vs Voc. Although the τn decreases with increasing Voc in every system, the value for the Au@CdS/mp-TiO2 cell is larger than that for CdS/mp-TiO2 at the
same Voc. The lifetime for the Au@#CdS/mp-TiO2 cell is further longer than that for the Au@CdS/mp-TiO2 cell. Clearly, the Au core greatly enhances the charge separation
to induce the remarkable increase in the STCE. In Figure 3A, no photocurrent is observed
at λ > 600 nm, which excludes the hot-electron transfer mechanism
in this system.8 Thus, the superior performance
of Au@#CdS/mp-TiO2 over Au@CdS/mp-TiO2 could
result from the shape change of the Au core rather than the high-quality
interface.10
Figure 4 (A) Time courses for
H2 generation for the QD-SPEC cells.
(B) Plots of hot electron lifetime (τn) as a function of photovoltage under open-circuit conditions (Voc). Photoanodes used in the measurements were
CdS/mp-TiO2 (black), Au@CdS/mp-TiO2 (blue),
and Au@#CdS/mp-TiO2 (red), respectively.
2.3 FDTD Calculations
Three-dimensional
FDTD simulations were performed for a model of Au@CdS/TiO2 consisting of a CdS shell (thickness, lCdS = 7.7 nm)-coated Au hemisphere (dAu =
8 nm) placed on a TiO2 slab (Figure 5A). To clarify the shape effect of the Au
core, we also modeled Au@#CdS/mp-TiO2 by a CdS shell-coated
Au nanocube placed on a TiO2 slab (Figure 5B), where the volumes of the cube and the
shell were set to be the same as those of Au@CdS/TiO2.
The models were illuminated with incident visible light parallel with
either the z-axis or x-axis toward
the hemisphere. The excited localized electromagnetic fields were
monitored at the cross-sectional planes of the models. To identify
the location of the excited fields, polarized light sources were used
in this simulation. Figure 5C shows wavelength dependence of maximum local electric field
enhancement factors monitored on the x–y plane (EFxy) and the x–z plane (EFxz) under x-polarized light incident from the z-axis direction (k//z, E//x). The enhancement factor
defined as the ratio of the local maximum electric field intensity
to the incident electric field intensity is highly dependent on the
excitation wavelength. The small EF in the off-resonant wavelength
region below 500 nm indicates that the interband transitions of Au
and CdS hardly contribute to the local electric field enhancement.
The peak value of EFxy for Au@#CdS/TiO2 (red dotted line) is 9.62 × 103 at an incident
light wavelength of 673 nm which is smaller than the value of 2.31
× 104 at 694 nm for Au@CdS/mp-TiO2 (black
dotted line). On the other hand, EFxz for
Au@#CdS/TiO2 (red solid line) surpasses EFxz for Au@CdS/TiO2 (black solid line) at
a wavelength of over 510 nm, where a significant difference in LSPR
absorption was observed (Figure 3A). The peak EFxz value
of 9.62 × 103 for the former is about 1 order of magnitude
larger than the value of 1.01 × 103 for the latter. Figure 5D shows the wavelength
dependence of EFs monitored on the x–y plane (EFxy) and the x–z plane (EFxz) under z-polarized light incident from the x-axis direction (k//x, E//z). EFxy and EFxz for Au@#CdS/TiO2 (red dotted and solid lines) far exceed those for Au@CdS/TiO2 (black dotted and solid lines) in a wavelength over ca. 530
nm, respectively. It is noteworthy that EFxy and EFxz for Au@#CdS/TiO2 are almost comparable with each other within the simulation wavelength
range both in Figure 5C,D, whereas EFs for Au@CdS/TiO2 are highly dependent
on the location of the monitor planes.
Figure 5 FDTD simulation models
of (A) Au@CdS/TiO2 and (B) Au@#CdS/mp-TiO2.
Inset image of (B) represents the structural notation for
a nanocube. Wavelength dependence of a maximum local electric field
enhancement factor (EF) under (C) x-polarized light
incident from the z-axis direction (k//z, E//x) and
(D) z-polarized light incident from the x-axis direction (k//x, E//z) for Au@CdS/TiO2 (black)
and Au@#CdS/mp-TiO2 (red). Values of the EF were monitored
on the x–y plane (EFxy, dotted line) and the x–z plane (EFxz solid line), respectively.
Figure 6A,C show
local electric field distribution in the x–y plane (upper row) and the x–z plane (lower row) for Au@CdS/TiO2 and Au@#CdS/mp-TiO2 excited by an x-polarized light incident
from the z-axis direction (k//z, E//x), respectively.
In all of these images, the LSPR is due to dipole resonance excitation
because the core size of the models is sufficiently smaller than the
incident light wavelength.30Figures 6Ai,ii and 6Ci,ii display an off-resonant electric field with the EFs
of approximately unity. As shown in Figure 6Aiii–viii, an intense local electric
field is formed on the equator of the Au hemisphere adjacent to the
CdS shell and the TiO2 slab irrespective of the incident
light wavelength. A similar local electric field distribution was
also confirmed for Au@SiO2/ZnO.31 The simulated field distribution can be explained by the lightning
rod effect (LRE), where the electric field at the curved surface is
highly intensified due to the condensation of electric field lines.32 As clearly seen in Figure 6Ciii–viii, the local electric field
for Au@#CdS/mp-TiO2 is confined at the edge and the corner
of the Au nanocube due to LRE likewise. The dominant LSPR mode for
each incident light wavelength was assigned by using structural notation
of B, S, T, E, and C which represent bottom, side, top, edge, and
corner, respectively (Figure 5B inset). The dominant modes are the BE–BC–SE–TC
mode at 591 nm, the BE–BC mode at 673 nm, and the BC mode at
795 nm, respectively. Among these modes, the first and the second
modes are the coupled mode denoted by the hyphened notation of more
than two single modes. As for the first mode, SE–TC modes are
the modes formed in the direction perpendicular to the TiO2 slab (parallel with the z-axis), whereas the BE–BC
modes are the modes existing on the perimeter of the bottom square
of the Au nanocube. Also, the presence of the TE mode that is out
of the monitor planes was confirmed by using the polarized light inclined
45° from the x-axis. Thus, local field enhancement
occurs at the sharpened edges and corners even in the position away
from the TiO2 slab. In contrast, the field enhancement
for Au@CdS/TiO2 is limited in the x–y plane and the mode component distant from the TiO2 slab surface is of negligible magnitude. To inspect SE–TC
modes in more detail, we carried out the FDTD simulation under irradiation
of z-polarized light incident from the x-axis direction. EFxz for Au@#CdS/TiO2 far exceeds that for Au@CdS/TiO2 in a wavelength
over 535 nm (Figure 5D). Figure 6B exhibits
electric field distribution for Au@CdS/TiO2 where intense
local fields are formed on the periphery of the Au hemisphere similar
to the local field excited by x-polarized light incident
from the z-axis direction (Figure 6A). Electric fields are present at the zenith
of the Au hemisphere due to the hemispherical structure resonating
with the incident electric field parallel to the z-axis. Also, asymmetric electric field distribution on the periphery
(Figure 6Bv–viii)
is due to damping of electromagnetic energy toward the surrounding
environment during propagation of the electromagnetic wave from the
right side (+x) to the left side (−x) of the model. The periphery of the hemisphere plays an
exclusive role of propagation pathway of electromagnetic energy, whereas
the curved surface of the hemisphere hardly does. As for Au@#CdS/TiO2, intense electric fields excited due to resonance with z-polarized light are recognized at the top corner of the
Au nanocube (Figure 6D). Interestingly, propagating electric fields do not weaken the
strength even on the outgoing side. Similarly to LSPR excitation by z-incident light, LSPR excitation occurs at the corners
(BC, TC) and edges (BE, TE, SE). From the analysis of the field distribution
and the LSPR modes, we can attribute the enhancement of EFxz for Au@#CdS/TiO2 mainly to the excitation
of SE and TC modes. Symmetric electric field distribution in the cubic
model would result from the presence of complex propagation pathways
consisting of BC, BE, SE, TC, and TE. Complex propagation pathways
such as the one from the right-side SE to the left-side SE through
TC and TE enable efficient energy transfer over the cubic model even
if energy loss occurs during light propagation.
Figure 6 Local electric field
distribution for Au@CdS/TiO2 excited
with (A) x-polarized light incident from the z-axis direction (k//z, E//x) at wavelengths of 401 (i,
ii), 601 (iii, iv), 694 (v, vi), and 728 nm (vii, viii) and (B) z-polarized light incident from the x-axis
direction (k//x, E//z) at wavelengths of 531 (i, ii), 608 (iii, iv),
694 (v, vi), and 723 nm (vii, viii). Local electric field distribution
for Au@#CdS/TiO2 excited with (C) x-polarized
light incident from the z-axis direction (k//z, E//x) at wavelengths of 435 (i, ii), 591 (iii, iv), 673 (v, vi), and
795 nm (vii, viii) and (D) z-polarized light incident
from the x-axis direction (k//x, E//z) at wavelengths
of 584 (i, ii), 651 (iii, iv), 708 (v, vi), and 791 nm (vii, viii).
Upper and lower row images are local electric field distribution monitored
on the x–y and x–z planes, respectively. Inset arrows represent
the relation between k and E. White
broken line is a guide to the eye for the CdS shell surface and the
TiO2 slab surface.
Field enhancement studies for hemispherical and cubic particles
have been reported so far, but are focused on the particles with a
geometrical length of over 10 nm.33−35 This is the first report
comparing the electric field enhancement between hemispherical and
cubic NPs with a size of sub-10 nm, i.e., 8.0 nm in equatorial diameter
for the former and 5.1 nm in edge length for the latter. The cubic
core structure is superior to the hemispherical structure with respect
to the ability to extend the local electric field away from the TiO2 slab surface even on the side opposite to incident light.
The results of FDTD simulation using polarized unidirectional light
illuminated to ideal model systems give an insight to interpret the
spectroscopic and photoelectrochemical data shown in Figure 3A,B which were obtained by
the omnidirectional illumination of unpolarized light on samples.
Thus, the presence of SE and TC modes in Au@#CdS/TiO2 suggests
that the electric interaction between the Au core and the CdS shell
is augmented by replacing the Au hemisphere with the Au nanocube.
2.4 Action Mechanism of Au@#CdS Hybrid QD-SPEC
Cell
The action mechanism of the Au@#CdS/mp-TiO2 system can be basically explained by the near-field enhancement
mechanism (Scheme 1)36 in contrast to the hot-electron transfer
mechanism for water splitting by the half-cut Au@#CdS plasmonic photocatalyst.10 Visible-light irradiation (λ > 430
nm)
excites the electrons in the VB of the CdS shell to the CB. The CB
electrons with a potential of ECB = −1.12
V (vs standard hydrogen electrode (SHE))37 are injected into the CB of TiO2 (ECB = −0.95 V at pH 14).38 Under irradiation conditions, the LSPR of the Au core is excited
simultaneously. The intense near-field generated at the Au/CdS and
Au/TiO2 interfaces can enhance the electron injection via
both path 1 and path 2 because the transition rates are proportional
to the square of the local electric field.39 For the effective operation of this enhancement mechanism, the spectral
overlap between the LSPR of the Au core and the interband transition
of the CdS shell or the electron transition from the VB of CdS to
the CB of TiO2 is necessary.40 First, the spectral overlap and the EFs in the energy region increase
with the deformation of the Au core from hemisphere to an angular
shape (Figures 3A and 5). Second, the angular shape Au core extends the
electric field distribution over the Au core–CdS shell (Figure 6C,D). The near field
of the Au core can also enhance the charge separation.41 Third, the assumption that the Au core-induced
local electric field in the direction normal to the TiO2 surface (z in Figure 5) mainly assists the electron injection from
CdS to the CB of TiO2 explains the longer lifetime of the
electrons or the more effective charge separation for Au@#CdS/mp-TiO2 than Au@CdS/mp-TiO2 (Figure 4B). Fourth, the higher crystallinity of the
CdS shell in Au@#CdS/mp-TiO2 would further contribute to
its excellent performance since the recombination through the defects
can be minimized. On the other hand, the holes in the VB of CdS (EVB = +1.30 V) easily oxidize S2– ions (E0(S2–/S) =
−0.45 V).42 These shape effects
of the Au core rationalize the excellent performances of the Au@#CdS
hybrid QD-SPEC cell for H2 generation from water.
Scheme 1 Action
Mechanism of the Au@#CdS/mp-TiO2 Photoanode in
the QD-SPEC Cell for H2 Generation
The
potential is shown with respect
to the standard hydrogen electrode (SHE).
3 Conclusions
This study has shown that the CdS photodeposition
on Au/TiO2 at as low as 50 °C leads to shape change
in the Au NP
from hemisphere-like shape to an angular shape with the formation
of a HEPI junction between Au and CdS (Au@#CdS/TiO2). Striking
shape effects are presented in the performance of the QD-SPEC cell
using Au@#CdS/TiO2 as the photoanode for H2 generation
from water under simulated sunlight. We anticipate that the versatility
of the present hot photodeposition technique40 widely contributes to the improvement in the solar-to-chemical conversion
efficiency of not only the QD-SPEC cells but also for heteronanostructured
photocatalysts.
4 Experimental Section
4.1 Sample Preparation
Mesoporous TiO2 thin
films (mp-TiO2) were prepared using a previously
reported procedure.27 An anatase TiO2 paste (20 nm in a mean particle size,
PST-18NR, Nikki Syokubai Kasei) was coated on fluorine-doped tin oxide
film-coated glass substrates (<10 Ω/square) by a squeegee
method, and air calcination at 773 K was conducted for the as-coated
samples to form a mesoporous structure in the film. The mp-TiO2 films thus prepared and anatase TiO2 particles
(A-100, specific surface area = 8.1 m2 g–1, Ishihara Sangyo) were used as supports of Au NPs. Au NP-loaded
TiO2 (Au/TiO2) was prepared by the deposition–precipitation
method. An aqueous solution of HAuCl4 (0.243 mM, 100 mL)
was neutralized by 1 M aq NaOH to be pH 6. To this solution, mp-TiO2 or TiO2 particles were added and stirred at 70
°C for 1 h. The resulting film or precipitate was harvested from
the solution and rinsed with distilled water. The sample was dried
in vacuo at room temperature and heated at 500 °C for 1 h to
obtain Au/mp-TiO2 and Au/TiO2. Au@CdS/(mp-)TiO2 and Au@#CdS/(mp-)TiO2 were prepared by photodeposition
of the CdS shell layer on the Au-loaded TiO2 film or particles.
The Au-loaded sample was immersed in a solution of S8 (1.36
mM) and Cd(ClO4)2 (13.6 mM) in EtOH (200 mL),
and deaerated by Ar bubbling for 0.5 h in the dark. UV irradiation
(λ > 320 nm, I310–400 =
3.6
mW cm–2) was carried out with a high-pressure mercury
lamp (H-400P, Toshiba) at 298 K for the preparation of Au@CdS/(mp-)TiO2 and at 323 K for the preparation of Au@#CdS/(mp-)TiO2 by varying the photodeposition time (tPD), respectively. After irradiation, the films were taken
out from the solution and the particles were harvested by centrifugal
separation from the solution. The obtained films and particles were
rinsed with ethanol repeatedly to be stored at ambient temperature
after vacuum drying. CdS-deposited mp-TiO2 (CdS/mp-TiO2) was prepared by the photodeposition method for the pristine
mp-TiO2 film.
4.2 Characterization
The loading amounts
of Au and CdS were quantified by inductively coupled plasma spectroscopy
(ICPS-7500, Shimadzu). X-ray diffraction (XRD) analysis was carried
out with a Rigaku SmartLab X-ray diffractometer. Diffuse reflectance
UV–vis spectra of the samples were recorded on a UV-2600 spectrometer
(Shimadzu) with an integrating sphere unit (Shimadzu, ISR-2600Plus)
at room temperature. BaSO4 was used as a reference material
to evaluate the reflectance (R∞) of the samples. The reflectance was transformed to the Kubelka–Munk
function [F(R∞)] presenting the relative absorption coefficient by the equation F(R∞) = (1 – R∞)2/2R∞.43 Transmission electron
microscopy (TEM) measurements were performed using a JEOL JEM-2100F
at an applied voltage of 200 kV. X-ray photoelectron (XP) spectroscopy
measurements were performed using a Kratos Axis Nova X-ray photoelectron
spectrometer with a monochromated Al Kα X-ray source (hν = 1486.6 eV) operated at 15 kV and 10 mA. The takeoff
angle was 90°, and multiplex spectra were obtained for Cd 3d
and Au 4f photopeaks.
4.3 Photoelectrochemical Measurements
The solar-to-current efficiency (STCE) was measured for a two-electrode
QD-SPEC cell consisting of CdS/mp-TiO2, Au@CdS/mp-TiO2, and Au@#CdS/mp-TiO2 (photoanode)|0.25 M Na2S + 0.35 M Na2SO3 (aqueous electrolyte
solution)|Pt (cathode). Photocurrents (Jph) of the cell were evaluated under illumination by a solar simulator
(PEC-L10, Peccell technologies, Inc.) at one sun (λ > 430
nm,
AM 1.5, 100 mW cm–2). Upon photoelectrochemical
measurement, a bias voltage (Eapp) in
the range between 0 and 0.23 V was applied to the cell. Also, argon
bubbling was carried out to remove the oxygen in the solution. A three-electrode
PEC cells consisting of CdS/mp-TiO2, Au@CdS/mp-TiO2, and Au@#CdS/mp-TiO2 (working electrode)|0.25
M Na2S + 0.35 M Na2SO3 (aqueous electrolyte
solution)|Ag/AgCl (reference electrode)|Pt (counter electrode) were
constructed to record the action spectra of IPCE. A 500 W-Xe short
arc lamp (UXL-500D-O, Ushio Inc.) was used as a light source to illuminate
one sun (λ > 430 nm, AM 1.5, 100 mW cm–2)
onto the cell. J–E curves
for the PEC cells under light illumination or in the dark were measured
with a potentiostat/galvanostat (HZ-5000, Hokuto Denko). The action
spectra of IPCE were recorded under illumination of monochromatic
light from a xenon lamp through a monochromator (full width at half-maximum
= 10 nm, HM-5, JASCO). The short-circuit current at the rest potential
was measured as a function of excitation wavelength (λ/nm).
Calculation formula for the incident photon-to-current efficiency
(IPCE) is shown below (3) 3 where Jph(E), NA, I (W
cm–2), F, h, and c are the photocurrent at an electrode potential of E, Avogadro constant, light intensity, Faraday constant,
Planck constant, and speed of light, respectively.
4.4 Three-Dimensional FDTD Simulations
Local electric field
distribution and wavelength dependence of the
enhancement factor (EF) for Au@CdS/mp-TiO2 and Au@#CdS/mp-TiO2 were simulated by the 3D FDTD-method Maxwell solver using
FDTD Solutions (Lumerical Solutions, Inc.). Au@CdS/mp-TiO2 was modeled by a CdS hemispherical shell-covered Au hemispherical
particle placed on a TiO2 slab (500 × 500 × 50
nm3). The diameter of the Au core particle and the thickness
of the CdS shell were set to be the experimental values (8 and 7.7
nm), respectively. For Au@#CdS/mp-TiO2, the Au core particle
was modeled by a nanocube incorporated into the CdS hemispherical
shell. The volumes of the Au nanocube (5.1 × 5.1 × 5.1 nm3) and the surrounding CdS shell for Au@#CdS/mp-TiO2 were kept the same as the corresponding volumes for Au@CdS/mp-TiO2. The origin of the Cartesian coordinate (x = y = z = 0) was located at the
midpoint of the cross-sectional plane of the Au hemisphere and the
center of the bottom rectangle of the Au nanocube. The position of
the top surface of the TiO2 slab was fixed at z = 0. The near-field enhancement for the models was simulated using
the total-field scattered-field source. In the simulation, a polarized
light source with the wavelength from 300 to 900 nm (f = 200–353 THz) was irradiated to the core–shell hemisphere
from the normal direction (wave vector k//z) or the parallel direction (k//x) to the TiO2 slab. The light incidence of k//z and k//x was performed with polarization along the x-axis
(E//x) and z-axis
(E//z), respectively. For the purpose
of improving the accuracy of simulation, the mesh override region
with a finer mesh size than that in the previous study41 was set to the core–shell hemispheres.
The simulation region was surrounded by a perfectly matched layer
absorbing boundary to remove unwanted light reflection at the simulation
boundary. To minimize the computational time, antisymmetric and symmetric
boundary conditions were used in the x-axis and y-axis directions, respectively. The enhancement factor
is defined by the following equation: EF = |E|2/|E0|2, where |E| and |E0| are the amplitude
of the local maximum electric field and the amplitude of incident
electric field, respectively. Optical constants for Au, CdS, and TiO2 used in the simulation were taken from refs (44−46). The refractive index of surrounding medium was set
to be a value of air (n = 1.0).
Supporting Information Available
The Supporting Information
is available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b00818.TEM image, photochronoamperometry
curves (PDF)
Supplementary Material
ao8b00818_si_001.pdf
The
authors
declare no competing financial interest.
Acknowledgments
The authors
acknowledge Dr. S. Naya for helpful discussion.
This work was partially supported by a Grant-in-Aid for Scientific
Research (C) no. 15K05654, and the MEXT-Supported Program for the
Strategic Research Foundation at Private Universities.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145808710.1021/acsomega.8b01714ArticleLanthanum Hydroxide Nanorod-Templated Graphitic Hollow
Carbon Nanorods for Supercapacitors Wang Zijie Perera Wijayantha A. Perananthan Sahila Ferraris John P. Balkus Kenneth J. Jr.*Department of Chemistry and
Biochemistry, The University of Texas at
Dallas, 800 West Campbell Road, Richardson, Texas 75080-3021, United States* E-mail: balkus@utdallas.edu.23 10 2018 31 10 2018 3 10 13913 13918 20 07 2018 11 10 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
Lanthanum
hydroxide nanorods were employed as both a template and
catalyst for carbon synthesis by chemical vapor deposition. The resulting
carbon possesses hollow nanorod shapes with graphitic walls. The hollow
carbon nanorods were interconnected at some junctions forming a mazelike
network, and the broken ends of the tubular carbon provide accessibility
to the inner surface of the carbon, resulting in a surface area of
771 m2/g. The hollow carbon was tested as an electrode
material for supercapacitors. A specific capacitance of 128 F/g, an
energy density of 55 Wh/kg, and a power density of 1700 W/kg at 1
A/g were obtained using the ionic liquid, 1-ethyl-3-methylimidazolium
bis(trifluoromethylsulfonyl)imide, as the electrolyte.
document-id-old-9ao8b01714document-id-new-14ao-2018-01714qccc-price
==== Body
Introduction
Graphene-based materials
with designed nanoarchitectures have been
studied for a wide range of applications.1,2 Many
methodologies have been established to prepare three-dimensional or
porous carbons with graphitic walls to achieve high surface area and
high conductivity, which are of great importance for electrical double-layer
capacitors.3−7 The hydrophobic nature and high surface area of carbon-based materials
also provide advantages when employed as catalyst supports, which
allows better adsorption and diffusion of reactions.8,9 Among these carbon materials, templated carbon has been prepared
using hard templates, such as zeolites and mesoporous silica.10−16 Unfortunately, most of them have amorphous carbon framework, which
limited their use in energy storage as well as catalysis.17 Graphene- and carbon nanotube (CNT)-based carbon
electrodes with porous or three-dimensional structures have shown
excellent performance in supercapacitors.18−22 Therefore, it is of great interest to make templated
carbon with graphene-like walls for energy storage and other applications.
Mesoporous silica has been used with various organic precursors to
produce carbons with improved graphitic content.17 Recently, a lanthanum-exchanged zeolite was reported to
be an excellent template for carbon synthesis.23 The resulting carbon replicated the zeolite pore structure
with graphene-like walls and conductivity comparable to gold. It is
assumed that the carbon source reacts with La first to form LaC2, which is then turned to La(OH)3 by reacting with
steam leading to the growth of graphitic carbon (Figure 1). This work demonstrated the
application of La as a catalyst for the synthesis of graphitic carbon
with controlled morphology and structure. In the present study, pure
lanthanum hydroxide nanorods (LaNR) were employed as templates to
produce hollow carbon nanorods. Compared to the La-zeolite, the pure
lanthanum hydroxide templates are removed by HCl, and the resulting
solution can be used to make new nanorods.
Figure 1 Schematic illustration
of the carbon formation mechanism on La(OH)3 surface.
Results and Discussion
The LaNRs
were hydrothermally synthesized using a solution of La(NO3)3·6H2O and NaOH at 110 °C
for 24 h followed by centrifugation, drying, and annealing at 200
°C for 1 h. The lanthanum hydroxide nanorod-templated carbon
(LaNRTC) was synthesized by chemical vapor deposition (CVD) using
acetylene and steam at 600 °C. Washing with concentrated HCl
removes the La(OH)3 template leaving hollow replicas of
the nanorods.
The LaNR shown in Figure 2a,d possesses a rod shape with an average
diameter of 16 nm
and an average length of 140 nm. The lattice fringes of LaNR (Figure 2b) have a d-spacing of 0.285 nm, corresponding to the (200) face of
La(OH)3 (JCPDS 36-1481). Figure 1b,e shows the morphology of the templated
carbon before removal of LaNR. The transmission electron microscopy
(TEM) image shows that carbon covers the surface of the LaNR. The
scanning electron microscopy (SEM) image (Figure 2b) shows better contrast compared to that
of the pure LaNR since the carbon covered on the surface of LaNR is
conductive. These images indicate that the carbon was grown only on
the surface of LaNR without formation of amorphous carbon elsewhere.
This demonstrates that the La(OH)3 serves as both a template
and catalyst for carbon growth, which is consistent to our previous
work that no carbon was formed under the same conditions if only mesoporous
silica was placed in the reactor.24 And
after La(OH)3 was deposited on mesoporous silica, carbon
was formed along the surface of the templates. After removal of the
LaNR by using acid, the resulting carbon retains the rod shape morphology
with similar particle size (Figure 2c), and the inner space is empty as shown in the TEM
image (Figure 2f).
The acid may access LaNR through defects in the carbon coating, leading
to openings in the tubular carbon network. The edge of the resulting
carbon exhibits lattice fringes with a d-spacing
of 0.40 nm attributed to the (002) planes of graphitic carbon, indicating
the graphitic nature of the lanthanum hydroxide nanorod-templated
carbon. The d-spacing is bigger than graphite (0.34
nm) due to less than five graphene layers on the edge of the carbon,
where the d-spacing has been reported to increase
as the number of the graphene layers decreases.25
Figure 2 SEM and TEM images of (a, d) lanthanum hydroxide nanorods (LaNR);
lanthanum hydroxide nanorod-templated carbon (b, e) before (C@LaNR)
and (c, f) after (LaNRTC) template removal.
The LaNRTC after template removal shows a broad peak around
22°
in the X-ray diffraction (XRD) and the corresponding d-spacing is calculated using Bragg equation, which is consistent
to the d-spacing measured in the TEM image. This
is attributed to the (002) planes of the carbon, whereas the LaNR
and C@LaNR mainly exhibit XRD patterns for nanocrystalline La(OH)3 (JCPDS 36-1481) (Figure 3a). This is also consistent to the TEM images (Figure 2), where the LaNRTC
shows a few layers of carbon. The Raman spectra exhibit a strong G
band (∼1600 cm–1) with a IG/ID ratio of 1.03. Previously,
a La-zeolite-templated carbon was reported to possess five- or seven-member
rings, which contributed to the peaks for disordered carbon (D band),
but they are still sp2 hybridized.23 In that case, the overall carbon material has graphitic framework
with good conductivity. Combining the results from TEM and Raman,
the LaNRTC possesses graphitic walls.
Figure 3 (a) Powder X-ray diffraction patterns
of LaNR, C@LaNR, and LaNRTC;
(b) Raman spectrum of LaNRTC; (c) N2 adsorption–desorption
isotherms of LaNR and LaNRTC; (d) density functional theory (DFT)
pore size distributions of LaNR and LaNRTC.
Figure 3c
shows
the N2 adsorption–desorption isotherms for the LaNR
template and the resulting carbon, LaNRTC. The isotherm of the pure
LaNR shows a type II isotherm with a low Brunauer–Emmett–Teller
(BET) surface area of 54 m2/g, indicating no porosity but
space between nanoparticles. In contrast, the LaNRTC shows a type
IV isotherm corresponding to mesoporous features with a clear hysteresis
between 0.4 and 1.0. The adsorption below 0.1 also indicates some
microporosity. The BET surface area of the LaNRTC is much higher than
that of the pure LaNR (771 vs 54 m2/g). The micropore volume
and total pore volume of LaNRTC is much higher than LaNR, as shown
in Table S1. Both LaNRTC and LaNR show
similar DFT pore size distribution, which might due to the absence
of uniform pore structure (Figure 3d). The large increase in surface area is due to the
transformation of the morphology from rods to tubular network with
accessibility to inner surface of the tubes. The TEM images in Figure 4 show both closed
ends and open ends. The open ends result in pore openings as large
as 30 nm (Figure 4).
Micropores resulting from defects are not apparent in these images.
Additionally, some of the tube junctions were fused together as interconnected
L-shaped channels. It is assumed that the carbon grows from one rod
to the other across the tightly packed junctions rather than just
covering an individual rod. This arises because during the CVD process
the carbon cannot completely coat the randomly stacked La(OH)3 nanorods. Thus, there are hollow nanorods and a complicated
tubular carbon network. Overall, the material is composed of carbon
tubes, tube stacks, and fused mazelike nano carbon tube networks.
The large increase in the surface area from pure LaNR to LaNRTC is
much higher than that of most CNTs (<500 m2/g).7 The TEM images in Figure 4 also represent the relationship between
the nanorods template and the pore structure of resulting carbon.
Since the synthesis of La(OH)3 nanorods with various sizes
and shapes has not been well established, the pore structure is not
controlled by different La(OH)3 templates here, but it
is of great interest for future work. The hollow carbon tubes with
different length and diameters are presented in Figure 4, and they are formed on La(OH)3 nanorods with various sizes. The size of La(OH)3 nanorods
controls the resulting carbon’s dimensions and inner diameters,
which affect the porosity of each carbon tube in the same batch. By
using different La(OH)3 templates, it is possible to control
the pore structure of the resulting carbon in bulk.
Figure 4 Schematic illustration
of the formation and TEM images of broken
ends and connected junctions in the LaNRTC.
The LaNRTC was tested as an electrode material for supercapacitors
using 1-ethyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide
(EMIM-TFSI) as the electrolyte. Figure 5a shows the cyclic voltammograms (CVs) of the LaNRTC
at different scan rates (10, 25, 50, 75, and 100 mV/s) in the range
of −2.0–2.0 V.26−29 The shape of the CV is nearly rectangular indicating
ideal double-layer capacitive behavior. The capacitances of the electrodes
were calculated from CV using the following equation where I is the current as
a function of time, υ is the scan rate. The specific capacitance
in different scan rates was calculated using following equation where m is mass of both electrodes.
The highest specific capacitance obtained for the LaNRTC was 128 ±
2 F/g at 10 mV/s. Table 1 summarizes the obtained specific capacitance values at different
scan rates. To compare the LaNRTC with a mesoporous carbon templated
by mesoporous silica, wrinkled mesoporous carbon was prepared according
to reported procedure.24 The capacitance
of LaNRTC is higher than the mesoporous carbon templated by La2O3 supported on wrinkled mesoporous silica (Figure S1), which has a capacitance of 70 F/g.
The capacitance of LaNRTC is among the best results for mesoporous
graphenes,20,30−36 and aligned CNTs18,37 as well as activated carbons38−41 using ionic liquids as the electrolyte. Unlike these carbons, the
LaNRTC does not require complicated porous silica templates, lengthy
preparation process, or additional activation steps. And the ionic
liquids allow a higher operating voltage window, which is more practical
for various applications.
Figure 5 Electrochemical characterizations of LaNRTC:
(a) cyclic voltammograms;
(b) charge–discharge curves from 1 to 6 A/g; (c) Nyquist plots;
(d) Ragone plot; (e) specific capacitance retention as a function
of cycle number.
Table 1 Specific
Capacitance (F/g) in Different
Scanned Rates
scan rates (mV/s) specific
capacitance (F/g)
10 128.1
25 126.2
50 125.0
75 122.6
100 120.2
Figure 5b shows
the charge–discharge curves for the LaNRTC in different current
densities (1–10 A/g). The JME cells were charged to 3.5 V and
discharged completely at different current densities. Linear discharge
curves show the ideal capacitive behavior. After charging up to 3.5
V, it is important to stabilize the coin cell before it starts to
discharge. A plateau at 3.5 V is purposely introduced to investigate
the stability of the coin cell. At 1 A/g, the IR drop
is ∼0.2 V, which shows the good conductive behavior of the
JME cell. Energy densities (Ed) and power
densities (Pd) were calculated using following
equations where t is the time taken
to discharge to 0 V from the initial voltage (ΔV), subtracting IR drop at the beginning of discharge.
The energy density and power density of the LaNRTC were found to be
55 Wh/kg and 1700 W/kg, respectively, at 1 A/g. In contrast, the mesoporous
carbon templated by La2O3 supported on wrinkled
mesoporous silica (Figure S1) has an energy
density of 35.8 Wh/kg and a power density of 1499 W/kg at 1 A/g.
Figure 5c shows
the Nyquist plots for the LaNRTC in EMITFSI electrolyte. Electrochemical
impedance spectroscopy (EIS) can provide information such kinetics
in the double-layer charging–discharging processes. The almost
vertical increase in the lower frequency region is indicative of an
ideal capacitance behavior. In the Nyquist plot, the x axis intercepts at the highest frequency region indicating bulk
electrolyte resistance, which mainly depends on the electrolyte solution.
Figure 5d shows
the Ragone plot of the LaNRTC, polyacrylonitrile (PAN) nanofibers,42 and carbon nanotubes (CNTs) at different current
densities 1–10 A/g by comparing energy densities and power
densities. Energy densities were determined by discharging from 3.5
to 0 V. When the current density increases, the energy density decreased,
but retained 90% of its original energy density at discharge rate
of 10 A/g, whereas PAN and CNTs retained only 75 and 80%, respectively.
The energy density of the LaNRTC is much higher than PAN nanofibers
and the pure CNTs, as shown in Figure 5d.
Figure 5e shows
the plot of specific capacitance retention against cycle number. After
the 100th cycle, 98% of the specific capacitance was retained, whereas
97% of the capacitance was retained after 1000th cycle. Capacitance
(89%) was retained after 5000th cycles, indicating the good cycling
ability. This combined with the high energy density, and power density
of the LaNRTC makes this carbon a good electrode material for supercapacitors.
Conclusions
In conclusion, the lanthanum hydroxide nanorods function as both
catalyst and template for carbon growth, resulting in hollow carbon
nanorods. The hollow carbon nanorods possess connected junctions and
open ends, which result in a mazelike structure with high surface
area and porosity. The LaNRTC shows excellent performance as an electrode
material for supercapacitors taking advantage of its unique structure
as well as low resistance. The templating method using lanthanum hydroxide
nanoparticles also creates possibilities for the preparation of other
graphitic carbons with controlled morphology.
Experimental Section
Synthesis
of La(OH)3 Nanorods
In a typical
synthesis, 5.77 g of La(NO3)3·6H2O in 10 mL of deionized water was mixed with a solution of 14.7 g
of NaOH in 20 mL of water and heated to 110 °C in a 45 mL Teflon-lined
autoclave for 24 h. The solid product was collected by centrifugation
and washed with water several times then dried overnight at 100 °C.
The product was then annealed at 200 °C for 1 h.
Synthesis of
La(OH)3 Nanorod-Templated Carbon
The La(OH)3 nanorods (∼1 g) were placed in a ceramic
boat centered in a horizontal quartz tube reactor. The reactor was
heated to 600 °C under N2 (200 mL/min). Then, acetylene
(30 mL/min) and steam (water is pumped at 5 mL/h) were fed into the
reactor for 1.5 h followed by carbonization under N2 at
850 °C for 2 h. The resulting carbon/La(OH)3 composite
was washed with concentrated HCl and water to remove the La(OH)3 template. For comparison, a mesoporous carbon was prepared
with the same method, but by using La(OH)3 supported on
wrinkled mesoporous silica as the template following reported procedure.24
Fabrication of Coin Cell-Type Supercapacitors
Symmetric
JME cells were fabricated according to a previously reported procedure
for JME packaging (Figure S2).43 Electrodes were prepared by mixing the La(OH)3 nanorod-templated carbon with 2% poly(tetrafluoroethylene)
binder. The carbon electrodes were immersed in the electrolyte, 1-ethyl-3-methylimidazolium
bis(trifluoromethylsulfonyl)imide (EMIM-TFSI), for 1 h at room temperature
under vacuum prior for assembling the coin cell. The two electrodes
were separated by a Teflon film (0.02 mm) and constructed under inert
environment.
Characterization
Scanning electron
microscope (SEM)
images were recorded on a Zeiss-LEO model 1530 scanning electron microscope.
Transmission electron microscope (TEM) images were recorded using
a JEOL 2100 transmission electron microscope. Powder X-ray diffraction
(XRD) patterns were acquired on a Rigaku Ultima IV diffractometer
using Cu Kα radiation. Raman spectra was obtained on a Jobin
Yvon Horiba high-resolution LabRam Raman microscope. The N2 adsorption–desorption isotherms and BET surface areas were
measured using a Quantachrome AS1 Autosorb. Electrochemical measurements
were made using a BT2000 Arbin battery testing system. Electrochemical
impedance spectroscopy (EIS) was measured on a EG&G Princeton
Applied Research potentiostat/galvanostat.
Supporting Information Available
The Supporting Information
is available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b01714.Experimental details
on the synthesis and characterizations
of lanthanum hydroxide nanorods and lanthanum hydroxide nanorod-templated
carbon as well as details of coin cell fabrication (PDF)
Supplementary Material
ao8b01714_si_001.pdf
Author Contributions
The manuscript
was written through contributions of all authors. All authors have
given approval to the final version of the manuscript.
The authors
declare no competing financial interest.
Acknowledgments
We thank
the financial support from Robert A. Welch Foundation
(AT-1153).
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145888610.1021/acsomega.8b00948ArticleKinetics of Catalytic Wet Peroxide Oxidation of Phenolics
in Olive Oil Mill Wastewaters over Copper Catalysts Maduna Karolina †‡Kumar Narendra ‡Aho Atte ‡Wärnå Johan ‡Zrnčević Stanka †Murzin Dmitry Yu. *‡† Faculty
of Chemical Engineering and Technology, Department of Reaction Engineering
and Catalysis, University of Zagreb, Marulicev trg 19, 10000 Zagreb, Croatia‡ Faculty
of Science and Engineering, Laboratory of Industrial Chemistry and
Reaction Engineering, Åbo Akademi University, Biskopsgatan 8, FI 20500 Turku-Åbo, Finland* E-mail: dmurzin@abo.fi.03 07 2018 31 07 2018 3 7 7247 7260 09 05 2018 21 06 2018 Copyright © 2018 American Chemical
Society2018American Chemical
SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
During olive oil extraction, large
amounts of phenolics are generated
in the corresponding wastewaters (up to 10 g dm–3). This makes olive oil mill wastewater toxic and conventional biological
treatment challenging. The catalytic wet peroxide oxidation process
can reduce toxicity without significant energy consumption. Hydrogen
peroxide oxidation of phenolics present in industrial wastewaters
was studied in this work over copper catalysts focusing on understanding
the impact of mass transfer and establishing the reaction kinetics.
A range of physicochemical methods were used for catalyst characterization.
The optimal reaction conditions were identified as 353 K and atmospheric
pressure, giving complete conversion of total phenols and over 50%
conversion of total organic carbon content. Influence of mass transfer
on the observed reaction rate and kinetics was investigated, and parameters
of the advanced kinetic model and activation energies for hydrogen
peroxide decomposition and polyphenol oxidation were estimated.
document-id-old-9ao8b00948document-id-new-14ao-2018-00948mccc-price
==== Body
1 Introduction
Phenols
are important industrial chemicals widely used as reactants
and solvents in numerous commercial processes and therefore are often
present in industrial effluents. The major anthropogenic sources of
phenol-contaminated wastewaters are petrochemical, pharmaceutical,
wood, pulp, and paper and food processing industries as well as landfill
and agricultural area leachate waters.1 There are several environmental concerns regarding phenols; thus,
they are considered to be hazardous in industrial wastewaters, harmful
even at low concentration levels (ppm range). Wastewaters containing
phenols should therefore undergo a special treatment. In EU, the current
limits for wastewater emission of phenols are 0.5 mg dm–3 (0.5 ppm) for surface waters and 1 mg dm–3 (1
ppm) for sewage systems with maximum allowed concentration levels
in potable and mineral waters of 0.5 μg dm–3 (0.5 ppb).
Significant quantities of phenolics are generated
in olive oil
mill wastewater (OOMW) including organic contaminants such as lignin,
tannins, and polyphenolic compounds. Significant amounts of olive
mill wastewater exceeding several million tons are produced in Europe
alone despite stringent legislation2 and
are not properly treated. The properties of OOMWs depend on the method
of extraction, feedstock properties, and region and climate conditions.
In general, OOMW is a dark brown acidic effluent (pH = 4.0–5.5),
with a distinctive odor and high conductivity, comprising besides
water (80–83%) organic compounds (15–18%) and inorganic
elements (2%, potassium salts and phosphates). The concentration of
phenols and polyphenols in OOMW can be as high as 20 wt %.3 Although several studies were reported on removal
of phenolics in OOMW,4 significant efforts
are still needed. Often separation-based technologies are suggested
as an alternative to biological processes, however, their effective
application can be hindered by high operational costs and sustainability
concerns such as generation of secondary toxic wastes because the
toxic compounds are not destroyed but only separated.5 Therefore, in the current work, the focus was on catalytic
approaches to diminish the content of phenolics in OOMW.
In
particular, the catalytic wet peroxide oxidation (CWPO) process
is a suitable method6 generating hydroxyl
radicals during hydrogen peroxide decomposition. Hydrogen peroxide
is generally considered as a nontoxic and ecologically attractive
oxidant. Application of heterogeneous catalysts, such as zeolites,7 in CWPO of organic compounds has been reported.
Transition metal-exchanged (mostly iron and copper) zeolites of FAU
or MFI morphology showed promising results; however, there are still
some open issues such as resistance to leaching of the active metal
during the reaction. Apart from few recent reports,8−11 most of the studies describe
application of powdered catalysts for which mass transfer limitations
can be neglected.7,12,13 It is apparently clear that scaling up of a commercial CWPO process
requires detailed studies with the pelletized catalysts. In this case,
external and internal mass transfers (i.e., diffusion processes in
the boundary layer surrounding the catalyst pellet and in the pores
of the catalyst) should be properly considered.
In this work,
the activity of copper-containing catalysts was tested
in catalytic wet peroxide oxidation of OOMW with a special attention
to the stability of copper during the reaction, namely, its resistance
to leaching. The influence of interparticle and intraparticle diffusion
was investigated, and the reaction kinetics parameters of the proposed
pseudo-second-order kinetic model were estimated.
2 Experimental Section
2.1 Catalyst Preparation
A series of
copper-containing 13X zeolite catalysts were prepared by postsynthesis
ion-exchange from the sodium form of the commercial 13X zeolite acquired
from UOP Italy (13X-APG Molsiv, SiO2/Al2O3 = 3.2, wNa2O = 20
wt %, dB, range ≤ 2 mm).
Depending on the bead size, between 2.5 and 10 g dm–3 zeolite was ion-exchanged with a 0.05 M copper acetate solution
under agitation at 298 K for 0.5 to 3 h, followed by filtration of
the samples and drying overnight at room temperature to obtain copper-bearing
zeolites with a similar metal content. The detailed preparation method
was described previously.14 After copper
ion-exchange, postsynthesis thermal treatment was performed consisting
of calcination at 1273 K for 5 h (ramp 2 K min–1) to achieve materials exhibiting a higher stability against the
loss of the active metal component during the reaction. The list of
prepared catalysts and their designated names is presented in Table 1.
Table 1 Overview of Prepared Catalysts and
Their Preparation Procedures and Designated Names
sample bead size
range mm preparation
method copper content, wt % (UV–vis)
Cu/13X-1 0.40–0.63 ion exchange (10 g dm–3, 2 h) 8.6
Cu/13X-K1273-1 ion exchange + calcination at 1273 K
Cu/13X-2 0.315–0.40 ion exchange (10 g dm–3, 0.5 h) 7
Cu/13X-K1273-2 ion exchange + calcination at 1273 K
Cu/13X-3 0.63–0.80 ion exchange (10 g dm–3, 3 h) 8
Cu/13X-K1273-3 ion exchange + calcination at 1273 K
Cu/13X-4 0.10–1.00 ion exchange (10 g dm–3, 3 h) 7
Cu/13X-K1273-4 ion exchange + calcination at 1273 K
Cu/13X-5 1.25–2.00 ion exchange (2.5 g dm–3, 1 h) 7
Cu/13X-K1273-5 ion exchange + calcination at 1273 K
2.2 Catalyst Characterization
Textural
characterization of the catalysts was performed by nitrogen physisorption
at 77 K using a Sorptomatic 1900 Carlo Erba instrument. Prior to measurements,
the samples were outgassed at 423 K for 3 h at reduced pressure below
0.1 mbar. The specific surface area and pore volume calculations were
performed using Dubinin’s equation for microporous and Brunauer–Emmett–Teller
equation for mesoporous samples. Pore size distributions were acquired
using the Horvath–Kawazoe method.
The crystalline structures
of the parent zeolite- and prepared zeolite-based catalysts containing
copper were evaluated by powder X-ray diffraction (XRD) analysis on
a XRD 600, Shimadzu instrument. Cu Kα was used as the radiation
source at the wavelength of 0.154 nm with 2θ from 5 to 60°
with a 0.02° step size. The peak identification was performed
using X’Pert HighScorePlus software.
The morphology of
the fresh- and spent-zeolite-based copper catalysts
Cu/13X and Cu/13X-K1273 was studied using scanning electron microscopy
(SEM) and transmission electron microscopy (TEM). SEM analysis was
performed on carbon-coated samples using a LEO Gemini 1530 instrument
equipped with a Thermo Scientific UltraDry Silicon Drift Detector.
The transmission electron microphotographs were taken by a JEM-1400
Plus transmission electron microscope (TEM) operated at 120 kV acceleration
voltage. The powdered samples were suspended in 100% ethanol under
ultrasonic treatment for 10 min. For each sample, a drop of ethanol
suspension was deposited on a Cu fiber carbon grid (200 mesh) and
evaporated, after which the images were recorded.
Copper loading
was measured using a UV/vis spectrometer (UV1600PC,
Shimadzu) at 270 nm for the parent solution of copper acetate applied
during ion exchange and later confirmed by energy-dispersive X-ray
microanalysis (EDXA) during SEM analysis and by inductively coupled
plasma-optical emission spectrometry (ICP-OES) (PerkinElmer, Optima
5300 DV) after dissolution in HF.
The basicity of the prepared
catalysts was elucidated using temperature-programmed
desorption (TPD) of CO2 on AutoChem 2010 (Micromeritics
Instruments) in the temperature range of 373–1173 K according
to the method described by Kumar et al.15
Infrared spectroscopy (ATI Mattson FTIR) was applied to elucidate
the strength of Brønsted and Lewis acid sites using the KBr pellet
technique working in the range of wavenumbers of 4000–400 cm–1 with pyridine as the probe molecule. A detailed description
of the analytical procedure is available.16
2.3 Catalytic Experiments
The catalytic
experiments were carried out under atmospheric pressure in a 250 cm3 glass batch reactor equipped with a pH electrode and a temperature
sensor. The stirring speed in the range between 50 and 800 min–1 and catalyst particle sizes from ca. 0.3 to 2.0 mm
were varied to address the impact of mass transfer. For elucidation
of reaction kinetics, the catalyst loading, reaction temperature,
and hydrogen peroxide concentration were varied. OOMW was supplied
by a private oilery (Dalmatia Region, Croatia) from a three-phase
extraction process of olive oil production from green olive stock
mixture (local sort Olea europaea var. oblica). Basic properties of the wastewater are presented
in Table 2.
Table 2 OOMW Properties at Source (293 K)
pH γTOC, g dm–3 COD, g O dm–3 γTPh, g dm–3 total solids, g dm–3
4.79 10.7 36 1.8a 27
a Total phenols content constitutes
17 wt % total organic carbon (TOC) content of the OOMW.
Prior to reactions, OOMW was filtered
through a 100 μm nylon
filter bag and diluted with distilled water (v/v = 50:50). UV–vis
absorbance was applied to monitor the concentration of phenolics and
hydrogen peroxide. The standard Folin–Ciocalteu method at 765
nm described in the literature17 was used
to measure the total phenol concentration. A standard curve of gallic
acid was used for quantification, and the results were expressed as
gallic acid equivalent (GAE) concentrations. The ammonium metavanadate
spectrophotometric method at 450 nm adopted from ref (18) was used for measuring
hydrogen peroxide concentrations. The measured absorbances were recalibrated
with reference to OOMW sample blanks not containing phenols or hydrogen
peroxide to eliminate the potential error from the existing color
or turbidity of the wastewater. Total organic carbon (TOC) was evaluated
with a TOC-V CSN Shimadzu analyzer using diluted reaction mixtures,
and chemical oxygen demand (COD) of the selected samples was measured
by a UV/vis spectrometer using the dichromate colorimetric method
at 605 nm (Hach-Lange cuvette tests). The copper content in the reaction
mixture reflecting metal leaching was determined by atomic absorption
spectrometry of diluted reaction mixture solutions on Shimadzu AAS
6300 using a Cu hollow cathode at λ = 324.9 nm. X-ray powder
diffraction analysis and N2 physisorption measurements
were conducted to reveal potential structural changes and coking.
3 Results and Discussion
3.1 Catalyst
Characterization
After testing
all prepared catalysts having different sizes, it was concluded (see
below) that Cu/13X-1 with the size range of 0.4–0.63 mm is
the most appropriate for CWAO. Table 3 thus contains results obtained from N2 physisorption
analysis of Cu/13X-1 and its thermally treated counterpart. The incorporation
of copper in 13X zeolite did not have a significant effect on the
measured surface area.
Table 3 Specific Surface
Areas, Pore Volumes,
and Copper Loadings of Prepared-Zeolite-Based Catalysts
copper content, wt %
sample UV/vis EDXA ICP-OES specific
surface area, m2 g–1 pore volume, cm3 g–1 average pore size,a nm
13X-APG Molsiv 59419 0.3119 2
Cu/13X-1 8.6 7.5 8.0 61819 0.3419 2
Cu/13X-K1273-1 11.5b 13.2 13.9 2619 0.0319 5
a Calculated
using dPORE = 4VPORE/S.
b Calculation based on a 25% reduction
of the catalyst’s mass during postsynthesis thermic treatment.
The thermal treatment resulted
in a decrease of both specific surface
area and pore volume with a shift of the pore size distributions (Figure 1) from the microporous
(Cu/13X-1) to the mesoporous range (Cu/13X-K1273-1). Such pronounced
differences in the physical properties for the catalyst calcined at
1273 K can be attributed to structural changes during thermal treatment.
Figure 1 Pore size
distributions in Cu/13X-1 and Cu/13X-K1273-1 catalysts.
XRD diffractograms of Cu/13X-1 already presented
in ref (19) confirm
the FAU structure
as no shifts in the peak positions and no significant diffraction
lines assigned to any new or impurity phase were observed.
XRD
suggested19 high crystallinity of
the copper-containing material as incorporation of copper into the
zeolite framework via ion exchange does not influence the crystal
structure. In agreement with the literature,20 the obtained results indicate that Cu2+ ions are well
dispersed in the zeolite framework of 13X and that the size of copper
particles is below the detection limit for the XRD measurement (<2–4
nm). In fact, from the TEM image of a Cu/13X-1 catalyst (Figure 2a), very small metal
particles highly dispersed in single zeolite crystals can be observed.
Their average size calculated using TEM analysis was 1.7 nm.
Figure 2 TEM images
of Cu/13X-1 (a) and Cu/13X-K1273-1 (b) catalysts.
The copper-bearing zeolite calcined at 1273 K exhibited phase
transformations
from a zeolite to a silicate-based material upon heating. As previously
reported,19 several phases were determined
for Cu/13X-K1273-1, including magnesium silicate, copper oxide, anorthoclase
(Na0.85K0.14AlSi3O8),
and andesine (Na0.685Ca0.347Al1.46Si2.54O8). Changes in crystal phases upon thermal
treatment were in line with a decrease of the surface area and pore
volume (Table 3). The
size of CuO in Cu/13X-K1273-1 according to the Debye–Scherrer
equation was 26.0 and 25.1 nm for the respective peaks at 35.5 and
38.6°. An average metal particle size analysis using TEM was
not applicable for the Cu/13X-K1273-1 catalyst because of a poor resolution
between the dark metal particles and the dark surface of single catalyst
crystals (Figure 2b).
The increase in the size of the metal particles in the Cu/13X-K1273-1
catalyst is most probably a consequence of metal sintering and clustering
of smaller metal particles into larger ones that occurs during thermal
treatment.21
The morphology, shape,
and size of crystals of Cu/13X-1 and Cu/13X-K1273-1
catalysts were additionally characterized by SEM. From the transmission
electron micrograph (Figure 2a) and the scanning electron micrograph (Figure 3a) of the Cu/13X-1 catalyst,
specific needle-shaped crystals were identified.
Figure 3 SEM images of Cu/13X-1
(a) and Cu/13X-K1273-1 (b) catalysts.
Although agglomerated, these can be associated with X zeolite
morphology
similar to that reported previously.22 Single
crystals in Cu/13X-K1273-1 were observed to be larger in size and
of irregular shapes and a broad crystal size range (Figures 2b and 3b) in agreement with XRD, showing the presence of several crystal
phases.
To evaluate metal dispersion across the surface, SEM
imaging in
a backscattering mode of the pellets and the cross sections of pellets
was performed (Figure 4).
Figure 4 Backscattering SEM images of pellets and cross sections of pellets:
Cu/13X-1 (a, b) Cu/13X-K1273-1 (c, d).
The brighter areas in the backscattering images are representative
of the higher densities of the more heavy elements (copper). It can
be noticed that copper is consistently spread over the surface of
the Cu/13X-1 catalyst (Figure 4a,b), whereas in the case of the Cu/13X-K1273-1 catalyst (Figure 4c,d), copper is mainly
located on the outer catalyst surface and in the narrow band close
to the pellet surface several micrometers in width. Migration of copper
from inside of the pellet to its outer surface is most probably a
consequence of the structural changes during thermal postsynthesis
treatment.
XPS analysis was used for the identification of the
oxidation state
of copper cations in Cu/13X-1 and Cu/13X-K1273-1. From the XPS spectra
presented in Figure 5, characteristic peaks were identified for Cu 2p, O 1s, Al 2p, and
Si 2p for both catalysts. Differences in the high-resolution spectra
of Cu 2p and O 1s indicate that the nature of copper species is different
in Cu/13X-1 and thermally treated Cu/13X-K1273-1 catalysts. The first
exhibits only two main peaks at 934 (Cu 2p3/2) and 953.3
eV (Cu 2p1/2), confirming the presence of Cu1+ as in Cu2O. In the high-resolution Cu 2p spectra of the
latter, strong Cu2+ satellite peaks at 943.3 and 964.2
eV were present, contributing to the presence of the CuO phase, as
previously identified by XRD.23 Differences
in O 1s signals additionally confirm the distinction between copper
oxides found on the surface of Cu/13X-1 and Cu/13X-K1273-1 catalysts.
It should be noted that reduction of finely dispersed Cu2+ under exposure to the X-ray beam during XPS analysis in the case
of the Cu/13X-1 catalyst cannot be excluded. Therefore, a difference
between the catalysts can also be related to difficulties in reduction
of larger CuO particles in the case of Cu/13X-K1273-1 during the XPS
measurements.
Figure 5 XPS survey and high-resolution spectra of Cu/13X-1 (a)
and Cu/13X-K1273-1
(b).
During catalyst preparation, the
influence of metal incorporation
into the zeolite support as well as the influence of postsynthesis
thermal treatment on the acid–base properties of the parent
and copper-bearing zeolites has been investigated. CO2-TPD
profiles of the parent zeolite as such (13X), calcined form (13X-K1273),
copper zeolite (Cu/13X-1), and the calcined material (Cu/13X-K1273-1)
were presented previously.19 The calculated
amounts of desorbed CO2 are given in Table 4.
Table 4 Basicity of the Prepared
Catalyst
Measured by TPD-CO2
basic
sites (mmol g–1)
sample weak 320–500 K medium 500–750 K strong >750 K total
basicity
13X 0.040 0.004 0.237 0.281
Cu13X-1 0.036 0.009 0.580 0.625
Cu13X-K1273-1 0.105 0.105
Weak, medium, and strong basic sites were
identified in 13X and
copper-modified 13X zeolites,19 which is
explained by the application of the sodium form of the commercial
zeolite for catalyst preparation as well as with the intrinsic (structural)
basicity of oxygen atoms present in the zeolite.24
Copper-containing zeolite Cu13X-1 exhibited much
higher quantities
of desorbed CO2 related to strong basic sites (>750
K),
indicating a more pronounced basicity of copper-exchanged zeolite.
High temperature, however, can in general also lead to structural
changes of the zeolite, thus preventing a straightforward assignment
of high-temperature peaks to strong basic sites. This possibility
was ruled out because only strong basic sites were seen for thermally
stable Cu/13X-K1273-1.
Acidity measurements were reported previously19 showing that copper-containing catalysts exhibited
Lewis
acidity, which can be explained by the presence of copper.2
Thermal treatment of Cu/13X-1 resulted
in a decrease in acidity.
Brønsted acid sites are degraded upon severe heat treatment above
773 K,24 whereas Lewis acidity from Cu2+ present in Cu/13X was diminished by the formation of copper
oxide, showing a more basic character. As reported previously,19 higher acidity was measured for Cu/13X-K1273-1
compared to that for the copper-free counterpart.
3.2 Preliminary Catalytic Experiments and Analysis
of Internal Mass Transfer
Catalytic wet peroxide oxidation
of OOMW was performed under mild reaction conditions. During preliminary
studies, the extent of thermal decomposition of polyphenols present
in the OOMW was investigated as well as the influence of catalyst
addition on the reactant conversion rates. The possible catalytic
activity of the parent Na-13X zeolite in the CWPO of phenol was excluded
during our previous investigations of a model catalytic system.14
Preliminary results on catalytic oxidation
were already reported,19 confirming the
role of catalysts in reducing the amount of phenolics and decomposing
hydrogen peroxide (Figure 6a,b). Thermal treatment of the catalyst at high temperature
was effective in decreasing hydrogen peroxide decomposition, improving
also the conversion of total phenols.
Figure 6 Kinetic curves for hydrogen peroxide (a)
and total phenols (b)
(cHP,0 = 0.25 M, T =
353 K, N = 600 min–1, mCAT = 2.5 g, dB = 0.4–0.63
mm).
These results indicate that the
oxidant is probably inefficiently
used in the reaction on Cu/13X-1 and that hydrogen peroxide is mainly
consumed in the reactions where hydroxyl radicals are lost and are
not used for degradation of the polyphenols. In CWPO, oxidation of
organic compounds is attributed to the presence of hydroxyl radicals
that are generated when hydrogen peroxide is decomposed. Reaction
pathways can be presented with Reactions 1–6. In the initial stages
of the reaction, hydroxyl and perhydroxyl radicals are produced by
hydrogen peroxide decomposition on the catalyst25 1 2 Both radical species are capable
of oxidizing
the organic compounds; however, the reactivity of hydroxyl radicals
is dominant.7 Catalytically produced hydroxyl
radicals react with phenolic compounds, oxidizing them through a series
of intermediates to carbon dioxide and water when complete mineralization
is achieved 3 Hydroxyl radicals are very reactive, and they
are involved in a number of competing side reactions such as scavenging
hydrogen peroxide and termination between the hydroxyl and perhydroxyl
radicals7 4 5 6 If the latter reactions
of hydroxyl radicals
are dominant, hydrogen peroxide will be consumed fast and majority
of the generated hydroxyl radicals will be spent inefficiently in
undesired side reactions. This could be considered a preferred reaction
pathway if the intraparticle diffusion resistances for the phenolic
molecules are present. In this case, only hydrogen peroxide would
be adsorbed and decomposed on the catalytically active sites on the
internal catalyst surface, whereas adsorption of polyphenols would
be limited mostly to the outer surface of the catalyst. In the absence
of organic compounds, the hydroxyl radicals formed inside the catalyst
would for the most part react with one another and hydrogen peroxide.
Taking into account the average pore sizes in the Cu/13X-1 catalyst
(2 nm) and cross sections of hydrogen peroxide (0.15 nm) and polyphenols
(1–2 nm), configurational diffusion limitations could be expected
for the phenolic compounds found in the OOMW. In addition to configurational
limitations, intraparticle resistances for hydrogen peroxide and polyphenols
could be present. They were verified using the Weisz–Prater
criterion26 7 where robs is
the observed reaction rate, R is the particle radius, cs is the molar concentration of the solute at
the catalyst surface, De is the effective
diffusion coefficient of the solute, and n is the
reaction order. For the porous media and the random pore model, the
effective diffusion coefficient is defined as , where D is the diffusion
coefficient, ε is the porosity, and τ is the tortuosity,
which are connected to the structural characteristics of the catalyst
and pore geometry. For the liquid–solid catalytic systems,
only molecular diffusion was taken into account, D ≈ DABo. The molecular diffusion coefficient was calculated
from the Wilke–Chang equation27 8 where Φ is the dimensionless association
factor of the solvent (Φ = 2.6 for water), MB is the molar mass of the solvent, μB is the dynamic viscosity of the solvent in cP at temperature T (K), and Vb(A)0.6 is the liquid molar
volume at the solute normal boiling point. For the purposes of this
study, the liquid molar volumes at the solute’s normal boiling
point were calculated from the Tyn and Calus equation 9 The calculations of the diffusion coefficients
were performed for hydrogen peroxide and phenol diffusing in water
using the data and expressions obtained from the thermodynamic properties
databank.28 In the absence of thermodynamic
data at the critical point for polyphenols such as hydroxytyrosol
or tyrosol that are most commonly found in the OOMW, phenol was chosen
as a model compound for the calculations. Because polyphenols are
more complex and larger molecules than phenol, it is reasonable to
expect that if the internal transfer limitations exist for phenol
they would be even more pronounced for polyphenols. The obtained values
of the diffusion coefficients at 353 K and normal pressure (typical
reaction conditions) were 6.0 × 10–9 m2 s–1 for hydrogen peroxide and 3.5 ×
10–9 m2 s–1 for phenol.
Application of the Weisz–Prater criterion (eq 7) for the observed initial reaction
rates of hydrogen peroxide decomposition (rHP,obs = 3.7 × 10–4 mol dm–3 s–1) and polyphenols oxidation (rTPh,obs = 5.3 × 10–5 mol dm–3 s–1) and their corresponding surface concentrations
with the mean catalyst particle diameter of 0.515 mm and ratio of 0.1 (generally valid
for zeolites)
resulted in the values of the dimensionless Weisz modulus of 0.15
for hydrogen peroxide diffusion and 2.25 for phenol. With this result,
the presence of intraparticle diffusion for hydrogen peroxide can
be eliminated, whereas the same cannot be concluded for the phenolics,
especially for the reaction orders higher than zero. For polyphenols
in OOMW, larger pore diffusion limitations can be expected being the
most probable cause of an inefficient use of hydrogen peroxide. Because
there are no pore diffusion limitations for the oxidant, hydrogen
peroxide mainly decomposes inefficiently inside the Cu/13X-1 catalyst
pores where negligible amounts of polyphenols are present.
On
the other hand, because of the larger pore sizes of the calcined
Cu/13X-K1273-1 catalyst (average pore size of 5 nm), the internal
diffusion in this reaction should not be as significant as in the
case of the Cu/13X-1 catalyst and faster decomposition of hydrogen
peroxide and oxidation of polyphenols should be expected. However,
this is not the case. The reason for a much slower radical generation
rate lies in the fact that the postsynthesis thermal treatment induced
migration of the catalytically active species (copper) toward the
pellet surface, which was confirmed by SEM imaging in the backscattering
mode of the cross sections of Cu/13X-1 and Cu/13X-K1273-1 pellets,
as presented in Figure 5b,d. Hydrogen peroxide decomposition in the Cu/13X-K1273-1 catalyst
takes place only in a narrow ring of few micrometers from the particle
surface where the presence of copper is identified and where polyphenols
are also present. In this case, it can be considered that the pore
diffusion for polyphenols is not as significant as in the case of
the Cu/13X-1 catalyst and that most of the generated hydroxyl radicals
are reacting with the organic compounds and are not inefficiently
spent in fast scavenging reactions inside the catalyst pellet (eqs 4–6). As a result, the rates of polyphenol oxidation are comparable
for both catalysts with a higher extent of oxidation for Cu/13X-K1273-1
resulting in an almost complete removal of the phenolic content after
180 min of reaction.
Comparison of Cu/13X and Cu/13X-K1273 during
preliminary studies
included also the investigation of their behavior in CWPO of OOMW,
namely, measuring the extent of copper leaching during the reaction
as well as by analyzing potential changes of the zeolite support after
the reaction. XRD diffractograms of both catalysts prior and after
catalytic experiments are close to each other (Figure 7a,b), indicating good stability of the support,
while copper leaching was
significantly different.
Figure 7 XRD diffractograms of the fresh and spent Cu/13X-1
(a) and Cu/13X-K1273-1
(b) catalysts.
By measuring the copper
content in diluted reaction mixtures using
atomic absorption spectroscopy, it was determined that after 180 min
38 wt % copper leached from the Cu/13X-1 catalyst in a striking contrast
to only 2 wt % for its counterpart calcined at high temperature, indicating
severe instability of Cu/13X-1. Contribution of the leached copper
in the solution to the overall catalytic performance was discussed
previously,29,30 concluding that it can be neglected
due to inactivation of copper by carboxylic acids. However, in this
case, when over 20% of copper leached from the catalyst before the
reaction was initiated by addition of hydrogen peroxide, the homogeneous
contribution should not be excluded because oxidation of organic compounds
catalyzed by copper cations in the liquid phase is possible. The copper
leaching results were confirmed by energy-dispersive X-ray spectroscopy
analysis of the fresh and spent catalysts, showing 42 wt % loss of
copper for the spent Cu/13X-1 catalyst and 4 wt % loss of copper for
the Cu/13X-K1273-1 catalyst. Specific surface area measurements were
also supporting the superior resistance against leaching of the thermally
treated catalyst.
For the Cu/13X-1 catalyst, the specific surface
area and pore volume
decreased from the initial SFRESH = 618
m2 g–1 and Vp,FRESH = 0.34 cm3 g–1 to SSPENT = 434 m2 g–1 and Vp,SPENT = 0.30 cm3 g–1, respectively, whereas the values for the Cu13X-K1273-1 catalyst
did not significantly change before and after the reaction: SFRESH = 26 m2 g–1 and Vp,FRESH = 0.03 cm3 g–1 to SSPENT = 24 m2 g–1 and Vp,SPENT = 0.04 cm3 g–1, respectively.
One of the possible explanations for large variations in stability
between calcined and noncalcined catalysts could be the different
copper speciation, namely, the presence of Cu+ in Cu/13X-1
as revealed by XPS. To our knowledge, no report on the differences
in the stability of Cu+ and Cu2+ in the CWPO
of phenolics has been published. However, different coordination of
copper inside the zeolite lattice for Cu+ and Cu2+ cations was reported by Vanelderen et al.,31 which could have an impact on their catalytic properties as well.
An alternative explanation was proposed by Taran et al. based on
a study of Cu-ZSM-5.13 The authors have
shown that copper catalysts with 1–2 wt % loading possessed
the highest activity and reasonable stability, whereas an increase
in copper resulted in a lower activity and stability. In the current
work, for the noncalcined catalysts, the amount of Cu could have been
too high to allow formation of a stable material. After calcination,
the zeolitic structure has been destroyed, giving several new phases.
It could be due to the fact that partial encapsulation of CuO particles
makes the catalyst less prone to leaching.
Whatever the explanation,
elucidation of mass transfer influence
and kinetic analysis was done for the Cu/13X-K1273 catalyst in which
the more efficient use of the oxidant was proven to take place.
3.3 Mixing Efficiency and External Mass Transfer
In the case of catalytic wet peroxide oxidation of polyphenols
over a solid pelleted catalyst, following mass transfer processes
should be considered: transport of the dissolved reactants from the
liquid bulk to the catalyst outer surface and transport inside the
pores of the pellet. These effects result in the concentration gradients
of reactants and products across phase boundaries and within the catalyst
particle, as present in Figure 8.
Figure 8 Mass transfer in catalytic wet peroxide oxidation of polyphenols
in OOMW.
To evaluate all possible mass
transfer limitations, a combined
theoretical/experimental approach was adopted in this study. Mass
transfer coefficients through the external boundary layer and inside
the pores were calculated for hydrogen peroxide and model compound
phenol, and the presence of diffusion limitations was evaluated by
the application of external mass transport and internal pore diffusion
criteria for the Cu/13X-K1273-1 catalyst. Additionally, the efficiency
of mixing in the reactor was verified and evaluation of reaction conditions
for achieving total suspension of the catalyst was performed.
External mass transfer or the mass transfer in the thin boundary
layer around the solid catalyst particle depends on hydrodynamic conditions
in the reactor (stirring speed), physical properties of the liquids,
and the size of the catalyst particles. In the catalytic reactions
in which the suspended solid catalyst is used, external mass transfer
resistances can be minimized by efficient mixing that establishes
thorough dispersion of reactants and catalyst in the liquid and the
use of the smaller catalyst particles. The first step in achieving
this is ensuring that under the conditions of the catalytic experiments
the solid catalyst is completely suspended in the liquid and no particles
remain at the bottom of the reactor for longer than 1 s. The minimum
stirrer speed necessary for total suspension can be calculated from
the empirical Zweitering equation32 10 where g is the
gravitational
constant (cm s–2), dP is the particle diameter (cm), dM is
the impeller diameter (cm), ρL and νL are the density and kinematic viscosity of water in g cm–3 and cm2 s–1, respectively, B is the percentage of the weight of the catalyst compared
to the weight of the liquid, and Δρ = ρS – ρL. S is a dimensionless
factor that depends on the reactor geometry and impeller type, , and is equal to 3.3 for the stirred baffled
tank with a diameter of 6.5 cm and pitched four-blade turbine impeller
4.5 cm wide positioned at 2.5 cm from the bottom of the reactor.33 For achieving the total suspension of the Cu/13X-K1273-1
catalyst (ρS = 1.3 g cm–3, dP = 0.04 cm, B = 1%) in OOMW
(approximated by water: ρL = 0.997 and νL = 0.009 cm2 s–1), the rotational
speed of the stirrer should be minimum, 244 rpm.
The absence
of external mass transfer for the stirring speed of
600 rpm was verified by applying the external mass transport criterion
that can be derived considering the mass transfer rate through the
boundary layer of the catalyst particle equal to the observed reaction
rate34 11 Assuming Cb – Cs < 0.05cb and
the nth-order reaction, the criterion takes the form 12 where robs is
the observed reaction rate, R is the particle radius, cb is the molar concentration of the solute in
bulk, and kLS is the liquid/solid mass
transfer coefficient. Liquid/solid mass transfer coefficients for
hydrogen peroxide and phenol were calculated on the basis of the correlation
between dimensionless Sherwood, Reynolds, and Schmidt numbers for
slurry reactors34 13 where Re number is expressed
as based on the Kolmogorov theory of turbulence.
By rearranging eq 13, the following expression for estimating liquid/solid mass transfer
coefficient kLS can be derived 14 In eq 14, ϵ denotes the energy of dissipation, D is the diffusion coefficient of the diffusing compound, dM is the impeller diameter, ρ and η
are the density and dynamic viscosity of water, and dP is the particle diameter. The energy of dissipation
or the maximum specific mixing power was calculated from 15 where P is the mixing power
that depends on the impeller type and stirring speed, NP is the power number of the impeller, and ρL and VL are the density and volume
of the liquid. For a 45° pitched four-blade turbine impeller
4.5 cm wide with NP = 1.3 in the turbulent
region (Re > 103) at a stirring speed
of 600 rpm mixing the volume of 250 cm3, the maximum specific
mixing power was calculated to be 0.96 W kg–1. The
mutual diffusion coefficients of solutes in water were calculated
using the Wilke–Chang equation (eq 8), resulting in the values of 6.0 × 10–9 m2 s–1 for hydrogen
peroxide and 3.5 × 10–9 m2 s–1 for phenol. Next, the external mass transfer coefficients
for hydrogen peroxide and phenol were calculated from eq 14, resulting in kLS,HP = 5.6 × 10–4 m s–1 and kLS,Ph = 3.8 × 10–4 m s–1. The application of the external mass transfer
criteria (eq 12) gave
the values on the left side of the equation several orders of magnitude
lower than those on the right side, showing that external mass transfer
for both hydrogen peroxide and polyphenols is negligible even at the
higher reaction orders and that the reaction mixture is effectively
mixed at 600 rpm.
The above theoretical approach results were
experimentally verified
by adopting the published procedures for the elimination of external
mass transfer.35 To confirm the specific
conditions under which the reaction was operating with negligible
external mass transfer resistances, the influence of the stirring
speed and particle size on the reaction rates of hydrogen peroxide
decomposition and polyphenols oxidation was investigated. The results
are presented in Figures 9, 10, and S1. From the results presented in Figure 9, it can be seen that already above 100 rpm
there are no significant changes in the reaction rates of hydrogen
peroxide decomposition and polyphenols oxidation and that the increase
in the stirring speed above 600 rpm does not further increase them.
This indicates that for the stirring speed above 600 rpm the external
mass transfer resistances are minimized and that the mass transfer
through the boundary layer proceeds faster that the surface reaction.
Figure 9 Influence
of the stirring speed on hydrogen peroxide (a) and total
phenol (b) content with time (N = 50–800 min–1, cHP,0 = 0.25 M, T = 353 K, mCu/13X-K1273-1 = 2.5 g, dB = 0.4–0.63 mm).
Figure 10 Influence of catalyst bead size on hydrogen
peroxide (a) and total
phenol (b) content with time (N = 600 min–1, cHP,0 = 0.5 M, T =
353 K, mCu/13X-K1273 = 2.5 g, dB = 0.315–2.00 mm).
From the above-presented results, it can be concluded that
the
reaction mixture is most effectively mixed at the stirrer speed of
600 rpm and that decreasing the particle size below 0.8 mm resulted
in only a slight improvement in the observed rate of phenol oxidation
excluding the presence of external mass transfer limitations that
could influence the reaction kinetics.
3.4 Influence
of Catalyst Loading, Initial Concentration
of Hydrogen Peroxide, and Temperature
The subsequent experiments
aimed at revealing the optimal initial concentration of hydrogen peroxide,
catalyst loading, and reaction temperature were performed under the
above-mentioned reaction conditions. The results of these studies
presented in Figure 11 showed that the most significant influence on the extent of total
phenols and TOC removal had the initial hydrogen peroxide concentration.
Figure 11 Time
dependence of hydrogen peroxide decomposition (a–c)
and total phenol content (d–f) with points representing the
experiment and lines representing the kinetic model. In (a) and (d), cHP,0 = 0–1.34 M, T =
353 K, mCu/13X-K1273-1 =
2.5; in (g), (b), and (e), cHP,0 = 0.5
M, T = 353 K, mCu/13X-K1273-1 = 0–5 g; and in (c) and (f), cHP,0 = 0.5 M, T = 323–353 K, mCAT = 2.5 g. In all cases, N = 600 min–1 and dB = 0.4–0.63
mm.
By increasing the initial content
of the oxidant, the rate and
the extent of the total phenols, TOC, and COD removal increased. At
higher initial concentrations of hydrogen peroxide (above 0.75 M),
when all total phenols that constitute approximately 17 wt % in TOC
loading are eliminated, no significant increase in the oxidation rate
of polyphenols can be observed. This is considered to be the consequence
of the intensification of side reactions of hydroxyl radicals and
the scavenging effect of the oxidant as described earlier (eqs 4–6). However, oxidation of intermediates that are formed by
polyphenol conversion becomes significant, further decreasing the
organic content of the reaction mixture. The best results were obtained
in the reaction conducted with the initial hydrogen peroxide concentration
of 1.34 mol dm–3 at 353 K and with 2.5 g of catalyst
when ∼97% of total phenols and 47% of TOC reduction were achieved
with a rather small copper leaching (Figure 12).
Figure 12 Influence of the initial hydrogen peroxide
concentration on TOC
and COD conversions and copper leaching in the reactions with the
Cu/13X-K1273-1 catalyst (cHP,0 = 0–1.34
M, T = 353 K, N = 600 min–1, mCu/13X-K1273-1 = 2.5
g, dB = 0.4–0.63 mm).
A higher catalyst bulk concentration gave more
prominent hydrogen
peroxide decomposition, and total phenol oxidation increased as expected
(Figure 11b,e).
In contrast to the reports published for similar catalytic systems,36 no limit of catalyst loading was observed and
the reaction rates increased proportionally with the mass of the catalyst
added to the reactor.
The increase in the reaction temperature
(Figure 11c,f) had
a similar beneficial effect on
the catalyst activity, yielding higher conversions of both reactants
at elevated temperatures.
3.5 Kinetic Analysis
In heterogeneous
catalysis, intrinsic kinetics can be evaluated only if the external
or internal mass transfer resistances are not affecting the surface
reaction rate. The above-presented results and discussion of the diffusion
influence in CWPO of polyphenols from OOMW over the Cu/13X-K1273-1
catalyst indicate that for a stirring speed of 600 rpm, catalyst size
of 0.4–0.63 mm, and the catalyst loading of 2.5 g the external
and internal mass transfer resistances for both the oxidant and the
polyphenols are minimized and that the surface reaction can be presumed
to be the slowest step in the overall reaction rate.
As mentioned
before, the CWPO reaction mechanism is very complex, consisting of
numerous parallel and serial reactions involving different molecular
and radical species. However, the following main reaction steps can
be identified: initiation of catalytic decomposition of hydrogen peroxide,
which results in the generation of hydroxyl radicals (eq 1), followed by the oxidation of
polyphenols and intermediates (propagation, eq 3), and finally a loss of hydroxyl radicals
in the nondesired side reactions (termination, eq 4–6). In a very
simplistic form, the oxidation pathway can be represented as 16 Because of the
complexity of the system, performing
a detailed kinetic analysis is challenge even for the model wastewaters
where most of the organic compounds present in the reaction mixture
are known. The composition of the real wastewater effluent produced
during olive oil extraction depends on the production process used,
olive species, and climate region, but, in general, OOMW contains
more than 30 different polyphenols as well as other prone to oxidation
organic acids that can engage in the reaction with hydrogen peroxide
and hydroxyl radicals.
The presence of inorganic salts such
as chlorides and phosphates
complicates the matter further.3 The heterogeneity
of the OOMW composition as well as the reaction scheme complexity
make carrying out the detailed kinetic study next to impossible that
would incorporate all individual reactions with all of the initial
and intermediate compounds and radicals.37,38 Because of this, the kinetic modeling is often limited to some parameter
that represents the group of targeted compounds or major constituents
of the wastewater such as COD, TOC, or total phenol content.
On the basis of the kinetic regularities and literature data for
similar catalytic systems,39,40 the following kinetic
model for polyphenol oxidation and decomposition of hydrogen peroxide
was proposed 17 18 where cTPh is
the molar concentration of total phenols expressed as gallic acid
equivalent, cHP is the molar concentration
of hydrogen peroxide, and γCAT is the catalyst loading in g
dm–3. The total phenol content was divided into
two fractions: more reactive (cTPh,1)
and less reactive (cTPh,2) based on preliminary
analysis of the obtained experimental data. In all performed experiments,
two reaction phases could clearly be distinguished: a fast decrease
of the total phenol content, which occurred within the first 30–60
min of the reaction, and slow oxidation of the remaining less-reactive
fraction of total polyphenols present in the reaction mixture. The
initial value of the concentration ratio of the two polyphenol fractions
was set as 0.5 during parameter estimation analysis. Reaction constants
(kTPh,1, kTPh,2, and kHP), reaction orders in reactants
and the catalyst (n1, n2, n3, n4), and concentration ratio of the polyphenol fractions are
the kinetic parameters that were estimated during modeling. These
expressions take into account that the oxidation rate of polyphenols
depends on the concentrations of both reactants and the catalyst loading
and that the decomposition rate of hydrogen peroxide considers the
contribution of not only the reaction with polyphenols but also the
side reactions of hydrogen peroxide decomposition. The contribution
of the noncatalytic hydrogen peroxide decomposition and polyphenol
oxidation was also considered based on the data acquired during reactions
without a catalyst. However, it was found that the noncatalytic contribution
to the overall reaction rate was marginal. The estimation of the kinetic
parameters was carried out by nonlinear regression analysis using
simulation and parameter estimation software MODEST.41 Ordinary differential equations (eqs 17 and 18) were solved
with the backward difference method. The sum of residual squares (Q) 19 was minimized with the hybrid Simplex–Levenberg–Marquardt
method, where yexp represents experimental
data and yest represents the estimated
values, i.e., the concentrations.
In the first iteration, the
polyphenol oxidation reaction orders
in polyphenols and hydrogen peroxide concentration were identified
in a run with all of the kinetic parameters set as floating. In most
cases, the polyphenol oxidation reaction orders with respect to phenol
(n1), hydrogen peroxide (n2), and catalyst concentration (n3) were close to 1, whereas the order of hydrogen decomposition
reaction with respect to hydrogen peroxide was close to 2 (n4). The second iteration of modeling was performed
with fixed reaction orders, and the results are shown in Table 5 and Figures 11 and 13.
Figure 13 Agreement of experimental and calculated data points for hydrogen
peroxide (a) and total polyphenol (b) concentration.
Table 5 Kinetic Modeling Results (n1 = n2 = n3 = l, n4 = 2)
estimated
parameter value standard
error relative
standard error (%)
kTPh,1 (dm6 mol–1 min–1 gCAT–1) 14.9 2.9 19.5
kTPh,2 (dm6 mol–1 min–1 gCAT–1) 3.16 0.025 0.8
kHP (dm6 mol–1 min–1 gCAT–1) 0.186 0.00344 1.8
ETPH,1 (kJ mol–1) 62.2 19.6 31.5
ETPH,2 (kJ mol–1) 90.1 0.7 0.8
EHP (kJ mol–1) 30.1 1.8 6.1
cTPh,1/cTPh,2 0.345 0.00186 0.5
Taking into account the complexity of the reaction
mixture and
limitations of the analytical methods, the obtained results show good
agreement of the experiment and the proposed kinetic model for both
hydrogen peroxide decomposition and polyphenol oxidation. In general,
the fit is better for hydrogen peroxide decomposition, whereas the
worst agreement for the polyphenol oxidation was achieved for the
reactions in which the initial concentration of hydrogen peroxide
was the lowest, indicating that for these reactions one of the kinetic
model assumptions does not hold.
Activation energies for hydrogen
peroxide decomposition and polyphenol
oxidation over the pelleted Cu/13X-K1273-1 catalyst were determined
from the temperature dependencies of the calculated rate constants
described by a modified Arrhenius equation 20 where kav is the
constant at the average temperature of the experiments Tav. The obtained values of activation energies for hydrogen
peroxide decomposition and polyphenol oxidation of Ea,HP = 30.1 kJ mol–1, Ea,TPh,1 = 62.2 kJ mol–1 and ETPH,2 = 90.1 kJ mol–1 are
in the range of values reported for similar model reaction systems
using powdered catalysts,9,14,29,39 i.e., 45–140 kJ mol–1.
3.6 Catalyst Testing in Olive
Oil Mill Wastewater
Treatment
The catalyst performance was finally tested in
the prolonged reaction over 10 h to determine whether the catalyst
gets deactivated with prolonged use. From the results presented in Figure 14, it can be seen
that the oxidation of organic content continues after phenolics are
eliminated, demonstrating the catalyst ability to enhancing peroxidation
of not only phenols but also other organic compounds present in the
olive oil mill wastewater, resulting in complete conversion of total
phenols and 52% conversion of TOC. The Cu/13X-K1273-1 catalyst preserved
its stability even after 10 h of reaction when only 3.3 wt % copper
leached from the catalyst. By a comparison of the fresh and spent
catalysts, it was observed that the catalyst maintained its initial
surface area and pore volume (SFRESH =
26 m2 g–1 and Vp,FRESH = 0.03 cm3 g–1 to SSPENT-10h = 25 m2 g–1 and Vp,SPENT-10h = 0.03 cm3 g–1). Although the loss of 3.3 wt % of
the initial copper content from the catalyst is not negligible, this
result is very encouraging when compared to that of similar catalytic
systems described in the literature. The extent of leaching of the
Cu/13X-K1273 pelletized catalyst is generally lower when compared
to that of other zeolite or zeolite-based catalysts9,13,42 and is comparable to leaching of copper-containing
pillared clay catalysts according to the work of Inchaurrondo et al.29 However, most of these results are connected
to CWPO studies of model or often highly diluted wastewaters, which
should be taken into account when comparing them with the results
of this study where a real industrial effluent was used because the
extent of metal leaching from the catalyst depends not only on the
catalyst type or support material but also very strongly on the reaction
conditions such as temperature, pH, and particular organic compound
species and their concentrations.
Figure 14 Concentrations of hydrogen peroxide (a),
total phenols, and TOC
(b) in the reactor for a prolonged reaction time experiment with the
Cu/13X-K1273-1 catalyst (cHP,0 = 0.5 M, T = 353 K, N = 600 min–1, dB = 0.40–0.63 mm, mCAT = 2.5 g, tR = 10 h).
4 Conclusions
Postsynthesis thermal treatment was beneficial for catalytic behavior
of the copper-containing 13X zeolite in catalytic wet peroxide oxidation
of OOMW as it resulted in an increased stability against leaching,
allowing better removal of total phenols TOC due to the presence of
pore diffusion limitations for polyphenols in the noncalcined Cu/13X-1
catalyst. Results of mass transfer and diffusion investigation for
the calcined Cu/13X-K1273-1 catalyst excluded the influence of both
external and internal mass transfer limitations. It was found that
the rate of phenol oxidation and hydrogen peroxide decomposition increased
with the increase of stirrer speed, catalyst loading, initial hydrogen
peroxide concentration, and reaction temperature and with the decrease
of catalyst bead size. Kinetic analysis of the catalytic system was
preformed, the reaction orders in reactants and in the catalyst were
identified, and parameters of the proposed kinetic model and activation
energies were determined. By treating the industrial olive oil mill
wastewater in a catalytic wet peroxide oxidation process over thermally
stabilized copper-containing zeolite-based catalyst under mild reaction
conditions (353 K and atmospheric pressure), it is possible to achieve
complete conversion of total phenols and over 50% conversion of TOC,
substantially minimizing copper leaching.
Supporting Information Available
The Supporting Information
is available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b00948.Observed reaction
rate dependence on the stirring speed
and catalyst bead size (PDF)
Supplementary Material
ao8b00948_si_001.pdf
The authors
declare no competing financial interest.
Acknowledgments
The authors
acknowledge the support of the European Commission
and the Croatian Ministry of Science, Education and Sports Co-Financing
Agreement No. 291823 as well as Åbo Akademi Johan Gadolin Process
Chemistry Centre. The contribution of Vilko Mandić to XRD analysis
is highly appreciated.
==== Refs
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==== Front
ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145898410.1021/acsomega.8b01003ArticleComputational Study on Ring Saturation of 2-Hydroxybenzaldehyde
Using Density Functional Theory Verma Anand
Mohan Agrawal Kushagra Kishore Nanda *Department of Chemical Engineering, Indian Institute of Technology Guwahati, Guwahati, Assam 781039, India* E-mail: nkishore@iitg.ac.in, mail2nkishore@gmail.com.01 08 2018 31 08 2018 3 8 8546 8552 15 05 2018 23 07 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
Bio-oil
produced from pyrolysis of lignocellulosic biomass consists
of several hundreds of oxygenated compounds resulting in a very low
quality with poor characteristics of low stability, low pH, low stability,
low heating value, high viscosity, and so on. Therefore, to use bio-oil
as fuel for vehicles, it needs to be upgraded using a promising channel.
On the other hand, raw bio-oil can also be a good source of many specialty
chemicals, e.g., 5-HMF, levulinic acid, cyclohexanone, phenol, etc.
In this study, 2-hydroxybenzaldehyde, a bio-oil component that represents
the phenolic fraction of bio-oil, is considered as a model compound
and its ring saturation is carried out to produce cyclohexane and
cyclohexanone along with various other intermediate products using
density functional theory. The geometry optimization, vibrational
frequency, and intrinsic reaction coordinate calculations are carried
out at the B3LYP/6-311+g(d,p) level of theory. Furthermore, a single
point energy calculation is performed at each structure at the M06-2X/6-311+g(3df,2p)//B3LYP/6-311+g(d,p)
level of theory to accurately predict the energy requirements. According
to bond dissociation energy calculations, the dehydrogenation of formyl
group of 2-hydroxybenzaldehyde is the least energy demanding bond
cleavage. The production of cyclohexane has a lower energy of activation
than the production of cyclohexanone.
document-id-old-9ao8b01003document-id-new-14ao-2018-01003cccc-price
==== Body
1 Introduction
Due
to declining fossil fuels and increasing pollution, there is
a strong necessity to find an alternative and clean energy resource
that can aid the present energy demands and reduce the pollution level.
Currently, renewable energy resources, e.g., tidal energy, solar energy,
biomass, wind energy, geothermal energy, and so on, are being largely
utilized. They are providing a good relief for the present energy
demand; however, their proper utilization still needs to be explored.
Nevertheless, out of all renewable energy resources, only biomass
has the ability to deliver sustainable carbon element.1−4 The sustainability of carbon element is necessary to achieve the
production of transportation fuels or specialty chemicals.5 The lignocellulosic biomass is cheap, abundant,
and easily available in most countries; therefore, the research based
on lignocellulosic biomass conversion into biofuel has enormously
increased in the last few decades.2 The
lignocellulosic biomass basically contains three fractions, viz.,
lignin, hemicellulose, and cellulose.1,6 The research
based on the cellulose and hemicellulose fractions of lignocellulosic
biomass has received considerable attention in the past few years,
but the lignin fraction has been ignored constantly because of its
complex structure, although it has a high energy density compared
to other two fractions.7 Nevertheless,
there are various channels to convert the lignocellulosic biomass
into bio-oil, e.g., pyrolysis, liquefaction, hydrolysis, and gasification,
and the pyrolysis process has been reviewed to be the most economical
and advantageous.3,8 However, the bio-oil produced
from pyrolysis of lignocellulosic biomass comprises several hundreds
of oxygenated compounds that lower its quality, endowing it with low
heating value, low pH, low stability, low stability, high viscosity,
and so on.4 Therefore, it needs to be upgraded
to serve as a fuel for vehicles. Furthermore, unprocessed bio-oil
is a great source of many specialty or platform chemicals, such as
hydroxymethyl furfural, furfural, levulinic acid, dimethyl furan,
and so on.1,5
As it has been pointed out that cellulose
and hemicellulose fractions
have received much attention compared to the lignin fraction, in this
study, 2-hydroxybenzaldehyde, a component of phenolic fraction derived
from lignin, has been selected as the bio-oil model compound. In the
past, a few phenolic components, such as guaiacol,9−15 catechol,9,16 phenol,10,14,16,17 vanillin,18,19 anisole,14 and so on, have been studied
both experimentally and numerically. This component has been recently
considered by Verma and Kishore20 for its
decomposition into benzene as the end product; however, there has
been no further study regarding its ring saturation, which is more
likely to occur in the presence of high hydrogen pressure-based hydrodeoxygenation
conditions. Although a few authors21−24 have carried out pyrolysis of
a few bio-oil model compounds and observed 2-hydroxybenzaldehyde as
one of the products in the pyrolysis product mixtures, further experiments
for upgrading 2-HB have not been carried out to date. For instance,
Robichoud et al.21 carried out a pyrolysis
study on dimethoxybenzene model compound and observed 2-hydroxybenzaldehyde
as one of the products. Similarly, Zhang et al.24 also carried out pyrolysis study on the lignin dimer model
compound and reported 2-hydroxybenzaldehyde as one of the products
along with guaiacol, catechol, and others. Since 2-hydroxybenzaldehyde
comprises two oxy-functionals, namely, hydroxyl and aldehyde groups,
it still needs to be upgraded to achieve the nonoxygenated component.
Therefore, 2-hydroxybenzaldehyde is selected as the bio-oil model
compound and its conversion to lower fractions has been numerically
attempted here.
In this numerical study, 2-hydroxybenzaldehyde
is allowed to undergo
two reaction pathways producing cyclohexane and cyclohexanone, respectively.
These reaction schemes are depicted in Figure 1. The notations in Figure 1 are labeled as X_Y, where X denotes the reaction pathway number and Y denotes
the structure under that reaction pathway. Similarly, transition-state
structures in the potential energy surfaces (PESs) are denoted as TSX_Y, where X is the
reaction pathway number and Y denotes the transition-state
number.
Figure 1 Reaction schemes for the conversion of 2-hydroxybenzaldehyde.
In Figure 1, it
can be seen that the reaction pathway 1 produces cyclohexane. The
preparatory part of reaction pathway 1 is the hydrogenation of carbon
atom (para-positioned to OH group), followed by ring saturation of
2-hydroxybenzaldehyde using five further atomic hydrogenation reactions.
The produced component 1_f after the ring saturation
undergoes hydroxyl cleavage, followed by a single-step hydrogenation
reaction to produce 1_h. Finally, structure 1_h follows two pathways. Under primary reaction pathway 1, the formyl
group is cleaved, followed by a single-step hydrogenation reaction
to produce cyclohexane, and under secondary reaction pathway 1, i.e.,
1a, structure 1_h undergoes decarbonylation reaction
to produce cyclohexane. On the other hand, reaction pathway 2 starts
from the dihedral change of hydrogen atom of the hydroxyl group to
initiate the keto–enol tautomerization reaction. The keto–enol
tautomerization reaction of structure 2_a produces 2_b, which further undergoes ring saturation to produce structure 2_f. Finally, structure 2_f undergoes the decarbonylation
reaction to produce cyclohexanone. All reaction steps of each reaction
pathway are considered theoretically at the B3LYP/6-311+g(d,p) level
of the theory under density functional theory (DFT) framework. The
single point energy (SPE) calculation is performed for each structure
at the M06-2X/6-311+g(3df,2p)//B3LYP/6-311+g(d,p) level of theory
to predict energies accurately.
2 Results
and Discussion
2.1 Bond Dissociation Energy
(BDE)
A
thorough analysis of bond dissociation energy (BDE) of 2-hydroxybenzaldehyde
with all possible bond cleavages was reported in our previous work.20 It has been reported that bond dissociation
energies of 2-hydroxybenzaldehyde are quite high, i.e., in the range
of 92–115 kcal/mol. The least energy demanding bond cleavage,
i.e., D3 (dehydrogenation of the formyl group), requires 92.22 kcal/mol.20 Along with the most favorable bond dissociation
site D3, dehydrogenation of the hydroxyl group (D2) was reported as
the second most favorable bond cleavage site.20 It is also clear that dehydrogenation of phenyl ring of 2-HB is
not favorable at all because the energy demand due to each hydrogen
bond cleavage from phenyl ring of 2-HB is in the range of 112–115
kcal/mol.20 Therefore, cleavage of hydrogen
atoms from phenyl ring is not advisable. In such scenario of high
bond dissociation energies due to scissions of atoms/functionals of
2-HB, it is highly probable that the ring saturation of 2-HB may lead
to a low energy demanding reaction pathway, which is the aim of this
work. There are two ways of saturating the aromatic ring of 2-HB,
i.e., first by direct ring hydrogenation and second by keto–enol
tautomerization followed by ring hydrogenation.
2.2 Reaction Pathway 1
Reaction pathway
1 is about the direct ring hydrogenation reaction. The potential energy
surfaces (PESs) of reaction pathways 1 and 1a are shown in Figure 2, and the corresponding
optimized molecular structures are shown in Figure 3. Interatomic bond distances in the transition-state
structures of Figure 3 are shown in angstrom (Å) units. The Cartesian coordinates
of a few optimized molecular structures are given in the Supporting Information.
Figure 2 Potential energy surfaces
of reaction pathways 1 and 1a.
Figure 3 Optimized molecular structures of reaction pathways 1 and 1a.
The reaction pathway 1 starts
with a single-step hydrogenation
reaction at the fifth carbon position of the aromatic ring of the
2-hydroxybenzaldehyde structure (see structure 1_a in Figure 1), followed by another
atomic hydrogenation reaction to saturate the generated radical by
the first hydrogenation reaction. The first hydrogenation reaction
requires 4.62 kcal/mol of activation barrier (see TS1_1 in Figures 3 and 4) according to single point energetics at the M06-2X/6-311+g(3df,2p)//B3LYP/6-311+g(d,p)
level of theory.
Figure 4 Potential energy surface of reaction pathway 2.
As it is known that bond dissociation
and radical recombination
reactions do not possess any transition-state structure, the energy
release during the recombination reaction of structure 1_a and H radicals is calculated by BDE approximation. According to
BDE at the B3LYP/6-311+g(d,p) level of theory, the recombination of
radicals 1_a and H to produce structure 1_b releases 73.58 kcal/mol of energy. Further, another transition-state
structure is located for the hydrogenation reaction of structure 1_b to produce 1_c at potential energy surface
(PES) as TS1_2 that requires only 2.89 kcal/mol of energy
to surpass the barrier height. This follows through another radical
recombination reaction of structure 1_c and H that releases
82.60 kcal/mol of energy. Similar to the reaction steps 2-HB → 1_a → 1_b, further hydrogenation reactions
of structure 1_d are carried out as 1_d → 1_e → 1_f, where the activation barrier
of 1_d → 1_e and energy release during 1_e → 1_f are calculated as 4.30 and 81.99
kcal/mol, respectively. The produced component after the aromatic
ring saturation of 2-HB is identified as 2-hydroxycyclohexane-1-carbaldehyde.
Further, the cleavage of hydroxyl group of structure 1_f is carried out with a calculated BDE of 86.57 kcal/mol, followed
by a radical recombination reaction of structure 1_g and
a hydrogen radical with an energy release of 94.49 kcal/mol. Afterward,
the produced component, i.e., cyclohexanecarbaldehyde (structure 1_h), follows two pathways. The first pathway proceeds as
the primary reaction pathway 1 (bold black arrows in Figure 1), which cleaves the formyl
group from structure 1_h with a BDE of 71.43 kcal/mol,
followed by saturation of generated radical with a hydrogen radical
releasing 94.19 kcal/mol of energy to produce cyclohexane. On the
other hand, the secondary reaction pathway 1 (nonbold black arrows
in Figure 1) involves
a decarbonylation reaction to directly produce cyclohexane. The barrier
height of the decarbonylation is calculated to be 87.31 kcal/mol.
In Figure 3, it
can be seen that the highest uphill is due to the very first hydrogenation
reaction of 2-HB, which is 4.62 kcal/mol at the potential energy surface,
and other stationary states are in the negative side. Figure 3 clearly suggests an overall
activation energy of only 4.62 kcal/mol of energy, which is a very
favorable environment for this system even at lower temperature and
pressure conditions. Also, it can be seen that the decarbonylation
reaction of structure 1_h is slightly favorable for the
direct cleavage of the formyl group followed by hydrogenation reaction.
2.3 Reaction Pathway 2
Reaction pathway
2 is about the production of cyclohexanone. The potential energy surface
is shown in Figure 4 by a blue smooth line, and the corresponding molecular structures
are shown in Figure 5.
Figure 5 Optimized molecular structures of reaction pathway 2.
Reaction pathway 2 starts with the dihedral change
of hydrogen
atom of the hydroxyl group. It can be seen from the potential energy
surface of reaction pathway 2 (Figure 4) that 2-HB is the ground-state structure and 10.57
kcal/mol more stable than structure 2_a (energetically
less stable configuration of 2-HB). The dihedral change of hydrogen
atom occurs with a barrier height of 13.80 kcal/mol, and this reaction
step is essential for further initiation of the keto–enol tautomerization
reaction. The keto–enol tautomerization reaction step (2_a → 2_b), i.e., migration of hydrogen
atom from hydroxyl group to the ortho-positioned carbon atom, produces
6-oxocyclohexa-1,3-diene-1-carbaldehyde with a barrier height of 73.90
kcal/mol. Further, a single-step hydrogenation reaction at structure 2_b is carried out with a barrier height of only 1.36 kcal/mol,
followed by combination reaction of a hydrogen radical and structure 2_c releasing 77.53 kcal/mol of energy. Further, similar to
the reaction steps 2_b → 2_c → 2_d, the reaction steps 2_d → 2_e → 2_f are performed with a barrier height of
1.75 kcal/mol for reaction step 2_d → 2_e and an energy release of 83.62 kcal/mol for reaction step 2_e → 2_f.
The produced compound
after the conversion of double bonds between
carbon atoms into single bonds is recognized as 2-oxocyclohexane-1-carbaldehyde.
Finally, to produce cyclohexanone from 2-oxocyclohexane-1-carbaldehyde,
a decarbonylation reaction is carried out, which occurs with a barrier
height of 71.04 kcal/mol.
The production of cyclohexanone from
2-hydroxybenzaldehyde witnesses
many reaction steps. It can be seen in Figure 4 that the energy state of TS2_2 is highest in the potential energy surface of reaction pathway 2;
therefore, this particular energy state will be responsible for the
overall activation energy. Therefore, the overall activation energy
of reaction pathway 2 is 84.47 kcal/mol, which is very high to achieve
at mild reaction conditions. Also, if compared, the production of
cyclohexanone requires a considerably larger overall activation barrier
(84.47 kcal/mol) than the overall activation barrier in the production
of cyclohexane (4.62 kcal/mol). Therefore, it is clear that the possibility
of production of cyclohexane from 2-HB will be considerably higher
compared to the production of cyclohexanone.
3 Conclusions
In this study, 2-hydroxybenzaldehyde (2-HB),
a bio-oil oxygenated
component that represents the phenolic fraction of bio-oil, is taken
as the bio-oil model compound and its ring saturation is carried out
to produce cyclohexane and cyclohexanone. The bond dissociation energy
calculations of 2-hydroxybenzaldehyde do not suggest the cleavage
of hydrogen atoms from either the phenyl ring or functional groups
because of high energy requirements. Therefore, the conversion of
2-HB by ring saturation is carried out to produce cycloproducts. It
is observed that the production of cyclohexane is highly favorable
compared to the production of cyclohexanone because the overall activation
energy of the former is only 4.62 kcal/mol, whereas the latter demanded
84.47 kcal/mol of overall activation energy. In other words, keto–enol
tautomerization followed by ring hydrogenation process of 2-HB in
gas phase is not preferred compared to direct ring hydrogenation process
of 2-HB.
4 Computational Details
The application
of density functional theory (DFT) as a computational
tool has enormously increased in the recent past due to its reliability
and accuracy. Although there are various functionals under DFT, such
as LSDA, B3LYP, BLYP, M05, M06-2X, etc., there has been much debate
among researchers regarding their accuracy.25 Recently, a few research groups26,27 carried out
an extensive survey of DFT functionals applied to various chemical
systems. For instance, Goerigk et al.26 performed an extensive review to assess numerous DFT functionals
and observed ωB97X-V functional as one of the best functionals
among GGA, meta-GGA, and hybrid-GGA functionals. They reported an
average performance of B3LYP functional compared to other DFT functionals.
Furthermore, Mardirossian and Head-Gordon27 also performed an extensive assessment of numerous DFT functionals
and reported root-mean-square deviation (RMSD) values for different
data types. They reported ωB97M-V as the best functional because
of low RMSD values for barrier heights (1.68) and thermochemistry
(2.48) data types. However, an interesting observation in their study
is that B3LYP functional performed excellently compared to many well-known
DFT functionals, such as PBE, PBE-D3, TPSS-D3, M06-L, and so on. In
addition, recently, Simón and Goodman28 have shown that the use of B3LYP functional is a better choice for
organic covalent bond-forming reactions; therefore, all geometries
and transition-state structures in this study are optimized using
B3LYP29,30 functional under DFT31,32 framework. The basis set has been selected as 6-311+g(d,p).33 Normal-mode vibrational frequency calculations
are carried out for all optimized structures to test the true natures
of optimized structures. One and zero imaginary frequencies in the
vibrational frequency result confirm the structure as first-order
saddle point and minimum structure on potential energy surface (PES).
Furthermore, an intrinsic reaction coordinate34 calculation is also carried out at each true transition-state structure
to evaluate the minimum energy path. The single point energy (SPE)
calculation is performed for each structure at the M06-2X/6-311+g(3df,2p)//B3LYP/6-311+g(d,p)
level of theory to predict energies accurately.
Bond dissociation
energy calculations are performed for organic
homolysis and radical recombination reactions because of the nonavailability
of transition-state structures for such reactions. BDE provides a
good approximation for the energy requirement to cleave a chemical
bond. The expression of BDE is as follows 1 where H298 is
the enthalpy. “A–B” is the molecule with considered
cleavage site, A and B are the radicals after bond cleavage of “A–B”.
All quantum chemical calculations are performed in the gas-phase
environment using Gaussian 0935 software
package with the help of a Gauss View 536 visualizer.
Supporting Information Available
The
Supporting Information
is available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b01003.Cartesian coordinates
of a few molecular structures,
i.e., structures 2-HB, 1_b, 1_d, 1_f, and 1_j involved in this study are
provided in this Supporing Information (PDF)
Supplementary Material
ao8b01003_si_001.pdf
The authors
declare no competing financial interest.
Acknowledgments
The authors acknowledge
the financial support (sanction no.
34/20/17/2016-BRNS) from Board of Research in Nuclear Sciences (India)
for this work.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145808610.1021/acsomega.8b01324ArticleElectronic Structure and Chemical Bonding of [AmO2(H2O)n]2+/1+ Hu Shu-Xian *†Liu Hai-Tao ‡Liu Jing-Jing †Zhang Ping *‡Ao Bingyun §† Beijing
Computational Science Research Center, Beijing 100193, China‡ Institute
of Applied Physics and Computational Mathematics, Beijing 100088, China§ Science
and Technology on Surface Physics and Chemistry Laboratory, Mianyang 621908, China* E-mail: hushuxian@csrc.ac.cn (S.-X.H.).* E-mail: zhang_ping@iapcm.ac.cn (P.Z.).23 10 2018 31 10 2018 3 10 13902 13912 13 06 2018 20 09 2018 Copyright © 2018 American Chemical
Society2018American Chemical
SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
Systematic americyl-hydration cations
were investigated theoretically
to understand the electronic structures and bonding in [(AmO2)(H2O)n]2+/1+ (n = 1–6). We obtained the binding energy using density
functional theory methods with scalar relativistic and spin–orbit
coupling effects. The geometric structures of these species have been
investigated in aqueous solution via an implicit solvation model.
Computational results reveal that the complexes of five equatorial
water molecules coordinated to americyl ions are the most stable due
to the enhanced ionic interactions between the AmO22+/1+ cation and multiple oxygen atoms as electron donors.
As expected, Am–Owater bonds in such series are
electrostatic in nature and contain a generally decreasing covalent
character when hydration number increases.
document-id-old-9ao8b01324document-id-new-14ao-2018-01324eccc-price
==== Body
Introduction
In the past several
decades, a rapid increased resurgence of nuclear
power in many countries for the goals of ensuring sustainable energy
supplies has raised a possible hazard to the environment due to the
problems of the radioactive waste and has increased the handling and
reprocessing challenge of spent nuclear fuel and high-level nuclear
waste.1−5 Especially, the long-term radioactivity of nuclear waste repositories
is one of the main issues at stake and is in part determined by the
presence of minor actinides, namely, americium (Am) and curium (Cm),
with the half-life t1/2 = 7370 year for 243Am and t1/2 = 340 000
year for 248Cm.6,7 During the actinide
waste storage, transportation, and separation, water is unavoidable.
Therefore, the characterization and identification of the behavior
of actinide ions in solution is of particular practical importance
in addition to the fundamental actinide chemistry, such as the dynamics
between the coordinated water molecules and the bulk solvent and the
coordination flexibility of actinyl ions.8 So, the solution chemistry of actinide complexes has been considerably
explored in experiment and theory; especially, the hydration of actinide
ions has been widely investigated.9−12 However, such studies have mostly
focused on early actinide ions due to their relatively substantial
quantities and extensive applications. The uranyl UO22+ ion, for example, has received a large amount of interest
because of its importance for environmental chemistry of radioactive
elements and its role as a benchmark system for heavier actinides.13 Experimentally, direct structural information
on the coordination of uranyl in aqueous solution has been mainly
obtained by extended X-ray absorption fine structure or X-ray absorption
near-edge structure measurements.9,14,15 Theoretically, the structural investigation has been
performed via various ab initio studies of uranyl and related molecules,
with a number of explicit water molecules or with a polarizable continuum
model to mimic the environment over the past years, such as [UO2(CO3)3]4–, [Th(H2O)n]4+, [U(H2O)n]3+, UO2Fn(H2O)5–n2–n, and [UO2(H2O)n]n+.10,16−21 With the rapid development of quantum chemical methods, the less
known transuranium elements have been increasingly studied, i.e.,
[NpO2(CO3)3]4–,
[NpO2(CO3)m(H2O)n], [Cm(H3O)n]3+, [UO2(H2O)n]n+, [NpO2(H2O)n]n+, and [PuO2(H2O)n]n+.7,12,13,22−28 There appears to be no theoretical report about americyl (AmO22+/1+) in aqueous solution but one study on the
water exchange mechanism in AmO2(H2O)52+ 15 years ago.29 In addition,
the understanding of the coordination chemistry of americyl ions in
solution can present the essentials to detect, characterize, and differentiate
this metal ion from transition metals or lanthanide metals through
the coordination characteristic. Hence, we will focus on speciation
of the americyl ions (AmO22+ and AmO21+) in this paper, bridging the gap between the wide-established
early actinides and the more complicate later actinides. However,
an accurate description of solvent effects of the actinide complexes
is inherently difficult due to their complicated electronic properties
and the challengeable aqueous environment to theoretical chemists.
There are two typical quantum chemistry strategies used to incorporate
the solvent effects on the geometry and energy of the actinide complexes
in aqueous solution. One is molecular dynamics simulations approach
with a discrete model, where a number of explicit solvent molecules
are included and treated at the same level of theory as that used
for the solute.30 Although this supermolecule
requires a substantial computational expense, the understanding improvement
of the structural and chemical behavior of actinyl in solution is
inconsequential because this method employs empirical potentials affecting
the accuracy significantly, especially for those transplutoniums having
few experimental data available. Another approach is the polarizable
continuum model, where the solvent is described by a dielectric polarizable
continuum.31 This model has shown a good
agreement with experimental results on the geometric and electronic
structures in actinyl–water complexes,15 where uranyl, neptunyl, and plutonyl coordinated to five water ligands
in the equatorial plane have been computationally confirmed.13,32
In this contribution, we report a systematic investigation
on the
chemistry of hydrated americyl ions in the [AmO2(H2O)n]2+/1+ (n = 1–6) complexes using a suite of computational
modeling and various bonding analysis methods. We address the equilibrium
structures of [AmO2(H2O)n]2+/1+, as well as the hydration number of americyl
ions and the bonding nature of americium ions and oxygen atoms. In
addition to the knowledge for the periodicity in bonding properties,
the influence of aqueous solvation of [AmO2(H2O)n]2+/1+ (n = 1–6) will provide a scientific comprehension to the actinide
solution chemistry.
Results and Discussion
The static
structures of hydrated complexes of AmO22+/1+ with one to eight water ligands have been regularly investigated
via geometry optimizations in gas phase and in aqueous phase at the
B3LYP/Am/ECP60MWB_SEG//O,H/cc-pVTZ level with or without the conductor-like
screening solvation model (COSMO) method. First, concerning the water
hydrogens lying either in the planes or perpendicular to the planes
defined by the OylAmOyl, two possible gas-phase
symmetric arrangements of water molecules for [AmO2(H2O)1]2+/1+ and [AmO2(H2O)2]2+/1+ have been optimized without
symmetry constraints. As shown in Figure S1, the one with hydrogens perpendicular to the plane has one imaginary
vibrational frequency (428i cm–1) showing the rotation
of water ligand, indicating its instability compared with the one
with hydrogens lying in the plane. Besides, the starting structure
of [AmO2(H2O)7]2+/1+ has
been assumed as a first-shell coordination number of seven when seven
water molecules are bonded to AmO22+/1+, in
which the seven equatorial water ligands lie rigorously in the equatorial
plane. After optimization within density functional theory (DFT),
seven water molecules have been arranged into two coordination shells;
there are five water molecules in the first shell with a relatively
shorter Am–Ow distance of <2.5 Å and two
water molecules in the second shell at a longer distance of >4.4
Å.
Therefore, the hydration number of AmO22+/1+ in the first shell is predicted to be less than seven. In addition,
the optimized structural parameters and calculated binding energies
of [AmO2(H2O)n]2+/1+ (n = 1–6) in the gas phase and
aqueous solution on the basis of different levels of theory are listed
in Tables S1–S4. As clearly shown
in the Tables S3 and S4, the energy destabilization
by roughly 32.0–128.2 kcal/mol for [AmO2(H2O)n]2+ (n = 1–6) complexes is due to the conductor-like polarized continuum
model; a similar trend is also observed for [AmO2(H2O)n]1+ (n = 1–6) complexes. Upon inclusion of the surrounding effects,
the binding energy decreases drastically to 62.4 kcal/mol for equatorial
[AmO2(H2O)6]2+ and to
−0.5 kcal/mol for equatorial [AmO2(H2O)6]1+ at scalar relativistic (SR)-B3LYP level
of theory, indicating the instability of this structure. In terms
of geometries of equatorial [AmO2(H2O)6]2+/1+, the six-water complexes with all six coordinated
Ow atoms in the equivalent position are subject to the
first-order Jahn–Teller instability and are only saddle points
having imaginary frequencies. The Ci symmetry
structure of [AmO2(H2O)6]2+ in which all six ligands are in the first coordination shell, shown
in Figure S2, is stable with or without
aqueous solution. The distance from the americium center to the water
molecules located above and below the equatorial plane in a symmetric
manner is longer (0.09 Å) than that for [AmO2(H2O)5]2+ and is significantly shorter
(0.13 Å) than that reported for NpO2(H2O)62+ having a similar structure largely owing
to the actinide contraction of ion radii. A somewhat different structure
of [AmO2(H2O)6]1+ is obtained,
whereas the sixth water is excluded to the second hydration shell
owing to the weak electrostatic interaction between AmO21+ and water oxygen. Thus, the hydration number of AmO22+/1+ is five in resulting minimum-energy structures
of both [AmO2(H2O)n]2+/1+ (n = 1–6) complexes.
Since the solvation effect is significant on the geometry of [AmO2(H2O)n]2+/1+ and also plays a typical role in practical application, we only
report the geometry optimization results under the effect of aqueous
solvation in text. Table 1 presents the binding energies obtained at SR-B3LYP and CCSD(T)
levels of theory for the following reaction of [AmO2]2+/1+ + nH2O → [AmO2(H2O)n]2+/1+ (n = 1–6) in solution. As shown in Table 1, each of these [AmO2(H2O)n]2+ (n = 1–6) complexes is significantly more
stable than the corresponding [AmO2(H2O)n]1+ (n = 1–6).
At the SR-B3LYP level of theory, the americyl–water binding
energies steadily increase from 34.0 kcal/mol for [AmO2(H2O)1]2+ (19.1 kcal/mol for [AmO2(H2O)1]1+) to 119.0 kcal/mol
for [AmO2(H2O)5]2+ (68.2
kcal/mol for [AmO2(H2O)5]1+), whereas at the spin–orbit (SO) level of theory, the binding
energies show the same trend by increasing from 45.4 kcal/mol at n = 1 to 135.0 kcal/mol at n = 5 in the
series of AmO2(H2O)n2+. Overall, the substantial stabilizations of [AmO2(H2O)5]2+/1+ relative to
the isolated americyl and free water molecules favors the formation
of a maximum of five water ligands in the equatorial plane in the
first hydration shell. This five-coordination structure has been commonly
observed in other actinyls in water environment in the available experimental
studies and is in good accord with the published theoretical studies
using quantum mechanical method or molecular dynamics approach.
Table 1 Binding Energy (kcal/mol) for the
Reaction of AmO22+/1+ + nH2O → [AmO2(H2O)n]2+/1+ (n = 1–6) in Solution
at Different Levels of Theory with COSMO
[AmO2(H2O)n]2+ [AmO2(H2O)n]1+
B3LYP CCSD(T) B3LYP CCSD(T)
n ΔESR ΔESO ΔE ΔESR ΔESO ΔE
1 –34.0 –45.4 –64.7 –19.1 –31.0 –35.0
2 –64.6 –77.1 –120.9 –36.4 –49.7 –66.0
3 –88.5 –104.4 –173.5 –52.5 –68.4 –95.7
4 –110.2 –126.2 –213.1 –63.7 –93.6 –117.6
5 –119.0 –135.0 –68.2 –84.4
6 –113.7 –128.0 –65.1 –71.9
Geometric
Structure of the [AmO2(H2O)n]2+/1+ (n = 1–5)
Two different density functionals (Perdew–Burke–Ernzerhof
(PBE) and B3LYP) were first employed for the geometrical optimization,
which gave similar results, so only the results obtained at B3LYP/Am/ECP60MWB_SEG//O,H/cc-pVTZ
level of theory are presented in the text and those obtained at the
PBE/TZ2P level are detailed in the Supporting Information (Tables S1 and S2). As noted in the last section,
the inclusion of solution therefore and the use of a solvation model
are important in modeling the coordination structures of actinyl.
So the calculated ground-state geometries for [AmO2(H2O)n]2+/1+ (n = 1–5) in aqueous solution using the COSMO solvation
model are listed in Table 2 and shown in Figure 1. In terms of geometry, [AmO2(H2O)n]2+ and [AmO2(H2O)n]1+ have similar
geometric structures; these are the water molecules coordinating to
AmO22+/1+ on the equatorial plane of americyl
with an increasing hydration number from n = 1–5,
as expected, with the same hydration number as that of of uranyl,
neputonyl, and plutonyl in aqueous solution. The calculated Am–Oyl distances in the [AmO2(H2O)n]2+ complexes elongate from 1.669 Å
in pure americyl ion to 1.681 Å in [AmO2(H2O)1]2+ and increase all through to 1.711 Å
in [AmO2(H2O)5]2+, whereas
the Am–Oyl bonds in the [AmO2(H2O)n]1+ complexes appear to
follow the same trend, consistent with the decrease in the bond order,
attributed to the weakening of both ionic and covalent bonding interactions
of Am–Oyl bond from n = 1–5.
In all [AmO2(H2O)n]2+/1+ (n = 1–5) complexes, the
americyl is coordinated by water O atoms (Ow) with bond
Am–Ow distances longer than 2.2 Å, which implies
weak bonding interactions. In addition, all Am–Ow bond lengths in the complexes are beyond the range of Am–O
covalent single-bond lengths estimated by the sum of the self-consistent
covalent radii derived by Pyykkö.33 Expectedly, the Am–Ow bond lengths in the [AmO2(H2O)n]2+ complexes are shorter than the corresponding bond lengths in the
[AmO2(H2O)n]1+ complexes, owing to the stronger electrostatic interaction
in dication complexes. The lengthening of the Am–Ow bond distances in the [AmO2(H2O)n]2+ complexes from 2.260 Å at n = 1 to 2.460 Å at n = 5 implies
the reduction of bond strength and the weakening of bonding interaction
of each Am–Ow bond along with increasing hydration
numbers. Although each of the Am–Ow bonds is not
particularly strong in comparison to Am–Oyl multiple
bond, the overall bonding interaction is substantial, as indicated
by significant binding energies (Table 1) and by the extreme redshift in the americyl asymmetric
stretch frequency (Table 3).
Figure 1 Optimized geometry and binding energy (kcal/mol, in parentheses)
of AmO2(H2O)n2+/1+ (n = 1–5) at SR-B3LYP/Am/ECP60MWB_SEG//O,H/cc-pVTZ
levels of theory.
Table 2 Selected
Optimized Geometrical Structures
(Bond Length, Å, Angle, °) and Formation Energy (Ef, kcal/mol) for the Reaction of fϕ1fδ2 [AmO2(H2O)n]2+ and fϕ2fδ2 [AmO2(H2O)n]1+ (n = 0–5) at SR-B3LYP/Am/ECP60MWB_SEG//O,H/cc-pVTZ Levels of
Theorya
[AmO2(H2O)n]2+ [AmO2(H2O)n]1+
n state (symm.) Am–Oyl Am–Ow ∠OylAmOyl ∠OwAmOw state (symm.) Am–Oyl Am–Ow ∠OylAmOyl ∠OwAmOw
0 4Φ (D∞h) 1.669 5∑g(D∞h) 1.735
1 4B1 (C2v) 1.681 2.260 179.5 5A1 (C2v) 1.747 2.398 179.8
2 4B1 (C2v) 1.692 2.286 179.0 96.8 5A1 (C2v) 1.758 2.420 179.8 103.1
3 4A′ (Cs) 1.699 2.331, 2.326 179.8 127.8, 113. 2, 118. 7 5A′ (Cs) 1.768 2.448, 2.447, 2.445 179.9 122.2, 120.4, 117.4
4 4B2u (D2h) 1.707 2.371 180.0 92.7, 87.3 5Ag (C4h) 1.778 2.496 180.0 90.0
5 4A′ (Cs) 1.710 2.420, 2.462, 2.470 179.4 66.3, 74.5, 78.4 5A (C1) 1.781 2.562, 2.548, 2.586, 2.568, 2.589 179.4 72.0
a All optimizations are fully relaxed
without constraints.
Table 3 Calculated Vibrational Frequencies
of [AmO2(H2O)n]2+/1+ (n = 1–5) at SR-B3LYP/Am/ECP60MWB_SEG//O,H/cc-pVTZ
Levels of Theory with COSMO
Am–Oyl Am–Ow Am–Oyl Am–Ow
v3 v1 Δq(v3) v3 v1 v3 v1 Δq(v3) v3 v1
0 1053.7 925.1 925.6 828.0
1 1027.6 904.7 26.1 420.4 904.4 810.7 21.2 316.8
2 1009.1 891.6 18.6 385.7 412.4 882.9 792.7 21.4 309.8 307.6
3 994.8 880.7 14.2 360.8 367.5 866.0 777.7 16.9 260.1 290.0
4 980.9 868.4 13.9 312.0 351.7 849.5 764.7 16.4 246.9 275.0
5 970.4 855.9 10.5 273.9 314.2 839.1 754.1 10.4 239.6 252.6
For the monoaqua, the ground electronic states of
[AmO2(H2O)]2+/1+ have been confirmed
as 4B1 and 5A1 via a comparison
among
different multiplicities. Upon the coordination of Ow in
[AmO2(H2O)]2+/1+, the linear OylAmOyl is broken into bent ∠OylAmOyl angles of 179.5 and 179.8°, respectively. The
water molecule coordinates to americyl on the equatorial plane with
the two hydrogen atoms lying symmetrically on both sides of the plane.
The shortest Am–Ow bond distance of 2.26 Å
among the [AmO2(H2O)n]2+ series is within the range of single covalent bond
radii of Am–O (2.29 Å), mainly because of the strongest
bonding. These distances are consistent with the bonding analysis
detailed in the next section. The singly filled highest occupied molecular
orbitals of [AmO2(H2O)]2+/1+ have
roughly 98% Am 5fϕ and 90% Am 5fδ character, indicating that the Am 5f orbital is largely unperturbed
by the coordination of the ligands. Thus, [AmO2]2+/1+ retain their electron configuration at Am ions in those [AmO2(H2O)]2+/1+ complexes, namely, fϕ1fδ2 and fϕ2fδ2, respectively.
For the dual aqua, one additional water molecule locates in the
equatorial plane with a bent ∠OwAmOw angle
of 96.8° in [AmO2(H2O)2]2+ and 103.1° in [AmO2(H2O)2]1+, inducing a weakening of both axial and equatorial
bond strength, as reflected by the increase of 0.10 and 0.02 Å
in the Am–Oyl and Am–Ow bond distances
compared to those in [AmO2(H2O)1]2+/1+. The optimized Am–Ow bond distance
is 2.286 Å in [AmO2(H2O)2]2+ and 2.420 Å in [AmO2(H2O)2]1+; the slightly longer distance in the monocation
complex is consistent with the small binding energy. Noticeably, the
favorable bent versus linear geometries of the ∠OwAmOw reveals the covalent characteristic of Am–Ow bond, which pulls the two Ow atoms much closer,
leading to an Ow–Ow distance of 3.420
Å in [AmO2(H2O)2]2+ and 3.790 Å in [AmO2(H2O)2]1+. The electrons singly occupy on Am 5f6d atomic orbital
(AO)-based molecular orbitals (MOs) in [AmO2(H2O)]2+/1+, which provides extensive Am 5f → Ow 2p back-bonding, involving donation from an Am 5fϕ orbital into in-plane Ow 2p orbitals, thus leading to
a three-center interaction. The effectiveness of the Ow 2p → Am 5f6d dative bonding and Am 5f → Ow 2p back donation is less obvious in [AmO2(H2O)2]1+ due to a longer Am–Ow distance, denoted by a relatively large ∠OwAmOw angle of 103.1°. In particular, the variety in the average
effective charges of the Ow ligand, listed in Table 4, is an evidence to
this statement. The average Hirshfeld charges on the Ow of [AmO2(H2O)2]2+ and
[AmO2(H2O)2]+ are −0.16
|e| and −0.20 |e|, respectively,
slightly greater relative to those of −0.15 |e| and −0.20 |e| in [AmO2(H2O)1]2+/1+, as the consequence of the
Am-to-Ow back donation.
Table 4 Average Hirshfeld,
Voronoi Deformation
Density (VDD) Charges, and Average Mulliken, Multipole Derived Charges
(MDC_q) Spin Density on the B3LYP with COSMO-Optimized Structures
of [AmO2(H2O)n]2+/1+ (n = 1–5) from the PBE/TZ2P Calculations
[AmO2(H2O)n]2+ [AmO2(H2O)n]1+
charge spin density charge spin density
n Hirshfeld VDD Mulliken MDC_q Hirshfeld VDD Mulliken MDC_q
0 Oyl –0.03 0.22 –0.22 –0.23 –0.26 –0.08 –0.23 –0.28
Am 2.06 1.55 3.44 3.46 1.52 1.17 4.46 4.57
1 Oyl –0.09 0.09 –0.21 –0.22 –0.30 –0.18 –0.23 –0.29
Ow –0.15 –0.15 –0.01 –0.09 –0.20 –0.15 –0.01 –0.09
Am 1.77 1.27 3.43 3.48 1.32 0.96 4.46 4.61
2 Oyl –0.13 –0.02 –0.20 –0.22 –0.33 –0.28 –0.22 –0.30
Ow –0.16 –0.16 –0.01 0.01 –0.20 –0.16 0.00 0.02
Am 1.53 1.04 3.42 3.46 1.14 0.79 4.46 4.61
3 Oyl –0.17 –0.13 –0.19 –0.15 –0.35 –0.35 –0.22 –0.06
Ow –0.18 –0.16 –0.01 0.01 –0.20 –0.15 0.00 0.10
Am 1.31 0.81 3.41 3.20 0.98 0.59 4.45 3.69
4 Oyl –0.19 –0.19 –0.19 –0.09 –0.37 –0.40 –0.21 0.00
Ow –0.19 –0.18 0.00 0.07 –0.21 –0.18 0.00 0.07
Am 1.18 0.75 3.39 2.94 0.89 0.54 4.41 3.52
5 Oyl –0.21 –0.20 –0.19 –0.01 –0.38 –0.41 –0.23 0.00
Ow –0.20 –0.20 0.00 0.04 –0.21 –0.19 0.00 0.06
Am 1.11 0.74 3.39 2.68 0.82 0.52 4.45 3.51
For the triaqua, one more water molecule added with
the formation
of [AmO2(H2O)3]2+/1+ further
weakens the Am–O bonds, as identified by the longer Am–Oyl and Am–Ow bond distances than those in
[AmO2(H2O)2]2+/1+. In
gas phase, three coordinated water molecules are equivalent with the
∠OwAmOw angle of 120.0°, giving
a C3v symmetry structure.
However, when concerning the presence of aqua solvent, this symmetry
has been broken into Cs symmetry with
the ∠OwAmOw angles of 127.8, 113.2, and
118.7° in [AmO2(H2O)3]2+ and 117.4, 120.4, and 122.2° in [AmO2(H2O)3]1+ complexes, largely ascribed to the differences
responding to the polarization of the hydration upon solvent inclusion.
In essence, the solvent polarity is more effective in those complexes
with larger polarity. As listed in Table 2, the deviation from the high-symmetry structure
of the ∠OwAmOw angle in [AmO2(H2O)n]2+ is more
obvious than that in [AmO2(H2O)n]1+, suggesting that the structure of
dication ions could result in engaging in stronger hydrogen bonding
with the bulk solvent than that of monocation ions. For example, the
∠OwAmOw angles are 92.7 and 87.3°
in [AmO2(H2O)4]2+ and
66.3, 74.5, and 78.4° in [AmO2(H2O)5]2+, whereas 90.0° in [AmO2(H2O)4]1+ and 72.0° in [AmO2(H2O)5]1+ are retained, thus confirming
that the solvent shows greater differential stabilization in [AmO2(H2O)n]2+ complexes.
From our above discussion of [AmO2(H2O)n]2+/1+ structures,
we would expect
the additional water molecules to extend the Am–Oyl and Am–Ow bond lengths and to decrease the overall
degree of dative bonding, consistent with the lower relative binding
energy for the [AmO2(H2O)q]2+/1+ compared to that of the [AmO2(H2O)p]2+/1+ (5 ≥ q = p + 1). The maximum of five hydration
number in the first coordination shell is in good agreement with the
equilibrium structure having five water coordination of actinyl (UO22+, NpO22+, and PuO22+) in aqueous solution. In the equilibrium structure
of [AmO2(H2O)5]2+/1+,
four water molecules bonded to the center americyl are perpendicular
to the equatorial plane and the fifth coordinated water molecule arranges
within the equatorial plane where the dihedral angle between the equatorial
water ligands and the equatorial plane is 0° (Figure 1). The bond length of the fifth
Am–Ow bond is 2.420 Å in [AmO2(H2O)5]2+ and 2.548 Å in [AmO2(H2O)5]1+, the shortest one
among five Am–Ow bond distances, thus leading to
a slight bent of ∠OylAmOyl angles of
179.4°.
Electronic Structure and Chemical Bonding
of the [AmO2(H2O)n]2+/1+ (n = 1–5)
To provide
further insights into
the interactions between americyl ion and the water ligands of [AmO2(H2O)n]2+/1+, several bonding analyses were performed, including the bond order
analyses, population partitioning schemes, energy decomposition approach,
Kohn–Sham orbital interaction, and electron localization function
(ELF) method.
The bond order analyses by three methods give
a similar trend that is consistent with the previous detailed bond
length trend. Taking the Mayer Am–O bond index as an example,
the calculated Mayer bond orders (Table 5) of Am–Oyl and Am–Ow for the [AmO2(H2O)n]2+ complexes lie in two ranges, at averaged 1.9
and averaged 0.2, respectively, whereas those for [AmO2(H2O)n]1+ complexes
lie in two ranges, at averaged 1.85 and averaged 0.2, respectively.
This result indicates relatively weak Am–Ow bonding
interactions compared with the Am–Oyl bonding in
[AmO2(H2O)n]1+ complexes, which is resulted from not only the ionic bonding
nature but also the somewhat longer bond distance induced by weaker
orbital interaction. The calculated Am–Oyl bond
order in [AmO2(H2O)n]2+ decreases gradually from 2.05 at n = 1 to 1.88 at n = 5, whereas the Am–Ow bond order decreases from 0.39 at n = 1
further to 0.19 at n = 5, suggesting there is a general
decrease in Am–O bond strength with an increasing hydration
number. In addition to the bond order, the effective atomic charges
on Am and Ow ions can imply the variation of the ionicity
of the Am–Ow bond. Several charge analyses were
carried out on the B3LYP stationary structure in solution via COSMO.
Although the absolute values are different on the basis of different
methods used, the trend is the same. As listed in Table 4, the averaged Hirshfeld charges
reveal that Am carries a considerable positive charge and the Ow ligands carry substantial negative charges in these [AmO2(H2O)n]2+/1+ complexes, which is in good agreement with the bond order analyses,
indicating an ionic An–Ow bonding interaction. Generally,
the Am ions become less charged and both Oyl and Ow atoms become more charged along with the increase of the
hydration number, i.e., the calculated Hirshfeld charge of Am decreases
from +2.06 |e| in pure AmO22+ to +1.77 |e| in monoaqua and further to +1.11 |e| in penta-aqua, accompanied by an increased charge of
each Oyl atom from −0.03 |e| to
−0.21 |e|; this is due to the charge rearrangement
of americyl unit upon inclusion of explicit water in the first shell
and implicit water by COSMO, which is in good agreement with the study
of [UO2(H2O)m(OH)n]2–n.34 The averaged Hirshfeld charges of Ow atoms becoming greater from −0.15 |e| to
−0.21 |e| suggests overall increasing of electron
back donation into Ow ligand, thus leading to the Am–Oyl bond weakening with an increasing hydration number. In addition,
the decreased electron density localized on americyl unit listed in Table 4 indicates that the
charge transfer is from americyl unit to water ligands, owing to the
Am-to-Ow back donation. Furthermore, the formal Am oxidation
state of +VI and +V is not apparently affected by the hydration number
in these [AmO2(H2O)n]2+/1+ complexes via population analyses.
Table 5 Average Mayer Bond Orders of [AmO2(H2O)n]2+/1+ (n = 1–5)
from the PBE/TZ2P Calculations
[AmO2(H2O)n]2+ [AmO2(H2O)n]1+
Am–Oyl Am–Ow Am–Oyl Am–Ow
n vacuum COSMO vacuum COSMO vacuum COSMO vacuum COSMO
0 2.12 2.12 1.99 2.00
1 2.06 2.05 0.37 0.39 1.94 1.94 0.26 0.27
2 2.00 2.00 0.34 0.34 1.90 1.90 0.21 0.21
3 1.96 1.95 0.31 0.32 1.86 1.86 0.18 0.19
4 1.91 1.90 0.22 0.22 1.83 1.83 0.13 0.14
5 1.89 1.88 0.17 0.19 1.80 1.81 0.11 0.12
To better understand the orbital
interactions, Figure 2 shows the Kohn–Sham
MO energy levels of [AmO2(H2O)n]2+ at SR-PBE/TZ2P level. In the linear AmO22+ moiety due to Am–Oyl bonding,
the Am 5f and 6d orbitals transform as 5fu and 6dg species, respectively. Upon dative coordination with the water oxygen
atoms in the equatorial plane, the Am–Ow orbital
interactions cause to 6dg level further destabilization.
While both dδg and fδu–fϕu orbitals lie around the equatorial plane, the Am–Ow orbital interactions mainly affect the 6d orbitals, indicating
that the coordinated water molecules only slightly interact with the
“nonbonding” contracted 5f orbitals. This bonding module
is in good agreement with the well-known bonding principle proposed
for actinides by Bursten, the FEUDAL (“f’s are essentially
unaffected, d’s accommodate ligands”).35,36 Overall, the Am–Ow bonding in [AmO2(H2O)1]2+ is strongest among these
[AmO2(H2O)n]2+ complexes and becomes progressively weaker on increasing
the hydration number, consistent with the indirect evidence from geometries,
vibrational frequencies, and bond order. These conclusions are consistent
with the bonding compositions of the natural localized MOs (NLMOs, Table S5), with analysis detailed below.
Figure 2 Kohn–Sham
molecular orbital analyses of the AmO2(H2O)n2+ complexes
based on SR-zero-order regular approximation (ZORA) B3LYP/TZ2P calculations.
In addition to these chemical
bonding analyses based on wave functions
and electron densities, the energy decomposition analysis (EDA) based
on canonical molecular orbitals and the extended transition state
(ETS) method combined with the natural orbitals for chemical valence
(ETS–NOCV) theory were further applied to reveal the intrinsic
bonding mechanism in terms of the major contributions to the orbital
interactions. The computed EDA results for AmO22+/1+ + nH2O → [AmO2(H2O)n]2+/1+ (Tables 6 and 7) show that electrostatic ionic interaction (ΔEelstat) accounts for almost 2/3 contribution
to the total bonding energy (ΔEint), playing more significant roles than those of orbital interaction
(ΔEorbital). The decreasing trend
of both electrostatic interactions and covalent orbital interactions
are the same as those of bonding energies, that is, generally increasing
with the hydration number from monoaqua toward penta-aqua. The change
of ΔEelstat or ΔEorbital is not significantly in tetra-aqua and penta-aqua,
reflecting that the variation of both ionic and covalent interactions
with the increasing number of the water molecules becomes smaller
in aqueous solution. In contrast to the monotonous increase of ΔEelstat or ΔEorbital, the Pauli repulsion increases remarkably from 65.3 kcal/mol in
monoaqua to 159.6 kcal/mol in tetra-aqua, then declines to 151.4 kcal/mol
in penta-aqua, indicating the formation of the stable penta-aqua.
The ETS–NOCV analyses additionally reveal the intrinsic bonding
mechanism in terms of the contributions to the orbital interactions.
The results of some representative contributions for [AmO2(H2O)n]2+/1+ are
listed in Tables 6 and 7, and their deformation densities describing the
density inflow are shown in Figures 3 and 4, respectively. The highest
covalent character of each Am–Ow bond can be observed
in monoaqua among these [AmO2(H2O)n]2+/1+ complexes in terms of the orbital
interaction, which is decomposed into two types (π-type and
σ-type) with several terms, taking orb1–orb3 as examples,
providing energetic stabilizations of ΔEorb1 = −29.2 kcal/mol, ΔEorb2 = −14.4 kcal/mol, and ΔEorb3 = −6.4 kcal/mol, respectively. These natural
orbitals denote the typical π- or σ-type orbital interactions
achieved via two fragments of americyl and water molecules, relating
to the Am 5f6d-hybridized atomic orbitals and π-MOs of water
molecules contributed by Ow 2p atomic orbitals. Note that
consistent with the reduced trend of bonding energy of each Am–Ow bond across the series, the trend of the donation character
is also decreased accompanied by a decrease of major orbital contributions
and a slight lengthening of Am–Ow bonds. The composition
of the stabilization energy of each Am–Ow bond in
[AmO2(H2O)n]2+/1+ complexes is small, but the summarization is substantial
and increases across the series. Therefore, the orbital interactions
between the An 5f6d hybrid orbitals and π-MOs of Ow result in a significant covalent bonding character not only stabilizing
[AmO2(H2O)n]2+/1+ complexes beyond electrostatic ionic interaction but
also effectively supporting the weak bonding characteristics of 5f
orbital, which is consistent with the ELF result shown in Figure 5 and with the NLMO
analyses (listed in Table S5).
Figure 3 Contours of
representative deformation densities (isovalue = 0.001
au) between the interacting fragments of AmO22+ and H2O unit from ETS–NOCV analysis, describing
the density inflow (blue) and outflow (white).
Figure 4 Contours of representative deformation densities (isovalue = 0.001
au) between the interacting fragments of AmO2+ and H2O unit from ETS–NOCV analysis, describing
the density inflow (blue) and outflow (white).
Figure 5 Two-dimensional ELF contours (isovalue = 0.03 au) for the Ow–Am–Ow planes containing the Am–Ow interactions. The results are based on the SR-ZORA calculated
densities.
Table 6 ETS–NOCV Energy
Decomposition
Analyses between the Interacting Fragments of AmO22+ and H2O Unit and Their Corresponding Energy ΔEiorb (kcal/mol) from Open-Shell PBE/TZ2P
Calculations
1(4A) 2(4A) 3(4A) 4(4A) 5(4A)
AmO22+ (4A) fϕ1fδ2 AmO22+ (4A) fϕ1fδ2 AmO22+ (4A) fϕ1fδ2 AmO22+ (4A) fϕ1fδ2 AmO22+ (4A) fϕ1fδ2
frag. H2O (1A)···8a2 H2O (1A)···16a2 H2O (1A)···24a2 H2O (1A)···32a2 H2O (1A)···40a2
ΔEint –68.5 –125.7 –177.8 –218.3 –241.9
ΔEPauli 65.3 114.6 143.9 159.6 151.4
ΔEelstat –76.5 –138.7 –190.0 –223.7 –229.6
ΔEorb –57.4 –101.6 –131.7 –154.2 –163.7
α β α β α β α β α β
ΔE1 –14.5 –14.6 –17.5 –16.3 –14.2 –12.7 –19.3 –17.8 –16.6 –15.4
ΔE2 –7.8 –6.6 –10.5 –11.6 –13.8 –12.0 –10.5 –10.4 –14.2 –14.6
ΔE3 –3.1 –3.2 –11.4 –13.5 –8.5 –7.4 –11.5 –10.8
Table 7 ETS–NOCV Energy Decomposition
Analyses between the Interacting Fragments of AmO21+ and H2O units and Their Corresponding Energy
ΔEiorb (kcal/mol) from
an Open-Shell PBE/TZ2P Calculation
1(5A) 2(5A) 3(5A) 4(5A) 5(5A)
AmO21+ (5A) fϕ2fδ2 AmO21+ (5A) fϕ2fδ2 AmO21+ (5A) fϕ2fδ2 AmO21+ (5A) fϕ2fδ2 AmO21+ (5A) fϕ2fδ2
interacting
fragments H2O (1A)···8a2 H2O (1A)···16a2 H2O (1A)···24a2 H2O (1A)···32a2 H2O (1A)···40a2
ΔEint –39.3 –69.7 –98.9 –121.7 –129.7
ΔEPauli 38.5 70.6 92.7 103.2 100.4
ΔEelstat –48.1 –89.7 –124.9 –147.9 –149.9
ΔEorb –29.8 –50.6 –66.7 –77.0 –80.2
α β α β α β α β α β
ΔE1 –7.3 –6.6 –8.3 –7.1 –6.9 –6.7 –9.9 –8.7 –7.7 –6.9
ΔE2 –2.2 –2.0 –5.7 –5.2 –6.7 –6.7 –6.1 –5.7 –7.2 –6.5
ΔE3 –0.5 –0.5
Considering that the Am–Ow dative bond and back
donation were observed from density deformation analyses, NLMO calculations
were further explored to describe the extent of this bonding interaction.
The localized σ- and π- MOs on Am–Ow are made up of Am 5f6d and O 2s2p hybrid orbitals, which are composed
by roughly 95% O 2s2p lone-pair AO and ∼5% Am df hybrid orbitals
in [AmO2(H2O)n]2+ and by ∼98% O 2s2p lone-pair AO and ∼2% Am
df hybrid orbitals in [AmO2(H2O)n]1+ on the basis of the NLMO analyses.
The enhanced stability of [AmO2(H2O)n]2+/1+ complexes across the series can
only be explained as a result of the water coordinates inducing the
increased electrostatic energy. Noticeably, the Am 6d participating
in the dative oxygen bonding plays an important role over Am 5f due
to both more extended radial distribution of the Am 6d orbitals and
the better energy level matching between the An 6d and O 2p orbitals.
The compositions of the NLMOs from Am valence atomic orbitals decline
from around 3% of the σ orbitals and 7% of the π orbitals
in [AmO2(H2O)1]2+ to 1%
and 6% in [AmO2(H2O)5]2+.
Conclusions
Through relativistic quantum chemical calculations,
the electronic
and geometric structures of the [AmO2(H2O)n]2+/1+ (n = 1–6)
complexes have been systematically studied. Full five-coordination
binding of water ligands in the first shell is preferred in the aqua
solution for [AmO2(H2O)n]2+/1+. Extensive chemical bonding analyses of the
charges, energy decomposition analysis, and natural orbitals, all
agree in that the Am–Ow interaction is predominantly
ionic in nature, with a small extent of covalent bonding contribution
resulted from the An 5f6d-hybridized orbitals and relevant Ow 2p orbitals. The covalent orbital interaction between the equatorial
Ow and Am ions raises several interesting features in the
bonding of Am–Ow: (1) a bonding interaction between
the Am AOs and the Ow 2p orbitals arranges the water ligand
deviation from linear in [AmO2(H2O)2]2+/1+ into bent; (2) the reduced dative bonding affects
the Am–Ow bond length and bond order across the
series; (3) the small back-bonding donations of Am 5f → Ow 2p decrease the population of americium ions. As noted, the
implicit solvation model is unable to provide the dynamics information
of actinide ions in solution or the exchange of ion-influenced solvent
molecules with the bulk, which is important to some extent in practical
application. Further quantum mechanics/molecular mechanics molecular
dynamics simulation with explicit solvent is necessary to study statistically
the equilibrium between americyl and water in different coordination
shells. We hope that this investigation represents only the beginning
of long-term research relevant to the mission in spent fuel reprocessing
of the transplutonium, in addition to enriching our knowledge of actinide
coordination chemistry.
Methodology
The calculations on
the open-shell americyl complexes were carried
out with unrestricted Kohn–Sham wave functions. As known, the
molecular orbital (MO) diagram of pure americyl is similar to that
of uranyl: the combinations of the 2p orbitals of the two oxygen with
the 6d orbitals of the americium atom form occupied bonding orbitals,
whereas the combinations of the O 2p orbitals with the 5f manifold
orbitals of the actinide atom result in nonbonding δu and ϕu orbitals and antibonding σu* and πu* orbitals; the corresponding bonding σu and πu orbitals are found to have rather
small 5f contributions. In AmO22+ and AmO21+, the americium has the configurations 5f3 and 5f4, respectively, and these electrons are
spread in the nonbonding 5fδu and 5fϕu orbitals. Following Hund’s rule, the ground electronic states
of hexavalent and pentavalent Am ions have been found to be of a high-spin
character, that is, fδ2fϕ1 and fδ2fϕ2 configurations and 4Δ and 5Σ electronic states for AmO22+ and AmO21+, respectively. The spin–orbit coupling
(SOC) effects should be considered during the calculations of the
electronic structures of americyl complexes in solution.37
The scalar relativistic DFT calculations
were performed with the
Gaussian 09 and ADF 2017 softwares38−40 for the geometry optimizations
and vibrational frequency analyses. First, for geometry optimizations
by the Gaussian code, we used the scalar relativistic Stuttgart energy-consistent
relativistic 32 valence electron pseudopotential and the associated
ECP60MWB_SEG valence basis set41,42 for the americium atom.
The split-valence triple-ζ basis sets with polarization functions
(cc-pVTZ)43,44 were used for the oxygen and hydrogen atoms.
The B3LYP hybrid density functional45,46 was used in
these calculations. The solvent effects were approximated using the
Gaussian 09 implementation of the conductor-like screening solvation
model (COSMO) solvent model,47,48 where the solute is
embedded in a shape-adapted cavity consisting of interlocking spheres
centered on each solute atom or group. The combination of these pseudopotentials
and basis sets with this functional (labeled as B3LYP/Am/ECP60MWB_SEG//O,
H/cc-pVTZ level) has been shown to give accurate predictions of the
properties and reaction energies of actinide complexes.19,20 At the same B3LYP theory level, vibrational frequency calculations
were further performed to ensure that all force constants should be
positive and all frequencies should be real. Ultrafine integration
grids and very tight optimization were applied. The spin–orbital
symmetry restrictions were relaxed, performing spin-unrestricted UDFT
calculations.
The coupled cluster with singles, doubles, and
perturbative triples
(CCSD(T)) method49−51 in MOLPRO 2012 program52 was used for single-point calculations on the optimized aqueous-phase
B3LYP geometries to check whether the systems have multireference
character and to acquire more accurate relative energies. The ECP60MWB
pseudopotential with ECP60MWB_SEG basis set for Am and the cc-pVTZ
basis for O and H were applied in the CCSD(T) calculations. However,
limited by the computer resources, the nonsymmetry molecules of [AmO2(H2O)5]2+/1+ or [AmO2(H2O)6]2+/1+ cannot be handled
by CCSD(T) due to the giant basis of those molecules.
Further
electronic structure and chemical bonding analyses at the
DF level were performed with the ADF 2017. The scalar relativistic
(SR) effects were taken into account by the zero-order regular approximation
(ZORA).53,54 The SOC effects were taken into account
by SO-ZORA. The frozen-core approximation was applied to the atomic
[1s2–5d10] shell of Am and the [1s2] shells of the O atoms. The B3LYP combined with slater basis
sets of triple-ζ plus two polarization function (TZ2P) quality
were applied.55 Single-point calculations
were carried out on the B3LYP/Am/ECP60MWB_SEG//O H/cc-pVTZ optimized
aqueous-phase structures to determine the charge distribution and
bond order. The bond order analyses based on the Mayer method,56 Gopinathan–Jug indices,57 and Nalewajski–Mrozek method58,59 were performed. The charge analyses based on the Mulliken method,60 Hirshfeld analysis,61 Voronoi deformation density (VDD),62 and
multipole derived charges (MDC)63 were
calculated as well. The energy decomposition analyses (EDA) based
on canonical molecular orbitals and theoretical analyses via combined
extended transition state (ETS) with the natural orbitals for chemical
valence (NOCV) theory59,64−66 were carried
out. The electron localization functions (ELF) were calculated to
investigate the feature of the weak dative bonding. Weinhold’s
natural bond orbital (NBO)67 and natural
localized molecular orbital (NLMO)67−70 analyses were performed at the
B3LYP/6-31G* level71 on optimized geometries
from B3LYP calculations by using the NBO 5.0 program.72,73
In further geometry optimizations, the generalized gradient
approximation
with the PBE exchange–correlation functional74 was used in ADF 2017. Scalar (SR) and SO relativistic effects
were accounted by applying the same stratagem as detailed in the above
paragraph. The effects of water considered by COSMO were determined
using single-point energy calculation on gas-phase structures. The
atomic COSMO-default radii 210.0 pm was used.48
Supporting Information Available
The Supporting Information
is available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b01324.Selected optimized
geometrical structures (bond length
Å and bond angle °) for the fϕ1fδ2 [AmO2(H2O)n]2+ (n = 0–6)
at SR-B3LYP/Am/ECP60MWB_SEG//O,H/cc-pVTZ levels of theory with or
without COSMO (in parentheses) (Table S1); selected optimized geometrical
structures (bond length Å and bond angle °) for the reaction
of fϕ2fδ2 [AmO2(H2O)n]1+ (n = 0–6) at SR-B3LYP/Am/ECP60MWB_SEG//O,H/cc-pVTZ
levels of theory with or without COSMO (in parentheses) (Table S2);
binding energy (kcal/mol) for the reaction of AmO22+ + nH2O → [AmO2(H2O)n]2+ (n = 0–6) at different levels of theory (Table S3);
binding energy (kcal/mol) for the reaction of AmO21+ + nH2O → [AmO2(H2O)n]1+ (n = 0–6) at different levels of theory (Table S4);
natural localized molecular orbital (NLMO) analyses of [AmO2(H2O)n]2+/1+ (n = 1–6) from open-shell B3LYP/cc-pVTZ/ECP60MWB_SEG calculations
(Table S5); average Mayer, Gopinathan–Jug and Nalewajski–Mrozek
bond orders for Am–Oyl and Am–Ow on the B3LYP-optimized geometry of AmO2(H2O)n2+/1+ (n = 0–6) at the SR–PBE/TZP level with COSMO (Table S6);
average Mulliken and MDC_q charges and spin density on the B3LYP-optimized
geometry of [AmO2(H2O)n]2+/1+ (n = 0–6) in solution
from the PBE/TZP calculations (Table S7); calculated vibrational frequencies
(cm–1) of [AmO2(H2O)n]2+/1+ (n = 0–6) in aqueous
solution considered by COSMO at SR-B3LYP/Am/ECP60MWB_SEG//O,H/cc-pVTZ
l level of theory (Table S8); ETS–NOCV energy decomposition
analyses between the interacting fragments of AmO22+ and ligand units and their corresponding energy ΔEiorb (kcal/mol) on the B3LYP-optimized
geometry of AmO2(H2O)n2+ (n = 1–5) in solution
from an open-shell PBE/TZ2P calculation (Table S9); ETS–NOCV
energy decomposition analyses between the interacting fragments of
AmO21+ and ligand units and their corresponding
energy ΔEiorb (kcal/mol)
on the B3LYP-optimized geometry of AmO2(H2O)n1+ (n = 0–5)
in solution from an open-shell PBE/TZ2P calculation (Table S10); two
isomers (in-plane and perpendicular-to-plane) of water molecules for
[AmO2(H2O)1]2+/1+ and
[AmO2(H2O)2]2+/1+ at SR-B3LYP/Am/ECP60MWB_SEG//O,H/cc-pVTZ
levels of theory (Figure S1); optimized geometry of D6h, Ci symmetry
structures of [AmO2(H2O)6]2+ and [AmO2(H2O)7]2+ at
SR-B3LYP/Am/ECP60MWB_SEG//O,H/cc-pVTZ levels of theory (Figure S2)
(PDF)
Supplementary Material
ao8b01324_si_001.pdf
The authors
declare no competing financial interest.
Acknowledgments
We gratefully acknowledge the financial
support for this research
from the Science Challenge Project (No. TZ2018004) and the NSAF (U1530401),
the Foundation of President of China Academy of Engineering Physics
(No. YZJJSQ2017072), the Foundation for Development of Science and
Technology of China Academy of Engineering Physics (No. 2015B0102020),
and the National Natural Science Foundation of China (Nos. 21701006,
21771167, and 11874089). We are also grateful to the Beijing Computational
Science Research Center for generous grants of computer time.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145900010.1021/acsomega.8b01275ArticleDesign and Synthesis of Reactive Perylene Tetracarboxylic
Diimide Derivatives for Rapid Cell Imaging Zhang Endong †‡Liu Libing *†‡Lv Fengting †‡Wang Shu *†‡† Beijing
National Laboratory for Molecular Sciences, Key Laboratory of Organic
Solids, Institute of Chemistry, Chinese
Academy of Sciences, Beijing 100190, P. R. China‡ College
of Chemistry, University of Chinese Academy
of Sciences, Beijing 100049, P. R. China* E-mail: liulibing@iccas.ac.cn (L.L.).* E-mail: wangshu@iccas.ac.cn (S.W.).06 08 2018 31 08 2018 3 8 8691 8696 07 06 2018 24 07 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
A new water-soluble
reactive perylene tetracarboxylic diimide derivative
(PDI-pfp) is designed and synthesized that can realize fast imaging
of the endoplasmic reticulum in living cells. The PDI-pfp comprises
three functional moieties: perylene tetracarboxylic diimide as fluorescent
backbone, poly(ethylene glycol) for providing good water disperse
ability, and pentafluorophenol active ester as the reactive group
under physiological condition. On the basis of covalent reaction between
the active ester group of PDI-pfp and amine groups on cytomembrane,
PDI-pfp can rapidly interact with cytomembrane, followed by uptake
by living MCF-7 cells within 1 min and also exhibit low cell cytotoxicity.
Furthermore, it is proved that PDI-pfp acts as a universal imaging
agent for other types of cells. This fluorescent probe is of great
potential for the application in the rapid imaging of organelles in
cells.
document-id-old-9ao8b01275document-id-new-14ao-2018-01275mccc-price
==== Body
Introduction
On account of the properties of intuition,
multi-information, high
sensitivity, and specificity,1−6 indispensable and emerging fluorescent probes and materials for
cell imaging have been greatly developed.7−10 Compared to fluorescent proteins11 and fluorescent nanoparticles,12−16 organic dyes, which have smaller size, higher emission intensity,
and broader available spectral range, play an important role in fluorescence
imaging of cells.17−20 Furthermore, the design and synthesis of advantageous cell imaging
materials with good water solubility, high fluorescence quantum yield,
good biocompatibility, and low cytotoxicity are extremely imperative.
Perylene tetracarboxylic diimide (PDI) and its derivatives with
excellent redox and optical properties as well as superior photochemical
and thermal stabilities21−24 have been extensively applied in organic pigments,
electrophotography, and photovoltaic cells.25−28 Owing to the delocalized π-electronic
rigid plane structure, PDI is endowed with high fluorescence quantum
yield and, recently, has been widely utilized as a chromophore.29 However, the hydrophobic backbone of PDI results
in its poor solubility in aqueous solution, which has greatly limited
its application in biological systems. Two strategies have been employed
so far to enhance the water solubility of PDI: 1) the attachment of
hydrophilic chains at the imide nitrogen of PDI;30,31 and 2) the introduction of charge groups at the bay region of PDI.32
Pentafluorophenol active ester exhibits
high reactivity with many
functional groups,33−35 especially with amino groups under physiological
conditions. Therefore, pentafluorophenol ester as an active group
could be used to facilitate fluorescent probe to enter cells because
of the widely distributed amino groups on the cell surfaces.36 In this work, we report the design and synthesis
of a new water-soluble reactive perylene tetracarboxylic diimide derivative
(PDI-pfp) with high brightness, good water solubility, and high chemical
reactivity. By introducing oxylalkyl chains to PDI, the water solubility
is enhanced without affecting its high fluorescence quantum yield
because of the inappreciable influence of N-substituent for nodes
of highest occupied molecular orbital (HOMO) and lowest unoccupied
molecular orbital (LUMO) orbitals of PDI.21 Pentafluorophenol active ester offers PDI-pfp a high reactive group
to interact with cells. It was demonstrated that the PDI-pfp exhibited
low cytotoxicity and sufficient fluorescence ability for rapid imaging
of the endoplasmic reticulum (ER) in living cells.
Results and Discussion
The synthetic procedure of PDI-pfp is shown in Scheme 1. The precursor molecule PDI–COOH
was first synthesized by reacting perylene-3,4,9,10-tetracarboxylic
dianhydride (PDI) and NH2-PEG10-COOH in imidazole
at 130 °C for 5 h with a yield of 70%. PDI-pfp was then prepared
by esterification of PDI–COOH with pentafluorophenol in the
presence of N,N-dimethylaminopyridine
(DMAP) and 1-ethyl-3-(3-dimethylaminopropyl)carbodiimide (EDCI) in
dichloromethane overnight with a yield of 53%. All of the chemical
structures were confirmed by the 1H NMR and mass spectra.
Scheme 1 Synthetic Procedure of PDI-pfp
The photophysical properties of PDI–COOH and PDI-pfp
were
investigated in aqueous solution because the linkage of low toxic
and uncharged alkoxy chains extremely enhanced their solubility. UV–vis
absorption and fluorescence emission spectra of PDI and PDI-pfp were
measured in aqueous solution. As shown in Figure 1, owing to the fact that both PDI–COOH
and PDI-pfp consist of the same backbones, they exhibited quite similar
absorption with a maximum peak at 498 nm. On the basis of Lambert
Beer’s law, molar absorption coefficients of PDI–COOH
and PDI-pfp were calculated to be 2.7 × 105 and 1.9
× 105 M–1 cm–1, respectively. Moreover, PDI-pfp has nodes in the orbital HOMO and
LUMO at nitrogen atoms, which cause decoupling of single bonds between
nitrogen atoms and substitutions.14 Thus,
compared to the precursor molecule PDI–COOH, there is less
influence on the fluorescence of PDI-pfp. PDI-pfp exhibited a bright
green fluorescence with a maximum emission at 548 nm and an absolute
fluorescence quantum yield of 0.35 in aqueous solution, which shows
good potential for fluorescent imaging.
Figure 1 UV–vis absorption
and fluorescence emission spectra of PDI–COOH
and PDI-pfp in aqueous solution. The excited wavelength of 507 nm
was used for emission spectra.
Low cytotoxicity is necessary for fluorescent probes to be
utilized
in cell imaging and biology applications.37 Cytotoxicities of PDI-pfp and PDI–COOH were investigated
through a standard MTT (3-[4,5-dimethylthiazol-2-yl]-2,5 diphenyl
tetrazolium bromide) assay, in which optical density values of formazan
reduced from MTT by dehydrogenase in mitochondria of viable cells
were measured. In this experiment, MCF-7 cells were incubated in 96-well
culture plates treated with different concentrations of PDI and PDI-pfp
for 30 min. Then, the supernatant was discarded, and MCF-7 cells were
continuously cultured in fresh Dulbecco’s modified Eagle’s
medium (DMEM) for the next 24 h, and cell viabilities were measured
and calculated. As shown in Figure 2, PDI–COOH displayed nearly nontoxic behavior
up to 10 μM concentration, whereas PDI-pfp also exhibited less
cytotoxicity at concentrations lower than 10 μM, indicating
their good biocompatibility for cell imaging.
Figure 2 Viability of MCF-7 cells
after incubating with PDI-pfp and PDI–COOH
for 30 min treatment. [PDI-pfp] or [PDI–COOH] = 0–10
μM.
The ability of imaging for living
cells of PDI-pfp was then determined
using MCF-7 cells. To investigate the effect of pentafluorophenol
active esters of PDI-pfp on cell imaging, PDI–COOH without
pentafluorophenol active esters was also studied as control. To accomplish
this, considering the cell viability in Hank’s balanced salt
solution (HBSS), the incubation time was set as 30 min. MCF-7 cells
were treated with PDI–COOH and PDI-pfp for 30 min, and the
treated cells were washed with Hank’s balanced salt solution
(HBSS), followed by the addition of serum-free medium into the plates
for confocal laser scanning microscopy (CLSM) characterization. As
shown in Figure 3,
PDI-pfp with pentafluorophenol active esters as terminal groups could
uptake into MCF-7 cells and well stain cells. It is noted that MCF-7
cells internalized by PDI-pfp were observed in a good condition.
Compared with PDI-pfp, PDI–COOH with carboxyl groups at the
terminal position being negatively charged in aqueous solution is
believed to be repelled by the negatively charged membrane of cells,
leading to no interaction between PDI–COOH and MCF-7 cells.
Furthermore, the imaging results indicated that PDI-pfp with higher
concentration (10 μM) stains cells better than that with lower
concentration (5 μM).
Figure 3 CLSM images of MCF-7 cells incubated with PDI–COOH
and PDI-pfp
(5 and 10 μM) for 30 min. The excitation wavelength was 488
nm, and the fluorescence images were collected at the signals from
500 to 600 nm.
To further confirm the
localization of PDI-pfp inside cells, MCF-7
cells were incubated with PDI-pfp for 30 min, and then dyes using
specific imaging of organelles in cells were added. It was observed
that the location of PDI-pfp was well overlapped with that of ER Tracker
Red, which is used for specific staining of the endoplasmic reticulum
(ER) in cells (Figure 4a), while poor overlaps were seen with those of other organelle-specific
dyes. A white line that was randomly selected in the fluorescent image
of MCF-7 cells was chosen for obtaining the Pearson coefficient (Figure 4b). The value of
the Pearson coefficient was calculated to be 0.79178, which showed
that PDI-pfp was uptaken into cells and mainly located in the endoplasmic
reticulum.
Figure 4 (a) Colocalizing with endoplasmic reticulum-specific ER Tracker
Red after treating MCF-7 cells with PDI-pfp for 30 min. (b) Line-series
analysis of PDI-pfp with ER Tracker Red. The Pearson coefficients
were calculated along the white line on the MCF-7 cells. PDI-pfp and
ER Tracker Red were excited at the wavelengths of 488 and 559 nm,
respectively.
Rapid imaging of cells
is an overwhelming superiority of biomaterials.
The incubating times of cells with PDI-pfp at 1, 5, 10, 30, and 60
min were set as a time node to investigate the imaging ability of
PDI-pfp toward cells. Figure 5a demonstrates that PDI-pfp could be internalized immediately
and distributed in the cytoplasm of MCF-7 cells even within 1 min.
With the extension of incubation time, the accumulation amount of
PDI-pfp increased and maintained the same distribution in MCF-7 cells.
It was noted that the accumulation amount of PDI-pfp did change up
to 10 min. To prove the generality of PDI-pfp in rapid imaging toward
cells, HeLa cells were chosen as the representative of cancer cells,
and 293T cells were chosen as the representative of normal cells for
imaging experiments. As shown in Figure 5b,c, similar imaging results for HeLa cells
and 293T cells by PDI-pfp were observed as that of MCF-7 cells. Thus,
PDI-pfp exhibits great potential for application in the rapid imaging
of cells within 1 min. The uptake is the main driving force for the
fast internalization of PDI-pfp, and the reaction between PDI-pfp
containing pentafluorophenol active ester groups and amino groups
on the surface of cells assists the process.31
Figure 5 CLSM
images of cells treated with PDI-pfp (10 μM) with different
incubation times: (a) MCF-7 cells; (b) HeLa cells; and (c) 293T cells.
PDI-pfp were excited at the wavelength of 488 nm, and the fluorescence
images were collected at the signals from 500 to 600 nm.
Conclusions
In summary, a new water-soluble
reactive perylene tetracarboxylic
diimide derivative, PDI-pfp, with pentafluorophenol active ester on
the ends of the backbone was designed and synthesized. The alkoxy
chains efficiently enhanced the solubility of PDI-pfp in aqueous solution.
PDI-pfp exhibited low cell cytotoxicity and realized rapid imaging
of the endoplasmic reticulum (ER) of living cells. The high reactivity
between pentafluorophenol active ester groups and amino group on the
cell surface led to the fast uptake of PDI-pfp into cells even within
1 min. PDI-pfp exhibited generality of rapid imaging toward different
types of cells, including cancer cells (MCF-7 and HeLa cells) and
normal cells (293T cells). This fluorescent probe is of great potential
for application in the rapid imaging of organelles in cells.
Experimental
Section
Materials and Measurements
All chemicals were procured
from Sigma-Aldrich Chemical Company, J&K Chemical Company or AMRESCO
and used as received. All organic solvents were purchased from Beijing
Chemical Works and used without further purification. NH2-PEG10-COOH were purchased from Yanyi Biotech Company
Shanghai. Dulbecco’s modified Eagle’s medium (DMEM)
was purchased from HyClone/Thermo Fisher (Beijing, China). (3-(4,5′-Dimethylthiazol-2′yl)-2,5-dipehenyl-2H-tetrazolium hydrobromide) (MTT) was purchased from Xinjingke
Biotech (Beijing, China) and dissolved in 1× phosphate-buffered
saline (PBS) before use. The 1H NMR and 13C
NMR spectra were recorded on Bruker ARX 300 and ARX 400 instruments
with tetramethylsilane as the internal standard. High-resolution mass
spectra (HRMS) were taken on a Bruker 9.4T Solarix FT-ICR-MS spectrometer.
The UV–vis absorption spectrum was measured on a JASCO V-550
spectrophotometer. The fluorescence spectrum was taken on a Hitachi
F-4500 fluorometer equipped with a Xenon lamp excitation source. Absolute
fluorescence quantum yield was measured on Hamamatsu absolute photoluminescence
quantum yield spectrometer C11347. The MTT assay was performed on
a BIO-TEK Synergy HT microplate reader. Cell counting was performed
on an automated cell counter (Countess, Invitrogen). Cell imaging
was recorded by a confocal laser scanning microscope (FV 1000-IX81,
Olympus, Japan).
Synthesis of Compound PDI–COOH
3,4,9,10-Perylenetetracareboxylic
dianhydride (254.89 mol, 100 mg), imidazole (36 mmol, 2.5 g), and
NH2-PEG10-COOH (764.68 mol, 404.99 mg) were
mixed together in a 10 mL flask. The solution was heated to 130 °C
and refluxed for 5 h. The resulting mixture was cooled down to room
temperature. After adding 5 mL of chloroform and 5 mL of 1 M HCl under
sonication, the mixture was extracted with chloroform for three times.
The combined organic layer was washed by 1 M HCl (5 mL × 3) and
dried with anhydrous Na2SO4. The mixture was
concentrated and filtrated to remove the solids. Then, the solvent
was removed by vacuum, and the residue was a red oily liquid (yield:
254.2 mg, 70%). 1H NMR (400 MHz, CDCl3) δ
(ppm) 8.4 (s, 4H), 8.24 (s, 4H), 4.42 (s, 4H), 3.86 (t, J = 4 Hz, 8 Hz, 4H), 3.75 (t, J = 4 Hz, 8 Hz, 4H),
3.63–3.60 (m, 72H), 2.59 (t, J = 8 Hz, 8 Hz,
4H). HRMS (MALDI-TOF) m/z: [M +
H]+ calcd 1437.619831, found: 1437.619519.
Synthesis of
Compound PDI-pfp
PDI–COOH (254.2
mg, 179.58 mmol) and pentafluorophenol (99.16 mg, 538.73 mmol) were
dissolved in dichloromethane. EDCI (89.51 mg, 466.9 mmol) was then
added to the reaction mixture at low temperature using an ice bath,
followed by the dropwise addition of DMAP (5.7 mg, 46.69 mmol). The
reaction mixture was stirred overnight to ensure the completion of
the reaction. Afterward, the reaction mixture was extracted by dichloromethane
(20 mL × 3), and the combined organic layer was washed with distilled
water (20 mL) and NaCl saturated solution (50 mL) separately. After
drying with anhydrous Na2SO4, the solvent was
removed, and the residue was purified by silica gel chromatography
using dichloromethane/methanol (20:1) as the eluent to afford the
red crystal. (Yield: 165.56 mg, 53%) 1H NMR (400 MHz, CDCl3) δ (ppm) 8.658 (d, J = 13.6 Hz, 4H),
8.93 (d, J = 10.8 Hz 4H), 4.47 (t, J = 0.8 Hz, 0.8 Hz 4H), 3.883 (t, J = 3.2 Hz, 5.2
Hz, 4H), 3.744 (t, J = 3.2 Hz, 5.6 Hz, 4H), 3.618–3.607
(m, 72H), 2.939 (t, J = 8 Hz, 8.4 Hz, 4H). HRMS (MALDI-TOF) m/z: [M + H]+ calcd 1769.588213,
found: 1769.587103.
Optical Experiment
First, 10 μM
PDI-pfp and 10
μM PDI–COOH in aqueous solution (with DMSO less than
1% to improve the water dispersibility) were separately used to investigate
the photophysical properties, and the UV–vis absorption spectra
and fluorescent emission spectra (excited at 507 nm) were obtained.
The absolute fluorescence quantum yield of PDI-pfp in distilled water
was measured at an excited wavelength of 507 nm.
Cell Viability
Assay
Breast carcinoma cells (MCF-7
cells) were cultured in DMEM with 10% fetal bovine serum (FBS) at
37 °C under 5% CO2 atmosphere. The cells were seeded
in a 96-well culture plate at a concentration of 8 × 104 cells per mL and grown for 24 h. After washing with Hank’s
balanced salt solution (HBSS), different concentrations of PDI–COOH
and PDI-pfp dissolved in HBSS were added separately. Addition of HBSS
was considered as the blank group. This was followed by washing with
PBS and adding culture medium again. After incubating for 24 h and
abandoning the culture medium, 100 μL of 1 mg mL–1 MTT in HBSS was added into each well and incubated at 37 °C
under 5% CO2 atmosphere for 4 h. The supernatant was discarded,
followed by the addition of 100 μL of DMSO per well to dissolve
the formazan. A microplate reader measured the absorbance value of
each well at a wavelength of 520 nm. The cell viability rates were
calculated with the following equation where A is the absorbance
value of the experimental group to which was added PDI or PDI-pfp. Ab is the absorbance value of the group without
cells. A0 is the absorbance value of the
control group with cells to which was added HBSS alone.
Localization
Analysis of PDI-pfp in MCF-7 Cells
PDI-pfp
was dissolved to prepare 10 μM solution in HBSS. First, 1 μM
ER Tracker Red solution was prepared with HBSS. MCF-7 cells were incubated
in 35 × 35 mm plates. After washing with HBSS twice, MCF-7 cells
were incubated with 1 μM ER Tracker Red solution for 30 min.
Then, the supernatant was discarded before washing with HBSS again.
MCF-7 cells were incubated with 10 μM PDI-pfp solution for 30
min. Cells were washed with HBSS followed by adding serum-free culture
medium, and then the fluorescence images of MCF-7 cells were recorded
by CLSM; PDI-pfp and ER Tracker was, respectively, excited at the
wavelengths of 488 and 559 nm.
Cell Imaging with PDI-pfp
and PDI–COOH
Human
cervical carcinoma cells (HeLa cells) and human epithelial cells (293T)
were cultured in DMEM with 10% FBS at 37 °C under 5% CO2 atmosphere. Then, 5 μM and 10 μM of PDI–COOH
and PDI-pfp solutions were prepared with HBSS, respectively. MCF-7
cells, HeLa cells, and 293T cells incubated in 35 × 35 mm plates
were washed with HBSS twice before using. Washed MCF-7 cells were
incubated with 5 and 10 μM of PDI–COOH and PDI-pfp solutions
at 37 °C for 30 min. In addition, washed MCF-7 cells, HeLa cells,
and 293T cells were incubated with the addition of 10 μM of
PDI-pfp solutions at 37 °C for 1, 5, 10, 30, and 60 min. Discarding
the supernatant and washing with HBSS twice was followed by adding
serum-free culture medium, and then the fluorescence images of cells
were recorded by CLSM using 488 nm as excitation wavelength.
Author Contributions
The manuscript
was written through contributions of all authors. All authors have
given approval to the final version of the manuscript.
The authors
declare no competing financial interest.
Acknowledgments
The authors
are grateful to the National Natural Science Foundation
of China (Nos 21473220, 91527306, and 21661132006).
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145909910.1021/acsomega.8b00675ArticleNew Generation of N-Chloramine/QAC
Composite Biocides: Efficient Antimicrobial Agents To Target Antibiotic-Resistant
Bacteria in the Presence of Organic Load Ghanbar Sadegh †Kazemian Mohammad Reza ‡Liu Song *†‡§†Department
of Chemistry, Faculty of Science and ‡Department of Biosystems Engineering,
Faculty of Agricultural and Food Sciences, University of Manitoba, Winnipeg R3T 2N2, Canada§ Department
of Medical Microbiology, Rady Faculty of Health Sciences, University of Manitoba, Winnipeg R3E 0J9, Canada* E-mail: Song.Liu@umanitoba.ca.22 08 2018 31 08 2018 3 8 9699 9709 10 04 2018 03 08 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
We previously reported
that covalently joining an amide-based N-chloramine
with a quaternary ammonium compound (QAC) can
yield a new composite biocide with faster inactivation of various
bacteria. Importantly, the composite biocide was found to reduce the
risk for potential bacterial resistance associated with QAC. However,
similar to other N-chloramines and QACs, this high-performance
composite biocide becomes less potent against pathogenic bacteria
in the presence of high protein fluids. In this study, we substituted
the amide-based N-chloramine moiety in the previously
reported composite biocide with a secondary amine-based N-chloramine to improve the biocidal efficacy in biological fluids.
The N–Cl bond in the synthesized tetramethylpiperidine-based
composite biocides is more stable in a high protein medium (HPM) than
that in the hydantoin (amide)-based composite biocides. The composite
biocide, 2-[4-(1-chloro-2,2,6,6-tetramethyl-piperidin-4-yloxymethyl)-[1,2,3]triazol-1-yl]-ethyl-dodecyl-dimethyl-ammonium
chloride (6a), showed the best antibacterial activity
in both phosphate-buffered saline and HPM among various composite
biocides and benzyldodecyldimethylammonium chloride used in this study.
document-id-old-9ao8b00675document-id-new-14ao-2018-00675hccc-price
==== Body
Introduction
Disinfection of hospital environment and
food processing facilities
has been an indispensable and valuable preventative measure for ensuring
human health. In the context of rising antibiotic resistance and cross-resistance
between antimicrobials and antibiotics,1−3 development of new potent
non-resistance-inducing disinfectants becomes even more pivotal.
Membrane active compounds, such as quaternary ammonium compounds
(QACs), account for a big portion of disinfectants. They have been
widely used in hospitals for infection control and by public for better
hygiene. Reports on bacterial resistance to QACs indicate a concerning
trend.4−7 In 2012, up to 83% of methicillin-resistant Staphylococcus
aureus (MRSA) isolates carry qac resistance genes
in comparison to 10.2% in 1992.4,5 A recent study suggests
that besides QacA efflux pump, membrane mutation also greatly contributes
to bacterial resistance against QACs. Such strategies as creating
multicationic centers have met with certain success in combating bacterial
resistance.8,9 Similarly, covalently joining QACs with
other disinfectants with different modes of action might also serve
as an effective strategy in thwarting bacterial resistance against
QACs.
Recently, we reported the synthesis of a series of composite
biocides
with both quaternary ammonium (QA) and N-chloramine
moieties.10,11 The potential of one composite biocide,
[3-(3-chloro-4,4-dimethyl-2,5-dioxo-imidazolidin-1-yl)-propyl]-dimethyl-tetradecyl-ammonium
chloride (compound 2), and its corresponding precursor,
[3-(4,4-dimethyl-2,5-dioxo-imidazolidin-1-yl)-propyl]-dimethyl-tetradecyl-ammonium
chloride, (compound 1), in inducing bacterial resistance
was studied.12 We were unsuccessful in
isolating Pseudomonas aeruginosa mutants
with decreased susceptibility to compound 2 despite arduous
efforts of achieving the goal with two different strategies: recovering
mutants from the zone of clearing and isolating mutants through exposure
to gradually increasing concentrations of biocides. Interestingly,
the presence of N-chloramine moiety in compound 2 seems potentially overcome the risk of selecting mutants
of P. aeruginosa with reduced susceptibility
against the quaternary ammonium part.
The antimicrobial action
of N-chloramines occurs
via different pathways, such as formation of chlorine cover and attack
of the bacterial cell wall proteins, penetration into the bacterial
cell followed by attacking the intracellular vital component. N-chloramines attack various targets in living cells, particularly,
sulfur-containing amino acids, such as cysteine and methionine, interfere
with hydrogen bonding in proteins and affect protein functions governed
by their structures.13,14
On the other hand, the
attraction between the positively charged
nitrogen on QACs and negatively charged head groups of bacterial membrane
phospholipids kicks off the antibacterial action of QACs. As soon
as this bond forms, the long alkyl chain penetrates and integrates
into the membrane core.4 When the concentration
of QAC is high, the bacterial membrane destruction (or hole generation)
occurs due to micelles formation and aggregation.15 Also, QACs can disrupt and denature the structure of proteins
and enzymes.4 Covalently joining a QAC
with an N-chloramine can give a composite biocide
that could inactive bacteria through all of the above-mentioned modes
of action. This can not only minimize the chance of bacterial resistance
but also enhance the overall biocidal activity.
However, disinfectants
often encounter interfering substances,
such as proteins and carbohydrates, while fulfilling their tasks.
Specifically, N-chloramines can be quenched by proteins
through direct contact.16 This challenge
presents a need to develop new antimicrobials, which are more resistant
to interfering substances, such as proteins. Thiol-containing proteins
can reduce N-chloramines and therefore quench their
antimicrobial activity. Also, active chlorine (Cl+) in N-chloramines can transfer to amine, amide, and imide groups
in proteins. In chlorine-transfer reaction (transchlorination), the
oxidation capacity is a good measure for the ability of N-chloramines to exchange chlorine with another amine, amide, and
imide groups. The reactivity of the active chlorine in N-chloramines is in the following order: amines < amides < imides,
and therefore stability of N-chloramines follows
the reverse order.17 The above-mentioned
compound 2 contains an amide-based N-chloramine. Given the following stability sequence of N-chloramines: amines > amides > imides, an amine-based N-chloramine composite biocide was designed in this study
to present
improved antibacterial activity in a high protein medium (HPM) consisting
of 5% fetal bovine serum (FBS). The proposed mode of action of a composite
biocide with both N-chloramine and QA moieties is
that the composite biocide punches holes in bacterial membrane due
to the QA moiety (mode of action of QACs) and therefore facilitates
the penetration of the whole composite molecule into the bacteria,
allowing its N-chloramine component to exert oxidative
stress inside cells causing fast inactivation of the bacterial cell.
We hypothesized that an amine-based N-chloramine
can better escape the quenching action of proteins and therefore be
preserved to exert oxidative stress inside a bacterial cell to result
a fast kill after the whole biocide gets into the cell through the
holes in the bacterial membrane generated by the QA moiety (Scheme 1). Specifically,
a secondary amine-based N-chloramine was linked to
a QA moiety with an alkyl chain of 12 or 14 methylene units via a
triazole ring linkage, and the antibacterial activity of these compounds
was evaluated against Gram-negative and Gram-positive bacteria. This
strategy led us to antimicrobial agents, which may be better suited
for applications with high protein loadings, such as disinfection
of wounds or food contact surfaces (Scheme 1).
Scheme 1 (a) Proposed Mode of Action of the
Secondary Amine-Based N-Chloramine and Its Resistance
against Protein Quench,
(b) Proposed Mode of Action of the Amide-Based N-Chloramine
and Its Quench by Proteins
Results
Chemistry Synthesis
We previously
demonstrated the
antibacterial enhancement effect of covalently bonding long alkyl
chain QAC moieties to an amide-based N-chloramine
(compound 2 in Scheme 2).10 In this study, we joined
an amine-based N-chloramine to QACs with an alkyl
chain of 12 or 14 carbon atoms (6a, 6b in Scheme 2) with an intention
to improve the antibacterial efficacy of the composite biocide in
the presence of organic matters, such as proteins. [3-(4,4-Dimethyl-2,5-dioxo-imidazolidin-1-yl)-propyl]-dimethyl-tetradecyl-ammonium
chloride (compound 1), dodecyl-dimethyl-{2-[4-(2,2,6,6-tetramethyl-piperidin-4-yloxymethyl)-[1,2,3]triazol-1-yl]-ethyl}-ammonium
chloride (5a), dimethyl-tetradecyl-{2-[4-(2,2,6,6-tetramethyl-piperidin-4-yloxymethyl)-[1,2,3]triazol-1-yl]-ethyl}-ammonium
chloride (5b) are the corresponding N-chloramine precursors (i.e., containing only a QA moiety) of the
composite biocide, and benzyldodecyldimethylammonium chloride (BC) was used as a QAC control in antibacterial tests. The
chemical reactions pathway is represented in Scheme 3. An overnight reaction between long chain
alkyl bromides and 2-azido-N,N-dimethyl-ethanamine
led us to azido-functionalized QACs 3a and 3b. 2,2,6,6-Tetramethyl-4-(prop-2-ynyloxy)piperidine 4 was prepared using the method reported by Barnes et al.18 from 2,2,6,6-tetramethylpiperidinol. Piperidinol
derivative 4 and two QACs 3a/3b were then linked together via a triazole bridge to get 5a and 5b with Br− counterion. 5a, 5b and compound 1 with Br− counterion were passed through an ion-exchange resin
to replace the counterion Br– with Cl– followed by performing the chlorination reaction using t-BuOCl to obtain {2-[4-(1-chloro-2,2,6,6-tetramethyl-piperidin-4-yloxymethyl)-[1,2,3]triazol-1-yl]-ethyl}-dodecyl-dimethyl-ammonium
chloride (6a), {2-[4-(1-chloro-2,2,6-trimethyl-piperidin-4-yloxymethyl)-[1,2,3]triazol-1-yl]-ethyl}-dimethyl-tetradecyl-ammonium
chloride (6b), and [3-(3-chloro-4,4-dimethyl-2,5-dioxo-imidazolidin-1-yl)-propyl]-dimethyl-tetradecyl-ammonium
chloride (compound 2), respectively.
Scheme 2 Structures of Biocides
Used in This Research
Scheme 3 Chemical Reaction Pathways
(a)
NaN3, KOH, H2O, reflux, overnight, (b) R-Br,
acetonitrile, reflux, overnight,
(c) propargyl bromide, NaH, tetrahydrofuran (THF), N2,
60 °C, 5 h, (d) CuSO4, Cu, MeOH/H2O, room
temperature, overnight, (e) anion-exchange resin (Amberlite R IRA-900,
Cl–) tert-butyl hypochlorite, acetone/H2O, 0 °C, 1 h. Ra: Alkyl substitution on the compounds
bearing the letter “a” in the name and Rb: alkyl substitution
on the compounds bearing the letter “b” in the name.
Copper Analysis
Cu(II) was used
as a catalyst in the
click reaction to link 2,2,6,6-tetramethyl-piperidin with the long
chain QA moiety. It is known that copper ion possesses antibacterial
activity.19 To avoid unwanted interference
in the antibacterial activity of the new composite biocides, copper
ion was removed by using a chelating column made of Sorbtech CR20-01
beads. Cu327.395 in 5a and 5b was quantified to be 0.13 and 0.075 ppm, respectively. The amount
of Cu324.754 also was measured and appeared to be 0.127
and 0.068 ppm for 5a and 5b. The amount
of copper left in each compound found to be much less than the minimum
concentration of copper required for antibacterial activity, reported
to be 40 ppm by Gyawali et al.20
Redox
Titration
We proceeded to study the stability
of N-chloramines in the HPM (5% FBS in phosphate-buffered
saline (PBS)) using a redox titration assay, and the results are presented
in Figure 1. The active
chlorine content of compound 2 (amide-based N-chloramine) dropped to 80% within the first 5 min of contact, and
the chlorine content reached a plateau at around 60% after 60 min.
On the other hand, both 6a and 6b compounds
(amine-based N-chloramines) were significantly more
stable (p < 0.05), and their chlorine content
was still maintained at >80% after 60 min. The loss rate of active
chlorine in HPM was significantly lower (p < 0.05)
for the two amine-based N-chloramines than the amide-based N-chloramine in the first 5 min. These results showed that
the N–Cl bond of secondary amines (6a and 6b) was less reactive with proteins in FBS than that of amides.
Figure 1 Stability
of N-chloramines 6a, 6b, compound 2 as reflected by the remaining
percent of active chlorine ([Cl+]%) in the high protein
medium (HPM). Studies were performed at 23 °C and pH 7.4. Values
represent the mean ± standard deviation (SD). n = 3 for all three compounds.
Antibacterial Evaluation of the Synthesized Biocides
Table 1 lists the
time needed (total kill (Tk)) for the
antimicrobial agents to inactivate all of the chosen bacteria (total
kill) in different solutions (PBS and HPM). The total kill is claimed
when the bacteria level is equal to or below the 1.82 log detection
limit and equivalent to 4.18 log bacterial reduction with the starting
bacterial concentration of 106 CFU/mL.
Table 1 Time Required to Reach the Total Kill
(Tk) (4.18 log Reduction) for Various
Compounds in PBS and HPM against Four Strains of Bacteriaa
time
to total kill (Tk) (min)
bacterial strain medium 5a 6a 5b 6b compound 1 compound 2 BC
methicillin-resistant Staphylococcus aureus (MRSA) (70065) PBS >60 3 60 5 10 3 10
HPM >60 10 >60 30 5 10 20
Escherichia
coli (25922) PBS >60 3 >60 3 30 3 3
HPM >60 3 >60 5 30 20 5
multidrug-resistant (MDR) P. aeruginosa (73104) PBS >60 <1 <1 <1 5 5 5
HPM >60 3 60 20 60 30 10
wild-type P. aeruginosa (PA01) PBS >60 3 5 3 5 5 5
HPM >60 20 60 >60 >60 >60 30
a Initial concentration of compounds
in PBS and HPM are 141.0 and 423.1 μM, respectively. n = 3 for all compounds.
As can be found in Table 1, when the medium was changed from PBS to
HPM, increase in Tk for 6a and 6b was
9 min on average, whereas Tk increase
in the case of compound 2 was 16 min (excluding data
of PA01). This means that the deterioration of antimicrobial activity
in the case of piperidine (a secondary amine)-based N-chloramine compounds (6a, 6b) was less
than compound 2. On the other hand, the performance of
compound 2 in PBS was better than compound 1, but their activity was almost the same in HPM, which indicates
that [Cl]+ on compound 2 is reduced in HPM,
and compound 2 is partially converted back to compound 1, as revealed in Figure 1.
Figures 2–5 present the quantitative
antibacterial results
over the contact time against four bacteria in various media. The
composite biocides appeared to be more effective against the Gram-negative
strains (E. coli and P. aeruginosa) than Gram-positive one (MRSA).
Figure 2 Bacterial viability
(log) as a function of contact time between
biocides and methicillin-resistant S. aureus (MRSA) in the high protein medium (HPM, 5% FBS in PBS) and PBS.
Studies were performed at 23 °C and pH 7.4. Values represent
the mean ± SD. n = 3 for all of the compounds
(the starting inoculum size is indicated in the bracket after each
compound in the legend).
Against MRSA (Figure 2), 6a and compound 2 showed the
best performance
in PBS. As expected, their activity deteriorated in HPM, but the extent
of deterioration varied with antimicrobial agents. Among all biocides
used in this study, compound 1 showed the best antibacterial
activity in HPM.
Biocides demonstrated different antibacterial
behavior against
Gram-negative bacteria E. coli and
MDR P. aeruginosa. The activity of
compound 2 against E. coli significantly dropped (p < 0.05) in HPM in comparison
to PBS (Figure 3).
However, 6a and 6b showed insignificant
change in their activity (p > 0.05) in two media
and were significantly faster in inactivating E. coli in HPM than compound 2 (Tk = 3, 5 versus 20 min). In the case of MDR P. aeruginosa (Figure 4), 6a and 6b illustrated significantly superior
killing than others in the first 5 min (p < 0.05)
in PBS. In HPM, 6a displayed the least decline in their
activity among the chlorinated biocides. compound 1 presented
a slow killing kinetics and the most severe deterioration of antimicrobial
activity in HPM against MDR P. aeruginosa.
Figure 3 Bacterial viability (log) as a function of contact time between
biocides and E. coli in the high protein
medium (HPM, 5% FBS in PBS) and PBS. Studies were performed at 23
°C and pH 7.4. Values represent the mean ± SD. n = 3 for all of the compounds (the starting inoculum size is indicated
in the bracket after each compound in the legend).
Figure 4 Bacterial viability (log) as a function of contact time
between
biocides and MDR P. aeruginosa in the
high protein medium (HPM, 5% FBS in PBS) and PBS. Studies were performed
at 23 °C and pH 7.4. Values represent the mean ± SD. n = 3 for all of the compounds (the starting inoculum size
is indicated in the bracket after each compound in the legend).
Wild-type P. aeruginosa was the
least susceptible strain among the tested Gram-negative bacteria.
All biocides, except 5a, were effective against this
strain in PBS and reached total kill within 5 min of contact (Figure 5). However, only 6a (in 20 min), BC (30 min) and 5b (60 minutes) reached total kill of
PA01 in HPM, and all other biocides failed to reach total kill in
HPM in the tested time frame (60 min). 6a clearly stands
out as the most potent biocide among all of the tested ones in both
PBS and HPM when being challenged with the least susceptible bacterium.
Figure 5 Bacterial
viability (log) as a function of contact time between
biocides and wild-type P. aeruginosa PA01 in the high protein medium (HPM, 5% FBS in PBS) and PBS. Studies
were performed at 23 °C and pH 7.4. Values represent the mean
± SD. n = 3 for all of the compounds and results
are significantly different (p < 0.05) (the starting
inoculum size is indicated in the bracket after each compound in the
legend).
MRSA, P. aeruginosa, E. coli, and wild-type P. aeruginosa were also challenged by sodium hypochlorite
in PBS at 141.0 and
282.1 μM (equivalent to 5 and 10 ppm [Cl+]) and in
HPM at 423.1 and 864.3 μM (equivalent to 15 and 30 ppm [Cl+]) for 10, 20, 30, and 60 min. The initial bacterial concentrations
for the above bacteria were 4.2 × 106, 4.8 ×
106, 5.4 × 106, and 3.6 × 106 CFU/mL, respectively. No significant bacterial reduction was observed
at the tested concentrations within 1 h of contact of all of the bacteria
(p > 0.05) except for one case: 23% reduction
of
MRSA achieved by 282.1 μM sodium hypochlorite (equivalent to
10 ppm [Cl+]) in PBS within 60 min of contact (p = 0.027 < 0.05).
Discussion
Antimicrobial
efficacy of multiple QACs compounds was tested against
different bacteria in PBS and HPM. It was observed from Table 1 that in PBS, chlorinated compounds
(6a, 6b, and compound 2) performed
better than nonchlorinated ones (5a, 5b,
and compound 1). This indicates that the introduction
of either amide or amine-based N-chloramine boosts
the antibacterial activity of the whole composite biocides. However,
in HPM, the antimicrobial efficacy of all biocides (chlorinated and
nonchlorinated) (except compound 1 against MRSA) deteriorated,
and Tks of all of the tested biocides (except compound 1 against MRSA) increased in comparison to those obtained in PBS.
In the case of QACs, this deterioration in activity might be the result
of ionic and hydrophobic interactions between QAC and negatively charged
peptides and hydrophobic domains on proteins, which resulted in binding
of QAC molecules to proteins and deactivation of QAC.21 On the other hand, N-chloramines could
transfer their active chlorine to proteins through direct contact
or be reduced by sulfur-containing amino acids, such as cysteine and
methionine in HPM.22 The reaction kinetics
of N-chloramine with proteins varies from one compound
to another. Active chlorine loading on the composite biocides was
monitored as a function of time in PBS and HPM (Figure 1). It is confirmed that secondary amine-based
composite biocides (6a and 6b) are more
resistant to protein quench than their amide-based counterpart (compound 2). This correlates well with their superior activity against E. coli in HPM as compared with compound 2 (Table 1). But the
result that Tks of 6a against the other three bacteria
in HPM were significantly shorter (p < 0.05) than
those of both 6b and compound 2 reveals
the existence of other important factors affecting their antibacterial
activity in HPM. The proper balance of hydrophobicity and hydrophilicity
in the composite biocide 6a with a C12 alkyl chain might
contribute to more effective membrane damage (mode of action of QACs)
and be one of the other factors. One more possible factor could be
associated with less protein binding of a QAC with a C12 alkyl chain
(6a) via hydrophobic interaction, as reported by Jono
and co-workers.21 They found that C14-benzalkonium
chloride was deactivated more than C12-benzalkonium chloride in the
presence of proteins. This led to less quench of the biocide by proteins
in HPM through the deactivation mechanism of QAC: electrostatic and
hydrophobic interactions.
Gilbert and Moore15 have shown that
antibacterial activity of QACs is a function of their structure, alkyl
chain length, and strain of bacteria. For example, to be effective
against Gram-positive bacteria, the alkyl chain of QACs should consist
of 12–14 carbon atoms, however, in the case of Gram-negative
bacteria, the number of carbon atoms in the alkyl chain should be
between 14 and 16. N-chloramines are more hydrophobic
than their amine/amide precursors, and the added hydrophobicity in N-chloramine/QAC composite biocides might move the optimum
alkyl chain length against Gram-negative bacteria from 14–16
to 12.
In antibacterial test against Gram-negative bacteria E. coli and P. aeruginosa, the antibacterial efficacy of 6a and 6b appeared to be less compromised by HPM than compound 2, whereas compound 2 and 6a showed similar
changes in antibacterial kinetics in two media (PBS and HPM) against
MRSA. These results still correlate with the stability of N-chloramine in HPM and can be explained using our hypothesized
mechanism. Proteins in HPM neutralize the amine-based N-chloramine at a slower pace than the amide-based N-chloramine so that the amine-based N-chloramine
is preserved to exert oxidative stress inside a bacterial cell after
the whole molecule diffuses into the cell through the holes in the
bacterial membrane due to the mode of action of the QA moiety. However,
to what degree this advantage of better preserved amine-based N-chloramine can be manifested is also dependent on how
effectively bacterial cells can adsorb the biocides, which is the
first step of QACs’ action of disrupting bacterial membranes. E. coli has a much higher number density of negative
charges (0.145 m–3 at pH 7) than S. aureus (0.025 m–3 at pH 7),23 which might be the reason why this advantage
of better preserved amine-based N-chloramine is not
clearly shown in the challenge test against MRSA in HPM (Figure 2). The thick cell
wall of MRSA might also play a role by delaying the interaction of
the positively charged biocides with bacterial cell membrane. As can
be seen from Figures 2 and 3, BC showed a faster killing
kinetics against E. coli than S. aureus.
5a and 5b were very ineffective against E. coli even in PBS (Figure 3). One possible reason is that the piperidine
functional group is very basic (pKa of
its conjugate acid is around 11)14 and
become protonated in pH 7.4 PBS, greatly increasing the hydrophilicity
of the whole molecules of 5a and 5b. QACs
act on bacterial membranes by inserting their hydrophobic tails into
the hydrophobic membrane core. The enhanced hydrophilicity due to
the protonated piperidine functional group might impede this interaction,
hence compromising the antibacterial potencies of both 5a and 5b. Chlorination of the synthesized QACs boosts
their antibacterial activity via two different mechanisms. First,
chlorine changes the hydrophilicity of QAC compounds by transforming
the positively charged piperidine functional group in biological pH
(7.4) to a neutral moiety (decreased basicity due to the presence
of chlorine). Therefore, the hydrophilicity of the compounds drops,
allowing QACs to better interdigitate into the bacterial membrane
and negatively impact on its osmoregulatory and physiological functions.24 Secondly, active chlorine also attacks targets
in bacterial cells. As reflected from the antibacterial results of
sodium hypochlorite, active chlorine [Cl+] alone at the
tested concentrations within the tested time frame (1 h) in either
PBS or HPM is not effective in killing those bacteria. This indicates
again that the N-chloramine moiety together with
the QA moiety attacks bacterial cells in a potentially synergistic
manner.
Conclusions
Nowadays, prevention of bacterial contaminations
in food industries
has become difficult due to long food production line, large production
volume of food, and antimicrobial resistance.25 Also, the number of effective antimicrobial agents with a good performance
in high protein containing environment is limited.26 In this study, two amine-based N-chloramine/QAC
composite biocides were synthesized. These synthesized biocides were
challenged with various bacterial strains, including Gram-positive
and Gram-negative bacteria MRSA, E. coli, MDR P. aeruginosa, and wild-type P. aeruginosa (PA01) in both PBS and HPM. The results
indicate that when a secondary amine as opposed of an amide-based N-chloramine is used, the loss of active chlorine in high
protein-loaded fluids decreases, which results in less deterioration
of antibacterial activity. The composite biocide 6a demonstrated
the best antibacterial efficacy in both PBS and HPM among all biocides
studied in this study. The relatively better antimicrobial activity
of the amine-based N-chloramine (6a)
in HPM is due to the relatively high stability of the active chlorine
as compared to the amide-based N-chloramine. Transchlorination
between the amine-based N-chloramines (6a, 6b) and proteins in the medium occurs at a slow rate
as compared to the amide-based N-chloramine (compound 2). The amine-based N-chloramine then has
a better chance to exert oxidative stress inside a bacterial cell
after the whole molecule finds its way into the cell due to the membrane
disruption action of the QA moiety. Interestingly, the amine-based
composite biocide with a QAC unit of C12 alkyl chain (6a) is more potent in the protein medium than its counterpart with
a QAC unit of C14 alkyl chain (6b). This is opposite
to the general order of antibacterial activity of QACs with different
alkyl chain lengths: C14 > C12 previously reported18,27 due to the presence of the piperidine-based N-chloramine
moiety in the composite biocide. These interesting findings bring
us one step closer to the design and synthesis of more potentially
non-resistance-inducing biocides potent in real world where organic
matters might be inevitable.
Experimental Section
Materials
All
of the reagents and solvents, which were
analytical grades and no further purification been used, were purchased
from suppliers namely, Sigma, Fisher, and VWR. NMR spectra were performed
using Bruker Avance 300 MHz NMR spectrometer at room temperature and
in 5 mm NMR tubes. High-resolution mass measurements were recorded
by AB SCIEX Triple TOF 5600+ (ESI-MS), Concord, ON with the direct
infusion method. Multidrug-resistant (MDR) P. aeruginosa #73104 and community-associated-MRSA #70065 and wild-type P. aeruginosa (PA01), which were obtained from the
CANWARD (Canadian Ward Surveillance) study assessing antimicrobial
resistance in Canadian hospitals, http://www.canr.ca. Escherichia coli ATCC 25922 was
sourced from ATCC.
Synthesis and Analysis
(2-Azido-ethyl)-dimethyl-amine
(2) (Scheme 3)
2-Chloro-N,N-dimethylethylamine
hydrochloride (1) (20 g, 139 mmol) was dissolved in 50
mL of water, and then
45.13 (0.69 mol, 5 equiv) of sodium azide was added to the solution
and reaction continued overnight at reflux. Then, 7g of potassium
hydroxide added to the mixture followed by extraction with dichloromethane
(DCM) (3 × 100 mL). After solvent evaporation, 10.3 g (95 mmol,
65% yield) of a yellow liquid was achieved.
1H NMR
(CDCl3, 300 Hz) δ [ppm]: 3.35 (t, J = 6.1 Hz, 2H: N–N=NCH2−),
2.5 (t, J = 6.2 Hz, 2H: −CH2N), 2.27 (s, 6H: −N(CH3)2).
13C NMR (CDCl3, 75 Hz) δ [ppm]: 46.6,
46.6, 48.7, 65.8; HRMS (ESI-TOF) m/z: [M + H]+ calculated for C4H10N4+, 114.0905; found: 114.0911.
3a, 3b (Scheme 3)
2-Azido-N,N-dimethylethanamine
(2) (5.0 g, 44 mmol) was
dissolved in 50 mL of acetonitrile, and then 48.4 mmol of 1-bromoalkane,
1-bromotetradecane (3a), or 1-bromotetradecane (3b) was added to the solutions and the reactions continued
overnight at reflux. After solvent evaporation, compounds were dissolved
in 5 mL of methanol followed by participation in 150 mL of 50:50 ethyl
acetate/hexane 3a (11.20 g, 35.11 mmol, 79% yield) and 3b (11.6 g, 33.4 mmol, 76% yield) of white solids were achieved.
3a: 1H NMR (D2O, 300 Hz) δ
[ppm]: 4.04 (t, J = 6.2 Hz, 2H: N–N=NCH2−), 3.62 (t, J = 6.2 Hz, 2H: −CH2N+), 3.43 (t, J = 7.8 Hz, 2H: N+CH2−), 3.22 (s, 6H: (CH3)2N+), 1.73–1.9 (m, 2H: −CH2CH2), 1.23–1.48 (m, 18H: −(CH2)9CH3), 0.91 (t, J = 6.3 Hz, 3H: −CH3).
13C NMR (D2O, 75 Hz) δ [ppm]: 13.8,
22.6, 26.2, 29.4, 29.5, 29.7, 29.8, 31.9, 44.9, 51.9, 61.6, 64.5;
HRMS (ESI-TOF) m/z: [M –
Br]+ calculated for C16H35N4+, 283.2856; found: 283.2864.
3b: 1H NMR (D2O, 300 Hz) δ
[ppm]: 4.04 (t, J = 6.2 Hz, 2H: N–N=NCH2−), 3.62 (t, J = 6.2 Hz, 2H: −CH2N+), 3.43 (t, J = 7.5 Hz, 2H: N+CH2−), 3.22 (s, 6H: (CH3)2N+), 1.73–1.9 (m, 2H: −CH2CH2), 1.23–1.48 (m, 22H: −(CH2)11CH3), 0.91 (t, 3H: −CH3).
13C NMR (D2O, 75 Hz) δ
[ppm]: 13.9,
22.7, 26.2, 29.2, 29.7, 29.9, 30.1, 32.0, 45.0, 52.1, 61.5, 64.3;
HRMS (ESI-TOF) m/z: [M –
Br]+ calculated for C18H39N4+, 311.3169; found: 311.3174.
2,2,6,6-tetramethyl-4-(prop-2-ynyloxy)piperidine
(4) (Scheme 3)
2,2,6,6-tetramethylpiperidin-4-ol (9.0 g, 57 mmol)
was added to 100
mL of anhydrous THF and kept under a nitrogen atmosphere for 30 min,
stirring at room temperature, followed by addition of 2.26 g (57.0
mmol) of NaH (60%). After 30 min of mixing, the flask sealed with
a rubber stopper and transferred into a 60 °C oil bath where
6.356 mL (57.00 mmol) of propargyl bromide (80%) was added to the
mixture and the reaction continued overnight at 60 °C. Afterward,
solid settlements were removed by filtration and THF evaporated using
rotary evaporator. After solvent removal, the compound dissolved in
50 mL of 1N HCl solution and was washed with 3 × 50 mL of DCM.
Then, sodium hydroxide was used to increase the pH to 10 (in an ice
bath). Then, the aqueous solution was washed with DCM (3 × 50
mL). The organic layer was dried on sodium sulfate, and the solvent
was evaporated. 5.10 g (26.2 mmol, 46% yield) of yellow solid was
achieved.
1H NMR (CDCl3, 300 Hz) δ
[ppm]: 4.17 (s, 2H: OCH2−),
3.83–3.96 (m, 1H: −CHO), 2.39 (s, 1H: −CH), 1.97–1.96 (d, 1H), 1.93–1.92 (d, J = 4 Hz, 2H: (CHCH)2), 1.17 (s,
6H: NH(C(CH3CH3))2), 1.12 (s, 6H: −(CH3CH3)2), 0.99 (t, J =
11.8 Hz, 2H: (CHCH)2−).
13C NMR (CDCl3, 75 Hz) δ [ppm]: 29.0,
35.0, 44.5, 51.6, 54.9, 71.9, 73.9; HRMS (ESI-TOF) m/z: [M + H]+ calculated for C12H22NO+, 196.1696; found: 196.1716.
Click Reaction, 5a, 5b (Scheme 3)
4:
(2.91 g, 15.0 mmol) was dissolved in 15 mL of MeOH. Then, 12.5 mmol
of azide 3a (4.62 g) or 3b (4.92 g) was
added to the solution. Afterward, 0.312 g (1.95 mmol, 10%) of CuSO4 was dissolved in 2 mL of water and added to the solutions.
Then, 2.38 g (37.4 mmol) of Cu was added to the solutions and reactions
continued overnight at room temperature. After filtration to remove
the copper particles, the solution passed through Sorbtech CR20-01
to remove Cu(I) and the anion-exchange resin to replace Br− with Cl−.
5a: 1H
NMR (D2O, 300 Hz) δ [ppm]: 8.22 (s, 1H: −CHN–N=N), 5.057 (s, 2H: OCH2−), 4.72 (t, J = 6.1
Hz, 2H: −CH2), 4.01 (t, J = 6 Hz, 2H: −CH2), 4.09–4.24 (m, 1H: −CHO), 3.31
(t, J = 7.4 Hz, 2H: N+CH2−), 3.18 (s, 6H: N+(CH3)2), 2.30 (d, J = 3.5 Hz, 1H: −CHCH), 2.25 (d, J = 3.5 Hz, 1H: −CHCH), 1.61 (m, 2H: −CH2CH2), 1.50 (s, 6H: C(CH3CH3)2), 1.48
(s, 6H: C(CH3CH3)2), 1.23–1.38 (m, 18H: −(CH2)9CH3), 1.18 (t, J = 11.1 Hz, 2H, (CHCH)2−),
0.88 (t, J = 5.5, 3H: −CH3).
13C NMR (D2O,
75 Hz) δ [ppm]: 13.8,
22.5, 26.3, 28.7, 29.4, 29.5, 30.3, 31.8, 41.9, 44.1, 51.6, 54.5,
61.4, 64.4, 71.7, 125.4, 145.1; HRMS (ESI-TOF) m/z: [M – Cl]+ calculated for C28H56N5O+, 478.4479; found: 478.4482.
Purity based on QNMR result (internal standard: maleic acid) >
99%.
5b: 1H NMR (D2O, 300
Hz) δ
[ppm]: 8.22 (s, 1H: −CHN–N=N), 5.057
(s, 2H: OCH2−), 4.72 (t, J = 6.1 Hz, 2H: −CH2), 4.01 (t, J = 6 Hz, 2H: −CH2), 4.09–4.24 (m, 1H: −CHO), 3.31 (t, J = 7.4 Hz, 2H: N+CH2−), 3.18 (s, 6H: N+(CH3)2), 2.30
(d, J = 3.5 Hz, 1H: −CHCH), 2.25
(d, J = 3.5 Hz, 1H: −CHCH), 1.61
(m, 2H: −CH2CH2), 1.50 (s, 6H: C(CH3CH3)2), 1.48 (s, 6H: C(CH3CH3)2), 1.23–1.38 (m, 22H,
−(CH2)11CH3), 1.18 (t, 2H, J = 11.1 Hz, 2H, (CHCH)2−), 0.88 (t, J = 5.5,
3H: −CH3).
13C NMR (D2O, 75 Hz) δ [ppm]: 14.0,
22.7, 27.2, 29.1, 29.5, 29.7, 30.2, 32.0, 42.9, 43.1, 51.9, 52.8,
60.8, 64.13, 72.6, 125.4, 145.4; HRMS (ESI-TOF) m/z: [M – Cl]+ calculated for C30H60N5O+, 506.4792; found:
506.4788.
Purity based on QNMR result (internal standard: maleic
acid) >
97%.
Chlorination of Compounds 5a and 5b (Scheme 3)
5a or 5b (500 mg) was dissolved in 10 mL
of water/acetone (2:8 by volume), then 3 equiv of tert-butyl hypochlorite (450 μL) was added to vials, which completely
wrapped with aluminum foil at 0 °C. Reactions continued for 60
min. Afterward, air flow was employed to remove acetone and unreacted tert-butyl hypochlorite, and water was removed using vacuum.
6a: 1H NMR (CDCl3, 300 Hz) δ
[ppm]: 8.53 (s, 1H: −CHN–N=N), 5.28
(s, 2H: OCH2−), 4.55 (t, J = 6.3 Hz, 2H: −CH2), 4.36 (t, J = 6.4 Hz, 2H: −CH2), 3.68–3.81 (m, 1H: −CHO), 3.4 (t J = 7.1 Hz, 2H: N+CH2−), 3.34 (s, 6H: N+(CH3)2), 2.1
(d, J = 3.1 Hz, 1H: −CHCH), 2.05
(d, J = 3.1 Hz, 1H: CHCH), 1.52 (m,
2H: −CH2CH2), 1.23–1.38 (m, 32H: −(CH2)9CH3, C(CH3)2 and −CHCH), 0.88 (t, J = 6.5, 3H: −CH3).
13C NMR (CDCl3, 75 Hz) δ [ppm]:
14.1,
22.5, 26.3, 29.1, 29.3, 29.5, 30.9, 31.9, 33.2, 44.2, 45.6, 51.5,
62.6, 70.4, 77.1, 125.1, 145.8; HRMS (ESI-TOF) m/z: [M – Cl]+ calculated for C28H55ClN5O+, 512.4090; found: 512.4080.
Purity based on QNMR result (internal standard: maleic acid) >
98%.
6b: 1H NMR (CDCl3, 300
Hz) δ
[ppm]: 8.5 (s, 1H: −CHN–N=N), 5.24
(s, 2H: OCH2−), 4.58 (t, J = 6.4 Hz, 2H: −CH2), 4.32 (t, J = 6.4 Hz, 2H: −CH2), 3.7–3.83 (m, 1H: −CHO), 3.4 (t, J = 7.6 Hz, 2H: N+CH2−), 3.33 (s, 6H: N+(CH3)2), 2.10
(d, J = 3.3 Hz, 1H: −CHCH), 2.05
(d, J = 3.3 Hz, 1H: CHCH), 1.54 (m,
2H: −CH2CH2), 1.11–1.38 (m, 36H: −(CH2)11CH3, C(CH3)2 and −CHCH), 0.88 (t, J = 6.5, 3H: −CH3).
13C NMR (CDCl3, 75 Hz) δ [ppm]:
14.1,
22.5, 26.2, 29.2, 29.4, 29.6, 29.7, 31.9, 33.3, 44.4, 45.6, 51.6,
62.7, 70.4, 77.1, 125.1, 145.8; HRMS (ESI-TOF) m/z: [M – Cl]+ calculated for C30H59ClN5O+, 540.4403; found: 540.4386.
Purity based on QNMR result (internal standard: maleic acid) >
95%.
Copper Analysis
Antibacterial effect of copper has
been reported in many studies.28 Copper
has been used as the catalyst for click reaction, and this copper
can interfere the antibacterial activity of compounds. Therefore,
copper removal to the noneffective concentration was crucial. To this
end, Sorbtech CR20-01 beads have been used. Copper concentration in
compounds was measured using ICP optical emission spectrometer, Varian
725-ES.
Redox Titration
Redox titration is a titration technique
in which a redox reaction takes place between an analyte and a titrant.19 A redox indicator and conductometer were used
during the titration. In this study, redox titration was carried on,
to track the chlorine lost in high protein-loaded fluid (5% FBS) for 6a, 6b, and compound 2.
To
this end, 0.25 mmol of each compound dissolved in 10 mL of Milli-Q
water to have an aqueous solution of each compound. Afterward, 50
μL of fetal bovine serum (FBS) was added to 950 μL of
the prepared solution and mix them on an orbital shaker for different
time frames (1, 5, 20, 60, 90, and 120 min). Mixture (100 μL)
was added to a mixture of 30 mL of Milli-Q water, 2 mL of 5% acetic
acid buffer solution, 1 g (6 mmol) potassium iodide, and five drops
of freshly prepared 1% starch solution to get a solution with a dark
purple color. Sodium thiosulfate standard solution (0.001 N) was used
to titrate (dropwise addition) the mixture using buret. The titration
stopped when the solution color turned clear, and the chlorine content
was calculated as below where Mw, m, and Vt stand for molecular
weight (g/mol), mass of the compound (g), and buret reading (mL),
respectively.
Quantitative Antimicrobial Assay (in PBS
and High Protein Medium)
A bacterial suspension was prepared
at a concentration of 108 CFU/mL in phosphate-buffered
saline (PBS, 0.1 M, pH 7.4)
using 0.5 McFarland standard. After 100 times dilution, 20 μL
of diluted suspension was added to 60 mL of different broths based
on the bacterial strains, Tryptone Soy Broth in the case of MRSA and
Mueller Hinton Broth for P. aeruginosa and E. coli, followed by 18 h incubation
at 37 °C. After incubation, 50 μL of bacterial suspension
was added to a solution of 5 [Cl]+ ppm (141.0 μM)
to 20 mL of PBS (0.1 M, pH 7.4) and 15 [Cl]+ ppm (423.1
μM) to a solution of 5% FBS in PBS and incubated on the orbital
mixer at 37 °C. At each time point (1, 3, 5, 10, 20, 30, 60 min),
150 μL of mixture was added to 150 μL of neutralizer solution
(PBS buffer consisting of 1.4% (w/v) l-α-phosphoatidylcholine,
10% (w/v) Tween 80, 1% peptone, and 0.316% sodium thiosulfate) to
deactivate antimicrobial agent. Bacterial suspension (30 μL)
and its serial dilutions were plated on Tryptone Soya Agar plates
and incubated for 24 h, followed by colony counting. To eliminate
the effect of bacterial growth in HPM and/or bacterial death due to
malnutrition in PBS at each time point, there was a negative control.
The bacterial log reduction was calculated as following Lecithin, tween, and peptone
have been proven
to be effective in quenching QACs.11,29,30 We have also run adequate inactivation tests to confirm
thorough quenching of our biocides at the tested concentrations (141.0
and 423.1 μM). Specially, we plated bacterial suspensions of
one series of antibacterial experiments 30 and 90 min after mixing
with the neutralizer, and no further decrease of bacterial concentration
was observed from the enumeration results, indicating thorough quench
of all biocides.
To compare the antibacterial efficacy of the
synthesized biocides with free chlorine, an antibacterial test was
also conducted against methicillin-resistant S. aureus (MRSA), P. aeruginosa, E. coli, and wild-type P. aeruginosa using sodium hypochlorite at two different concentrations (5 and
10 ppm [Cl+] (141.0 and 282.1 μM)) in PBS and two
concentrations (15 and 30 ppm [Cl+] (423.1 and 864.3 μM))
in HPM.
The
authors
declare no competing financial interest.
Acknowledgments
The authors are
grateful for the financial support from the
Collaborative Health Research Project (CHRP) operating grant (Grant
no.: CHRP 413713-2012) and the Natural Sciences and Engineering Research
Council of Canada (NSERC) Discovery grant (Grant no.: RGPIN/04922-2014).
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145782710.1021/acsomega.7b00429ArticleBinding and Selectivity of Essential Amino Acid Guests
to the Inverted Cucurbit[7]uril Host Gao Zhong-Zheng †Kan Jing-Lan ‡Chen Li-Xia †Bai Dong †Wang Hai-Yan †Tao Zhu †Xiao Xin *†† Key
Laboratory of Macrocyclic and Supramolecular Chemistry of Guizhou
Province, Guizhou University, Guiyang 550025, P. R. China‡ College
of Chemistry, Chemical Engineering and Materials Science, Collaborative
Innovation Center of Functionalized Probes for Chemical Imaging in
Universities of Shandong, Key Laboratory of Molecular and Nano Probes,
Ministry of Education, Shandong Normal University, Jinan 250014, P. R. China* E-mail: gyhxxiaoxin@163.com (X.X.).08 09 2017 30 09 2017 2 9 5633 5640 16 06 2017 24 08 2017 Copyright © 2017 American Chemical Society2017American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
Interactions
between inverted cucurbit[7]uril (iQ[7]) and essential
amino acids have been studied at pH = 7.0 by 1H NMR spectroscopy,
electronic absorption spectroscopy, isothermal titration calorimetry,
and mass spectrometry. The interactions can be divided into three
binding types at pH = 7.0. Experimental results from the present study
showed that the host displays a strong binding to the aromatic amino
acids, Trp and Phe, and the guests of Lys, Arg, and His lie outside
the cavity portal of the host. Meanwhile, the alkyl moieties of the
guests Met, Leu, and Ile were accommodated within the cavity of iQ[7],
but there was no significant interaction between iQ[7] and Thr or
Val. The complexation behavior of iQ[7] with essential amino acids
was explored at pH = 3, and the binding of Lys, Arg, and His revealed
an unexpected behavior, with their side chains located in the cavity
of iQ[7], whereas those of the aromatic Trp and Phe were deeper within
the iQ[7] cavity. The alkyl side chains of the guests Met, Leu, Ile,
Thr, and Val were also located inside the iQ[7] cavity and formed
the host–guest complexes.
document-id-old-9ao7b00429document-id-new-14ao-2017-00429sccc-price
==== Body
Introduction
In recent years, molecular
recognition in biomolecules has attracted
considerable attention,1−4 especially regarding amino acids and aromatic peptides. As the building
blocks of proteins, amino acids are essential components of life processes
and play critical roles in metabolism growth and development. A lack
of any essential amino acids can lead to an abnormal physiological
function and eventually to diseases such as nutritional imbalances,
Alzheimer’s, and pancreatitis.
Research on amino acid
and aromatic peptide complexation and recognition
by cyclodextrins,5 calixarenes,6 pillararenes,7 and
other macrocyclic receptors has been reported. The novel family of
macrocycles, cucurbit[n]urils (Q[n]s, where n = 5–8, 10, and 13–15),8−12 can selectively accommodate and interact with various organic molecules.
Several examples of interactions of amino acids with different members
of the cucurbit[n]urils (Q[n]s)13−18 have been described. Thuéry built chiral assemblies l-Cys-lanthanide–Q[6] complexes using l-cysteine as
a chiral linker;19a Gamal-Eldin’s
work on the selective molecular recognition of methylated lysines
and arginines by Q[7] had been reported;19b and supramolecular structures of tryptophan with Q[6] showed a very
interesting and peculiar structure.20 Kim
et al. explored the specific high-affinity binding of Q[7] to amino
acids (Lys, Arg, and His and Phe, Tyr, and Trp) in water.21 Urbach and co-workers observed the 1:1 binding
of phenylalanine derivatives to Q[7] and the binding of aromatic amino
acids to Q[8].22 Nau and co-workers did
some work of monitoring of amino acids based on self-assembly.23
Scherman’s group reported the first
example of the recognition
of a selected amino acid epitope within a protein by Q[8] complexation.24 Isaacs’s group obtained ‘‘turn-on’’
fluorescent sensors for amino acids using fluorescent cucurbituril
derivatives.25 In 2006 and 2016, our group
reported supramolecular receptors for the detection and recognition
of amino acids by TMeQ[6],26 Q[7, 8],27 and twisted cucurbit[14]uril.28 This area has seen a large expansion in the number of publications
on the binding of amino acids.
In 2005, Isaacs and Kim reported
the isolation, characterization,
and recognition properties of inverted cucurbit[n]urils (iQ[n]s, where n = 6 and
7),29 and some related properties of iQ[n]s were also described.30−32 However, to date, few
reports have focused on the newest member of the Q[n]s, iQ[7]. Our group studied the coordination chemistry of an iQ[7]
with a series of metal ions.33−35 To investigate the host–guest
chemistry of the iQ[7], we investigated the binding interaction of
an inverted cucurbit[7]uril with α,ω-alkyldiammonium guests36 and 4,4′-bipyridine derivatives.37,38 In a continuation of this research, herein, we explored the binding
of essential amino acids to the iQ[7] host to expand our knowledge
of the supermolecular chemistry of iQ[n]s. We studied
the binding interactions of iQ[7] with 10 essential amino acids (Scheme 1) in buffered solution
by 1H NMR spectroscopy, isothermal titration calorimetry
(ITC), and matrix-assisted laser desorption ionization time-of-flight
mass spectrometry (MALDI-TOF MS). Meanwhile, we also characterized
the interaction between iQ[7] and basic amino acids at pD = 3 by 1H NMR spectroscopy. The experimental results provide new insights
into the interactions of amino acids and iQ[7].
Scheme 1 Structures of iQ[7]
and Essential Amino Acids Investigated in This
Work
Results and Discussion
NMR Spectroscopy
The complexation of iQ[7] with essential l-α-amino
acids was first examined by 1H NMR
spectroscopy of host–guest mixtures. Figure 1 shows the 1H NMR spectra of Lys
recorded in the absence and presence of approximately 1.0 equiv of
the host in D2O, and D2O was adjusted to pD
= 7.0 with sodium phosphate. In the presence of iQ[7], the peaks for
all methylene protons of Lys display a substantial downfield shift
compared with those of the free guest, indicating that all methylene
protons interact with the carbonyl groups of iQ[7]. It has been reported
that the 1H NMR peaks of the guest protons inside the low-polarizability
cavity of Q[n] shift upfield, and interactions with
the carbonyl oxygen molecules of Q[n] result in downfield
shifts owing to the deshielding of the protons.21,39,40 Additionally, the signal corresponding to
the α-proton of the amino acid (Hα) is shifted
downfield (Δδ = 0.37 ppm). This indicates that the guest
is located just outside the portal of the host.
Figure 1 1H NMR spectra
(400 MHz, pD = 7.0) of iQ[7] in the absence
(A) and presence of 0.15 (B), 0.40 (C), 0.70 (D), 0.82 (E), and 1.02
(F) equiv of Lys and free guest Lys (G) at 20 °C.
Similar iQ[7] complexation-induced 1H NMR changes (downfield
shifts and peak splitting) were observed for another two essential
amino acids, Arg and His, indicating similar binding modes. The results
of titration 1H NMR spectroscopy obtained using a fixed
amount of iQ[7] and various equivalents of Arg are shown in Figure S1. The side-chain proton (Hβ and Hγ) signals for Arg showed a downfield shift
of 0.04 and 0.18 ppm, respectively, and the signal for the proton
Hα showed a downfield shift of 0.29 ppm when the
iQ[7]–Arg ratio reached 1:1.02. As shown in Figure S2, the imidazole proton signal of His is shifted downfield
compared to that of the free guest, as are the peaks for methylene
protons Hβ and Hα.
This may
reflect the fact that Arg and His lie outside the portal
of the host, unlike the interaction of Q[7] with Lys and Arg.21 The possible reason leading to the difference
lies in the smaller cavity of iQ[7] which contains a single inverted
glycoluril unit.
The binding behavior of iQ[7] with the aromatic
amino acids Trp
and Phe clearly departs from our observations with Lys, Arg, and His.
As shown in Figure 2, all aromatic protons (Hγ–Hη) of Trp move upfield considerably and are broadened compared with
those of the free guest as a consequence of inclusion-induced shielding
effects. This indicated that they were averaged signals of the free
and bound guest molecules due to a rapid exchange rate of binding
and release on the NMR time scale. Meanwhile, one of the CH2 protons of Trp is moved upfield, which indicates that it is located
inside the cavity. By contrast, the proton Hα of
Trp moved downfield by 0.07 ppm when the iQ[7]–Trp ratio reached
1:1.05, which indicates that it is located outside the cavity. It
is noted that the two methine protons (H1 on Scheme 1) of the inverted glycoluril unit in the
cavity of iQ[7] were shifted upfield with increasing amounts of Trp,
suggesting that Trp also interacts with these methine protons (H1)
in the cavity of iQ[7]. These observations suggest that the CH2 group and indole moiety of the Trp guest are encapsulated
in the cavity of the iQ[7] host. This is also the case for the binding
interactions of iQ[7] with Phe; as shown in Figure S3, the aromatic ring protons of Phe are clearly subject to
upfield shifts upon binding to iQ[7].
Figure 2 1H NMR spectra (400 MHz, pD
= 7.0) of iQ[7] in the absence
(A) and presence of 0.18 (B), 0.40 (C), 0.64 (D), 0.85 (E), and 1.05
(F) equiv of Trp and free guest Trp (G) at 20 °C.
Meanwhile, the signal corresponding to the α-proton
of the
bound amino acid (Hα) is shifted obviously downfield
(Δδ = 0.13 ppm), similar to the binding interactions of
iQ[7] with Trp. This result is consistent with the binding behavior
of Q[7] with aromatic amino acids.21
The interaction of iQ[7] with Ile could be conveniently monitored
by 1H NMR. A slight upfield shift of the signals of the
protons of the alkyl chain (Hβ–Hδ) and a slight downfield shift of the signal of the Hα were observed upon the addition of iQ[7] (Figure 3), suggesting that there is a weak interaction
between iQ[7] and Ile. Similar 1H NMR spectra for the interaction
of iQ[7] and the guests Leu and Met were also recorded (Figures S4 and S5). This indicates that the alkyl
moiety of the guests was accommodated within the cavity of iQ[7] but
the interaction is weak. Meanwhile, no obvious shift was observed
when mixing the host with the essential amino acids, Val or Thr (Figures S6 and S7).
Figure 3 1H NMR spectra
(400 MHz, pD = 7.0) of iQ[7] in the absence
(A) and presence of 0.45 (B), 0.68 (C), 0.85 (D), and 1.05 (E) equiv
of Ile and free guest Ile (F) at 20 °C.
To compare the binding patterns of the essential amino acids
with
iQ[7] under different conditions, we also investigated the interactions
between the protonated forms of the amino acids and iQ[7] by 1H NMR titration at pD = 3. We first studied the binding behavior
of three basic amino acids with iQ[7]. A trace amount of the acid
was added together with iQ[7] to ensure the formation of the complexes.
With 1.0 equiv of Lys, Arg, or His, the proton of the side chains
of these amino acids showed a significant upfield displacement (Figures 4, S8, and S9), indicating the formation of complexes. Lys, Arg,
and His showed unexpected changes at pD = 3 compared with D2O because 1H NMR experiments confirmed that these amino
acids formed inclusion complexes with iQ[7]. This change in behavior
is likely due to a change in the protonation state.21 We concluded that the side chains of Lys, Arg, and His
were predominantly located in a shielded environment.21,39,40 This is because the binding to
iQ[7] causes His, Lys, and Arg to favor the fully protonated state.
As Kim reported before, paying the thermodynamic penalty for the protonation
of the carboxylate group is favored over the binding to iQ[7] as the
deprotonated form.
Figure 4 1H NMR spectra (400 MHz, pD = 3) of iQ[7] in
the absence
(A) and presence of 0.35 (B), 0.75 (C), and 1.05 (D) equiv of Lys
and free guest Lys (E) at 20 °C.
For Trp and Phe, the amino groups of the guests remained
protonated
at pD = 3. Next, we investigated the binding interactions of the aromatic
amino acids Trp and Phe with iQ[7]. The interaction of Trp with iQ[7]
was studied first (Figure 5), and the results showed that the proton of the indole moiety
was shifted upfield, suggesting that the indole moiety of Trp was
located inside the cavity, as concluded previously. Upon comparing
the differences, it became apparent that the protons Hα and Hβ of Trp were shifted upfield, indicating
that the methylene and methine groups of the guest were also encapsulated
in the iQ[7] cavity. This conclusion was also reached for Phe. As
shown in Figure S10, all protons of the
benzyl moiety underwent a considerable upfield shift; meanwhile, the
Hα protons also experienced a small upfield shift.
These iQ[7]-induced shift patterns suggested that the benzene ring
and alkyl chain moiety of Phe were situated inside the iQ[7] cavity.
Overall, the results suggest that Trp and Phe guests were buried deeper
within the iQ[7] cavity. This indicates that the aromatic amino acids
can maintain their binding affinities reasonably well even if their
carboxyl groups are deprotonated, which is consistent with the results
of the binding of Q[7] with aromatic amino acids.
Figure 5 1H NMR spectra
(400 MHz, pD = 3) of iQ[7] in the absence
(A) and presence of 0.35 (B), 0.70 (C), 0.85 (D), and 1.05 (E) equiv
of Trp and free guest Trp (F) at 20 °C.
The host–guest interactions of iQ[7] with charged
amino
acids (Ile, Leu, Met, Val, and Thr) at pD = 3 were also investigated
by 1H NMR spectroscopy. The 1H NMR spectra of
Ile and Ile bound to iQ[7] are shown in Figure 6. All protons of the alkyl side chain of
Ile were clearly shifted upfield by between 0.23 and 0.41 ppm, indicating
burial within the iQ[7] cavity. Similarly, when the amino acids were
added to iQ[7] at pD = 3, the alkyl side-chain protons of Leu, Met,
Val, and Thr experienced a significant upfield shift, suggesting a
deep inclusion in the cavity of iQ[7] due to the formation of inclusion
complexes (Figures S11–S14). Upon
comparing with nuclear magnetic titration experiments in D2O, it became apparent that the alkyl side-chain protons of the guests
were shifted upfield, confirming that these four amino acids were
more likely to form inclusion complexes at pD = 3. Major binding differences
were observed (using NMR spectroscopy) between pD = 7 and 3, which
can be explained as a consequence of the different protonation state
for the carboxylate group. Upon the protonation of the carboxylate
group, the amino acid inclusion into the cucurbituril cavity is favored.
Figure 6 1H NMR spectra (400 MHz, pD = 3) of iQ[7] in the absence
(A) and presence of 0.30 (B), 0.65 (C), 0.85 (D), and 1.05 (E) equiv
of Ile and free guest Ile (F) at 20 °C.
Ultraviolet–Visible Absorption and Fluorescence Emission
Spectra
The interaction of iQ[7] with Trp was also examined
by UV absorbance spectrophotometry and fluorescence spectroscopy.
According to the UV absorption spectroscopic results (Figure 7A), the gradual addition of
iQ[7] to Trp in buffered solution (pH = 7) was accompanied by a significant
decrease in the intensity at 218 nm and a slight bathochromic shift
because of the strong interaction between iQ[7] and Trp. As can be
seen in Figure 7B,
Trp displayed an emission peak at 366 nm at an excitation wavelength
of 269 nm. Successive addition of iQ[7] caused a decrease and a hypsochromic
shift from 359 to 350 nm in the fluorescence intensity at 359 nm.
These substantial changes in the emission profile further confirm
the strong host–guest interaction between iQ[7] and Trp. From
the ultraviolet–visible (UV–vis) absorption and fluorescence
intensity, the binding constant (Ka) for
iQ[7]–Trp could be determined to be 2.32 × 104 M–1 and 2.68 × 104 M–1. Furthermore, Job’s plots (Figure 7C,D) based on the continuous variation method
clearly showed that the UV spectra and fluorescence spectra of Trp
fitted well with 1:1 stoichiometry of the host–guest inclusion
complexes.
Figure 7 Electronic absorption (A) and fluorescence emission spectra (B)
of Trp (2 × 10–5 mol·L–1) upon the addition of increasing amounts (0, 0.1, 0.2, 0.3, 0.4,
0.5, 0.6, 0.7, 0.8, 0.9, 1.0, 1.1, 1.2, 1.3, 1.4, 1.5, 1.6, 1.7, 1.8,
1.9, and 2.0 equiv) of iQ[7]. ΔA (C) and ΔF (D) vs NiQ[7]/(NiQ[7] + NTrp) plots.
Isothermal Titration Calorimetry
To better understand
the host–guest interactions between iQ[7] and the 10 essential l-α-amino acids, we carried out at least two ITC experiments
at 25 °C in 10 mM sodium phosphate (pH 7.0). Table 1 and Figures S15 and S16 show the equilibrium association constants (Ka) and thermodynamic parameters for iQ[7]–amino
acid interaction systems for Lys, Arg, His, Trp, and Phe. The experimental
results revealed Ka values ranging from
∼103 to ∼105 M–1 and negative ΔG° values ranging from
−25.4 to −28.2 kJ/mol for iQ[7]–amino acid interactions.
Thus, these l-α-amino acids could effectively bind
to the iQ[7] host. However, the amino acids Met, Ile, Leu, Thr, and
Val showed no effective interaction with iQ[7] (Figure S17). The revealed Ka values
indicated a strong binding with the aromatic amino acids Trp and Phe,
among which iQ[7] binds with Phe with the highest binding affinity,
which is consistent with the binding behavior of Q[7] with aromatic
amino acids (Table 2).21,41 The observations can be explained in terms
of a combination of ion-dipole and electrostatic interactions between
the positively charged side chains of the amino acids and the polar
carbonyl groups of iQ[7] and hydrophobic interactions between the
aromatic moieties of the amino acids and the macrocyclic cavity. From
the ΔH° and TΔS° values shown in Table 1, all intermolecular complexation interactions
between the iQ[7] host and l-α-amino acids guests appear
to be driven by favorable enthalpy changes, accompanied by small negative
(unfavorable) entropy changes. According to the NMR data, the interactions
between iQ[7] and Met, Ile, and Leu are relatively weak; meanwhile,
iQ[7] with Thr and Val shows no interaction. These facts might be
a reasonable explanation why the ITC experiments showed no effective
interaction of iQ[7] with these amino acids Met, Ile, Leu, Thr, and
Val.
Table 1 Complex Stability Constant (Ka), Enthalpy (ΔH°),
Entropy Changes (TΔS°),
and Gibbs Free Energy (ΔG°) for iQ[7]–Guest
Interactions in Buffered Solution at pH = 7
guest Ka (×104 M–1) ΔH° (kJ/mol) TΔS°(kJ/mol) ΔG° (kJ/mol)
Lys 0.87 ± 0.15 –31.2 ± 14.0 –4.17 –27.1
Arg 1.60 ± 0.97 –32.4 ± 9.55 –4.23 –28.2
His 0.66 ± 0.13 –33.8 ± 11.0 –7.93 –25.9
Trp 2.83 ± 0.66 –37.4 ± 5.71 –12.0 –25.4
Phe 10.7 ± 0.24 –37.6 ± 2.25 –9.62 –28.0
Table 2 Complex Stability
Constant (Ka), Enthalpy (ΔH°),
and Entropy Changes (TΔS°)
for Q[7]–Guests
guest Ka (M–1) ΔH° (kJ/mol) TΔS° (kJ/mol)
Lys a2.1(±0.7) × 102 –4.4 ± 0.3 8.8 ± 0.3
Arg anot available
b327 ± 16 –5.0 ± 0.1 9.2 ± 0.1
His anot available
Trp a1.2(±0.1) × 103 –28.9 ± 0.6 –11.3 ± 0.6
Phe a1.8(±0.5) × 105 –30.5 ± 2.8 –0.6 ± 2.8
a Measured in sodium
phosphate buffer
at pH = 7.0, ref (21).
b Measured in sodium phosphate
buffer
at pH = 6.0, ref (41).
Mass Spectrometry
We further studied the formation
of the inclusion complexes of iQ[7] and guests for 10 of the essential l-α-amino acids by MALDI-TOF MS. In the resultant MALDI-TOF
MS spectra (Figure S18), major signals
at m/z = 1309.012, 1336.526, 1317.864,
1367.793, 1328.397, 1294.573, 1294.498, and 1312.410 were observed,
corresponding to Lys–iQ[7] (calculated 1309.151), Arg–iQ[7]
(calculated 1337.164), His–iQ[7] (calculated 1318.118), Trp–iQ[7]
(calculated 1367.189), Phe–iQ[7] (calculated 1328.152), Ile–iQ[7]
(calculated 1294.136), Leu–iQ[7] (calculated 1294.136), and
Met–iQ[7] (calculated 1312.175), respectively. These intense
signals provide direct support for the formation of 1:1 stoichiometric
host–guest inclusion complexes for these eight amino acids.
It is noted that no significant host–guest interaction signals
were observed between iQ[7] and Thr or Val in the MS spectra. The
results of the mass spectra are consistent with the results from the
NMR experiments.
Conclusions
We explored the binding
interactions between 10 essential l-α-amino acid guests
and the iQ[7] host using a variety of
characterization methods in buffered solution (pH = 7). The experimental
results indicated a strong binding with the aromatic amino acids Trp
and Phe, and iQ[7] binds with Phe with the highest binding affinity,
which is consistent with the binding behavior of Q[7] with aromatic
amino acids. Lys, Arg, and His guests lie outside the portal of the
host, whereas the alkyl moieties of Met, Leu, and Ile guests were
accommodated within the iQ[7] cavity, and there was no significant
interaction between iQ[7] and Thr or Val. Additionally, interactions
between the protonated form of Lys, Arg, and His with iQ[7] were also
investigated at pH = 3, and unexpectedly, the side chains were located
in the cavity of iQ[7] under acidic conditions. Furthermore, the aromatic
amino acids Trp and Phe were more deeply buried in the iQ[7] cavity
at the lower pH. An upfield chemical shift for the protons of the
alkyl side chains of Met, Leu, Ile, Thr, and Val guests indicated
that they were located inside the iQ[7] cavity and hence formed host–guest
complexes. These results not only enhance our knowledge of the molecular
recognition of amino acids but may also be of significance for the
design and synthesis of new macrocyclic compounds for biological identification
and simulation.
Experimental Section
Materials and Reagents
Ten essential l-α-amino
acids were purchased from Aldrich. iQ[7] was prepared and purified
according to our previously published procedure.33 All other reagents were of analytical grade and were used
as received. Double-distilled water was used for all experiments.
Nuclear Magnetic Resonance Measurements
All 1H NMR spectra, including those for titration experiments, were measured
on a Varian INOVA-400 NMR spectrometer with SiMe4 as an
internal reference at 20 °C. D2O was used as a field-frequency
lock, and the observed chemical shifts are reported in parts per million
(ppm) relative to that for the internal standard (TMS at 0.0 ppm).
The ratio of amino acids versus iQ[7] was calculated by the ratio
of their integral areas for special peaks. The concentrations of the
amino acids were 1.0 × 10–4 mol/L in the NMR
experiments. D2O was adjusted to pD = 7.0 with sodium phosphate.
The value was verified on a pH meter calibrated with two standard
buffer solutions. D2O was adjusted to pD = 3.0 with 1 M
DCl. The pD = 3 of the solution was also verified on a calibrated
pH meter.
UV–Vis Absorption and Fluorescence Emission Spectra
UV–vis absorption spectra of the host–guest complexes
were recorded with an Agilent 8453 spectrophotometer at room temperature.
Fluorescence spectra measurements were performed on a Varian Cary
Eclipse fluorescence spectrophotometer equipped with a xenon discharge
lamp at room temperature. The absorption and fluorescence titration
experiments were performed as follows: 200.0 μL of 1.0 ×
10–3 mol/L stock solution of Trp and various amounts
of 1.0 × 10–4 mol/L iQ[7] aqueous solution
were transferred into a 10 mL volumetric flask, and then the volumetric
flask was filled to the final volume with distilled water. The pH
was adjusted to pH = 7 with sodium phosphate.
ITC Measurements
Microcalorimetric experiments were
performed using an isothermal titration calorimeter Nano ITC (TA,
USA). The heat evolved was recorded at 298.15 K. The heat of the reaction
was corrected for the heat of the dilution of the guest solution determined
in separate experiments. All solutions were degassed prior to the
titration experiment by sonication. A stock solution (1.0 × 10–3 mol/L) of amino acids and 1.0 × 10–4 mol/L stock solution of iQ[7] were prepared with 10 mM sodium phosphate
(pH 7.0). A typical ITC titration was carried out by titrating the l-α-amino acid solution (pH = 7, 1.0 × 10–3 mol/L, 6 μL of aliquots, at 250 s intervals) into an iQ[7]
solution. The concentration of iQ[7] in the sample cell (1.3 mL) was
1.0 × 10–4 mol/L at pH = 7. Computer simulations
(curve fitting) were performed using the Nano ITC analyze software.
First points in the ITC data were excluded when fitting the model
to acquire the binding constant, enthalpy change, and entropy change.
MALDI-TOF MS
MALDI-TOF MS spectra were recorded on
a Bruker BIFLEX III ultrahigh-resolution Fourier transform ion cyclotron
resonance mass spectrometer with α-cyano-4-hydroxycinnamic acid
as the matrix. The MALDI-TOF experiments were carried out by adding
the l-α-amino acid solution (1.0 × 10–3 mol/L, 100 μL) into an iQ[7] solution (1.0 × 10–4 mol/L, 1.0 mL). The solution concentration was about 1.0 ×
10–4 mol/L (l-α-amino acids–iQ[7]
= 1:1).
Supporting Information Available
The Supporting
Information is
available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.7b00429.NMR spectra, MALDI-TOF
MS spectra of inclusion complexes,
and ITC profiles of iQ[7] with guests (PDF)
Supplementary Material
ao7b00429_si_001.pdf
The authors
declare no competing financial interest.
Acknowledgments
This work was
financially supported by the National
Natural Science Foundation of China (no. 21561007), the Innovation
Program for High-level Talents of Guizhou Province (no. 2016-5657),
the Science and Technology Fund of Guizhou Province (no. 2016-1030),
and the Scientific Research Foundation of Guizhou University (no.
2015-62).
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145889310.1021/acsomega.8b00411ArticleSynthesis of an Alleged Byproduct Precursor in Iodixanol
Preparation Haarr Marianne
Bore †Lindbäck Emil †Håland Torfinn *‡Sydnes Magne O. *†† Faculty
of Science and Technology, Department of Mathematics and Natural Sciences, University of Stavanger, NO-4036 Stavanger, Norway‡ GE
Healthcare AS, NO-4521 Lindesnes, Norway* E-mail: torfinn.haaland@ge.com (T.H.).* E-mail: magne.o.sydnes@uis.no (M.O.S.).05 07 2018 31 07 2018 3 7 7344 7349 05 03 2018 20 06 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
N1,N3-Bis(2,3-dihydroxypropyl)-2,4,6-triiodo-5-(N-(oxiran-2-ylmethyl)acetamido)isophthalamide (1), the alleged precursor of several minor byproducts formed when
the X-ray contrast agent iodixanol is synthesized from 5-acetamido-N1,N3-bis(2,3-dihydroxypropyl)-2,4,6-triiodoisophthalamide
(2), has been successfully prepared with an overall yield
of 25%. Epoxide 1 enabled the confirmation of its presence
in the reaction mixture during the preparation of iodixanol when amide 2 was used as the starting material.
document-id-old-9ao8b00411document-id-new-14ao-2018-00411pccc-price
==== Body
1 Introduction
Fully
understanding an industrial process is of great importance
when process improvements are to be made.1 Small quantities of byproducts formed in a reaction, which on a
laboratory scale synthesis are neglectable, become important to minimize
when the reaction takes place on a ton-scale on a daily basis. From
an industrial perspective, it is therefore important to fully understand
how byproducts are formed in a given process. With such knowledge
in hand, it could be possible to alter the reaction conditions to
diminish the byproduct formation, or even better, remove them totally.
X-ray-contrast agent iodixanol (Figure 1) can be prepared by several methods.2−4 If amide 2 is used as the starting material under basic
conditions, its anion would react with epichlorohydrin, a reagent
in the reaction, to give epoxide 1 as an intermediate
in a two-step process. Because of the reactive nature of epoxides,5 and the presence of several nucleophilic sites
in amide 2, epoxide 1 could potentially
be a precursor for the formation of several minor byproducts in addition
to the major and desired product iodixanol.
Figure 1 Structure of iodixanol,
epoxide 1, and amide 2.
Previous results have shown that amide 2 is
present
in two anionic forms, compounds 2a and 2b (Figure 2a), upon
treatment with base where anion 2a is the dominating
species.6 Anion 2b can react
with epoxide 1, which results in the formation of the
imidate byproduct depicted in Figure 2b. The formation of the imidate has previously been
proved experimentally.6 Another plausible
pathway to this product could be via the intermediate, as shown in Figure 2c. This byproduct
and other byproducts1 are then removed
from crude iodixanol during work-up and purification processes, resulting
in pure iodixanol.
Figure 2 (a) Two anionic forms of amide 2; (b) byproduct
formed
if epoxide 1 reacts with the anionic form of amide 2; and (c) potential intermediate from the reaction between
anionic amide 2 and epichlorohydrin.
Epoxide 1 is expected to have a short lifetime
under
the reaction conditions, and its isolation from the reaction mixture
is therefore not a viable option when substantial amount of material
is needed for reactivity studies and for studies directed toward elucidating
its role in byproduct formation. Herein, we communicate our synthetic
approach for the preparation of epoxide 1, which also
allowed us to confirm its presence in small amounts during iodixanol
synthesis when amide 2 is used as starting material.
2 Results and Discussion
2.1 Synthesis
Initially,
we attempted
a protection group-free synthesis of epoxide 1 by performing
a regioselective N-alkylation7 of the acetamide
moiety within substrate 2, followed by a direct epoxidation
of the resulting alkene by a Prileschajew reaction.5 However, to our disappointment, we quickly ended up with
solubility problems of the material under solvent conditions required
to conduct the necessary synthetic transformations. To get around
the solubility issue, protection of the free hydroxyl groups was inevitable.
Substrate 2 was therefore converted to the tert-butyl(dimethyl)silyl (TBS)-protected product 3 in 96% yield, utilizing standard reaction conditions (Scheme 1).8 The TBS protection group was thought to be suitable for
the chemistry required for the formation of epoxide 1 and, at the same time, to be relatively easy to remove in the final
step, utilizing a global deprotection strategy. Silyl ether 3 was then subjected to a regioselective N-alkylation of the
acetamide, resulting in the formation of the desired alkene 4 in 90% isolated yield.
Scheme 1 Synthetic Pathway toward Epoxide 1
Attempts to convert
substrate 4 directly to epoxide 7 upon oxidation
by m-CPBA in a range of
solvents9 and with hydrogen peroxide in
glycine buffer10 were all unsuccessful.
A more labor-intensive route was therefore required to prepare the
target epoxide. Thus, alkene 4 was subjected to an Upjohn
dihydroxylation in acetone/water (6:1) resulting in a clean conversion
to the corresponding diol 5 (96% yield).11−13
Treating glycol 5 with methanesulfonyl chloride
(MsCl)
under conditions described by O’Donnel and Burke14 gave predominant mesylation of the primary hydroxyl
group, resulting in the isolation of mesylate 6 in 73%
yield. In addition, 10% of the product resulting from mesylation of
both hydroxyl groups (compound 8 in Scheme 1) was isolated from the reaction.
The 1H and 13C NMR chemical-shifts for the mesyl
groups in compounds 6 and 8 were in good
agreement with literature reports for similar compounds.14−16 Treating compound 6 with 2 M NaOH (aq) in ether at
room temperature, according to the Izuhara and Katoh procedure,17 resulted in the formation of epoxide 7 (70% isolated yield) over the course of 1 h. Finally, subjecting
substrate 7 to tetrabutylammonium fluoride (TBAF) in
tetrahydrofuran (THF) at room temperature gave target compound 1 in 86% isolated yield after a tedious purification process,18 which involved three rounds of flash chromatography
to fully remove all salt from the product. Attempts to remove salts
and excess TBAF from the product by using a mix of mildly acidic Ca2+ and basic ion-exchange resins were only partly successful,19 and unfortunately also resulted in significant
loss of product.
Epoxide 1 was found to be stable
under neutral conditions
and when stored neat. However, when exposed to acidic conditions,
the epoxide underwent ring opening readily. Comparing the high-performance
liquid chromatography (HPLC) chromatograms of compound 1 prepared herein and the reaction mixture during industrial production
of iodixanol enabled us to confirm that epoxide 1 was
indeed present in small quantities during the preparation of iodixanol
(see Figures S1 and S2 in the Supporting Information), thus opening up for potentially being the precursor of byproducts
formed during production. Interestingly, we also found that epoxide 1 partly ring-opens to iohexol (Figure 3) on the analytical HPLC column.
Figure 3 Structure of
iohexol.
2.2 Rotational
Conformation
The predominant
rotational conformation of the acetamide bond CO–N in compounds 2 and 3 was in the endo-form, where the carbonyl
moiety is directed toward the ring, as shown in Figure 4.20 However, the
most favored rotational isomer of the alkylated acetamide in compounds 4–7 and 1 was the exo-form. The exo-conformation
is also the dominating species in iohexol, where the acetamide is
alkylated.21 Isomerism of all compounds
was determined by the split acetyl signal in 1H NMR into
one major and one minor peak, with the endo-peak positioned downfield
of the exo-peak, because of ring-current effects.22 For compound 3, the endo-/exo-peaks were positioned
at chemical shifts 2.01 and 1.58 ppm in a 27:1 ratio, respectively,
and the equivalent peaks for compound 4 were located
at 2.18 and 1.73 ppm in a 1:20 ratio (see Figure S3 in the Supporting Information).
Figure 4 Endo-/exo-isomerism of
the acetamide attached to the triiodinated
benzene ring.
1H NMR analysis
conducted at 400 K (127 °C) showed
that rotation of the amide bond was more restricted in compound 4 (containing a tertiary acetamide moiety) compared with compound 3. At 400 K, the endo- and exo-peaks in compound 3 overlapped forming one broad singlet. However, for alkene 4, the endo- and exo-peaks remained separated, with an endo-/exo-ratio
of 1:7 at 127 °C, compared to a ratio of 1:20 obtained at room
temperature. Further evidence of rotational isomerism was observed,
but not investigated, in this work. For more information on the subject,
we refer to relevant literature on the topic.20−23
3 Conclusions
Epoxide 1 was prepared over six synthetic steps with
an overall yield of 25% using a strategy, where the hydroxyl groups
were protected with TBS groups. Our synthesis of compound 1 enabled us to confirm the presence of epoxide 1 in
the reaction mixture in small quantities during the synthesis of iodixanol
making compound 1 a potential starting point for byproduct
formation. Work is now going on in these laboratories to study whether
compound 1 is involved in the byproduct formation when
iodixanol is synthesized from amide 2.
4 Experimental Section
4.1 General
All commodity
chemicals and
reagents were purchased from commercial suppliers and used without
further purification. Petroleum ether (pet. ether, 40–65 °C)
was used for column chromatography. Silica gel NORMASIL 60 40–63
μm was used for flash chromatography. Proton (1H)
and carbon (13C) NMR spectra were acquired at 20 °C.
Proton and carbon NMR spectra were recorded using an Ascend 400 NMR
spectrometer from Bruker (Ascend 400), operating at 400 and 100 MHz.
NMR spectra are referenced to residual dimethyl sulfoxide (DMSO) (δ
2.50 ppm, 1H; δ 39.52 ppm, 13C). 1H NMR data are recorded as follows: chemical shift (δ)
[multiplicity, coupling constant(s) J (Hz), and relative
integral] where multiplicity is reported as: s = singlet; d = doublet;
t = triplet; q = quartet; quint = quintet; dt = doublet of triplet;
m = multiplet; and bs = broad singlet. For 13C NMR spectra,
the data are given as chemical shift (δ), (protonicity), where
the number of protons is defined as: C = quaternary (where ArC = quaternary
aromatic carbon); CH = methyne; CH2 = methylene; and CH3 = methyl. The assignment of signals in various NMR spectra
was often assisted by correlation spectroscopy (COSY), nuclear Overhauser
effect and exchange spectroscopy, heteronuclear single quantum COSY,
and/or heteronuclear multiple bond COSY. Analytical HPLC was performed
on an Agilent 1100 or a TSP (Thermo Separation products) instrument
with UV detection at 254 nm using an RP-18 column (YMC 150 ×
4.6 mm, 5 μm). The following linear gradient program with mixtures
of water (A) and acetonitrile (B) as eluent was applied. Program:
3.0% B (0–2.7 min), 3.0–7.2% B (2.7–5.5 min),
7.2% B (5.5–16.5 min), 7.2–13.0% B (16.5–19.5
min), 13.0–45.0% B (19.5–26.5 min), 45.0% B (26.5–31.5
min). The flow rate was 1.25 mL/min. No acid was mixed with the eluents
unless otherwise stated. The amount of each component is given in
percentage, based on its relative area.
4.1.1 5-Acetamido-N1,N3-bis(2,3-bis((tert-butyldimethylsilyl)oxyl)propyl)-2,4,6-triiodoisophthalamide
(3)
Imidazole (6.58 g, 96.7 mmol), 4-dimethylaminopyridine
(DMAP) (3.27 g, 26.8 mmol), and tert-butyldimethylsilyl
chloride (13.38 g, 88.8 mmol, 6.6 equiv) were added to a solution
of amide 2 (10.0 g, 13.5 mmol) in dimethylformamide (100
mL). The reaction was left stirred at 60 °C under a nitrogen
atmosphere for 5 h. The reaction was then quenched with NaHCO3 (sat. aq solution, 100 mL) and extracted with EtOAc (150
mL × 3), and the organic layers were washed with brine (100 mL
× 2) and water (50 mL). The crude product was purified by flash
column chromatography using petroleum ether/EtOAc, 7:3 → 1:4
(gradient elution). Isolation of the appropriate fractions (Rf = 0.32 in petroleum ether/EtOAc 7:3) gave
15.6 g (96%) of the O-silylated product 3 as a white
solid, mp 241.0–241.5 °C. IR (KBr) νmax: 3280, 2929, 2857, 2602, 2489, 2359, 1648, 1540, 1472, 1256, 1139,
1101, 984, 938, 835, 777, 668 cm–1; 1H NMR (400 MHz, DMSO-d6): δ 9.97
and 9.52 (2br s in ratio 93:4, 1H), 8.70–8.71, 8.56–8.58,
8.32–8.37, and 8.19–8.24 (2m + 2m in ratio 78:80:18:12,
2H), 3.89–3.95 (m, 2H), 3.78–3.80, and 3.51–3.55
(2m in ratio 1:1, 4H) 3.38–3.36, 3.25–3.23, 3.15–3.13,
and 3.01–2.99 (4m in ratio 1:1:1:1, 4H), 2.01 and 1.58 (2br
s in ratio 27:1, 3H), 0.88, 0.87, 0.86, and 0.84 (4br s in ratio 8:6:3:1,
36H), 0.12, 0.08, 0.03, −0.05 (3br s and 1s in ratio 6:6:12:1,
24H); 13C NMR (400 MHz, DMSO-d6): δ 169.9 (C), 168.2 (C), 150.3 (ArC), 78.6 (CH), 66.6 (CH2), 42.8 (CH2), 26.4 (CH3), 23.5 (CH3), 18.6 (C), 18.3 (C), −2.5 (CH3), −4.0
(CH3), −4.2 (CH3), −4.8 (CH3) (specific aromatic carbons were not visible because of slow
relaxation and rotamerization). HRMS found: [M + H]+, 1204.1972.
C40H77I3N3O7Si4 requires [M + H]+, 1204.1967.
4.1.2 5-(N-Allylacetamido)-N1,N3-bis(2,3-bis((tert-butyldimethylsilyl)oxy)propyl)-2,4,6-triiodoisophthalamide
(4)
To a solution of compound 3 (15 g, 12.5 mmol) in EtOH (100 mL) and isopropyl alcohol (50 mL),
a solution of H3BO3 (1.55 g, 25 mmol) in water
(15 mL) was added with pH adjusted to approx. 12.5 by dropwise addition
of 10 M KOH. Allyl bromide (1.08 mL, 12.5 mmol, 1 equiv) was added,
and the reaction was left stirred for 3 h at 40 °C, whereas the
pH was monitored and constantly adjusted to approx. pH 12.5 by dropwise
addition of 10 M KOH. A second addition of allyl bromide (0.54 mL,
6.25 mmol, 0.5 equiv) was conducted, and the reaction was left stirred
for an additional 20 h. EtOH was then removed in vacuo, the product
was extracted with EtOAc (50 mL × 2), and the combined organic
fractions were washed with water (40 mL). The crude product was then
purified using a prepacked silica gel column (HP silica 50 μm)
from PuriFlash (Interchim 215, petroleum ether/EtOAc, 95 →
50% petroleum ether (gradient elution), 35 mL/min) and yielded 13.9
g (90%) of the N-alkylated product 4 as white crystals,
mp 115–116 °C. IR (KBr) νmax: 3420, 3287,
3082, 2953, 2929, 2885, 2857, 2360, 2339, 2244, 1654, 1546, 1528,
1502, 1471, 1314, 1139, 1101, 982, 937, 921, 835, 778, 734, 668 cm–1; 1H NMR (400 MHz, DMSO-d6): δ 8.58–8.57 (m, 2H), 5.91–5.86
(m, 1H), 5.17–5.16, 5.12, 5.05, and 5.03 (4m in ratio 1:1:1:1,
2H), 4.14–4.12 and 4.06–4.04 (2m in ratio 1:1, 2H),
3.94–3.93 and 3.88–3.86 (2m in ratio 1:1, 2H), 3.78–3.75
and 3.56–3.52 (2m in ratio 1:1, 4H), 3.37–3.33, 3.26–3.24,
3.20–3.18, and 3.07–3.05 (4m in ratio 1:1:1:1, 4H),
2.1,9 2.18, 1.74 and 1.73 (4br s in ratio 1:1:20:20, 3H), 0.88, 0.87
(2br s in ratio 1:1, 36H), 0.12, 0.11, 0.08, and 0.03 (4br s in ratio
1:1:2:4, 24H); 13C NMR (400 MHz, DMSO-d6): δ 169.3 (C), 168.5 (C), 150.8 (ArC), 146.8 (ArC),
132.6 (CH), 119.0 (CH2), 101.1 (ArC), 100.6 (ArC), 90.8
(ArC), 71.7 (CH), 66.0 (CH2), 50.7 (CH2), 42.0
(CH2), 25.9 (CH3), 22.8 (CH3), 18.1
(C), 17.9 (C), −4.7 (CH3), −5.2 (CH3); HRMS found: [M + H]+, 1244.2287. C43H81I3N3O7Si4 requires
[M + H]+, 1244.2280.
4.1.3 N1,N3-Bis(2,3-bis((tert-butyldimethylsilyl)oxy)propyl)-5-(N-(2,3-dihydroxypropyl)acetamido)-2,4,6-triiodoisophthalamide
(5)
To a solution of substrate 4 (12 g, 9.65 mmol) in acetone (150 mL) and water (25 mL) at room
temperature were added NMO (1.8 g, 15.4 mmol, 1.6 equiv) and OsO4 in tBuOH (1.95 mL, 2 mol %). The reaction
was left stirred for 20 h and then quenched by the addition of Na2S2O3 (20 mL, 1 M aq). The product was
then extracted with EtOAc (50 mL × 3), and the combined organic
fractions were concentrated to dryness under reduced pressure. The
crude product was purified on a prepacked silica gel column (HP silica
50 μm) from PuriFlash (Interchim 215, petroleum ether/EtOAc,
95 → 40% petroleum ether (gradient elution), flow rate 35 mL/min).
Isolation of the fractions with Rf = 0.19
(pet. ether/EtOAc, 11:9) gave 11.8 g (96%) of compound 5 as white crystals, mp 122–123 °C. IR (KBr) νmax: 3274, 2953, 2929, 2857, 2885, 2357, 2337, 1652, 1471,
1392, 1255, 1139, 1100, 835 cm–1; 1H
NMR (400 MHz, DMSO-d6): δ 8.62–8.57
(m, 2H), 4.60–4.56 (m, 2H), 3.97–3.94, 3.89–3.86
(2m in ratio 1:1, 2H), 3.91–3.88, 3.82–3.79 (2m in ratio
1:1, 1H), 3.79–3.77, 3.57–3.55 (2m in ratio 1:1, 4H),
3.38–3.42 (m, 2H), 3.83–3.81, 3.69–3.67, 3.34–3.32,
3.15–3.13 (4m in ratio 1:1:1:1, 4H), 2.24, 2.22, 1.78, and
1.77 (4br s in ratio 1:1:15:15, 3H), 0.89–0.88, 0.87–0.86
(2m in 1:1 ratio, 36H), 0.12, 0.11, 0.09, 0.04 (4br s in ratio 1:1:2:4,
24H); 13C NMR (400 MHz, DMSO-d6): δ 170.6 (C), 169.9 (C), 151.5 (ArC), 148.6 (ArC), 100.7
(ArC), 90.9 (ArC), 72.2 (CH), 71.9 (CH), 70.4 (CH), 66.4 (CH2), 65.0 (CH2), 53.9 (CH2), 42.5 (CH2), 26.4 (CH3), 23.3 (CH3), 18.6 (C), 18.3 (C),
−4.01 (CH3), −4.72 (CH3); HRMS
found: [M + H]+, 1278.2340. C43H82I3N3O9Si4 requires [M
+ H]+, 1278.2335.
4.1.4 3-(N-(3,5-Bis((2,3-bis((tert-butyldimethylsilyl)oxy)propyl)carbamoyl)-2,4,6-triiodophenyl)acetamido)-2-hydroxypropyl
Methanesulfonate (6)
To a solution of diol 5 (9.5 g, 7.44 mmol) in dichloromethane (DCM) (100 mL) at
0 °C was added pyridine (5.5 mL, 68.0 mmol, 9.1 equiv), DMAP
(5 mol %), and MsCl (0.92 mL, 11.9 mmol, 1.6 equiv). The reaction
was left stirred for 22 h at 5 °C and was then quenched with
water (50 mL), extracted with DCM (80 mL × 3), washed with HCl
(75 mL, 2 M), K2CO3 (75 mL, sat. aq solution),
and water (75 mL), dried over MgSO4, and concentrated under
reduced pressure. Purification was conducted on a prepacked silica
gel column (HP silica 50 μm) from PuriFlash (Interchim 215,
petroleum ether/EtOAc, 95–30% petroleum ether (gradient elution),
flow rate 35 mL/min). Excess pink/orange salt was further removed
from product by filtration through silica gel (petroleum ether/EtOAc,
9:1). Isolation of the fractions with Rf = 0.19 (petroleum ether/EtOAc 1:1) gave 7.3 g (73%) of the primary
mesylate 6 as white crystals, mp 146–149 °C.
IR (KBr) νmax: 3368, 3293, 2953, 2929, 2886, 2857,
2360, 2341, 1653, 1540, 1472, 1394, 1361, 1254, 1174, 1139, 1100,
982, 938, 835, 777 cm–1; 1H NMR (400
mHz, DMSO-d6): δ 8.63–8.59
(m, 2H), 5.43–5.38 and 5.36–5.30 (2m in ratio 1:1, H),
4.36–4.34 and 4.12–4.10 (2m in ratio 1:1, 2H), 4.10–4.08
and 4.02–3.99 (2m, 2H), 4.02–4.00, 3.97–3.95,
and 3.02–3.00 (3m, 2H), 3.96–3.94 and 3.89–3.86
(2m, H), 3.79–3.77 and 3.57–3.54 (2m in ratio 1:1, 4H),
3.42–3.41, 3.25–3.24, and 3.04–3.03 (3m, 4H),
3.17 (br s, 3H), 2.25, 2.24, 1.80, and 1.79 (4br s in ratio 2:2:13:13,
3H), 0.88 and 0.87 (2br s in ratio 1:1, 36H), 0.12, 0.09, and 0.04
(3br s in ratio 1:1:2, 24H); 13C NMR (400 MHz, DMSO-d6): δ 170.6 (C), 169.9 (C), 73.7 (CH2), 72.3 (CH), 71.9 (CH), 67.4 (CH), 66.4 (CH2),
53.0 (CH2), 42.6 (CH2), 37.0 (CH3), 26.4 (CH3), 23.3 (CH3), 22.7 (CH3), 18.4 (C), −4.0 (CH3), −4.1 (CH3), −4.7 (CH3) (aromatic carbons were not visible
because of slow relaxation and rotamerization); HRMS found: [M + Na]+, 1378.1935 C44H84I3N3O11SSi4 requires [M + Na]+, 1378.1930.
Isolating of the fractions with Rf = 0.41 (petroleum ether/EtOAc 1:1) gave the dimesylated
product 8 as white crystals (1.1 g, 10%), mp 152–154
°C. IR (KBr) νmax: 3368, 2953, 2929, 2886, 2857,
2362, 2341, 1654, 1541, 1472, 1396, 1361, 1254, 1174, 1143, 1102,
982, 938, 834, 777 cm–1; 1H NMR (400
MHz, DMSO-d6): δ 8.60–8.58,
8.52–8.50, and 8.48–8.45 (3m in 10:3:3 ratio, 2H), 4.65–4.60
and 4.45–4.43 (2m, 2H), 4.45–4.41 and 4.41–4.37
(2m, HCOMs), 4.37–4.29, 4.32–4.24,
3.44–3.36, and 3.27–3.20 (4m, 2H), 3.95–3.88
and 3.87–3.80 (2m, 2H), 3.97–3.92 and 3.91–3.86
(2m in 1:1 ratio, 4H), 3.78–3.73 and 3.30–3.19 and 3.11–2.99
(3m, 4H), 3.25 (2br s, 3H), 3.17 (br s, 3H), 2.25, 2.24, 1.80, and
1.79 (4br s in ratio 2:2:13:13, 3H), 0.88 and 0.87 (2br s in ratio
1:1, 36H), 0.12, 0.09, and 0.04 (3br s in ratio 1:1:2, 24H); 13C NMR (400 MHz, DMSO-d6): δ
170.3 (C), 169.4 (C), 152.3 (ArC), 151.6 (ArC), 147.7 (ArC), 101.1
(ArC), 99.4 (ArC), 91.5 (ArC), 71.7 (CH), 71.4 (CH), 65.9 (CH2), 56.7
(CH2), 52.6 (CH2), 42.1 (CH2), 36.9
(CH3), 25.9 (CH3), 25.8 (CH3), 22.5
(CH3), 18.1 (C), 17.9 (C), −4.5 (CH3),
−4.7 (CH3), −5.3 (CH3).
4.1.5 N1,N3-Bis(2,3-bis((tert-butyldimethylsilyl)oxy)propyl)-2,4,6-triiodo-5-(N-(oxiran-2-ylmethyl)acetamido)isophthalamide (7)
To a solution of mesylate 6 (6.5 g, 4.8 mmol)
in Et2O (150 mL) was added NaOH (10 mL, 2 M aq). After
stirring for 23 h at room temperature, the mixture was extracted with
Et2O (100 mL × 2). The extract was washed with water
(75 mL) and dried over MgSO4, filtered, and concentrated.
The crude product was purified by flash column chromatography (petroleum
ether/EtOAc, 3:1). Concentration of the fractions with Rf = 0.22 (petroleum ether/EtOAc 7:3) yielded 4.2 g (70%
yield) of epoxide 7 as white crystals, mp 119–120
°C. IR (KBr) νmax: 3288, 3059, 2929, 2885, 2857,
2246, 1655, 1542, 1472, 1389, 1316, 1256, 1139, 1101, 981, 938, 910,
836, 778, 734, 668 cm–1; 1H NMR (400
MHz, DMSO-d6): δ 8.62–8.58
(m, 2H), 3.96–3.94 and 3.90–3.88 (2m in ratio 1:1, 2H),
3.78–3.76 and 3.57–3.55 (2m in ratio 1:1, 4H), 3.70–3.69,
3.52–3.51, and 3.28–3.27 (3m, 2H), 3.41–3.39,
3.25–3.24, and 3.06–3.05 (3m, 4H), 3.28–3.26
and 3.22–3.20 (2m, 1H), 2.73–2.72, 2.51–2.49,
and 2.48–2.46 (3m, 2H), 2.24, 2.23, 1.80, and 1.79 (4br s in
ratio 1:1:24:24, 3H), 0.89 and 0.88 (2br s in ratio 1:1, 36H), 0.12,
0.10, and 0.05 (3br s in ratio 1:1:2, 24H); 13C NMR (400
MHz, DMSO-d6): δ 169.3 (C), 169.2
(C), 151.0 (ArC), 147.3 (ArC), 100.4 (ArC), 91.0 (ArC), 71.7 (CH),
71.4 (CH), 65.9 (CH2), 52.0 (CH2), 51.3 (CH2), 49.2 (CH), 48.7 (CH), 46.4 (CH2), 42.0 (CH2), 25.9 (CH3), 24.1 (CH3), 22.4 (CH3), 18.1 (C), 17.9 (C), −4.5 (CH3), −4.7
(CH3), −5.2 (CH3); HRMS found: [M + H]+,1260.2235. C43H81I3N3O8Si4 requires [M + H]+,
1260.2229.
4.1.6 N1,N3-Bis(2,3-dihydroxypropyl)-2,4,6-triiodo-5-(N-(oxiran-2-ylmethyl)acetamido) Isophthalamide (1)
To a solution of epoxide 7 (1.64 g, 1.3 mmol)
in THF
(35 mL) was added 1 M TBAF in THF (7.2 mL, 7.2 mmol, 5.5 equiv). After
2 h, the solvent was removed by vacuum. Three subsequent purifications
using flash column chromatography EtOAc/MeOH (3:1) (Rf = 0.26) yielded 895 mg (86% yield) of epoxide 1 as a white powder, mp 285 °C (dec). IR (KBr) νmax: 3343, 2926, 2350, 1730, 1650, 1429, 1393, 1347, 1316,
1270, 1173, 1110, 1044, 981, 921, 727 cm–1; 1H NMR (400 mHz, DMSO-d6): δ
8.57 (br s, 2H), 4.77–4.75 and 4.55–4.53 (2m, 2H), 3.71–3.68
(m, 2H), 3.45–3.42 (m, 4H), 3.69–3.68, 3.57–3.56,
3.49–3.48, and 3.32–3.31 (4m, 2H), 3.49–3.48,
3.30–3.29, and 3.07–3.06 (3m, 4H), 3.26–3.24
and 3.22–3.19 (2m, 1H), 2.72–2.71, 2.52–2.51,
and 2.47–2.46 (3m, 2H), 2.24, 2.22, 1.80, and 1.79 (4br s in
ratio 1:1:11:11, 3H); 13C NMR (400 MHz, DMSO-d6): δ 169.6 (C), 169.5 (C), 151.1 (ArC), 146.6 (ArC),
100.5 (ArC), 92.1 (ArC), 70.2 (CH), 64.0 (CH2), 51.9 (CH2), 51.3 (CH2), 49.3 (CH), 48.7 (CH), 46.5 (CH2), 42.6 (CH2), 22.5 (CH3), 22.1 (CH3); HRMS found: [M + H]+, 803.8779. C19H25I3N3O8 requires [M]+, 803.8776.
Supporting Information Available
The Supporting Information is
available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b00411.Components of
the reaction mixture during preparation;
HPLC chromatogram of synthesized epoxide 1 and ring-opening
product iohexol; endo-/exo-configuration of compounds 3 and 4 at 298 K and 400 K; and 1H, 13C NMR, and/or 2D spectra for all new compounds (PDF)
Supplementary Material
ao8b00411_si_001.pdf
The authors
declare no competing financial interest.
Acknowledgments
The University of Stavanger, the research program
Bioactive, and GE Healthcare are thanked for the financial support
of the project. Dr. Holmelid, University of Bergen, is also thanked
for recording mass spectra. Professor Tanaka, Okinawa Institute of
Science and Technology Graduate University, Okinawa, Japan, is thanked
for excellent working conditions during a sabbatical stay.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145899210.1021/acsomega.8b01375ArticleHierarchical Nickel–Cobalt Dichalcogenide Nanostructure
as an Efficient Electrocatalyst for Oxygen Evolution Reaction and
a Zn–Air Battery Hyun Suyeon Shanmugam Sangaraju *Department of Energy Science Engineering, Daegu Gyeongbuk Institute of Science & Technology
(DGIST), Daegu 42988, The Republic of Korea* E-mail: sangarajus@dgist.ac.kr. Phone: +82-53-785-6413 (S.S.).02 08 2018 31 08 2018 3 8 8621 8630 19 06 2018 20 07 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under a Creative Commons Attribution (CC-BY) License, which permits unrestricted use, distribution and reproduction in any medium, provided the author and source are cited.
A unique
three-dimensional (3D) structure consisting of a hierarchical
nickel–cobalt dichalcogenide spinel nanostructure is investigated
for its electrocatalytic properties at benign neutral and alkaline
pH and applied as an air cathode for practical zinc–air batteries.
The results show a high oxygen evolution reaction catalytic activity
of nickel–cobalt sulfide nanosheet arrays grown on carbon cloth
(NiCo2S4 NS/CC) over the commercial benchmarking
catalyst under both pH conditions. In particular, the NiCo2S4 NS/CC air cathode shows high discharge capacity, a
narrow potential gap between discharge and charge, and superior cycle
durability with reversibility, which exceeds that of commercial precious
metal-based electrodes. The excellent performance of NiCo2S4 NS/CC in water electrolyzers and zinc–air batteries
is mainly due to highly exposed electroactive sites with a rough surface,
morphology-based advantages of nanosheet arrays, good adhesion between
NiCo2S4 and the conducting carbon cloth, and
the active layer formed of nickel–cobalt (oxy)hydroxides during
water splitting. These results suggest that NiCo2S4 NS/CC could be a promising candidate as an efficient electrode
for high-performance water electrolyzers and rechargeable zinc–air
batteries.
document-id-old-9ao8b01375document-id-new-14ao-2018-01375jccc-price
==== Body
Introduction
Splitting water into
pure hydrogen and oxygen to generate sustainable
green hydrogen energy has been intensively studied in recent years,
which can replace fossil fuel use.1,2 However, the
efficiency of water splitting has so far been limited by the lack
of sustainable catalysts toward the oxygen evolution reaction (OER)
that can accelerate the kinetics.3−5 So far, IrOx and RuO2 are the best-known OER catalysts,
although their high cost and scarcity limit their widespread use.4 Meanwhile, some promising attempts have been
devoted to developing an efficient nonprecious metal OER catalyst
under alkaline conditions. However, an almost harsh alkaline medium
presents severe corrosion and related environmental issues.6,7 In this regard, someday, the splitting of water at neutral pH from
ocean or river would be the target goal to satisfy renewable future
hydrogen energy.4 It is thus highly required
to develop efficient OER electrocatalysts that can operate in both
alkaline and neutral media for overall water splitting even though
it is relatively tough searching for those catalysts.
Nowadays,
various nonprecious transition metal-based catalysts
are being explored, for example, transition metals,8 transition-metal oxides,9,10 chalcogenides,11−14 phosphides,15−17 hydroxides/oxyhydroxides,18,19 carbides,20 borides,21 and so on. Although lots of established catalysts have
been reported concerning their excellent OER activity under alkaline
conditions, only a few of them could still maintain their catalytic
activity in neutral media. Cai et al. reported that the amorphous
cobalt sulfide porous nanocubes showed a low OER onset potential of
1.5 V, comparable to that of RuO2 (1.49 V).22 However, a still substantial overpotential of
570 mV is needed to generate 4.59 mA cm–2 in phosphate-buffered
solutions (PBSs; pH 7.0), whereas it could generate 10 mA cm–2 current density at 290 mV in 1 M KOH (pH 14.0). Similarly, sulfur-incorporated
NiFe2O4 nanosheets (NSs) on nickel foam (S–NiFe2O4/NF) developed by Liu et al. exhibited a remarkably
enhanced water-splitting performance for both OER and hydrogen evolution
reaction (HER) as a bifunctional electrode under both alkaline and
neutral conditions.23 The S–NiFe2O4/NF still requires 1.921 V to deliver 10 mA cm–2 in 1 M PBS (pH 7.4) for overall water splitting in
three electrode systems, mostly occurring during OER with an overpotential
of 494 mV. As air cathode catalysts for Zn–air batteries, Prabu
et al., demonstrated a highly active one-dimensional structure of
a spinel NiCo2O4 catalyst in rechargeable Zn–air
batteries and Li–O2 batteries.24,100 Recently, Meng et al. constructed Co0.85Se nanocrystals
in situ coupled with N-doped carbon with a metal–nitrogen–carbon
(M–N–C) structure and short diffusion pathways for the
transport of electron/ion to improve the Zn–air battery performance.25,26 For instance, Wu et al. reported zinc cobalt sulfide, the nanoneedle
(NN) arrays grown on the carbon fiber paper electrode catalyst, which
enables the Zn–air battery operation with an overpotential
of 0.85 V and a long cycle life time of up to 200 cycles at 10 mA
cm–2 as well as comparable water-splitting performance.27 Wang et al. proposed Co3FeS1.5(OH)6 hydroxysulfides serving as a superb air electrode
catalyst with a low overpotential of 0.84 V and prolonged cyclability
over 36 h test for 108 cycles at 2 mA cm–2.28
In pursuit of high electrochemical performance
in water electrolyzers
and for a Zn–air battery application, the spinel bimetallic
sulfide NiCo2S4 with abundant redox chemistry
has been considered to be the most promising electrochemically active
material, which exhibits 2 orders of magnitude larger than that of
NiCo2O4 and ∼104 times better
electric conductivity than conventional single-metal compounds.12,29 Moreover, the stable spinel structures of bimetallic sulfide with
a formula of AB2S4 possess plentiful exposed
edge sites, leading to a higher electrochemical activity. Therefore,
it has been widely applied for supercapacitors, Li-ion batteries,
and a counter electrode for dye-sensitized solar cells as well as
in water electrolyzers.30 For example,
in our group, NiCo2S4 nanowire arrays were directly
grown on 3D Ni foam (NiCo2S4 NW/NF) as a water-splitting
catalyst and applied in an alkaline water electrolyzer. Because of
its intrinsic properties, large surface area, and well-separated NW
structures, NiCo2S4 NW/NF afforded continuous
water-splitting reaction of generating hydrogen and oxygen gas at
a cell voltage of only 1.63 V to generate 10 mA cm–2 current density.31 Ma et al. developed
3D networked porous NiCo2S4 nanoflakes on NF,
which can offer more exposed active sites and easy transport of electrons
and ions, thereby leading to significantly improved HER activity and
stability.32 The outstanding OER performance
of the spinel bimetallic sulfide NiCo2S4 has
also become a promising application for rechargeable Zn–air
batteries involving reversible OER and ORR.
Also, hybridizing
NiCo2S4 with the 3D structure
of NS or NN with a carbon cloth (CC) (NiCo2S4 NS/CC or NN/CC) substrate by an in situ growth hydrothermal approach
can be an efficient way to enhance the robustness of the electrode.
It could also help to minimize the agglomeration of NiCo2S4 nanostructures and the detachment during long-term
operation, and make faster ion/electron kinetics. Also, the advantages
of CC, such as flexibility, high conductivity, and corrosion/dissolution
resistivity might lead to enhanced catalytic activity and stability
in a wide pH range.33 Meanwhile, tuning
the nanostructure and the morphology, as well as porosity, can be
another promising strategy to produce numerous exposed catalytic active
sites on the catalyst surface.17
On the basis of our knowledge, we describe the physical and electrochemical
properties of NiCo2S4 NS/CC as a highly active
OER catalyst in both neutral and alkaline media, which have not been
thoroughly investigated so far. Mainly, this is the first time a bimetallic
sulfide, the NiCo2S4-based material, is reported
to catalyze OER under a neutral condition. The catalytic performance
of NiCo2S4 NS/CC is remarkably enhanced compared
to the recent reports, particularly under a neutral condition. The
NiCo2S4 NS/CC electrocatalyst exhibits the lowest
OER overpotentials of 260 and 402 mV to generate 10 mA cm–2 in alkaline and neutral media, respectively. Specifically, it exhibits
a low Tafel slope of 123 mV dec–1 and a high turnover
frequency (TOF) of 8.17 × 10–3 s–1 at 1.63 V applied potential to drive 10 mA cm–2 current density under neutral conditions, confirming superior intrinsic
activity with a substantial electrochemical active surface area (ECSA)
of NiCo2S4 NS/CC compared with commercial RuO2/CC and other previously reported OER electrocatalysts. In
addition, the constructed NiCo2S4 NS/CC air
cathode for primary and rechargeable Zn–air batteries exhibits
high discharge capacity, a narrow overall overpotential, and a long
cycling life time exceeding the benchmark for precious metal-based
electrodes.
Experimental Methods
Material Synthesis
Cobalt nitrate
hexahydrate [Alfa
Aesar, Co(NO3)2·6H2O], nickel
nitrate hexahydrate [Sigma-Aldrich, Ni(NO3)2·6H2O], urea (Sigma-Aldrich, CH4N2O), and sodium sulfide hydrate (Sigma-Aldrich, Na2S·xH2O) were used to synthesize
the electrodes. A piece of CC (NARA CELL-TECH, 0.7 cm × 0.7 cm)
was utilized with further treatment with ethanol. The NiCo2S4 NSs grown on CC (NiCo2S4 NS/CC)
were prepared through a two-step hydrothermal process. A nickel nitrate
of 0.004 M and cobalt nitrate of 0.008 M was dissolved in 120 mL of
deionized water; further, 0.012 M urea was added. The obtained solution
was transferred into a Teflon-lined stainless steel autoclave of 200
mL capacity, and a piece of CC was immersed in the solution. The autoclave
was heated at 120 °C for 8 h in an electric oven. After the first
step, the electrode was washed with deionized water several times
to eliminate unreacted residues. Consequently, sodium sulfide flakes
were dissolved in deionized water to prepare a 0.2 M sulfide solution
for a sulfurization process. This sulfur-containing solution was again
transferred to the autoclave and heated at 160 °C for 8 h in
an electric oven. After cooling down to room temperature naturally,
we washed the synthesized electrode several times with ethanol and
deionized water, followed by the drying step in the vacuum oven at
60 °C overnight. For comparison, NiCo2S4 NN arrays on CC (NiCo2S4 NN/CC) were prepared
by changing the temperature of the first hydrothermal step from 120
to 130 °C and maintaining the heating time of 8 h. To synthesize
NiCo2O4 with NSs morphology, which is grown
on CC (NiCo2O4 NS/CC), the electrode after the
first step of the hydrothermal growth process was annealed at 450
°C for 2 h in an air atmosphere.
Microstructural Characterizations
The morphology and
element compositions were studied on a field-emission scanning electron
microscopy (FE-SEM, Hitachi-S4800, 3 kV) system equipped with a Horiba
Scientific energy dispersive spectrometer and using transmission electron
microscopy (TEM, Hitachi HF-3300, 300 kV). The crystal structures
of all catalysts were examined by powder X-ray diffraction (XRD, Rigaku
MiniFlex600). The composition of the catalyst was studied using X-ray
photoelectron spectroscopy (XPS, Thermo-Scientific ESCALAB 250Xi).
Electrochemical Measurements
For electrochemical measurements,
the OER catalytic performance was evaluated by linear sweep voltammetry
(LSV) with a low scan rate of 1 mV s–1 in an electrolyte
of 1 M KOH and a PBS without purging oxygen. The OER performance was
evaluated in a three-electrode configuration directly using synthesized
electrodes such as NiCo2S4 NS/CC, NiCo2S4 NN/CC, and NiCo2O4 NS/CC as a
working electrode (1.0 mg cm–2), a saturated calomel
electrode (SCE) as a reference electrode, and a Pt wire as the counter
electrode. Similarly, commercial RuO2 cast onto CC was
used as a working electrode (1.4 mg cm–2), Pt wire
as a counter electrode, and SCE as a reference electrode. The potentials
reported were converted to the reversible hydrogen electrode (RHE).
All electrochemical results were iR-corrected, considering
the ohmic resistance from the electrolyte. The current densities presented
in this paper are normalized concerning the geometric surface area
of the electrode. The cyclic voltammetry (CV) was performed in N2-saturated 1 M KOH at room temperature with a scan rate of
10 mV s–2. Electrochemical impedance spectroscopy
(EIS) was performed within a frequency range of 0.01 Hz to 0.1 MHz.
The ECSA is calculated by following an established methodology
reported in the literature.31 In detail,
through the cyclic voltammogram obtained in a non-faradaic region
at various scan rates (1, 2.5, 5, 10, 20, and 50 mV s–1), double-layer capacitance (Cdl) can
be estimated. By plotting the anodic and cathodic current densities
against the scan rate, the obtained linear slope value is Cdl. Finally, the ECSA can be obtained from the
following equation:
Cs denotes the specific capacitance
of a flat, smooth surface of the electrode material, which is assumed
to be 26 μF cm–2 for Ni- and Co-containing
materials.
Zinc–Air Battery Fabrication and Testing
For
full-cell zinc–air battery evaluation, the as-synthesized NiCo2S4 NS/CC or commercial catalyst of RuO2 + Pt/C/CC was used as an air-breathing cathode (1.54 cm2). Typically, the NiCo2S4 NS/CC air cathode
was prepared with a loading amount of 1.0 mg cm–2. The commercial catalyst-based cathode was fabricated by coating
with 2 mg of RuO2 and 40 wt % Pt/C on CC to achieve a loading
of 1.30 mg cm–2. A polished zinc plate with a thickness
of 0.1 mm, 6 M KOH solution with 0.2 M zinc acetate, and a Whatman
glass microfiber filter membrane were prepared as an anode, an electrolyte,
and a separator, respectively, to assemble the zinc–air battery
with a coin cell (MTI Korea) configuration. The specific capacity
and the charge–discharge curves were reported with a battery
analyzer (BST8-3), which consumed ambient air. The discharge capacity
of the primary zinc–air cell was normalized to the consumed
mass of Zn metal, whereas the current density was normalized to the
area of the electrode.
Results and Discussion
The hierarchical
bimetallic sulfide NS arrays/CC hybrids were developed
using an in situ two-step hydrothermal method, as graphically represented
in Scheme 1. In the
first step of the hydrothermal process, nickel nitrate hexahydrate
and cobalt nitrate hexahydrate in a stoichiometric ratio were dissolved
in deionized water and then urea was added. The solution was transferred
into an autoclave and heated at 120 °C for 8 h, forming cobalt–nickel
carbonate hydroxide hydrate NS arrays on a CC substrate. Subsequently,
after oxidation reaction, a solution of sodium sulfide flakes dissolved
in deionized water was prepared for the next sulfurization process.
The anion exchange reaction from Co32–/OH– anions to S2– anions occurred
at 160 °C for 6 h, thereby leading the complete phase transformation
from cobalt–nickel carbonate hydroxide hydrate to nickel–cobalt
sulfide on the CC. The morphology and composition of NiCo2S4 NS/CC were studied by FE-SEM and TEM. The bare CC consists
of interconnected fibers with a smooth surface, as shown in Figure 1a. After the first
hydrothermal reaction, numerous NS arrays are stacked onto the surface
of CC with a rough surface shown in Figures 1b and S1. Consequently,
the second hydrothermal process for sulfurization treatment is conducted,
and its NS-like morphology perpendicular to a substrate with a rough
surface still preserves its architecture (Figure 1e). From the top view of NiCo2S4 NS/CC, as shown in Figure 1c,d, the NiCo2S4 NSs
that are interconnected with each other and form a porous architecture
with submicron-size pores, providing ample space for the fast diffusion
of redox ions during the reaction, uniformly cover the surface of
CC. For comparison, the needle-like shape of NiCo2S4 vertically grown on the surface of CC with the average length
of 3 μm is also synthesized to understand the effect of morphology
on catalytic activities in both alkaline and neutral medium (Figure S2a–c). Also, the NiCo2O4 NS/CC was fabricated to have the same morphological
characteristics as NiCo2S4 NS/CC (Figure S2d–f).
Figure 1 FE-SEM images of (a)
bare CC, (b) NiCo-precursor/CC after the first
step in the hydrothermal process, (c–f) NiCo2S4 NS arrays grown on the surface of CC at different magnifications.
Scheme 1 Schematic Preparation Process of Self-Supported
NiCo2S4 NS/CC Nanostructures
The XRD patterns of NiCo2S4 NS/CC, NiCo2S4 NN/CC, and NiCo2O4 NS/CC
are presented in Figure 2a. After oxidation reaction in the first step of the hydrothermal
process, nickel–cobalt carbonate hydroxide hydrate NS arrays
are uniformly formed on the CC, as shown in Figure S1 (ICDD 00-040-0216). During the sulfurization in the second
hydrothermal step, the nickel–cobalt carbonate hydroxide hydrate
phase is completely transformed into spinel nickel–cobalt sulfide
without destroying the original nanostructures. The diffraction peaks
of NiCo2S4 NS/CC and NiCo2S4 NN/CC at 16.2°, 26.7°, 31.4°, 38.1°, 50.3°,
and 55.1° are assigned to the (111), (220), (311), (400), (511),
and (440) planes of cubic-phase NiCo2S4, respectively
(ICDD 00-043-1477). The high-resolution TEM image in Figure 2b reveals the interplanar distance
of 0.28, 0.23, 0.16, 0.33, and 0.18 nm, corresponding to the (311),
(400), (440), (220), and (511) planes of NiCo2S4, respectively, confirming the successful formation of NiCo2S4. The formation of NiCo2S4 NS/CC
is confirmed based on the energy-dispersive X-ray (EDX) using TEM,
which shows that the atomic percentages of nickel, cobalt, and sulfur
are 15.2, 30.7, and 54.1 at. %, respectively, as shown in Figure S3. Note that the two characteristic peaks
at 26° and 43° for all prepared electrodes are attributed
to the CC (ICDD 01-074-2329). The diffraction peaks of the NiCo2O4 NS/CC catalyst obtained after the first step
in the hydrothermal process and heat treatment are consistent with
the standard pattern of NiCo2O4 (ICDD 01-073-1702).
Meanwhile, the NN-like morphology of NiCo2S4 NN/CC can be confirmed from the TEM elemental mapping images shown
in Figure S4.
Figure 2 (a) XRD patterns of NiCo2S4 NS/CC, NiCo2S4 NN/CC,
and NiCo2O4 NS/CC
catalysts. (b) High-resolution TEM images of NiCo2S4 NS/CC. High-resolution XPS deconvolution spectra of the NiCo2S4 NS/CC catalyst for (c) Ni 2p, (d) Co 2p, (e)
S 2p, and (f) C 1s.
To further characterize
the chemical composition of electrodes,
the XPS analysis is carried out, and results are given in Figure 2c–f. As shown
in Figure 2c, the Ni
2p spectrum consists of two spin–orbit doublets of Ni2+ and Ni3+, including Ni2+ at 853.8 eV for Ni
2p3/2 and 873.8 eV for Ni 2p1/2, and Ni3+ at 857.7 eV for Ni 2p3/2 and 875.6 eV for Ni
2p1/2.24,30,34,35 The XPS spectrum of Co 2p (Figure 2d) contains well-resolved peaks
of Co2+ 2p3/2, Co3+ 2p3/2, Co2+ 2p1/2, and Co3+ 2p1/2 at 798.8, 793.9, 783.0, and 778.9 eV, respectively, implying the
co-presence of Co2+ and Co3+ species in NiCo2S4 NS/CC.23,34 The S 2p XPS spectrum
(Figure 2e) shows two
peaks at 163.0 and 161.8 eV, which are assigned to metal–sulfur
bonds and the low coordination state sulfur ion that exists at the
surface of NiCo2S4 NS/CC, respectively, with
the satellite peak appearing at 170.1 eV in Figure 2e.34,35 The C 1s spectrum of
NiCo2S4 NS/CC is deconvoluted into four peaks
located at 284.8, 285.5, 287.0, and 291.3 eV, which correspond to
the C 1s orbital of C–C (sp2), C–C (sp),
C–O, and π–π interactions, respectively
(Figure 2f). The additional
π–π interaction indicates the strong interactions
between NiCo2S4 NSs arrays and the CC, which
can minimize contact resistance to generate a direct electron pathway.29 The binding energy values of Ni 2p, Co 2p, and
S 2p are matched well with the previous reports on NiCo2S4-based materials.
The OER catalytic activity of
NiCo2S4 NS/CC
was first evaluated with a three-electrode setup using a low scan
rate of 1 mV s–1 to eliminate the capacitive current
effects in alkaline solution (1 M KOH, pH = 14). For comparison, NiCo2S4 NN/CC, NiCo2O4 NS/CC,
bare CC, and RuO2/CC benchmarking OER catalysts were also
tested under the same condition. All the synthesized electrodes in
this work are directly used as free-standing oxygen-evolving electrodes,
including conventional RuO2/CC, to avoid possible influencing
factors. The LSV polarization curves and Tafel plots for all samples
are revealed, as shown in Figure 3a,b. The NiCo2S4 NS/CC exhibits
a superior catalytic activity toward OER with a low onset potential
of only 180 mV. Moreover, the overpotential of 260 mV is required
to generate 10 mA cm–2, which is smaller than that
of NiCo2S4 NN/CC (316 mV), NiCo2O4 NS/CC (368 mV), RuO2/CC (322 mV), and bare CC
(484 mV). Also, it requires only a 280 mV overpotential to afford
10 mA cm–2 when the scan rate is 5 mV s–1 (Figure S5). It is lower than those of
many other reported nonprecious metal-based OER electrocatalysts tested
under 1 M KOH conditions, such as NiCo2S4 NWs/graphdiyne
foam (300 mV), NiCo2S4/NF (306 mV)—, NiCo2S4 NAs/CC (310 mV), and so on.22−24,29,31,36−39 A detailed comparison is further
summarized in Table S1. The cyclic voltammograms
for NiCo2S4 NS/CC and NiCo2O4 NS/CC in the potential region from 1.0 to 1.8 V show a broad
peak at 1.36 and 1.22 V, indicating the redox behavior of Ni2+ and Ni3+, respectively (Figure S7). The catalytic kinetics of OER is evaluated by Tafel plots in alkaline
medium. The Tafel slope of NiCo2S4 NS/CC is
72 mV dec–1, which is lower than that of all other
electrodes, such as RuO2/CC (87 mV dec–1), NiCo2S4 NN/CC (84 mV dec–1), NiCo2O4 NS/CC (114 mV dec–1), and bare CC (178 mV dec–1), indicating a more
favorable rate of OER at the NiCo2S4 NS/CC electrode.
The favorable kinetics of OER on NiCo2S4 NS/CC
is also supported by EIS analysis to measure the charge transfer resistance
during OER (Figure S6). The charge transfer
resistance of NiCo2S4 NS/CC, which forms NSs
morphology is 8.94 Ω at 1.5 V versus RHE, smaller than that
of NiCo2S4 NN/CC with NN-like architectures
(16.3 Ω). In contrast, NiCo2O4 NS/CC shows
at least five times higher charge transfer resistance than that of
NiCo2S4 NS/CC and NiCo2S4 NN/CC under the same applied potential because of the lower electrical
conductivity of NiCo2O4 NS/CC.
Figure 3 OER in alkaline media
(1 M KOH, pH = 14): (a) LSV polarization
curves for OER and (b) Tafel plots of NiCo2S4 NS/CC, along with NiCo2S4 NN/CC, NiCo2O4 NS/CC, RuO2/CC, and CC electrodes
for comparison. (c) Cyclic voltammogram measured in a non-faradaic
region at various scan rates for the NiCo2S4 NS/CC electrode. The inset shows the plot of anodic and cathodic
charging current density vs different scan rates. (d) Current density
based on intrinsic catalytic activity vs voltage curves. (e) TOF and
the specific (intrinsic) activities of NiCo2S4 NS/CC, NiCo2S4 NN/CC, and NiCo2O4 NS/CC electrodes at η = 350 mV. (f) Time dependence
of the current density for NiCo2S4 NS/CC at
a fixed potential of 1.55 V for 162 h.
To better understand the different OER catalytic activities
of
NiCo2S4 NS/CC, including NiCo2S4 NN/CC and NiCo2O4 NS/CC catalysts,
the ECSA and roughness factor (RF) of all electrodes are determined
to estimate the real catalytic activities in the same pH condition.
It can be easily calculated based on the double-layer capacitance
(Cdl) through CV in a non-faradaic region
at different scan rates of 1, 2.5, 5, 10, 20, and 50 mV s–1 (Figure 3c). The
NiCo2S4 NS/CC electrode shows over twofold higher
ECSA value of 5.5 mF cm–2 than that of NiCo2S4 NN/CC (2.0 mF cm–2) and NiCo2O4 NS/CC (2.3 mF cm–2), respectively
(Figure S8). This indicates that plenty
of catalytically active sites for OER might form on NiCo2S4 NS/CC.
The surface roughness for all electrodes
was also calculated by
dividing the estimated ECSA to the geometric area of the electrode,
and the values of 27.5, 10, and 11.5 were achieved for each electrode,
NiCo2S4 NS/CC, NiCo2S4 NN/CC, and NiCo2O4 NS/CC, respectively. On
the basis of these results, 2D NS architecture arrays can offer larger
space and have a rougher surface; hence, they lead to more electrochemical
active sites on the catalyst surface. As a result, the excellent electrocatalytic
performances of the NiCo2S4 NS/CC electrode
can be partially ascribed to the high ECSA and consequently highly
exposed active sites.
We further calculate the TOF, which could
provide the intrinsic
OER catalytic activities of NiCo2S4 NS/CC, NiCo2S4 NN/CC, and NiCo2O4 NS/CC
electrodes. The TOF of various electrocatalysts was derived using
the following equation: J is the geometric current
density at a specific overpotential. A denotes the
geometric area of the electrode. The number of electrons consumed
for generating 1 mol of O2 from water is 4. F is the Faraday constant value of 96 485 C mol–1. m denotes the mole numbers of active materials.40 On the basis of this calculation, at an overpotential
of 350 mV, the TOF of NiCo2S4 NS/CC and NiCo2S4 NN/CC is calculated as 7.46 × 10–2 and 4.12 × 10–2 mol O2 s–1, respectively (Figure 3e). In sharp contrast, NiCo2O4 NS/CC has the
lowest TOF value of 1.19 × 10–2 s–1. Moreover, it is almost fourfold higher than that of the IrOx catalyst (0.89 × 10–2 s–1), indicating that the NiCo2S4 NS/CC is highly efficient toward OER.41
The specific activity of catalysts with different
surface areas
or loading is calculated with current normalization by the catalyst
RF. NiCo2S4 NS/CC can deliver a high specific
current density of 2.67 mA cm–2, whereas NiCo2O4 NS/CC can produce only 0.96 mA cm–2 at the same overpotential of 350 mV. Even though their morphology
appears to be similar, that is, the density and the distribution of
NiCo2S4 NSs on the CC are virtually the same
as those of NiCo2O4 NSs on CC, NiCo2S4 NS/CC outperforms NiCo2O4 NS/CC.
This result shows that NiCo2S4 NS arrays on
CC have a higher intrinsic OER catalytic activity than that of NiCo2O4 NS arrays on CC (Figure 3d), which can be explained by the difference
in the crystal structure of NiCo2S4 and NiCo2O4. NiCo2S4 that formed closely
packed arrays of large S2– anions with nickel and
cobalt metal cations in different oxidation states occupying the tetrahedral
and octahedral sites, respectively, possesses more octahedral active
sites of Co(III) concerning NiCo2O4, which has
smaller anions of O2– in the spinel structure.31,42 On the basis of the previous literature, σ* orbital (eg) occupation–related metal cations at octahedral sites
are mostly coordinated with electrocatalytic activities.43 In view of this point, NiCo2S4 NS/CC might afford better OER intrinsic activity compared
to NiCo2O4 NS/CC.
The electrocatalytic
activity toward the OER of NiCo2S4 NS/CC is
also evaluated in PBS (pH = 7) as well as
control samples as shown in Figure 4a. Similar to the OER activity trend in alkaline media,
the NiCo2S4 NS/CC catalyst exhibits the highest
OER performance compared with other electrodes. Surprisingly, NiCo2S4 NS/CC requires only 321 and 402 mV to afford
5 and 10 mA cm2, respectively. However, RuO2/CC as a state-of-the-art OER catalyst needs an extremely large overpotential
of 700 mV to deliver 5 mA cm–2 current density.
At the same time, NiCo2S4 NN/CC and NiCo2O4 NS/CC require at least 368 and 460 mV to produce
5 mA cm–2, respectively. Bare CC shows negligible
OER performance. The catalytic activity of NiCo2S4 NS/CC for OER in neutral media is exceptional compared to that of
many electrodes reported recently, such as CoS4.6O0.6 (η = 570 mV for 5 mA cm–2),19 ultrathin Co3S4 NS (η
= 650 mV for 3.27 mA cm–2),40 Co3O4 nanorod (η = 385 mV for 1 mA cm–2),44 Co-Pi NA/Ti foam (η
= 450 mV for 10 mA cm–2),15 Co–Bi NSs/graphene (η = 570 mV for 14.4 mA cm–2),18 and Fe–Ni–P (η
= 429 mV for 10 mA cm–2).14 The detailed comparison is summarized in Table S2. Figure 4b shows the Tafel plots of all electrodes for a better understanding
of the obtained catalytic behavior. The Tafel slope of 123 mV dec–1 in a neutral electrolyte for NiCo2S4 NS/CC is achieved. It is the smallest value among NiCo2S4 NN/CC (125 mV dec–1) and NiCo2O4 NS/CC (203 mV dec–1) and comparable
to that of RuO2/CC (115 mV dec–1), which
in turn favors the kinetics of OER. Notably, in comparison with NiCo2O4 NS/CC, the NiCo2S4 NS/CC
catalyst presents a lower Tafel slope value, originating from the
increase in electrical conductivity as well as more plentiful electrocatalytic
active sites correlated with its intrinsic activities.
Figure 4 OER in neutral media
(phosphate buffer, pH = 7): (a) LSV polarization
curves for OER. (b) Corresponding Tafel plots of NiCo2S4 NS/CC, along with NiCo2S4 NN/CC, NiCo2O4 NS/CC, RuO2/CC, and CC electrodes
for comparison. (c) Cyclic voltammogram measured in a non-faradaic
region at various scan rates for the NiCo2S4 NS/CC electrode. (d) Anodic and cathodic current density vs scan
rate plot of NiCo2S4 NS/CC. (e) Mass activities
and TOF of NiCo2S4 NS/CC, NiCo2S4 NN/CC, and NiCo2O4 NS/CC electrodes
in PBS. (f) Time dependence of the current density for NiCo2S4 NS/CC at a fixed potential of 1.6 V for 11 h.
We further measure the double-layer
charging of electrodes via
scan-rate-dependent CVs to estimate the effective surface areas for
catalytic activity. The potential range in which the non-faradaic
region was chosen with the potential window of 0.04 V centered at
an open-circuit voltage (OCV) of each system.34 The electrochemical double-layer capacitance for NiCo2S4 NS/CC is 0.044 mF cm–2, whereas those
for NiCo2S4 NN/CC and NiCo2O4 NS/CC are 0.025 and 0.023 mF cm–2, respectively,
indicating the rougher surface of the NiCo2S4 NS/CC electrode. It is noticeable that NiCo2S4 NS/CC still possesses almost twofold higher electrochemical double-layer
capacitance than NiCo2O4 NS/CC in neutral media,
which is probably because of the well-aligned hierarchical NSs architecture
and the formation of numerous electrochemically active sites. The
TOF at the overpotential of 400 mV in neutral media is evaluated to
compare the intrinsic activities of NiCo2S4 NS/CC
with those of other comparison electrodes. The calculated TOF for
NiCo2S4 NS/CC is 9.89 × 10–3 s–1, which is much larger than those for previously
reported cobalt-based catalysts, including Co3S4 (1.32 × 10–3 s–1 at η
= 500 mV),40 Co–Pi (∼2 ×
10–3 s–1 at η = 410 mV),45 Co–Bi (1.5 × 10–3 s–1 at η = 400 mV),46 and Co3O4 (≥0.8 × 10–3 s–1 at η = 414 mV),40 further suggesting the remarkable OER catalytic activity of NiCo2S4 NS/CC under neutral conditions. The NiCo2S4 NN/CC for which NiCo2S4 NN arrays are grown on CC indicates a TOF of 4.83 × 10–3 s–1, implying its lower intrinsic
activities compared with that of the NiCo2S4 NS/CC electrode, whereas the TOF of NiCo2O4 NN/CC is calculated as 2.47 × 10–3 s–1, which shows the lowest value among the three electrodes.
Therefore, the remarkable electrocatalytic activity of NiCo2S4 NS/CC can partially originate from the higher electrochemical
surface area and the direct contact between NiCo2S4 NS arrays and the CC, which facilitate fast electron transfer
as well as enhanced mass transportation. In addition, (i) the intrinsic
electrocatalytic activity of the NiCo2S4 with
larger anions compared with NiCo2O4 so as to
expose more cation active sites; (ii) the enough void space among
interconnected NiCo2S4 NSs, which allows facile
redox ion diffusion; (iii) the 2D morphology of NiCo2S4 NSs that yields a large contact area between the catalyst
and the electrolyte; and (iv) the formation of the nickel–cobalt
(oxy)hydroxide active layer on its surface, which will be discussed
later, all contributed to the superb performance of NiCo2S4 NS/CC in the OER.
The long-term operation of
the OER catalyst is a critical issue
for practical application. Figure 3f exhibits the chronoamperometric (CA) curve of the
NiCo2S4 NS/CC measured at 1.55 V potential in
alkaline media (1 M KOH). After the 29 h CA test, the electrode entirely
stabilizes and retains a current density of 10 mA cm–2 (without iR corrected) and then is reduced to 85%
of its original activity over 160 h long-term operation. The inset
of Figure 3f shows
the linear polarization curves of NiCo2S4 NS/CC
before and after 1000 CV cycles with 50 mV s–1 scan
rate and a potential range from 1.2 to 1.7 V. Accordingly, there is
no difference in the LSV curve recorded after 1000 CV cycles, indicating
its high stability. Meanwhile, we detected losses of larger than 24,
29, and 47% in their current densities within 50 h for NiCo2S4 NN/CC, NiCo2O4 NS/CC, and RuO2/CC, respectively, at the same potential of 1.55 V in 1 M
KOH solution. We also performed the durability test for same electrodes
under the neutral condition. NiCo2S4 NS/CC presents
excellent durability for 11 h, achieving 6 mA cm–2 at 1.6 V versus RHE with only 10% loss. During CA, O2 gas bubbles were visibly observed from the NiCo2S4 NS/CC electrode and dissipated quickly into the electrolyte.
The NiCo2S4 NN/CC and NiCo2O4 NS/CC electrodes show a dramatic catalytic activity loss
of 45 and 54%, respectively. Moreover, RuO2/CC almost lost
its catalytic activity after 4 h durability test. The morphological
robustness of NiCo2S4 NS/CC was examined by
post-OER FE-SEM analysis under alkaline and neutral conditions (Figure S12). Maintaining morphology with negligible
damage is another convincing evidence of the structural robustness
of NiCo2S4 NS/CC observed in the FE-SEM micrographs.
Recently, Li et al.46 reported that
the nonoxide transition metal-based chalcogenides, especially cobalt
selenide catalysts, usually oxidize during the OER under the basic
condition and progressively transform to the corresponding TM (oxy)hydroxides,
which is proposed to be the true active species to catalyze the OER.47 In the case of the Co3Se4/CF electrode, the XPS peak intensity of Se virtually disappears
after a 3 h chronopotentiometric electrolysis duration, and after
12 h, Co3Se4 is converted to CoOOH. Similarly,
in our study, we investigated the composition of the electrode after
160 h CA operation by XPS (Figure S11)
to confirm the real surface species of NiCo2S4 NS/CC. The XPS Ni 2p shows that Ni2+ at 853.8 eV for
Ni 2p3/2 and 873.8 eV for Ni 2p1/2 visibly disappears
and the peaks located at 855.7 and 873.2 eV are assigned to Ni3+ species of the nickel (oxy)hydroxide.31,48 Moreover, the binding energy shift of Ni 2p for 1.4 eV reveals the
occurrence of electron transfer during extended CA electrolysis. Similarly,
the XPS Co 2p3/2 peak is deconvoluted into two peaks of
780.7 and 782.3 eV, which represent the formation of Co(OH)2 and CoOOH, implying the formation of a higher valence state of cobalt
(Co3+).49,50 Meanwhile, the peak intensity
of S 2p was weakened, whereas the two strong peaks of O 1s spectra
were observed at 531.3 and 532.7 eV, indicating the O–H bond
in NiCoOOH and the adsorption of H2O on the surface of
NiCo2S4 NS/CC, respectively.48−50 The XPS results
demonstrate that in situ electrochemical tuning of nickel–cobalt
sulfide to nickel–cobalt mixed (oxy)hydroxide phase occurred,
which is highly active for the OER catalytic activity attributed to
the enhanced surface area and electrochemically active sites. This
transformation might change the electronic states and the interactions
with intermediate products during OER. Hence, it leads to the catalyst
becoming more catalytic active for OER, which is also shown in other
chalcogenide materials.46,50
The post-OER
durability measurement for over 11 h in the neutral
medium was also carried out using XPS analysis to confirm the chemical
composition (Figure S12). Similarly, in
an alkaline environment, the Ni2+ peak disappeared from
the surface of catalyzed NiCo2S4 NS/CC and transformed
to Ni3+ of TM (oxy)hydroxides with binding energy values
at 855.7 and 873.2 eV as well as satellite peaks at 865.1 and 879.9
eV. Also, the new peaks formed at 779.9 and 781.1 eV are also assigned
to the (oxy)hydroxides phase.47−50 It is noticeable that similar phenomena of in situ
electrochemical tuning for NiCo2S4 NS/CC have
occurred under a neutral condition, achieving an increase in the surface
area as well as electrochemically active sites for primarily improved
catalytic activity for OER.
To validate the practical application
of the NiCo2S4 NS/CC catalyst, a primary zinc–air
battery was demonstrated
and fully discharged to 0.6 V at a current density of 5 mA cm–2 (Figure 5a). The NiCo2S4 NS/CC cathode shows
an OCV of 1.18 V with a specific capacity of 722 mA h g–1, which is almost 88.1% utilization of theoretical capacity (∼820
mA h g–1), whereas the commercial catalyst-based
cathode shows an OCV of 1.31 V with a discharge capacity of 590 mA
h g–1. Moreover, the galvanostatic discharge–charge
cycling performance was evaluated at a current density of 5 mA cm–2 with a 5 min discharge followed by 5 min charge for
each cycle (Figure 5b). For the initial cycle of NiCo2S4 NS/CC,
the rechargeable battery discharged at 1.11 V versus Zn, with the
corresponding charging potential of 1.90 V giving an overall overpotential
of 0.79 V, which increased only 0.04 V (1.95 V for charge and 1.12
V for discharge potential) after 30 h battery operation (173 cycles).
However, in the case of RuO2 + Pt/C/CC, the potential gap
between charge and discharge increased continuously from 0.61 to 1.00
V even after 1350 min (135 cycles) cycling. The superior cycling durability
over 173 cycles with a high discharge capacity of 722 mA h g–1 indicates the excellent electrocatalytic activity and stability
of NiCo2S4 NS/CC for zinc–air batteries.
Figure 5 Zn–air
battery performance: (a) specific discharge capacities
of primary zinc–air batteries with NiCo2S4 NS/CC and commercial RuO2 + Pt/C/CC air cathodes. (b)
Comparative galvanostatic charge–discharge profiles of rechargeable
zinc–air batteries based on NiCo2S4 NS/CC
and RuO2 + Pt/C/CC air cathodes at 5 mA cm–2 in 10 min interval cycles.
A two-electrode alkaline water electrolyzer was developed
for full
water splitting with NiCo2S4 NS/CC and Pt/C/CC
as the anode and cathode, respectively, in 1 M KOH solution (Figure 6). To achieve a current
density of 10 mA cm–2, a voltage of 1.53 V was needed
for water splitting with gas evolution on both electrode surfaces,
showing more advantages to split water than precious metal-based electrodes,
which requires higher cell voltages of 1.64 V.
Figure 6 Overall water electrolysis:
the polarization curves based on NiCo2S4/CC//PtC/CC
and commercial RuO2/CC//Pt/C/CC
electrodes with a scan rate of 5 mV s–1 in 1 M KOH
solution. The inset is the photograph of the two-electrode configuration.
Conclusions
In summary, the hierarchical
spinel bimetallic sulfide nanostructures
in situ grown on the CC were investigated for their electrochemical
properties in different pH media and evaluated for their capability
in practical primary and rechargeable zinc–air batteries. The
most active NiCo2S4 NS/CC electrode can catalyze
the OER at an overpotential of 260 mV at 10 mA cm–2 with good durability of over 160 h operations under an alkaline
condition. Moreover, the NiCo2S4 NS/CC electrode
still maintained its superior OER catalytic activity under the neutral
condition. The enhanced intrinsic catalytic properties, morphology-based
advantages of nanostructures, and the generation of the Ni–Co
oxyhydroxide active layer were considered responsible for the excellent
OER performance in water splitting. Especially, the in situ fabricated
NiCo2S4 NS/CC-integrated air cathode exhibits
excellent durability and electrocatalytic activity in zinc–air
batteries compared with the precious metal-based catalyst. This work
supports a snapshot of the rational design and construction of nonprecious
electrode materials with excellent catalytic activity and durability
for the future practical system toward OER in water electrolyzers
and zinc–air batteries.
Supporting Information Available
The Supporting Information is
available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b01375.Experimental section;
XRD patterns; FE-SEM images; TEM
EDX pattern and mapping images; LSV curves; EIS spectra; CV curves
measured in the OER region; CV curves and their corresponding charging
current density versus different scan rates; postmortem FE-SEM and
XPS analysis; and comparison of OER performance with the recently
reported literature (PDF)
Supplementary Material
ao8b01375_si_001.pdf
The authors
declare no competing financial interest.
Acknowledgments
This work was supported by the DGIST R&D Program
of the Ministry of Science, ICT and Future Planning of Korea (18-IT-02),
the Korea Institute of Energy Technology Evaluation and Planning (KETEP),
and the Ministry of Trade, Industry & Energy (MOTIE) of the Republic
of Korea (no. 20174030201590). Additionally, we thank the DGIST-Center
for Core Research Facilities (CCRF) for providing various facilities
for sample analysis.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145783210.1021/acsomega.7b01051ArticleFree-Standing Sandwich-Structured Flexible Film Electrode
Composed of Na2Ti3O7 Nanowires@CNT
and Reduced Graphene Oxide for Advanced Sodium-Ion Batteries Li Zhihong †Ye Shaocheng †Wang Wei †Xu Qunjie †Liu Haimei *†Wang Yonggang *‡Xia Yongyao ‡† Shanghai
Key Laboratory of Materials Protection and Advanced Materials in Electric
Power, College of Environmental and Chemical Engineering, Shanghai University of Electric Power, Shanghai 200090, China‡ Department
of Chemistry and Shanghai Key Laboratory of Molecular Catalysis and
Innovative Materials, Institute of New Energy, Fudan University, Shanghai 200433, China* E-mail: liuhm@shiep.edu.cn. Tel: +86 021 35303476 (H.L.).* E-mail: ygwang@fudan.edu.cn. Tel: +86 021 51630319 (Y.W.).12 09 2017 30 09 2017 2 9 5726 5736 26 07 2017 17 08 2017 Copyright © 2017 American Chemical
Society2017American Chemical
SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
A free-standing flexible anode material
for sodium storage with
sandwich-structured characteristics was fabricated by modified vacuum
filtration, consisting of stacked layers of Na2Ti3O7 nanowires@carbon nanotubes (NTO NW@CNT) and graphene
oxide. The NTO NWs have a larger specific surface area for Na+ insertion/extraction with shortened ion diffusion pathways,
accelerating the charge transfer/collection kinetics. The added CNTs
both facilitate the uniform dispersion of the nanowires and nanotubes
and also contribute to the connectivity of the nanowires, improving
their conductivity. More importantly, the unique sandwichlike layered-structured
film not only provides large numbers of electron-transfer channels
and promotes the reaction kinetics during the charging and discharging
process but also ensures the structural stability of the NTO NWs and
the electrode. Electrochemical measurements suggest that this rationally
designed structure endows the electrode with a high specific capacity
and excellent cycling performance. A satisfactory reversible capacity
as high as 92.5 mA h g–1 was achieved after 100
cycles at 2C; subsequently, the electrode also delivered 59.9 mA h
g–1 after a further 100 cycles at 5C. Furthermore,
after the rate performance test, the electrode could be continuously
cycled for 100 cycles at a current density of 0.2C, which demonstrated
that durable cyclic capacity with a high reversible capacity of 114.1
mA h g–1 was retained. This novel and low-cost fabrication
procedure is readily scalable and provides a promising avenue for
potential industrial applications.
document-id-old-9ao7b01051document-id-new-14ao-2017-01051fccc-price
==== Body
Introduction
In modern society,
portable and wearable electronics, such as flexible
sensors and hand-held displays, are highly desired, which has motivated
research into the necessary lightweight and flexible high-performance
power sources.1−3 At present, the study of flexible power sources is
mainly focused on lithium-ion batteries (LIBs)4−6 and supercapacitors
(SCs). In the energy-storage field, great attention has been focused
on flexible SCs because of their convenient processability, fast charging
and discharging ability, excellent rate capability, and their superior
cycle lifetime.7−9 However, the energy density of SCs is not very high
considering the need for long-term resilience, and thus flexible LIBs
perhaps hold greater promise for smart electronics, rollup displays,
wearable devices, and other applications.10−12 Flexible LIBs
are of particular interest due to their higher energy storage densities.
However, at present, with the commercialization of electric vehicles
powered by LIBs, the limited availability of lithium storage will
progressively increase its cost. As a result, low-cost sodium ion
batteries (SIBs) have become a very popular topic in the research
field of energy storage and conversion devices.
Sodium ion batteries
have attracted interesting attention because
they have similar electrochemical properties to LIBs in addition to
their low cost and environmental friendliness.13,14 However, flexible SIBs are still rarely reported at present. It
is well-known that characteristics of batteries, such as flexibility,
specific capacity, and rate capability, are mainly determined by their
electrode materials.15 Therefore, it is
highly desirable to search for suitable electrode materials with appropriate
flexibility for use in SIBs. Actually, some endeavors have been made
to study flexible electrode materials for flexible SIBs, such as MoS2,16,17 Sb,18 and Li4Ti5O12.19 Among the various anode materials, Na2Ti3O7 (NTO) has been most promising on account of its high specific
capacity (177 mA h g–1) and its low charging/discharging
voltage plateau of 0.3 V versus Na/Na+.20 Nevertheless, the structural instability and the low electronic
conductivity of Na2Ti3O7 limit its
further practical application. To solve these problems, lots of efforts
have been made to design and fabricate Na2Ti3O7 nanostructures, including nanorods, nanoparticles,
microspheres, nanotubes, and nanocomposites with carbon.21−26 However, the design and fabrication of reliable flexible electrodes
with high storage capacity, high rate capability, and excellent stability
remain challenging.
For the fabrication of SIB electrodes, conventional
methods usually
involve mixing, casting, and pressing the mixed compounds. These compounds
comprise a cathode or an anode material for sodium storage, the metal
current collectors, a conductive agent to maintain the electrode conductivity
onto the metal current collectors, and a binder to inhibit the shedding
of the active materials from metal current collectors.27−29 Such electrodes usually have little flexibility due to their rigid
structure. Moreover, they contain a significant amount of inert components
(e.g., binders) and cumbersome current collectors are used in the
electrodes, inevitably compromising the energy density of the devices.
Lightweight flexible substrates, such as textiles30 or plastics,31 have been proposed
as replacements for metal substrates. To address sluggish Na reaction
kinetics, Li et al. first designed the surface-engineered Na2Ti3O7 nanoarrays on flexible Ti substrates
by using the atomic layer deposition and hydrogenation process, through
which the Na-ion batteries demonstrated the high-rate and long-cycled
operation.32,33 Zhang et al. reported that NTO
nanosheet array/carbon textiles exhibited excellent performance when
used as the anode materials of sodium-ion pseudocapacitors.34 Our previous work also showed that ultralong
NTO nanowires@carbon cloth as a binder-free flexible electrode demonstrated
a large capacity and long lifetime for sodium-ion batteries.35 However, the preparation of these flexible electrodes
usually requires a substrate, such as carbon cloth, carbon paper,
etc., and they are difficult to develop for large-scale production.
In addition, the loading mass of the active material in these flexible
electrodes is limited and difficult to control.
Herein, by introducing
an architectural design strategy, a hybrid
free-standing and sandwich-structured electrode was developed, which
is a combination of one-dimensional nanowires together with nanotubes
and two-dimensional graphene sheets in hierarchically structured composites.
In this work, we demonstrate a simple method of hydrothermal-assisted
vacuum filtration to prepare Na2Ti3O7 nanowires@CNT@reduced graphene oxide (NTO NW@CNT@rGO) sandwich-structured
flexible film electrodes for flexible SIBs for the first time. The
unique sandwich-structured NTO NW@CNT@rGO flexible electrode materials
were prepared by layer-by-layer vacuum filtration. This not only affords
stability and robustness in the electrodes but also facilitates the
diffusion of the electrolyte and improves their electrical conductivity,
thus enhancing the electrochemical properties of Na2Ti3O7. In addition, this method is suitable for large-scale
production due to the low cost of the raw materials and the fact that
the amount of active material can be modulated at will.
Results and Discussion
The free-standing and sandwich-structured flexible NTO NW@CNT@rGO
film electrode was prepared using a two-step fabrication method. First,
NTO NW@CNT was synthesized by a hydrothermal method. In the hydrothermal
process, the carbon nanotubes are combined with Na2Ti3O7 nanowires and can be used as bridges between
nanowires to improve the conductivity of the nanowires. NTO NW@CNT@rGO
flexible electrode materials with a sandwich structure were then prepared
via layer-by-layer vacuum filtration (Figure 1). The graphene therein has a large specific
surface area and good electrical conductivity. The NTO NW@CNT layer
is sandwiched between graphene layers during the process of vacuum
filtration. On the one hand, this method is beneficial as it increases
the contact area between nanowires and graphene and improves the electrical
conductivity of the material. On the other hand, it can improve the
infiltration of the electrolyte and increase the ion conductivity
of the electrode material, thereby improving the electrochemical properties
of Na2Ti3O7.
Figure 1 (a–c) Schematic
illustration and ideal electron-transfer
pathway of a free-standing and sandwich-structured flexible film electrode.
Meanwhile, the great flexibility
of the film can be clearly observed
in Figure 2a. The as-prepared
electrodes can remain stable while being folded, which show great
potential for use in highly flexible devices. To investigate the morphological
and structural characteristics of the film, scanning electron microscopy
(SEM) was employed. SEM images showing cross-sectional and top views
of the S–NTO NW@CNT@rGO film are presented in Figure 2b–e. Figure 2b,c shows cross-sectional SEM
images of the as-formed S–NTO NW@CNT@rGO film and the corresponding
EDX mapping. As can be seen from Figure 2b, the thickness of the film is about 20
μm and the structure of the cross section is clearly considered
as a layer-by-layer structure. Energy-dispersive X-ray (EDX) spectrometry
mapping analysis was further employed for one layer of the film, and
the results are shown in Figure 2c. The main elements of this layer are C (red), O (green),
Na (cyan), and Ti (pink) and are shown in Figure 2c. C refers to the graphene on the upper
surface and is evenly distributed. The shallow red color indicates
that the graphene layer is relatively thin. Na, Ti, and O are the
main elements of NTO and are evenly distributed. The color of the
elements is deep, indicating that NTO is the main constituent of this
layer. The structure of each layer is similar to the sandwich structure,
which is consistent with the effect we expect to achieve by layered
titration and filtration. Subsequently, the upper surface of the film
was observed and is shown in Figure 2d,e. The top-view SEM image reveals that the thin graphene
layer is uniformly distributed on the upper surface of the film on
a large scale and through the graphene layer, interdigitated NTO nanowires
can be clearly seen. At a greater magnification shown in Figure 2e, the graphene layer
is indeed observed, and NTO NW@CNT composites exist under the graphene
layer. Thus, it can be seen that in the as-formed S–NTO NW@CNT@rGO
film, the CNT of the NTO NW@CNT layer serves mainly to increase the
connections between nanowires, thus extending the pathway of electron
transfer of the NTO nanowires. The upper and lower graphene layers
serve mainly to increase the contact area with the NTO nanowires and
improve the electrical conductivity of the crossed nanowires.
Figure 2 (a) Digital
optical image of the bending state of the NTO NW@CNT@rGO
film; (b, c) SEM images of the cross section and corresponding EDX
mapping of C (red), O (green), Na (cyan), and Ti (pink); and (d, e)
SEM images of the upper surface.
In addition, in Figure 2b, we also see that there is a certain gap between
the layers
in the as-formed S–NTO NW@CNT@rGO film, which can facilitate
the penetration of the electrolyte. But how did these gaps form? To
illustrate the problem, the graphene film and the NTO NW@CNT film
were prepared by the same process and then observed and analyzed by
SEM. Figure S1 shows the SEM images of
NTO NW@CNT. It can be seen in Figure S1a that NTO nanowires with the large aspect ratio are very uniform
on the upper surface of the film. The distributions of NTO nanowires
and CNT are also uniform. It is regrettable that after vacuum filtration
the NTO NW@CNT film does not form a multilayer structure that could
be seen in the cross section. However, multilayer graphene is clearly
observed in the cross section of the film after vacuum filtration,
as shown in Figure S2b, which means that
the formation of the multilayered S–NTO NW@CNT@rGO film may
be related to the graphene itself. After filtration, graphene oxides
are formed in the film and then undergo a high-temperature process
where some of the oxygen-containing functional groups between the
layers become vaporized oxygen, leading to the emergence of a gap
between the layers, as shown in Figure S2. Therefore, the gaps in the as-prepared sandwich-structured film
containing the graphene oxide occur due to the volatilization of oxygen
after the high-temperature treatment. It is precisely because the
film prepared by our method exhibits a certain gap that the film both
improves the electrical conduction of the electrode and facilitates
the penetration of the electrolyte.
To further understand the
structure of the S–NTO NW@CNT@rGO
film electrode, transmission electron microcopy (TEM) was applied
to observe the Na2Ti3O7 nanowires,
CNT, and rGO of the film. As shown in Figure 3a,b, the interdigitated long NTO nanowires,
including several hundred nanometers or even up to several micrometers
in length, form a three-dimensional (3D) network structure, resulting
in lots of porous structures. As we all know, these porous structures
of the electrode materials likely facilitate the penetration of the
electrolyte and also promote sufficient contact between the NTO nanowires
and the electrolyte, providing shortened ionic diffusion pathways
that may contribute to the improvement of the electrochemical performance
in sodium storage. At the same time, it is clear that the distribution
of the homogeneous NTO nanowires and the CNT is very uniform. CNT
wrapped around the NTO nanowires increases the connectivity between
the nanowires and improves their electrical conductivity. In Figure 3b, the graphene above
the NTO nanowires and CNT can be seen to completely cover the nanowires
having a large contact area with nanowires that greatly improves the
conductivity of the nanowires. Figure 3c shows an HRTEM image of the NTO nanowires. The lattice
fringes show interplanar spacings of 0.84 and 0.35 nm, corresponding
to the distances of the (001) and (102) lattice planes in the NTO
structure. The figure also shows that the NTO nanowires have good
crystallinity, which is beneficial to the electrochemical performance
of NTO. The colored diagrams in Figure 3d show the EDX mapping of NTO nanowires. It can be
seen that the distribution of Na (cyan), O (green), and Ti (red) comprising
Na2Ti3O7 is consistent with the orientation
of the nanowires, indicating that the nanowires are made of sodium
trititanate.
Figure 3 (a, b) Low-magnification TEM images of the NTO NW@CNT@rGO
film;
(c) HRTEM image; and (d) TEM and corresponding EDX mapping of Na (cyan),
O (green), and Ti (red).
To quantify the amount of NTO and carbon in the flexible
film,
TGA was carried out in air. The sample was heated from 25 to 800 °C
at a rate of 10 °C min–1. Figure 4a shows the TGA curve of the
S–NTO@CNT@rGO film. The weight loss of the sample is about
16.3%, indicating that the carbon content of the film is about 16.3%,
in line with the requirements for the carbon content of a flexible
film material. In contrast, the NTO nanowires comprise approximately
83.6% of the mass and are the main component of the film. This shows
that the as-prepared film has a certain flexibility, the key being
that the nanowires themselves are also easily prepared as part of
a flexible film. To gain further knowledge of the crystallographic
phase and structure of the different samples, X-ray diffraction (XRD)
tests were performed. As can be seen in Figure 4b, all of the diffraction peaks of NTO NW@CNT
powder correspond to those of layered Na2Ti3O7 (JCPDS card no. 31-1329). In addition, for the as-prepared
NTO NW@CNT@GO film and the NTO NW@CNT@rGO film, the sharp and well-defined
peaks correspond to those of Na2Ti3O7 according to the standard PDF card data. However, compared to that
of the NTO NW@CNT sample, the intensity of the diffraction peak of
NTO NW@CNT@GO becomes stronger at 10.5° and weaker near 25 and
30°. The reason for this phenomenon is that graphene oxide has
a strong diffraction peak at 10.5°, as shown in Figure 4c.36 The diffraction peaks of Na2Ti3O7 and graphene oxide are superimposed at 10.5° so that the intensity
of the diffraction peak is enhanced, whereas those at 25 and 30°
are weakened. After high-temperature treatment, graphene oxide is
reduced to graphene (Figure 4c) and the intensity of the diffraction peak of the S–NTO
NW@CNT@rGO film becomes weaker at 10.5°, consistent with that
of NTO NW@CNT powder. Figure 4d displays the Raman scattering spectra of the rGO film and
the S–NTO NW@CNT@rGO film. Two distinctive characteristic carbon
bands between 1200 and 1700 cm–1 can be observed.
The asymmetrical shape of the carbon characteristic bands implies
the existence of two types of bonding states of carbon.37 The Raman scattering spectra near 1300 and 1600
cm–1 are the characteristic bands of the C-atom
crystals corresponding to the disorder-induced phonon mode (D band)
and the graphite band (G band) of the sp2 carbon, which
represents the lattice defect of the carbon atom and the in-plane
stretching vibration of the sp2 hybrid of the carbon atom,
respectively.38,39
Figure 4 (a) TGA of the NTO NW@CNT@rGO film; (b)
XRD patterns of various
samples; (c) XRD of GO and rGO; (d) Raman spectra of rGO and NTO NW@CNT@rGO
film.
To quantify the excellent electrochemical
performance of the free-standing
sandwich-structured film prepared by vacuum filtration, the electrochemical
sodium storage characteristics of the flexible S–NTO NW@CNT@rGO
film were evaluated by assembling an appropriate mass of the material
in a Na-haft cell. The electrical energy storage capability of the
film electrode was first examined using cyclic voltammograms (CVs). Figure 5a shows the CV curve
at a scanning rate of 0.02 mV s–1 in the potential
range between 2.5 and 0.01 V versus Na/Na+. A couple of
redox peaks located at 0.25 V (cathodic peak) and 0.63 V (anodic peak)
versus Na/Na+ can be observed, representing typical Na+ insertion/extraction in the Na2Ti3O7 crystal lattice. The distinct and well-defined redox peaks
of Na2Ti3O7 indicate its excellent
kinetics performance in the S–NTO NW@CNT@rGO film electrode.
Moreover, the CV of the S–NTO NW@CNT@rGO electrode in a voltage
window of 0.01–2.5 V at various sweep rates ranging from 0.01
to 0.1 mV s–1 is presented in Figure S3. The redox peaks in the potential range of about
0.2–0.6 V in the CV data could be attributed to the redox of
the Ti4+/Ti3+ couple. With increasing cycles
and increasing scanning rates, the peak current and the voltage of
the electrodes increased continuously, which is consistent with the
characteristics of the electrode material itself, indicating the great
stability of the as-prepared electrode materials and the good reversibility
of the de/intercalation of sodium ions. The charge/discharge curves
of S–NTO NW@CNT@rGO were calculated at 1C in the voltage range
0.01–2.5 V for 1st, 10th, 20th, 50th, 70th, and 100th cycles,
as shown in Figure 5b. The initial discharge and charge capacities of the S–NTO
NW@CNT@rGO film were 372.2 and 184.4 mA h g–1, respectively,
which are higher than the theoretical capacity of 177 mA h g–1. Similar phenomena have been observed from self-assembled TiO2–graphene hybrid nanostructures40 and graphene-wrapped porous Li4Ti5O12 nanofiber composites.41 The higher capacity suggests additional interfacial Na storage at
the NTO/electrolyte (solid–liquid) and NTO/graphene (solid–solid)
interfaces. The interfacial reaction between the electrode and the
electrolyte led to the formation of a solid electrolyte interphase
(SEI) film, causing a large irreversible capacity loss. In addition,
the electrode displays sloped reaction plateaus located at 0.6 V (charge)
and 0.2 V (discharge), in keeping with the CV curves (Figure 5a) and showing the typical
charge/discharge profiles of the Na2Ti3O7 electrode in SIBs.26,34
Figure 5 Electrochemical measurements
of the as-formed NTO NW@CNT@rGO electrode
in a range of 0.01–2.5 V. (a) Cyclic voltammograms at a scan
rate of 0.02 mV s–1; (b) charge–discharge
curves at different cycles; and (c–f) cycling performance at
current densities of 0.5C, 1C, 2C, and 5C.
To investigate the cycling stability of the film electrodes,
a
cycling performance test was performed at different current densities. Figure 5c–f shows
the cycling performance of the S–NTO NW@CNT@rGO film when the
current densities were 0.5C, 1C, 2C, and 5C, respectively. As can
be seen from Figure 5c–e, the film electrodes show good discharge specific capacity
and Coulombic efficiency. At lower current densities 0.5C, 1C, and
2C, S–NTO NW@CNT@rGO delivers a high initial discharge capacity,
and capacities of 419, 372.2, and 380.5 mA h g–1 can be respectively achieved. Remarkably, after 100 cycles, the
electrode retains high capacities of 107.2, 101, and 97.9 mA h g–1, respectively, which confirms the excellent properties
of Na storage capacity and cycling stability. For the NTO@CNT film
electrode, its initial discharge capacity is only 141.7 mA h g–1, and after 70 cycles, a capacity of 34.2 mA h g–1 is retained, as shown in Figure S4. Similarly, the cycling performance of the NTO@CNT+rGO film
electrode is also very poor. As shown in Figure S5, the NTO@CNT+rGO electrode delivers only 65.3 and 26.5 mA
h g–1 at 0.5C and 1C, respectively, after 100 cycles.
On the other hand, the most impressive observation is that the S–NTO
NW@CNT@rGO electrode still retained a discharge capacity of 80.6 mA
h g–1 after 150 cycles at the highest current density
of 5C, which is a relatively high discharge capacity when Na2Ti3O7 is presently used as the anode material
of SIBs under the same conditions.23,24,42
To further explore the effectiveness of the
sandwich-structured
film in improving the electrochemical performance of Na2Ti3O7 electrodes, the long-term cycling performance
and the rate capability were investigated, as shown in Figure 6. In Figure 6a, the S–NTO NW@CNT@rGO film electrode
starts at 363.8 mA h g–1 and maintains at 105.7
mA h g–1 after initial precycling. From 11 cycles,
the discharge capacity has remained in a stable range at 2C, and it
is satisfactory that a reversible capacity as high as 92.5 mA h g–1 is still achieved after 100 cycles. Subsequently,
the S–NTO NW@CNT@rGO electrode also delivers 59.9 mA h g–1 after a further 100 cycles at 5C. This experiment
fully demonstrates that the as-prepared S–NTO NW@CNT@rGO electrode
possesses better capacity retention and longer lifetime. Figure 6b shows the rate
capabilities of S–NTO NW@CNT@rGO at various current densities.
For each stage, the process was taken from 0.2C to 10C over five cycles.
Compared with the S–NTO NW@CNT+rGO electrode (Figure S6), the S–NTO NW@CNT@rGO electrode delivers
discharge capacities of 204.8, 162, 115.5, 86.5, 56, and 31.9 mA h
g–1 at current densities of 0.2C, 0.5C, 1C, 2C,
5C, and 10C, respectively. When cycled back to 5C, 2C, 1C, 0.5C, and
0.2C from 10C, the discharge capacity of the electrode can still reach
up to 59.7, 91.7, 133.6, 166, and 196.8 mA h g–1, indicating the excellent reversibility of the S–NTO NW@CNT@rGO
electrode. To further confirm the excellent electrochemical performance
of the film, the electrode was even continuously cycled for 100 cycles
at a current density of 0.2C, which showed that durable cyclic capacity
with a high reversible capacity of 114.1 mA h g–1 was retained. The above results indicate that the S–NTO NW@CNT@rGO
electrode has a significant advantage in terms of lifetime and capacity
retention.
Figure 6 Electrochemical measurements of the as-formed S–NTO NW@CNT@rGO
electrode in a range of 0.01–2.5 V. (a) Long cycling performance
at different current densities from 2C to 5C; and (b) rate performance
at various current densities from 0.2C to 10C and then cycling performance
at 0.2C.
From the above results, it can
be seen that the as-prepared S–NTO
NW@CNT@rGO flexible electrode materials have excellent electrochemical
performance, which is mainly attributed to the design strategy and
fabrication method of the electrodes. First, the absence of a binder
is beneficial because of the increased electrical conductivity of
the electrodes. The conventional electrode preparation process involves
mixing the active materials, the electronic conductor, and the binder
with the n-methyl-2-pyrroludone solvent and coating
the resultant slurry on copper foil as a current collector.43,44 However, our film electrode without the binder or current collector
can not only improve the electrical conductivity but also effectively
decrease the weight of the SIB system and enhance its energy density.
Second, the Na2Ti3O7 nanowires grown
in situ using the hydrothermal method have many advantages, including
a larger specific surface area for Na+ insertion/extraction
and shortened ion diffusion pathways that promote the charge transfer/collection
kinetics. In addition, many porous structures are formed by intertwined
nanowires, which are more conducive to the infiltration of the electrolyte,
increasing the ion diffusion rate. Third, in the hydrothermal process,
the added nanotubes not only facilitate the uniform dispersion of
nanowires and nanotubes but also contribute to the formation of Na2Ti3O7 nanowires, in which the nanotubes
wrap around the nanowires or connect them, improving the conductivity
of the nanowires themselves. Fourth, to ensure the largest contact
area between the graphene and Na2Ti3O7 nanowires, the process of the as-prepared film is repeated first
with the filtration of graphene and then with that of the NTO NW@CNT.
If this step is not performed, the contact area between graphene and
nanowires is very small because most of the nanowires are inside the
graphene layer rather than lying on the graphene surface, as seen
in Figure S7b,c, leading to the poor conductivity
of the material even with the addition of graphene. Fifth, the sandwichlike
layered-structured film is formed via vacuum filtration. As can be
seen in Figures 2b
and S2, there is a certain gap between
two layers because of the volatilization of oxygen in the reduction
process of graphene oxide, which is beneficial to the infiltration
of the electrolyte. Of course, the gap does not exist for the NTO
NW@CNT+rGO sample in Figure S7a. Finally,
the biggest advantage of sandwich-structured NTO NW@CNT@rGO is its
ability to improve the electrical conductivity itself. Figure 1 shows the schematic representation
and ideal electrotransfer pathway for the as-prepared S–NTO
NW@CNT@rGO film. It can be seen that the electrons can transfer at
will in the graphene layer and between the graphene layer and NTO
NW@CNT layers. In addition, in the NTO NW@CNT layer, CNT connecting
the nanowires can allow the electrons to move freely, implying that
many electron-transfer channels are added. All of these benefits endow
the electrode with the proposed flexible, current collector-free,
binder-free, and sandwich-structured anode configuration, which significantly
improve the cycling performance and the rate capability of the electrode.
To further confirm the structural integrity of the electrodes,
the battery was disassembled after the charge and discharge cycles
and the electrode material was analyzed by both XRD and SEM (Figure 7). In Figure 7a, compared with the diffraction
peaks before cycling, the diffraction peak of the electrode material
after charging and discharging is very obvious at 10.5°, which
is the typical peak of the Na2Ti3O7 pattern corresponding to JCPDS no. 31-1379. This proves that the
electrode material itself does not change after undergoing a rigorous
process of intercalation and deintercalation of sodium ions. SEM images
of a cross section of the S–NTO NW@CNT@rGO film electrode after
cycling are shown in Figure 7b,c. The hierarchical structure is still obviously maintained,
and the graphene and NTO nanowires of the interlayer are still observed,
indicating that the sandwich-structured film is very stable. Meanwhile,
as seen in the top view in Figure 7d,e, the morphology of the NTO nanowires remains intact,
and there is still a graphene layer covering the surface of the NTO
nanowires. This means that the graphene layer not only protects the
multilayer structure of the electrode from damage and improves the
electrode conductivity but also ensures that the NTO nanowires are
not destroyed during the charging and discharging process.
Figure 7 (a) XRD patterns
of the NTO NW@CNT@rGO film electrode before and
after the cycling test and morphology and structure of the NTO NW@CNT@rGO
film electrode after the cycling test: (b, c) SEM images of the cross
section and (d, e) SEM images of the upper surface.
Conclusions
In summary, we have
presented a facile approach to produce free-standing
and sandwich-structured NTO NW@CNT@rGO flexible film anode electrodes
for high-performance sodium ion batteries by hydrothermal-assisted
modified vacuum filtration. The as-obtained S–NTO NW@CNT@rGO
flexible electrodes are not only binder-free and current-collector-free
but also exhibit excellent electrochemical performances with a long
cycle lifetime and large capacity for NIBs. At current densities of
0.5C, 1C, and 2C, the discharge capacities of the electrodes can be
maintained at 107.2, 101, and 97.9 mA h g–1 after
100 cycles, respectively. The S–NTO NW@CNT@rGO electrode still
retain a discharge capacity of 80.6 mA h g–1 after
150 cycles at a higher current density of 5C. During a long-term cycling
performance test, after 100 cycles at a current density of 2C, a reversible
capacity of 92.5 mA h g–1 was achieved; the discharge
capacity could reach 59.9 mA h g–1 at 5C after 100
cycles. More importantly, after the rate performance test, a high
reversible capacity of 114.1 mA h g–1 was retained
after a further 100 cycles at 0.2C. The superior electrochemical performance
of the electrodes is believed to be in connection with the unique
sandwich architecture formed by the ultralong Na2Ti3O7 nanowires@CNT layer and highly conductive graphene
layer. Furthermore, this general strategy explores exciting new methods
for the design and fabrication of other flexible films applying to
catalysis, energy storage, and other energy transformation processes.
Experimental
Section
Synthesis of Graphene Oxide (GO)
GO was prepared from
natural graphite by a modified Hummers method.45,46 Briefly, 3 g of graphite powder was slowly added into a mixture
of 50 mL 98% H2SO4, 3 g of K2S2O8, and 3 g of P2O5 and then
the solution was stirred continuously at 80 °C for 5 h. The prepared
preoxidized product was cleaned using deionized water and dried in
a vacuum oven at 80 °C for 12 h. Afterward, it was mixed with
150 mL of 98% H2SO4, forming a black uniform
dispersion. KMnO4 (15 g) was slowly added at a temperature
below 20 °C, then the ice bath was removed, and the mixture was
stirred at room temperature for 1 h. After slowly heating to 35 °C
for 2 h, additional ice–water mixture and 20 mL of 30% H2O2 were slowly added into the mixed solution to
completely react with the excess KMnO4. After 10 min, a
bright yellow solution appeared. The resulting mixture was washed
with diluted aqueous HCl (1/10 v/v) solution and H2O. Graphite
oxide was prepared after freeze-drying in a vacuum oven.
Synthesis of
Na2Ti3O7 Nanowires@CNT
(NTO NW@CNT)
Na2Ti3O7 nanowires@CNT
was synthesized via a simple hydrothermal process. In brief, 20 mL
of 0.2 M tetrabutyl titanate ([CH3(CH2)3O]4Ti) solution in ethanol was mixed with 20 mL of 10 M aqueous
NaOH solution. After adding 0.0403 g of CNT into the solution, the
mixed solution was magnetically stirred and then transferred into
a Teflon-lined stainless steel autoclave. It was heated in an oven
at 190 °C for 12 h. After being air-cooled to room temperature
(25 °C), the precipitate was collected by centrifugation, washed
with deionized water and ethanol several times, and dried in air at
80 °C for 24 h, finally obtaining Na2Ti3O7 nanowires@CNT.
Fabrication of Free-Standing
and Sandwich-Structured Na2Ti3O7 Nanowires@
CNT@Reduced Graphene
Oxide (S–NTO NW@CNT@rGO) Flexible Film Electrode
The
flexible S–NTO NW@CNT@rGO film was fabricated by the vacuum
filtration method. Typically, 20 mg of GO and 10 mg of NTO NW@CNT
were respectively dispersed in 50 mL ethanol and then sonicated for
8 h to form solutions A and B. Subsequently, a sandwich-structured
film was prepared by adding the solution dropwise to a vacuum filter
with a 0.2 μm porous PTFE membrane according to the order “ABAB···”.
Finally, the obtained filter film was peeled off from the microporous
membrane and vacuum-dried at 100 °C for 12 h to obtain a free-standing
film. The film was cut into pieces with a diameter of 10 mm and vacuum-dried
at 200 °C for 4 h to convert graphene oxide to reduced graphene
oxide.
For comparison, a Na2Ti3O7 nanowires@CNT (NTO NW@CNT) film and a Na2Ti3O7 nanowires@CNT+rGO (NTO NW@CNT+rGO) film were also prepared
by vacuum filtration. A dispersion with Na2Ti3O7 nanowires@CNT powder dispersed in ethanol by ultrasonication
was filtered to produce a NTO NW@CNT film. The NTO NW@CNT+rGO film
was obtained by filtering a mixture of the ethanol solution with Na2Ti3O7 nanowires@CNT powder and graphene
oxide.
Material Characterization
The X-ray diffraction patterns
of the prepared samples were obtained using a Bruker D8 advance instrument
at 40 kV and 40 mA with Cu Kα radiation (λ = 0.154 nm)
(the scanning rate: 3 min–1; the 2θ range:
5–70°). The morphology and particle size of the samples
were investigated using field-emission scanning electron microscopy
(FESEM, JSM-7800F) and energy-dispersive X-ray spectroscopy (EDX).
TEM and HRTEM images were obtained using a JEM-2100F instrument under
a different resolution transmission electron microscope. Raman spectra
were recorded on a PerkinElmer system at a laser wavelength, λ,
of 532 nm. Thermogravimetric analysis (TGA) was carried out using
a STA409 PC thermogravimetric analyzer to determine the carbon content
in the flexible samples.
Electrochemical Measurements
The
electrochemical performance
of the as-prepared samples was investigated by CR2016-type coin half-cells
using Na metal foil as the counter electrode. The free-standing and
flexible S–NTO NW@CNT@rGO films were directly used as the working
electrodes without the involvement of any metal current collector,
conductive additive, or polymeric binder. The half-cells were assembled
in an argon-filled glove box. The mass loading of the active material
in each coin cell was typically 1.0–1.5 mg cm–2. NaClO4 (1 M) in a mixture (1:1, volume) of propylene
carbonate (PC) and ethylene carbonate (EC) was used as the electrolyte,
and a glass microfiber filter (Whatman GF/D) was used to separate
the contacts of the cathode and anode electrode materials. Galvanostatic
charge/discharge measurements were conducted using a LAND CT2001A
test system (Wuhan, China) under various current densities in the
potential range 0.01–2.5 V (vs Na+/Na) at room temperature.
Cyclic voltammetry (CV) measurements were performed using a CHI650D
(Chenhua, Shanghai) electrochemical workstation.
Supporting Information Available
The Supporting Information
is available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.7b01051.SEM images of
the as-formed NTO NW@CNT film electrode
and as-formed rGO film, CV curves of the S–NTO NW@CNT@rGO electrodes
at various sweep rates, cycling performance of the as-formed NTO NW@CNT
film electrode at the current density of 0.2C, cycling performance
of the as-formed NTO NW@CNT+rGO film electrode at current densities
of 0.5C and 1C, rate performance of the as-formed NTO NW@CNT+rGO film
electrode, SEM images of the as-formed NTO NW@CNT+rGO film electrode
(PDF)
Supplementary Material
ao7b01051_si_001.pdf
The
authors
declare no competing financial interest.
Acknowledgments
This work was financially supported by the National Nature
Science Foundation of China (Nos. 21543015, 21336003, and 21371021),
the National Key Research Program of China (No. 2016YFB0901501), and
Science and Technology Commission of Shanghai Municipality (No. 14DZ2261000).
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145911310.1021/acsomega.8b01508ArticleHybrid Noble-Metals/Metal-Oxide Bifunctional Nano-Heterostructure
Displaying Outperforming Gas-Sensing and Photochromic Performances Tobaldi David Maria *†Leonardi Salvatore Gianluca ‡Movlaee Kaveh ‡§Lajaunie Luc ∥#¶Seabra Maria Paula †Arenal Raul ∥⊥Neri Giovanni ‡Labrincha João António †† Department
of Materials and Ceramics Engineering/CICECO−Aveiro Institute
of Materials, University of Aveiro, Campus Universitário de Santiago, 3810-193 Aveiro, Portugal‡ Department
of Engineering, University of Messina, C.da Di Dio, 98166 Messina, Italy§ Center
of Excellence in Electrochemistry, School of Chemistry, College of
Science, University of Tehran, 14155-6455 Tehran, Iran∥ Laboratorio
de Microscopías Avanzadas, Instituto de Nanociencia de Aragón, Universidad de Zaragoza, 50018 Zaragoza, Spain⊥ ARAID
Foundation, 50018 Zaragoza, Spain* E-mail: david.tobaldi@ua.pt and david@davidtobaldi.org. Phone: +351 234
370 041.24 08 2018 31 08 2018 3 8 9846 9859 01 07 2018 10 08 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under a Creative Commons Non-Commercial No Derivative Works (CC-BY-NC-ND) Attribution License, which permits copying and redistribution of the article, and creation of adaptations, all for non-commercial purposes.
As
nanomaterials are dominating 21st century’s scene, multiple
functionality in a single (nano)structure is becoming very appealing.
Inspired by the Land of the Rising Sun, we designed a bifunctional
(gas-sensor/photochromic) nanomaterial, made with TiO2 whose
surface was simultaneously decorated with copper and silver (the Cu/Ag
molar ratio being 3:1). This nanomaterial outperformed previous state-of-the-art
TiO2-based sensors for the detection of acetone, as well
as the Cu–TiO2-based photochromic material. It indeed
possessed splendid sensitivity toward acetone (detection limit of
100 ppb, 5 times lower than previous state-of-the-art TiO2-based acetone sensors), as well as reduced response/recovery times
at very low working temperature, 150 °C, for acetone sensing.
Still, the same material showed itself to be able to (reversibly)
change in color when stimulated by both UV-A and, most remarkably,
visible light. Indeed, the visible-light photochromic performance
was almost 3 times faster compared to the standard Cu–TiO2 photochromic material—that is, 4.0 min versus 10.8
min, respectively. It was eventually proposed that the photochromic
behavior was triggered by different mechanisms, depending on the light
source used.
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1 Introduction
As
nanostructured materials are dominating the scene in the 21st
Century, their potential influence on future products and services
is enormous. This has led to a huge advance in research and development
efforts related to nanoscale materials and devices. As such, researchers
are willing to engineer complex multifunctional and, to a certain
degree, smart devices and systems. There is consequently a request
for a higher level of complexity in materials design, that is, in
other words, combining multiple functionalities in the same nanostructure.1
Metal oxides (MOs) are a very important
family of nanomaterials,
having unique properties and advantageous functionalities that clearly
are attractive for a number of applications ranging from electronic
devices to energy conversion.2 Titanium
dioxide (titania, TiO2) nanoparticles (NPs), because of
their versatility, are a well-investigated class of MOs. Indeed, they
are widely used in everyday applications, becoming by far the most
popular material in light-to-energy conversion and storage.3 The “sun” of TiO2 as
photocatalyst rose indeed in Japan more than 4 decades ago, when a
paper by Honda and Fujishima about semiconductor photo-electrochemistry
was published in 1972.4 This initiated
research on liquid junction solar cells and semiconductor-assisted
photocatalysis.5 The photocatalytic (PC)
mechanism is now well known: when the surface of a semiconductor material
is irradiated with photons having energy higher than or equal to its
band gap energy (Eg), photo-electrons
e– and photo-holes h+ are generated.6 Taking advantage of this phenomenon, multifunctional
nanomaterials might be engineered—that is, simultaneous PC
and antibacterial activities have been shown to exist in silver-modified
titania.7
Furthermore, Japan was
also the cradle of that phenomenon that
was named “multicolour photochromism”
by their discoverers, Tatsuma’s group and, once again, Fujishima’s
group.8 This was found exploiting the PC
phenomenon in anatase TiO2 films loaded with silver NPs
when triggered by UV-light. This outcome led Parkin et al. to demonstrate
a relationship between the photochromic state of a Ag–TiO2 thin-film and its UV-light PC activity,9 thus showing multifunctionality within the Ag–TiO2 system. Following on from these findings, Tobaldi and co-authors,
first reported the photochromism and PC activity of multifunctional
silver-modified TiO2 NPs, triggered by a purely visible
white-light.10 It has also been recently
shown that a nanomaterial exhibiting reversible color properties can
be engineered by coupling copper and TiO2, and the redox
process from Cu2+ to Cu+ linked to a change
in color, can be simply controlled by regulating the light source
(UV or visible light) and exposure time.11 Hence, decorating titania with a noble metal can yield to a purely
inorganic photochromic noble-metal/MO hybrid nanomaterial. Conversely,
most of the existing photochromic systems are based on polymers or
organogels containing organic moieties, thus displaying limitations
for being implemented on commercial devices.12
Besides, TiO2 nanomaterials have also been extensively
employed for sensing applications,3 because
of their unique chemical and physical properties as well as the nontoxic
and environmentally friendly nature, excellent biocompatibility, and
stability. In particular, it has been widely demonstrated that resistive
gas sensors based on TiO2 nanostructures are highly effective
in detecting both reducing [i.e., H2, CO, volatile organic
compounds (VOCs)],13 and oxidizing (e.g.,
NO2, O3) gases.14 TiO2 nanostructures—because of the extremely high
surface to volume ratio and their ability to absorb reactive oxygen
species at their surface15—can provide
a large number of active sites for the interaction with the gas, thus
resulting in high sensitivity. Despite this, some drawback related
to high working temperatures and long recovery times are the main
disadvantages of that material.3 Modifications
of TiO2 by doping and/or the formation of metal/TiO2 or MO/TiO2 heterostructures are amongst the simplest
ways to enhance the sensitivity and selectivity yet shortening the
response/recovery times.16
Our previous
works were inspired by light and its ability to trigger
redox reactions on the surface of a semiconductor nanomaterial when
this is decorated with noble-metals NPs (i.e., silver and copper,
as in refs (10) and (11), respectively). Those
redox reactions are indeed associated to a reversible change in color
of the (photochromic) material. Color is definitely an essential characteristic
of Japanese traditional metal art and craft.17
As a result, this research was greatly inspired by the Land
of
the Rising Sun—photocatalysis,4 photochromism,8 and Japanese traditional alloys.17Shibuichi—a copper–silver
alloy used mainly for sword ornaments, that is, tsuba—is one of the most representative Japanese traditional alloys. Shibuichi means literally “one-fourth”, to indicate its standard formulation of a copper alloy
containing 25% of silver.17 Hence, we designed
a multifunctional photochromic/gas-sensing nanomaterial, made with
TiO2 decorated expressly with copper and silver having
the Cu/Ag molar ratio constrained to be 3:1—that is, one part
of Ag, and three parts of Cu. As far as we know, this is the first
research of its kind involving multifunctionality (i.e., UV and most
remarkably visible-light photochromism as well as gas-sensing properties)
on TiO2 modified with Ag NPs and CuxO nanoclusters, certainly without neglecting the particular
ratio of the noble metals used in here. As a matter of fact, previous
research works involved TiO2 modified with Cu and Ag, but
solely with a view limited to PC or antibacterial applications.18,19
2 Results and Discussion
2.1 QPA and
Microstructural Analyses: XRD and
HR-STEM
X-ray diffraction (XRD) patterns of the specimens
are shown in Figure 1. Results of the XRD-quantitative phase analysis (QPA) analysis are
listed in Table 1,
and a graphical output of a Rietveld QPA refinement is shown in Figure S1. Unmodified titania is composed of
all the three main natural occurring TiO2 polymorphs/anatase
(56.5 wt %), rutile (19.8 wt %), and brookite (23.6 wt %). The presence
of brookite has to be linked to the strongly acidic synthesis conditions.20 The modification with both copper and silver
led to a huge decrease in the weight fraction of rutile and brookite,
meaning a delay in the anatase-to-rutile phase transition (ART). Specimen SBC1, for instance, is composed of 94.5 wt % anatase, 4.4
wt % rutile, and 1.2 wt % brookite. By contrast, SBC10 contains 93.7 wt % anatase, 3.7 wt % rutile, and 2.6 wt % brookite,
see Table 1. Actually,
in Shibuichi specimens, the trend with the increase
in the Ag + Cu mol % content is a slight decrease in the anatase and
rutile fractions (from 94.5 to 93.7 wt %, and from 4.4 to 3.7 wt %,
respectively) and a small increase in brookite amount—from
1.2 to 2.6 wt %. The delay in the ART, when including Ag + Cu in the
system, can be explained as being caused by a grain-boundary pinning
(Zener drag),21 which culminates in delaying
the ART—that is a nucleation-growth mechanism.22 Microstructural information, as extracted by means of whole
powder pattern modeling (WPPM), is listed in Tables 2 and 3; an example
of WPPM graphical output is shown in Figure S2. From the negligible differences in unit cell volumes, it can be
inferred that neither Cu nor Ag entered the TiO2 lattice.
Indeed, the ionic radii of [VI]Cu1+/2+, [VI]Ag1+/2+, and [VI]Ti4+ are
0.77/0.73, 1.15/0.94, and 0.61 Å, respectively.23 Modification of TiO2 with Ag + Cu also led to
a decrease in the mean average diameter of the crystalline domains,
cf Table 3 and Figure 2a–c. Anatase
domains in unmodified TiO2 have an average diameter of
10.4 nm, rutile of 14.4 nm, and brookite averages of 7.0 nm. Shibuichi modification of TiO2 led not only to
smaller crystalline domain diameters, but also to narrower size distribution
of those crystalline domains, refer to Table 3 and Figure 2a–c. The average crystalline domain diameter
in anatase and rutile that are in SBC1 is 6.7 and 11.2
nm, respectively; on the other hand, that of anatase and rutile in SBC10 is 4.6 nm for both the polymorphs. This outcome means
that copper and silver NPs likely nucleate on the grain boundaries,
pinning them, thus limiting their further growth. This also explains
the observed delay of the ART and crystal growth. The decrease in
the size of anatase nanocrystals is also confirmed by Raman analysis:
the Raman Eg mode of anatase is shifted
toward higher energies in the Ag + Cu specimens, thus confirming their
reduced dimensions (cf Table S1).24
Figure 1 XRD patterns of synthesized specimens. The vertical bars
represent
the XRD reflections of anatase (black, JCPDS-PDF card no. 21-1272),
rutile (blue, JCPDS-PDF card no. 21-1276), and brookite (red, JCPDS-PDF
card no. 29-1360—only the three most intense reflections were
reported here).
Figure 2 Size distribution, as
obtained from the WPPM modeling of (a) anatase,
(b) rutile, and (c) brookite, contained in the synthesized specimens.
Table 1 Rietveld Agreement
Factors and Crystalline
Phase Composition of the Unmodified and Cu/Ag-Modified TiO2a
agreement factors phase composition (wt %)
sample no. of variables RF2 (%) Rwp (%) χ2 anatase rutile brookite
Ti450 20 3.54 4.03 1.74 56.5 ± 0.1 19.8 ± 0.2 23.6 ± 0.6
SBC1 19 2.27 3.01 1.59 94.5 ± 0.1 4.4 ± 0.2 1.2 ± 0.2
SBC2 18 2.04 3.48 1.56 93.4 ± 0.1 4.8 ± 0.2 1.8 ± 0.2
SBC5 16 2.72 3.42 1.66 93.6 ± 0.1 4.2 ± 0.2 2.2 ± 0.3
SBC10 17 4.22 3.16 1.64 93.7 ± 0.1 3.7 ± 0.2 2.6 ± 0.4
a There were 2285
observations for
every refinement; the number of anatase, rutile, and brookite reflections
was 32, 31, and 154, respectively.
Table 2 WPPM Agreement Factors and Unit Cell
Parameters for the Three Phases in the Synthesized Samples
unit cell parameters
agreement
factors anatase rutile brookite
sample Rwp (%) Rexp (%) χ2 a = b (nm) c (nm) V (nm3) a = b (nm) c (nm) V (nm3) a (nm) b (nm) c (nm) V (nm3)
Ti450 6.17 1.96 3.15 0.3791(1) 0.9515(1) 0.137(1) 0.4598(1) 0.2959(1) 0.063(1) 0.5440(2) 0.9206(4) 0.5157(1) 0.258(1)
SBC1 2.83 2.04 1.39 0.3790(1) 0.9516(2) 0.137(1) 0.4608(1) 0.2955(1) 0.063(1)
SBC2 3.56 1.88 1.89 0.3790(2) 0.9514(4) 0.137(1) 0.4596(3) 0.2959(4) 0.062(1) 0.5440(42) 0.9057(26) 0.5153(8) 0.254(3)
SBC5 2.26 1.76 1.28 0.3793(2) 0.9508(11) 0.137(1) 0.4608(4) 0.2959(5) 0.063(1) 0.5519(62) 0.9276(117) 0.5107(34) 0.261(8)
SBC10 2.13 1.62 1.32 0.3797(2) 0.9504(13) 0.137(1) 0.4613(5) 0.2959(8) 0.063(1) 0.5525(43) 0.9138(62) 0.5141(17) 0.260(5)
Table 3 Mean Crystalline Domain Size of Anatase
(Ant), Rutile (Rt) and Brookite (Brk)—Defined as the Mean of
the Lognormal Size Distributions; Maximum Values and Skewness of the
Lognormal Size Distributions
mean crystalline domain diameter mode of the size distribution skewness of the size distribution
sample ⟨Dant⟩
(nm) ⟨Drt⟩ (nm) ⟨Dbrk⟩ (nm) Ant (nm) Rt (nm) Brk (nm) Ant (nm) Rt (nm) Brk (nm)
Ti450 10.4 ± 0.7 14.4 ± 0.6 7.0 ± 0.1 9.4 ± 0.6 9.9 ± 0.4 5.3 ± 0.1 0.8 ± 0.1 1.8 ± 0.1 1.4 ± 0.1
SBC1 6.7 ± 0.3 11.2 ± 0.1 5.3 ± 0.2 9.4 ± 0.1 1.3 ± 0.1 1.1 ± 0.1
SBC2 5.2 ± 0.8 9.4 ± 0.3 5.3 ± 1.4 4.0 ± 0.1 8.2 ± 0.3 4.6 ± 1.2 1.4 ± 0.1 0.9 ± 0.1 1.0 ± 0.1
SBC5 5.1 ± 0.1 5.8 ± 0.8 5.7 ± 0.9 3.9 ± 0.1 3.4 ± 0.5 5.0 ± 0.8 1.4 ± 0.1 2.0 ± 0.1 1.0 ± 0.1
SBC10 4.6 ± 0.1 4.6 ± 0.8 5.8 ± 1.2 3.5 ± 0.1 3.2 ± 0.6 5.5 ± 0.1 1.4 ± 0.1 1.8 ± 0.1 0.6 ± 0.1
High-resolution scanning transmission electron microscopy (HR-STEM)
experiments were performed on the Shibuichi samples
with the highest Ag + Cu concentrations (SBC5 and SBC10) in order to investigate the possible formation of a
metallic@TiO2 heterostructure and to determine their morphology
and microstructure. Figure 3a shows a low-magnification STEM–high-angle annular
dark-field imaging (HAADF) micrograph of the sample SBC5, in which two distinct kinds of NPs, displaying two distinct contrasts,
can be clearly seen. A single NP displaying a brighter contrast (highlighted
by the green arrow) can be observed in contact with a matrix of agglomerated
NPs showing a darker contrast. NPs displaying the brighter contrast
are scarce and hard to find. To get more information on the nature
of the NPs, they were investigated by a combination of energy dispersive
X-ray spectroscopy (EDS) and high-resolution TEM (HR-TEM) techniques,
that is, a powerful tool to extract structural and chemical information
at the nanoscale.25 A darker contrast in
STEM–HAADF images highlights materials having lower atomic
number and/or lower mass density and/or lower thickness. Thus, these
NPs showing a darker contrast correspond to TiO2 NPs. This
is confirmed by the EDS spectrum acquired on these NPs (displayed
in red in Figure 3b).
The EDS spectrum acquired at the center of the brighter particle (displayed
in blue in Figure 3b) highlights the presence of Ag. It has to be highlighted that Cu
signal can be seen in both the NPs. However, Cu signal can emerge
from the specimen, but it might also come from the TEM sample-holder
or even from the TEM column, thus making a univocal conclusion difficult. Figure 3c displays the HR-STEM
ADF micrograph of a facetted NP standing in the vacuum and showing
a brighter contrast. These NPs have a diameter typically between 7
and 10 nm and, as it can be clearly seen from Figure 3c, they are crystalline. Automatic indexation
of the fast Fourier transform (FFT) pattern (displayed in the inset)
performed on one of the facet revealed that the NP corresponds to
the Ag face-centered cubic structure in the [011] zone axis. Same
results have been obtained on all the investigated NPs, showing this
kind of bright contrast. This is also confirmed by the EDS spectrum
acquired at the center of the NP (displayed in Figure 3d), which highlights the presence of the
Ag lines. A HR-STEM–HAADF micrograph of the TiO2 NPs is shown in Figure S3. All of the
TiO2 NPs are crystalline with a diameter between 1.8 and
8 nm. A similar analysis is shown in Figure S4 for SBC10 sample. The surface of this sample is flecked
due to the presence of smaller but more abundant Ag NPs (diameter
between 1.5 and 8 nm). These results are in good agreement with the
WPPM modeling and clearly show the formation of (at least) an Ag@TiO2 heterojunction for the Shibuichi samples.
Figure 3 (a) Low-magnification
STEM–HAADF micrograph of sample SBC5. The green
arrow highlights the presence of a NP having
brighter contrast in contact with a matrix of NPs with a darker contrast.
(b) EDS spectra acquired on the NPs with the darker and brighter contrasts
highlighted by a red and blue circle in the STEM–ADF micrograph
displayed in the inset, respectively. (c) HR-STEM ADF micrograph of
a NP with a brighter contrast standing in the vacuum. The inset displays
the FFT pattern obtained on the area highlighted by the red square.
(d) EDS spectrum acquired at the center of the NP displayed in (c).
2.2 Optical
Properties: Photochromism
Diffuse reflectance spectroscopy
(DRS) spectra of fresh un-irradiated
samples are depicted in Figure 4. As per Ti450, a single absorption band is observable
at <360 nm, due to the band-to-band transition in titania.26Shibuichi-modified specimens,
besides these bands, also display other absorption features. The absorption
band located at >600 nm is assigned to the d–d electronic
transitions
in Cu2+. The absorption at around 450 nm belongs to the
electron transferring from the valence band (VB) of TiO2 to CuxO clusters that are around titania
(interfacial charge transfer, IFCT);27,28 consistent
with what was reported in an earlier work, this IFCT band increases
itself as the amount of Cu in the specimens increases.11 Furthermore, when the Cu amount is higher than
1.50 mol % (i.e., specimens SBC5 and SBC10), an absorption tail extending itself up to ∼575 nm, assigned
to interband absorptions in Cu2O, is also noticeable.29,30 Optical signatures of metallic Ag0 (i.e., the surface
plasmon resonance band, SPR) are not seen at this un-irradiated stage.
This is likely because silver is present as Ag2O, thus
displaying just its IFCT feature mingling itself with that of CuxO clusters around TiO2.31
Figure 4 Absorption data, derived by Kubelka–Munk analysis,
of the
optical spectra (un-irradiated specimens).
When the Ag + Cu-modified specimens are exposed to UV-A light,
progressive changes are observable to their optical spectra, as shown
in Figure S5a–d. As per SBC1, as the UV-A irradiation time increases, there is also a gradual
decrease in the Cu2+ d–d band, thus being accompanied
by a continuing increase in the band due to the IFCT. Interestingly,
with only 0.25 s of UV-A irradiation time, also the band belonging
to the interband absorptions in Cu2O starts to appear (and
its magnitude increases with the irradiation time as well). These
phenomena imply that upon UV-A irradiation, the Cu2+ is
swiftly and gradually reduced to its cuprous oxidation state.11 There is also no signature of the appearance
of the Ag0 SPR band, likely because of the much reduced
amount of silver. With higher mol % amounts of Ag + Cu (specimens SBC2, SBC5, and SBC10), qualitatively
the same change in the optical features as in SBC1 was
observed. It is worth to highlight that the SPR band in Ag0 is not detected even with higher amounts of silver, probably because
the optical bands of copper cover that of Ag0 SPR. However,
an indirect evidence of the reduction of silver into Ag0 after light exposure is given by Raman spectroscopy. As shown in Figure S6, the Raman signal is enhanced in the
specimen that has been subjected to UV-A irradiation, thus indeed
proving the presence, in this latter, of metallic Ag, giving rise
to the surface-enhanced Raman scattering effect.32
These changes in the optical properties (i.e., photochromism)
are
caused, mechanistically, by the PC process in titania: when TiO2 specimens are irradiated with a light having supra Eg energy, the electron that migrated to the
conduction band (CB) is able to reduce the CuO oxides (and allegedly
also the Ag2O) that are clustered around the semiconductor
surface. Looking at the evolution of the increase in the IFCT band
area in the Shibuichi samples after UV-A irradiation, Figure 5a–d, it is
seen that these all follow a third-order exponential function, for
all the Ag + Cu modified specimens. This being partly consistent with
our previous investigations: indeed, when dealing only with copper-modified
TiO2 and Ag–TiO2 NPs, the best fit was
always obtained adopting a double exponential function.11,31 This suggesting that, in the case of Ag + Cu modified TiO2, the simultaneous adoption of two noble metals increases the degree
of complexity of the photochromic phenomenon—there is indeed
an electron “pumping” from TiO2 to CuO and
Ag2O NPs decorating it.
Figure 5 Evolution of the increase in the IFCT
band area in the Shibuichi samples after UV-A irradiation.
(a) SBC1; (b) SBC2; (c) SBC5; and (d) SBC10. The coefficients of determination R2 of the third-order exponential function adopted
for the fittings
were ≥0.9984.
When specimens are irradiated with the white lamp, the same
changes
in the optical properties happen, though in a lesser extent, Figure S7a–d. This is better shown in Figure 6a–d, and in Table 4, where is listed
the time needed to halve the IFCT integrated area—data obtained
using both UV-A and visible light are compared. As listed in Table 4, for instance, the
time to reach half of the IFCT integrated area in SBC1 using the UV-A radiation is equal to 0.23 min, while, with the visible
light, that time is 4.04 min (∼18 times faster using the UV-A
lamp). This latter is indeed a striking result, being the time to
halve the IFCT-integrated area in a specimen made only of 1 mol %
Cu and TiO2 and using the very same visible-light source,
equal to 10.8 min11—that is, almost
3 times faster by adding only 0.25 mol % of silver and decreasing
from 1 to 0.75 mol % the Cu content.
Figure 6 Evolution of the increase in the IFCT
band area in the Shibuichi samples after visible-light
exposure. (a) SBC1; (b) SBC2; (c) SBC5; and (d) SBC10. The coefficients of determination R2 of the third-order exponential function adopted
for
the fittings were ≥0.9923.
Table 4 Time to Reach One-Half of the Final
Extent of the Integrated IFCT Area, After UV-A and Vis-Light Irradiation
t1/2 IFCT band (min)
sample UV-A Vis-light
SBC1 0.23 4.04
SBC2 0.44 11.96
SBC5 4.65 15.89
SBC10 9.34 33.29
On the other hand, specimen SBC10 and
UV-A lamp, the
time needed to reach half of the final extent of the IFCT integrated
area is 9.34 min, versus 33.29 min when using the Vis-light (approximately
4 times faster). This means that a lamp irradiating with an energy
that is ≥TiO2Eg triggers
in a faster way the photochromic effect, through the PC mechanism.
However, this also means that the specimens show themselves to be
photochromic, even under visible-light exposure. This is explained
invoking a different phenomenon, that is, photosensitization of the
Cu(II)/TiO2 system. Indeed, as suggested by Irie et al.,
visible light triggers IFCT from the VB of titania to the Cu(II) that
are grafted onto the surface of TiO2 NPs.27 That is to say that the electrons in the VB of TiO2 are directly transferred to the CuO decorating the TiO2 NPs, reducing Cu2+ to Cu+, as spectroscopically
shown by the decrease in the Cu2+ d–d transitions
and the resultant increase in the extent of the IFCT band—and
visually by the change in color of the specimens, that is, photochromism.
A proposed mechanism of these two distinct phenomena is given in Figure 7a–c, where
the energy band diagrams of TiO2, whose surface is modified
with CuO and Ag2O, are given—the electrochemical
potentials of the band edges of TiO2, CuO, and Ag2O, with respect to the absolute vacuum scale, were taken from the
literature.33 [It has to be stressed that,
although the data in Figure 7a–c might not reflect a rigorous picture of the absolute
values of CB and VB potentials of the materials studied here, they
provide a reasonable estimate of the relative band edge positions.]
In both cases (UV-A and visible-light sources), TiO2 acts
itself as an electron shuttle.34
Figure 7 Proposed mechanism
for the UV-A and visible-light photochromism.
(a) After UV-A exposure, an electron is promoted from the VB to the
CB of TiO2, a CB transferring from TiO2 to CuO
is then favored, thus reducing Cu2+ to Cu+.
(b) Visible light triggers IFCT from the VB of titania directly to
the CB of Cu2+ that are grafted on the TiO2 surface,
reducing it and promoting the photochromic effect. The same proviso,
considering their band edge positions, can be made with TiO2 and Ag2O. (c) After UV-A and visible-light irradiation,
(most of) the Ag(I) and Cu(II) oxides have been reduced into Ag0 and Cu2O. This situation promotes charge separation,
as shown by the yellow arrow in the energy band diagram: electrons
move themselves from Ag0 to the CB of TiO2 and
from the CB of Cu2O to that of TiO2.
Photochromism is, per se, a reversible change in
color (and/or
optical absorption spectra) under electromagnetic radiation.35 Reversible photoswitches of specimens SBC1 and SBC2 were thus investigated. Specimens
were irradiated for 10 or 30 s with visible light (irradiance = 50
W m–2), then the reversibility of the process was
triggered by annealing the irradiated specimens in a dark oven at
100 °C for 15 min. As displayed in Figure 8a–d, SBC1 and SBC2 exhibit similar changes, both specimens show an increase in the
ΔRt value from
the un-irradiated state after the first exposure to visible light.
This is followed by a partial recovery of the initial virgin state
after annealing the samples in the dark at 100 °C for 15 min.
However, after that initial loss in the initial R % value, very close reflectance values are obtained from the 4th
switching cycle on, as a clear and repeatable gap is noticeable for
both specimens, exhibiting a high degree of stability and repeatability
in the switching values for repeated cycles (up to a total of 14),
as reported in Figure 8a,b. This initial instability seems to be originated from the swift
decrease from the virgin state: the time granted for the annealing
did not seem enough to fully reverse it.
Figure 8 Photochromic recovery
switches with repeated visible light (red
spheres)/dark@100 °C for 15 min (green spheres) cycles; the blue
sphere represent the un-exposed specimen. (a) SBC1 upon
10 s Vis and 15 min@100 °C; (b) SBC1 upon 30 s Vis
and 15 min@100 °C; (c) SBC2 upon 10 s Vis and 15
min@100 °C; and (d) SBC2 upon 30 s Vis and 15 min@100
°C.
2.3 Electrical
and Gas-Sensing Properties
The electrical behavior of the
prepared sensors was first investigated
by recording the resistance of the sensitive films directly printed
on the alumina substrates, in the temperature range of 100–400
°C in the presence of dry air. In order to favor the complete
desorption of humidity and other species likely adsorbed during environmental
exposure, each sensor was first allowed to stabilize at 400 °C,
and then, the resistance was recorded during a 50 °C step decrease
of the temperature. The plots of the resistance versus temperature
of pure TiO2 and Ag + Cu (Shibuichi)-modified
samples are reported in Figure 9. All samples show a decrease in the resistance with increase
in the temperature, according to typical semiconductor behavior in
the whole range of temperatures. Ti450 shows two linear
regions with different slopes, in the range 150–250 and 250–400
°C, respectively. This can be attributed to a strong adsorption
of oxygen species which, in turn, act increasing the electrical resistance.
As known, MOs are able to adsorb oxygen species as ions (•O2–, O–, O2–) on their surface as a function of the temperature.36 This implies that electrons are subtracted from the bulk,
increasing the electrical resistance. Furthermore, a different equilibrium
between adsorption and desorption of these species was established
as a function of the temperature. Therefore, if adsorption prevails
over desorption, a large quantity of oxygen is adsorbed on the MO
surface, which leads to a stronger removal of electrons from the bulk.
For an n-type semiconductor as TiO2, this
results in an increase of the resistance.37 According to this, it is plausible that Ti450 is able
to strongly adsorb oxygen in the temperature range of 150–250
°C showing two different slopes of the log resistance versus
temperature in the investigated range.
Figure 9 Electrical resistance
as a function of the temperature of the as-fabricated
gas sensors recorded in dry air.
On the contrary, as per Shibuichi samples
(SBC1, SBC2, SBC5, and SBC10), the trend of resistance fluctuation with the temperature
is linear
in the entire investigated range of temperatures, suggesting a lower
ability in adsorbing oxygen species. In addition, the effect of Ag
+ Cu modification is to decrease the electrical resistance in comparison
to Ti450 when the load is higher than 2 mol % as for SBC2, SBC5, and SBC10 samples. In
this regard, it was possible to record the resistance of these samples
up to 100 °C, while for Ti450 and SBC1 the resistance was much higher than the detection limit of the apparatus
employed.
The effect of Ag + Cu modification of TiO2 on the sensing
performance toward acetone was first investigated at different working
temperatures. Figure 10 shows the responses of the prepared sensors toward 20 ppm of acetone
as a function of the temperature, in the range 100–400 °C.
Owing to the high resistance of both Ti450 and SBC1, it was not possible to record the response at a temperature
lower than 150 °C. As observed, all sensors show a Gaussian-like
behavior, where a first rise of the responses up to 150–200
°C is followed by a decrease with further increase of the temperature.
These typical response behaviors can be simply explained, bearing
in mind the effect of different activation energies for the gas adsorption/desorption
and reaction processes occurring at the surface. At a low operating
temperature, the activation energy is not enough to promote the reaction
of acetone molecules with the active species present on the material
surface. This leads to a very weak or no alteration of the electrical
properties of the sensitive material and, consequently, to a weak
response.38 On the other hand, the adsorption
ability of acetone molecules onto the surface is reduced at higher
operating temperatures, thus leading again to a lower response.39
Figure 10 Gas responses toward 20 ppm acetone in dry air of Ti450- and Shibuichi-based sensors at different
operating
temperatures.
Among Shibuichi-based sensors, SBC2 is the one that shows the best
performances and have the maximum
response S = 9 at the lowest operating temperature,
150 °C. A further increase of Ag + Cu modification of TiO2 over 5 mol % as for the SBC10 sample resulted
in a strong decrease of the response to acetone. However, all Shibuichi-based sensors showed lower response in comparison
to Ti450, in the whole range of investigated temperatures.
However, response is not the sole parameter that is investigated
to define the performances of a gas sensor. In this regard, Figure 11 shows a comparison
of the transient responses recorded for each sensor at the operating
temperature of 200 °C to a pulse of 20 ppm acetone. Still in
a relatively low temperature, all Shibuichi-based
sensors show fast signal variations after acetone exposure, reaching
the equilibrium state in less than 30 s, which is faster than that
observed for Ti450-based sensor (Figure S8a). When the sensors are again exposed to pure air,
a fast recovery of the 90% of response is obtained in less than 30–40
s on the Shibuichi-based sensors. As per the Ti450-based sensor, it is worth noting that the time at 90%
of response recovery is close to that of the SBC2-based
sensor (Fig S8b); nevertheless, the time
to the full recovery of the baseline signal is much higher, thus leading
to a serious drawback in real applications. Therefore, a positive
effect of the incorporation of Ag + Cu into TiO2 is to
ease the desorption of subproducts of acetone reaction from the surface
of the material. In this regard, Dutta et al.,40 investigating the CO-sensing performance of anatase TiO2, suggested that CuO incorporation, favoring the decomposition
of carbonate intermediate species, aids the desorption of subproduced
CO2 and then the recovery time of the sensor. It is well
known that the typical sensing mechanism of reducing gases with MOs
involves the interaction of gas molecules with chemisorbed oxygen
species at the surface.41 At temperatures
lower than 200 °C, the predominant chemisorbed oxygen species
on MOs are O2– and O–. Therefore, because of the lower activation energy of these species
than the more reactive species, a proposed sensing mechanism of
acetone might involve the quasi–chemical reactions, as given
by eqs 1 and 2(42) 1 2
Figure 11 Transient responses toward 20 ppm acetone
in dry air of Ti450- and Shibuichi-based
sensors at the operating temperature
of 200 °C.
Accordingly, because
the reaction of acetone with surface-adsorbed
oxygen species may involve the formation of carbonates before the
evolution to CO2 and H2O, a similar catalytic
effect coming from CuO and/or AgO nanoclusters could be the reason
of faster recovery times of Shibuichi-TiO2 based sensors in comparison to Ti450.
All investigated
sensors show a reduction in the electrical resistance
when exposed to acetone, according to n-type semiconductor MOs when
they interact with reducing gases. This suggests that the addition
of such load of p-type species, like copper, is not enough to alter
the typical n-type behavior of anatase TiO2.43 Teleki et al.,44 showed
a p-type behavior in a heat-treated 100 wt % rutile TiO2 sensors toward CO at 500 °C, while the same authors observed
a n-type response for a 5 at. % Cu/TiO2-based sensor, having
a rutile content of 50 wt %.45 On the other
hand, Savage et al.46 investigated the
sensing behavior of mixed anatase–rutile TiO2 toward
CH4 and CO gases. They reported stable n-type response
for rutile phase less than 75 wt % and p-type response for pure rutile.
As all Shibuichi samples show contents of anatase
higher than 90 wt % and about 56 wt % for Ti450 (cf Table 1), this might explain
the stable n-type behavior of all the sensors reported here.
Among Ag–Cu samples, because of the higher response, lower
operating temperature, and reduced electrical resistance, the sensor
based on SBC2 was chosen to be investigated for further
sensing performances. Figure 12a shows the transient response recorded during subsequent
exposure of the SBC2-based sensor to different concentrations
of acetone ranging from 1 to 40 ppm in dry air at the working temperature
of 150 °C. The sensor shows a fast reduction of the electrical
resistance after acetone exposure. In addition, this sensor is able
to quickly and fully recover the baseline resistance after each pulse,
displaying a perfect reversible behavior. Figure 12b shows the calibration curve extrapolated
by the above transient responses. In the range of investigated concentration,
the response follows a typical log–log behavior, which can
be fitted by eq 3 3
Figure 12 (a) Transient response of the SBC2-based sensor during
consecutive exposures ranging from 1 to 40 ppm of acetone in dry air
at the operating temperature of 150 °C; (b) calibration curve.
In eq 3, S is the response and c is the concentration of acetone.
The determination coefficient (R2 = 0.994)
suggests a good linear trend between the logarithm of response and
the logarithm of concentration, in the studied range. Using this data,
a limit of detection lower than 100 ppb of acetone can be estimated,
that is 5 times lower compared to the actual state-of-the-art TiO2-based sensors reported in the literature (i.e., 500 ppb).47
Aiming at exploring the reliability and
stability of the sensor,
the reproducibility of response was investigated by recording consecutive
pulses of acetone in the same and different days, respectively. Figure S9a displays the perfect repeatability
and reversibility of response when the sensor was exposed to five
consecutive pulses of 5 ppm of acetone in air. In addition, as observed
in Figure S9b, the response to 20 ppm acetone,
recorded during 3 different days after various cycles of heating–cooling
and exposure to different gases, is almost similar, also suggesting
excellent long-time reproducibility and stability of the sensing material.
The selectivity of the sensor was also investigated at the optimal
operating temperature for acetone, by analyzing the response toward
common organic and inorganic gases. The sensor shows low response
to typical concentration of the investigated gases (Figure 13a). Only the response to ethanol
at the same concentration of the acetone was very similar, suggesting
this sensor as a possible candidate for VOCs detection. Finally, in
practical applications, acetone coexists with humidity, whose typical
aftermath is to decrease the sensitivity of the sensor toward VOCs.
The effect of humid air was thus evaluated:48Figure 13b shows
a comparison of calibration curves recorded in dry and humid air (50%
RH at 25 °C) operating at the temperature of 150 °C. The
presence of humidity causes a decrease in response to acetone from
2- to 5-folds compared to that obtained in dry condition. Regardless
of that, the sensor was still able to show appreciable response to
a concentration of acetone as low as 500 ppb.
Figure 13 (a) Gas responses of
the SBC2-based sensor toward
common reducing and oxidizing gases in dry air, operating at 150 °C;
(b) comparison of SBC2-based sensor responses toward
different concentrations of acetone in dry and humid air (50 RH %
at 25 °C) at the operating temperature of 150 °C.
3 Conclusions
Inspired by the Land of the Rising Sun, TiO2 NPs have
been decorated with one part of silver to three parts of copper—Shibuichi. This made a multifunctional nanomaterial, which
shows simultaneously photochromism and gas-sensing abilities. It has
been shown that photochromism might be triggered by UV-A and, most
strikingly, also visible light. However, two distinct phenomena are
responsible of the same effect. When using a UV-A lamp (i.e., an energy
≥ Eg), photocatalysis sensu
strictu happened to activate photochromism. On the other
hand, when employing a visible light, a photosensitization of Cu(II)/TiO2 system happens, triggering photochromism. Gas-sensing tests
showed that the modification of TiO2 NPs with Ag + Cu leads
to an improvement of the transient response to acetone, shortening
the response an recovery times in comparison to the pure TiO2-based sensor even working at a relatively low temperature of 150
°C. Furthermore, it also exhibited a lower detection limit for
acetone (5 times lower) compared to state-of-the-art TiO2-based sensors reported in the literature, for example, 100 ppb in
this work versus 500 ppb in previous work. Still, among the Shibuichi samples, a gas sensor based on TiO2 decorated with 2 mol % Ag + Cu showed excellent sensing performance
toward VOCs, exhibiting good sensitivity, stability, and selectivity
in comparison with other inorganic gases, as well as capability of
being implemented at lower operating temperature. All these characteristics
together make our material attractive for real commercial application.
4 Experimental Section
4.1 Sample Preparation
An adapted aqueous
sol–gel method, developed by the authors, was used for the
synthesis of TiO2-based nanomaterials; precise detail of
it can be found elsewhere.49 To do the
Ag/Cu-modified TiO2, stoichiometric amounts of silver nitrate
(1 M aqueous solution, Sigma-Aldrich) and copper(II) nitrate trihydrate
(Aldrich, ≥98.5%) were added to the sol, which had a concentration
of 1 M Ti4+. The Ag/Cu molar ratio was strictly constrained
to be 1:3, to follow the Shibuichi formulation. Four
Ag/Cu-modified sols were prepared, with (Ag + Cu) molar amounts equal
to 1, 2, 5 and 10 mol % [i.e., in the case of (Ag + Cu) = 1 mol %,
Ag molar amount was 0.25 mol %, and Cu was 0.75 mol %, with Ag/Cu
= 0.25:0.75 = 1:3]. Afterward, dried gels were thermally treated at
450 °C under a static air flow, using an electric muffle furnace.
The heating/cooling rate was 5 °C min–1, with
a 2 h dwell time at the selected temperature. Samples were referred
to as Ti450 (unmodified TiO2), SBC1 (Ag + Cu = 1 mol %), SBC2 (Ag + Cu = 2 mol %), SBC5 (Ag + Cu = 5 mol %), and SBC10 (Ag + Cu
= 10 mol %).
4.2 Sample Characterization
Information
about the microstructure of the specimens was attained via advanced
X-ray methods. The Rietveld method was used to obtain semiquantitative
information about the phase composition of the samples (i.e., not
accounting for the presence of amorphous fraction). XRD patterns for
QPAs were recorded on a θ/θ diffractometer (PANalytical
X’Pert Pro, NL), equipped with a fast RTMS detector (PIXcel
1D, PANalytical), with Cu Kα radiation (45 kV and 40 mA, 20–80°
2θ range, with a virtual step scan of 0.02° 2θ and
a virtual time per step of 200 s). Rietveld refinements were accomplished
by means of GSAS-EXPGUI software suite,50,51 following
the refining strategy that we reported previously;31 structure models of anatase, rutile, and brookite were
taken from the literature.52−54 WPPM formalism,55 through the PM2K software package,56 was used to extract microstructural information from the XRD data.
In this latter case, aiming to manipulate data with a high signal-to-noise
ratio, XRD patterns were recorded in the same instrument and setup
as described above, but in the 20–145° 2θ range,
with a virtual step of 0.1° 2θ, and virtual time per step
of 500 s. The instrumental contribution was obtained by parameterizing
the profile of 14 hkl reflections from the NIST SRM
660b standard (LaB6), according to the Caglioti et al.
relationship.57 The following parameters
were refined: background (modeled with a sixth-order Chebyshev polynomial),
peak intensities, specimen displacement, lattice parameters, and mean
and variance of the size distributions. Crystalline domains were approximated
to be spherical with their diameter distributed according to a lognormal
curve.
HR-STEM experiments were performed using an FEI Titan
low-base microscope operated at 300 kV and equipped with an EDS detector,
a CESCOR Cs probe corrector, an ultrabright X-FEG electron source,
and a monochromator. HR-STEM imaging was performed using HAADF and
ADF detectors. The inner and outer angles for most of the micrographs
recorded with the HAADF and ADF detector were 48 and 200 mrad and
22 and 120 mrad, respectively. Automatic indexation of the FFT patterns
was performed by using the JEMS software.58 For TEM studies, samples were dispersed in ethanol in an ultrasound
bath for a few minutes and a drop of the suspension was placed onto
a molybdenum/nickel grids coated with carbon membrane.
Optical
properties of the specimens were investigated by means
of DRS on a Shimadzu UV-3100 spectrometer (JP), equipped with an integrating
sphere, and a white reference material made of Spectralon; the UV–Vis
spectral range (250–850 nm) was investigated, with 0.2 nm in
resolution. To explore the photochromic properties of the specimens,
they were exposed (0.1 g), for different irradiation times, to either
UV-A or visible light. A protocol described in more detail in our
previous works10,11,31 was severely followed to get comparable data. The UV-A and visible-light
lamps were placed above (vertically) the specimen, adjusting the distance
between the lamp and the specimen to get the desired irradiance values.
The intensity of the radiation reaching the samples, measured with
a radiometer (Delta OHM, HD2302.0, IT), was estimated to be ∼22
W m–2 in the UVA range (315 nm < λ <
400 nm) and ∼50 W m–2 in the visible region
(λ > 400 nm, being nil in the UVA); irradiation times were
considered
to be consecutive and absolute. Reflectance data were transformed
into pseudo-absorption spectra F(R) by means of the Kubelka–Munk transformation:59F(R) = α
= (1 – R)2/2R,
where R is the reflectance. To explore the reversibility
of the photochromic process, fresh un-irradiated samples were exposed
to visible light (as above) for periods ranging from 10 to 30 s, at
room temperature, and their DRS spectra were recorded immediately.
They were then placed in a dark oven at 100 °C for 15 min to
reverse the process, and the optical spectra were measured again.
The degree of photoswitching has been described as the difference
between the maximum value in reflectance at time zero (R0) and the reflectance after each irradiation/annealing
cycle (Rt): ΔRt (%) = (R0 – Rt)/R0 × 100. Raman spectra were measured
using a RFS 100/S (Bruker, DE) equipped with a 1064 nm Nd:YAG laser
as the excitation source, in the 50–1000 cm–1 wavenumber range, with 2 cm–1 resolution.
4.3 Gas Sensing
Gas-sensing performance
of the synthesized materials was investigated by fabricating resistive
gas sensor devices. The screen printing method has been used to make
reproducible thick films (3 × 3 mm2 area, and ∼10
μm in thickness). The synthesized nanopowders were mixed with
an appropriate volume of double distilled water to obtain a paste.
Appropriate water amounts have been added to have an ink paste with
suitable rheological properties. Then, the ink has been deposited
by means of a hand screen printer over the interdigitated area of
the sensor. This latter was made of an alumina substrates (6 ×
3 mm2 × 0.5 mm), supplied by a pair of Pt interdigitated
electrodes on one side and a Pt heater on the other side. The film
has been printed with the appropriate geometric characteristic by
using a proper plastic mask.
Sensing measurements were carried
out in the range of temperature 100–400 °C under a controlled
atmosphere, by placing the sensors in an optimized stainless steel
test chamber where a constant gas steam of 100 scc/min was allowed
to flow. All gases and acetone vapor (coming from certified bottles)
can be progressively diluted in air using mass flow controllers, in
order to obtain the desired working concentrations. Electrical resistance
of the sensitive films was recorded by a Keithley 6487 picoammeter/voltage
source, while an Agilent 3632A was employed to power the heater of
the sensor substrate in order to control the operating temperature.
The gas sensor response, S, is defined as the ratio Rair/Rg, where Rair is the electrical resistance of the sensor
in reference air (baseline resistance) and Rg is the electrical resistance at the fixed target gas concentration.
The response and recovery times, unless otherwise indicated, were
calculated at 90% of response variation.
Supporting Information Available
The Supporting Information is
available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b01508.Graphic output
of the Rietveld refinement of the sample SBC1; graphic
output of the WPPM modeling of SBC1; HR-STEM–HAADF
micrographs (samples Ti450 and SBC10); DRS
spectra of irradiated samples (UV-A and visible
light); Raman spectra before and after UV-A irradiation; response
time at 90% signal variation as a function of temperature (Ti450- and SBC2-based sensors); recovery times of Ti450- and SBC2-based sensors; reproducibility of the SBC2-based sensor; and position and full width half-maximum
of Raman Eg mode of anatase (PDF)
Supplementary Material
ao8b01508_si_001.pdf
Author Present Address
# Departamento de Ciencia de los Materiales e Ingeniería Metalúrgica
y Química Inorgánica, Facultad de Ciencias, Universidad
de Cádiz, Campus Río San Pedro S/N, Puerto Real 11510,
Cádiz, Spain.
Author Present Address
¶ Instituto
Universitario de Investigación de Microscopía
Electrónica y Materiales (IMEYMAT), Facultad de Ciencias, Universidad
de Cádiz, Campus Río San Pedro S/N, Puerto Real 11510,
Cádiz, Spain.
The authors
declare no competing financial interest.
Acknowledgments
This work was developed within the scope of the
project CICECO–Aveiro Institute of Materials, POCI-01-0145-FEDER-007679
(FCT Ref. UID/CTM/50011/2013), financed by national funds through
the FCT/MEC and when appropriate co-financed by FEDER under the PT2020
Partnership Agreement. The STEM measurements were performed in the
Laboratorio de Microscopias Avanzadas (LMA) at the Instituto de Nanociencia
de Aragon (INA)—Universidad de Zaragoza (Spain). R.A. gratefully
acknowledges the support from the Spanish Ministerio de Economia y
Competitividad (MAT2016-79776-P), from the Government of Aragon, and
the European Social Fund under the project “Construyendo Europa
desde Aragon” 2014–2020 (grant number E/26).
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145880010.1021/acsomega.8b01065ArticleSynthesis of (Arylmido)niobium(V) Complexes Containing
Ketimide, Phenoxide Ligands, and Some Reactions with Phenols and Alcohols Srisupap Natta Wised Kritdikul Tsutsumi Ken Nomura Kotohiro *Department of Chemistry,
Faculty of Science, Tokyo Metropolitan University, 1-1 Minami Osawa, Hachioji, Tokyo 192-0397, Japan* E-mail: ktnomura@tmu.ac.jp.07 06 2018 30 06 2018 3 6 6166 6181 19 05 2018 28 05 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under a Creative Commons Non-Commercial No Derivative Works (CC-BY-NC-ND) Attribution License, which permits copying and redistribution of the article, and creation of adaptations, all for non-commercial purposes.
Reactions
of Nb(NAr)(N=CtBu2)3 (3a, Ar = 2,6-Me2C6H3) with 1.0, 2.0, or 3.0 equiv of Ar′OH
(Ar′ = 2,6-iPr2C6H3) afforded Nb(NAr)(N=CtBu2)2(OAr′), Nb(NAr)(N=CtBu2)(OAr′)2,
or Nb(NAr)(OAr′)3, respectively (at 25 °C),
whereas the reaction with 2.0 equiv of 2,6-tBu2C6H3OH afforded Nb(NAr)(N=CtBu2)2(O-2,6-tBu2C6H3) upon heating (70 °C) without the formation of bis(phenoxide)
and the reaction of 3a with 2.0 equiv of 2,4,6-Me3C6H2OH afforded Nb(NAr)(N=CtBu2)(O-2,4,6-Me3C6H2)2(HN=CtBu2). Similar reactions of 3a with 1.0 equiv of (CF3)3COH or 2.0 equiv of
(CF3)2CHOH afforded Nb(NAr)(N=CtBu2)2[OC(CF3)3](HN=CtBu2)
or Nb(NAr)(N=CtBu2)[OCH(CF3)2]2(HN=CtBu2), respectively. On the basis of their structural
analyses and the reaction chemistry, it was suggested that these reactions
proceeded via coordination of phenol (alcohol) to Nb and the subsequent
proton (hydrogen) transfer to the ketimide (N=CtBu2) ligand. The reaction of Nb(NAr)(N=CtBu2)2(OAr′)
with 1.0 equiv of 2,4,6-Me3C6H2OH
gave the disproportionation products Nb(NAr)(N=CtBu2)(OAr′)2 and Nb(NAr)(N=CtBu2)(O-2,4,6-Me3C6H2)2(HN=CtBu2) with 1:1 ratio, clearly indicating
the presence of the above mechanism and the fast equilibrium (between
the ketimide and the phenoxide). The reaction of 3a with
1.0 or 2.0 equiv of C6F5OH afforded Nb(N=CtBu2)2(OC6F5)3(HN=CtBu2) as the sole isolated product, which was formed from
once generated Nb(NAr)(N=CtBu2)2(OC6F5)(HN=CtBu2) by treating with C6F5OH.
document-id-old-9ao8b01065document-id-new-14ao-2018-010659ccc-price
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Introduction
Arylimido ligands have
been widely used to stabilize the high-oxidation-state
early transition-metal complexes,1−10 which are especially used as catalysts or catalyst precursors for
carbon–carbon bond formation exemplified in olefin metathesis,6−10 and olefin polymerization.11,12 Introduction of a steric
bulk in the arylimido ligand should be effective not only to stabilize
the oxidation state, but also to avoid the formation of dimeric species
through the bridged imido ligand or certain dimeric decomposition
pathways in metal-alkylidenes;4,6−9 the ligand modification is also effective to control the electronic
nature through the metal–nitrogen double bond.6−8,10,13 Monodentate anionic ancillary donor ligands (such as phenoxy,10,14−16 ketimide,15−19 imidazolin-2-iminato,20 and others15,16,21,22) have also been known to play a role to stabilize the oxidation
state as well as control of electronic/steric natures by the ligand
modification.10,15,16
Studies on the synthesis and some reaction chemistry of half-sandwich
niobium complexes containing arylimido ligands,23−31 which would exhibit metallocene-like reactivity through the “isolobal”
relationship,25 were known. Moreover, synthesis
of some (called nonmetallocene type) (arylimido)niobium(V) complexes,32−40 especially those containing monoanionic chelate guanidinato ligand
(Scheme 1),37−39 was also known. However, in contrast to a number of reports of (tert-butyl-imido)niobium complexes especially containing
β-diketiminate ligand (Scheme 1),41−44 reports concerning the synthesis and reaction chemistry of (arylimido)niobium(V)
complexes containing “monodentate” anionic ancillary
donor ligands still have been limited so far (Scheme 1).32−34,40 Since certain (arylimido)vanadium(V) complexes containing anionic
donor ligands (such as phenoxy, ketimide, imidazoline-iminato) exhibit
promising characteristics as catalysts or catalyst precursors for
olefin metathesis9,10,13,45 and coordination/insertion polymerization12,46−49 and also (arylimido)niobium(V)-alkylidene complexes containing fluorinated
alkoxo ligand catalyze metathesis polymerization of cyclic olefins
and disubstituted acetylene (Scheme 1),40 synthesis and some
reactions of (arylimido)niobium(V) complexes containing ketimide and
aryloxo ligands have been a promising subject.50−52
Scheme 1 Reported
Examples for (Arylimido)niobium(V) Complexes,32−34,38−40 and Selected
Four-, Five-, and Six-Coordinate (t-Butylimido)niobium
Complexes41,42
In this study, we thus focus on the synthesis of (arylmido)niobium(V)
complexes containing ketimide (N=CtBu2) ligand, not only because use of this ligand plays
a role to stabilize the oxidation state,50 as demonstrated by the synthesis of a series of (arylimido)vanadium(V)
complexes,9,53−55 but also because, as
described below, the solvent-free tris(ketimide) complex, Nb(NAr)(N=CtBu2)3 (3a), could be isolated from Nb(NAr)Cl3(dme) (Ar = 2,6-Me2C6H3, dme = 1,2-dimethoxyethane) and
subsequent substitution with phenol was expected.54,55
Moreover, on the basis of the reaction chemistry of V(NAr)Me(N=CtBu2)2 with phenols,
it was demonstrated that the reactions of ketimide with phenols proceed
by coordination with phenol and not by protonation (protonolysis,
H+) and also proceed by coordination of phenol to the electron-deficient
metal center trans to the methyl group to give a pentacoordinated
trigonal bipyramidal species and subsequent proton (hydrogen) transfer
to the aryloxide/ketimide affording ketimine/phenol dissociation.55−58 Therefore, we herein present our explored reaction chemistry of
the (arylimido)niobium(V)-ketimide complexes with phenols and the
unique contrast in the reactivity between the vanadium and niobium
complexes.
Results and Discussion
Synthesis of (Arylimido)niobium(V) Complexes
Containing Phenoxide,
Ketimide Ligands, and Some Reactions with Phenols and Fluorinated
Alcohols
Reactions of (imido)niobium(V) trichloride, Nb(NR′)Cl3(dme) [R′ = 2,6-Me2C6H3 (Ar),40 2,6-iPr2C6H3 (Ar′),32,33 1-adamantyl (Ad),32,33 dme = 1,2-dimethoxyethane] with
LiOAr′ in Et2O afforded corresponding Nb(NR′)Cl2(OAr′)(dme) (Scheme 2, R′ = Ar (1a), Ar′ (1b), Ad (1c)) in high yields (76–84%),
and the reaction of Nb(NAr)Cl3(dme) with Li(O-2,6-Ph2C6H3) also afforded Nb(NAr)Cl2(O-2,6-Ph2C6H3)(dme) (1d).a These complexes were identified by NMR
spectra and elemental analysis (except 1b),a and the structures of 1a and 1d were determined by X-ray crystallography as a distorted octahedral
geometry around niobium.b It turned out that
both 1a and 1d showed low catalytic activities
for ethylene polymerization in the presence of methylaluminoxane (MAO)
(activities for 1a and 1d = 23 and 12 kg
PE/(mol Nb h), respectively, ethylene 8 atm at 25 °C for 1 h).c The reason for the low catalytic activities would
be coordination of dme, which seems difficult to cleave from Nb, as
described below.
Scheme 2 Synthesis of (Imido)niobium(V) Complexes Containing
Aryloxide, Ketimide,
and Triflate (OTf) Ligands (Detailed Synthetic Procedures Are Shown
in the Supporting Information (SI))a,b
It turned out that dme was strongly coordinated
to Nb in CDCl3 even at 100 °C (variable-temperature
spectra are shown
in Figure S2-1, Supporting Information
(SI)),a and attempted treatments of 1a with NiBr2 or ZnCl2 (3 equiv) in toluene at
50 °C recovered 1a. Treatment of 1a with 2 equiv of AgOTf (OTf = CF3SO3) in CH2Cl2 afforded corresponding Nb(NAr)(OAr′)(OTf)2(dme) (2a) without liberation of dme (Scheme 2); 2a was identified by NMR spectra and elemental analysis.a Similarly, Nb(NAr)Cl3(dme) was treated with 3
equiv of AgOTf in CH2Cl2 to afford Nb(NAr)(OTf)3(dme) (2b), which was also isolated as the sole
product confirmed by NMR spectra.a Structure
of 2a was suggested on the basis of that of 1a (confirmed by X-ray crystallography) and the NMR spectra, but two
resonances were observed in the 19F NMR spectrum when the
CDCl3 solution was kept at room temperature (25 °C)
for 21 h, probably due to isomerization of the OTf ligand (trans to
cis, the spectra are shown in Figure S2-3, SI).a
In contrast, reactions of Nb(NAr)Cl3(dme) with 3.0 equiv
of Li(N=CtBu2) in toluene
afforded the corresponding four-coordinate tris(ketimide) analogue,
Nb(NAr)(N=CtBu2)3 (3a), and treatment of NbCl5 with
3.0 equiv of Li(N=CtBu2) in toluene also afforded trans-NbCl2(N=CtBu2)3 (3b) as the sole isolated product (Scheme 2).a These
complexes (3a and 3b) were identified by
NMR spectra and elemental analysis.a
As
described in Introduction, reports concerning
synthesis and reaction chemistry of (arylimido)niobium(V) complexes
containing monodentate anionic donor ligands (without solvent coordination)
still have been limited (Scheme 1).32−34,40,50 Since the ketimide (N=CtBu2) ligand in the (arylimido)vanadium(V) complexes were known
to be replaced with phenoxide (alkoxide) upon addition of phenol (alcohol),
reactions of Nb(NAr)(N=CtBu2)3 (3a) with phenols were thus conducted.a
It turned out that reaction of 3a with 1.0 equiv of
Ar′OH in n-hexane afforded the mono phenoxide,
Nb(NAr)(N=CtBu2)2(OAr′) (4a), as the sole isolated product
(Scheme 3).a The similar reactions with 2.0 and 3.0 equiv of
Ar′OH afforded the corresponding bis- and tris(phenoxide) complexes,
Nb(NAr)(N=CtBu2)(OAr′)2 (5) and Nb(NAr)(OAr′)3 (6), respectively, in high yields (Scheme 3);a the reaction of
Nb(NAr)Cl3(dme) with 3.0 equiv of LiOAr′ in Et2O also afforded 6. Complexes 4a, 5, and 6 were identified by NMR spectra and elemental
analysis, and the structure of 4a was determined by X-ray
crystallography (Figure 1).a,d
Figure 1 ORTEP drawings
for Nb(N-2,6-Me2C6H3)(N=CtBu2)2(O-2,6-iPr2C6H3) (4a, left) and Nb(N-2,6-Me2C6H3)(N=CtBu2)2(O-2,6-tBu2C6H3OH) (4b, right). Thermal ellipsoids
are drawn at the 50% probability level, and H atoms are omitted for
clarity. Detailed analysis data are shown in the Supporting Information.d
Scheme 3 Reactions of Nb(N-2,6-Me2C6H3)(N=CtBu2)3 (3a) with Phenols (Detailed Synthetic Procedures
Are Shown in the Supporting Information)a
In contrast, the similar reaction of 3a with
1.0 equiv
2,6-tBu2C6H3OH (in n-hexane at 25 °C) afforded a
mixture of 3a and the corresponding mono phenoxide, Nb(NAr)(N=CtBu2)2(O-2,6-tBu2C6H3) (4b), even after stirring overnight (Figure S2-4, SI).a The reaction did not reach
full conversion of 3a upon heating at 70 °C overnight,
and 4b could be isolated from the mixture after purification,
including separation of 2,6-tBu2C6H3OH by extraction of 4b with n-hexane.a It turned out that monitoring
the reaction of 3a with 2.0 equiv of 2,6-tBu2C6H3OH at 70
°C (by 1H NMR spectra in C6D6) showed resonances ascribed to 4b (and those in the
phenol) solely with complete conversion of 3a, and further
reaction did not take place even after 1 week (Figures S2-5 and S2-6, SI).a Moreover, 1H NMR spectrum of the reaction of 3a with 2.0
equiv of 2,6-tBu2C6H3OH in toluene-d8 at 100
°C for 1 day also showed resonances ascribed to 4b with complete conversion of 3a (Figure S2-8).a Complex 4b was identified by NMR spectra and elemental analysis, and the structure
was determined by X-ray crystallography (Figure 1).a,d As shown in Scheme 3, the resultant complexes (4a, 4b, 5, and 6) are four-coordinate (arylimido)niobium
complexes without coordination of HN=CtBu2 (product by reaction with phenol).
In
contrast, it should be noted that the similar reaction of 3a with 1.0 equiv of C6F5OH in n-hexane afforded Nb(N=CtBu2)2(OC6F5)3(HN=CtBu2) (7, isolated
from the mixture), and the same reaction with 2.0 equiv
of C6F5OH also afforded 7 as the
sole isolated product from the mixture (Scheme 4, 33% isolated yield). The results clearly
suggest that the reaction of arylimido ligand in 3a with
C6F5OH took place, whereas the reaction of the
ketimide ligand in 3a cleanly took place with 2,6-iPr2C6H3OH,
2,6-tBu2C6H3OH (and 2,4,6-Me3C6H2OH shown
below). The complex 7 was identified by NMR spectra and
elemental analysis, and the structure was determined by X-ray crystallographic
analysis.a,d
Scheme 4 Reactions of Nb(N-2,6-Me2C6H3)(N=CtBu2)3 (3a) with C6F5OH, (CF3)3COH, and (CF3)2CHOH (Detailed Synthetic Procedures
Are Shown in the Supporting Information)a
It turned out that reactions of 3a with 1.0
equiv
of (CF3)3COH afforded the mono alkoxide, Nb(NAr)(N=CtBu2)2[OC(CF3)3](HN=CtBu2) (8), which coordinates HN=CtBu2 to Nb trans to the arylimido ligand (Scheme 4). The fact could
strongly suggest that (CF3)3COH coordinates
to Nb through the N(arylimido)–N(ketimide)–N(ketimide)
face and the ligand exchange took place with proton transfer (not
protonation) from (CF3)3COH to the ketimide
ligand. However, it was difficult to reach complete conversion of 3a upon heating monitored by 1H NMR spectra, and
the reaction reached 50% conversion of 3a when the mixture
was heated at 40 °C overnight. In contrast, the reaction of 3a with 2.0 equiv of (CF3)2CHOH in n-hexane (at 25 °C) afforded the bis(alkoxide), Nb(NAr)(N=CtBu2)[OCH(CF3)2]2(HN=CtBu2) (9, Scheme 4). The complexes 8 and 9 were identified
by NMR spectra and elemental analysis, and their structures were determined
by X-ray crystallography (Figure 2).a,d It is thus clear that the reaction with the arylimido ligand
did not take place, whereas the reaction with the arylimido ligand
took place in the reaction of 3a with C6F5OH (described above). It also turned out that coordinated
HN=CtBu2 in 9 could be removed by treatment with NiBr2 (ca. 3 equiv)
in toluene; the 1H NMR spectrum of the reaction mixture
(after filtration and removal of toluene) suggested the formation
of Nb(NAr)(N=CtBu2)[OCH(CF3)2]2 (10) due to disappearance
of resonances ascribed to tBu protons
(and shift of resonances in 19F NMR spectra, Figures S1-28 and S1-29, SI).a
Figure 2 ORTEP drawings for Nb(N-2,6-Me2C6H3)(N=CtBu2)2[OC(CF3)3](HN=CtBu2) (8, left), Nb(N-2,6-Me2C6H3)(N=CtBu2)[OCH(CF3)2]2(HN=CtBu2) (9, middle),
and Nb(N-2,6-Me2C6H3)(N=CtBu2)2(OC6F5)(HN=CtBu2) (11, right). Thermal ellipsoids are drawn at the 50%
probability level, and H atoms are omitted for clarity. Detailed analysis
data are shown in the Supporting Information.d
To explore why reaction of 3a with C6F5OH afforded Nb(N=CtBu2)2(OC6F5)3(HN=CtBu2) (7) as the isolated
product, we conducted reaction of 3a with 0.50 equiv
of C6F5OH under diluted conditions (details
are shown in the SI).a Interestingly, upon careful dropwise addition of n-hexane solution containing C6F5OH under diluted
conditions at −30 °C, the reaction mixtures consisted
of Nb(N-2,6-Me2C6H3)(N=CtBu2)2(OC6F5) (11), which could be isolated from the
mixture and was identified by NMR spectra and X-ray crystallographic
analysis, and 3a was monitored by NMR spectra (Scheme 5, data shown in Figures S2-9–12, SI).a,d The results strongly suggest
that the reaction to afford 7 proceeded via formation
of 11 as the initial product, which would be formed by
coordination of C6F5OH to Nb through N(arylimido)-N(ketimide)-N(ketimide)
face in 3a (and the subsequent proton transfer from C6F5OH to the ketimide ligand). In fact, further
careful experiments of dropwise (and two- or three-step) addition
of C6F5OH afforded 11 even in the
reaction with 0.8 equiv of C6F5OH (monitored
by NMR spectra, Figures S2-13 and S2-14, SI).a Importantly, after the above experimental
procedure (careful three-step addition of C6F5OH under highly diluted conditions), further addition of 1.0 equiv
of C6F5OH afforded Nb(N=CtBu2)2(OC6F5)3(HN=CtBu2) (7) as the major observed product on NMR spectra (Scheme 5, Figures S2-15 and S2-16, SI).a Although
the equivalence of C6F5OH was uncertain, the
results could suggest that 7 was formed from the mono
phenoxide (11) by reaction with the arylimido ligand.
Scheme 5 Reactions of Nb(N-2,6-Me2C6H3)(N=CtBu2)3 (3a) with C6F5OH under Diluted Conditions (Detailed
Synthetic (Reaction) Procedures Are Shown in the Supporting Information)a
Structural Analysis of (Arylimido)niobium(V)
Complexes Containing
Phenoxide and Ketimide Ligands
Figure 1 shows ORTEP drawings for Nb(NAr)(N=CtBu2)2(O-2,6-iPr2C6H3) (4a) and Nb(NAr)(N=CtBu2)2(2,6-tBu2C6H3OH) (4b) determined by X-ray
crystallography,d and the selected bond distances
and angles are summarized in Table 1. These complexes fold a distorted tetrahedral geometry
around Nb, and the Nb–N(1) distances in the imido ligands for 4a and 4b [1.783(3) and 1.790(9) Å, respectively]
are rather longer than those in Nb(NAr)Cl2(O-2,6-iPr2C6H3)(dme) (1a) [1.7643(15) Å] and Nb(NAr)Cl2(O-2,6-Ph2C6H3)(dme) (1d) [1.7569(16)
Å] (shown in the SI)b and Nb(N-2,6-iPr2C6H3)(NMe2)2[η3-tBuNC(NMe2)NEt] (shown in Scheme 1, 1.768(3) Å),39 but are close to that in Nb(N-2,6-iPr2C6H3)(NMe2)2[η2-(NMe2)C=NtBu] (shown in Scheme 1, 1.783(2) Å).38 The Nb–N(1)–C(arylimido) bond angles in 4a and 4b [174.5(2) and 170.1(7)°, respectively]
are rather smaller than those in 1a and 1d [176.53(12) and 175.74(14)°, respectively]b and Nb(N-2,6-iPr2C6H3)(NMe2)2[η2-(NMe2)C=NtBu] [177.3(2)°],38 but larger than that in Nb(N-2,6-iPr2C6H3)(NMe2)2[η3-tBuNC(NMe2)NEt] [167.3(2)°].39 The Nb–N bond distances in the ketimide ligands in 4a and 4b [Nb–N(2) and Nb–N(3):
1.946(8)–1.957(3) Å] are close to or slightly longer than
those reported [1.937(2) and 1.939(2)] in Nb(N=CtBu2)4,50 and the Nb–N–C bond angles [173.4(3)–178.9(3)°]
are close to those reported in Nb(N=CtBu2)4 [176.5(2)°].50
Table 1 Selected Bond Distances and Angles
for Complexes 4a, 4b, 8, 9, and 11d
4a 4b 8 9 11
Bond Distances
in Angstrom
Nb–O(1) 1.939(3) 1.965(7) 2.0642(13) 1.9986(12) 2.066(3)
Nb–O(2) 1.9879(14)
Nb–N(1)imido 1.783(3) 1.790(9) 1.7877(15) 1.790(2) 1.796(3)
Nb–N(2)ket 1.957(3) 1.946(8) 1.9647(18) 1.9399(16) 1.963(4)
Nb–N(3)ket 1.947(3) 1.949(8) 1.9670(17) 1.965(4)
Nb–N(H)CtBu2 2.5448(17), Nb(1)–N(4) 2.440(2), Nb(1)–N(3) 2.443(3), Nb(1)–N(4)
Bond Angles in
deg
Nb–O(1)–C(1) 168.6(2) 148.2(6) 145.75(11),
C(39) 134.76(12), C(27) 123.9(2), C(36)
Nb–O(2)–C 129.15(15),
C(30)
Nb–N(1)–C(imido) 174.5(2), C(13) 170.1(7), C(15) 177.56(13), C(1) 177.89(14), C(1) 170.1(3), C(1)
Nb–N(2)–C(ket) 173.4(3), C(21) 173.4(7), C(23) 178.00(17), C(9) 174.01(12), C(9) 175.6(3), C(9)
Nb–N(3)–C(ket) 178.9(3), C(30) 177.0(8), C(32) 177.13(14), C(23) 178.8(3), C(18)
Nb–N(4)H–C 159.78(14), Nb(1)–N(4)–C(18) 157.30(12), Nb(1)–N(3)–C(18) 160.7(3), Nb(1)–N(4)–C(27)
N(1)–Nb–O(1) 114.86(12) 112.3(3) 101.32(6) 98.64(7) 93.68(13)
N(1)–Nb–O(2) 98.38(7)
N(1)–Nb–N(2) 106.01(12) 102.9(4) 99.88(7) 99.42(8) 103.15(13)
N(1)–Nb–N(3) 104.88(12) 102.9(3) 99.14(7) 99.00(15)
N(1)–Nb–N(4) 174.27(6) 170.26(6), N(1)–Nb–N(3) 165.90(13)
N(2)–Nb–N(3) 118.09(12) 120.4(3) 125.68(7) 125.63(14)
O(1)–Nb–N(2) 107.28(11) 108.2(3) 111.69(6) 116.07(6) 111.40(13)
O(1)–Nb–N(3) 106.09(11) 109.9(3) 113.58(6) 115.97(12)
O(1)–Nb–N(4) 73.34(5) 72.16(6), O(1)–Nb(1)–N(3) 72.68(11)
83.62(6), O(2), –Nb(1)–N(3)
The Nb–O(1) bond distance in 4b [1.965(7) Å]
is longer than that in 4a [1.939(3) Å], but these
distances are longer than those in 1a [1.8878(12) Å]
but within the range of those in 1d [1.9231(9) Å],b NbCl2[(O-2,4-Me2C6H2-6-CH2)3N] [1.8838(19)–1.925(2)
Å],59 NbCl[2,2′-CH3CH(O-4,6-tBu2C6H2)2]2(CH3CN)2 [1.8768(18)–1.9355(18) Å],60 and CpNbCl[(O-C6H4-6-CH2)3N] [1.970(5)–2.009(6) Å].61 The Nb–O–C(phenyl) bond angles in 4a and 4b [114.86(12) and 112.3(3)°, respectively] are smaller
than those in 1a and 1d [158.00(10) and
159.159(6)°, respectively];b these values
are influenced by the steric bulk around the metal center.15,16
Figure 2 shows
ORTEP
drawings for Nb(NAr)(N=CtBu2)2[OC(CF3)3](HN=CtBu2) (8), Nb(NAr)(N=CtBu2)-[OCH(CF3)2]2(HN=CtBu2)(9), and Nb(NAr)(N=CtBu2)2(OC6F5)(HN=CtBu2) (11) determined
by X-ray crystallographic analysis,d and the
selected bond distances and angles are summarized in Table 1. These complexes fold a distorted
trigonal bipyramidal structure around niobium consisting of N(arylimido)–Nb–N(in
HN=CtBu2) axis [N(1)–Nb–N(4) (for 8 and 11) or N(1)–Nb–N(3) (for 9) bond
angles: 174.27(6), 165.90(13), and 170.26(6)°, respectively]
and a N–N(O)–O plane from alkoxide (or OC6F5) and N=CtBu2 ligand [sum of N(2)–Nb–N(3) or N(2)–Nb–O(2),
O(1)–Nb–N(2), and O(1)–Nb–N(3) or O(1)–Nb–O(2):
350.95° (8), 353.09° (9), 353.0°
(11)].
The Nb–N(arylimido) bond distances
in complexes 8, 9, and 11 [1.7877(15)–1.796(3)
Å] are longer than those in 1a and 1d [1.7643(15) and 1.7730(8) Å, respectively],b but close to those in 4a and 4b [1.783(3) and 1.790(9) Å, respectively]. The Nb–N(1)–C(phenyl)
bond angles in 8 and 9 [177.56(13) and 177.89(14)°,
respectively] are larger than those in 11 [170.1(3)°]
and 4a and 4b [174.5(2) and 170.1(7)°,
respectively] and are relatively close to those in 1a and 1d [176.53(12) and 175.806(3)°, respectively].b The Nb–N bond distances in the ketimide (N=CtBu2) ligand [1.9399(16)–1.9670(17)
Å] in 8, 9, and 11 are
within the range of 4a and 4b [1.946(8)–1.957(3)
Å], but apparently shorter than the Nb–N(H)=CtBu2 bond distances [2.440(2)–2.5448(17)
Å];d the Nb–N(4)–C or Nb–N(3)–C
bond angles in Nb–(H)N=CtBu2 [157.30(12)–160.7(3)°] are apparently
small compared to the Nb–N(2)–C bond angle in the ketimide
ligand [174.01(12)–178.8(3)°]. The Nb–O bond distances
in 8, 9, and 11 [1.9879(14)–2.066(3)
Å] are longer than those in 1a and 1d [1.8878(12) and 1.9231(9) Å, respectively],b4a and 4b [1.939(3) and 1.965(7)
Å, respectively], and NbCl2[(O-2,4-Me2C6H2-6-CH2)3N]
[1.8838(19)–1.925(2) Å],59 but
close to those in CpNbCl[(O-C6H4-6-CH2)3N] [1.970(5)–2.009(6) Å].61
As shown in Figure 3, ORTEP drawing for Nb(N=CtBu2)2(OC6F5)3(HN=CtBu2) (7), the complex
folds a distorted octahedral geometry around niobium, and both OC6F5 ligands and two of ketimide (N=CtBu2) ligands are positioned trans
[172.10(14), 168.32(12)°]. These four ligands fold a plane [sum
of O(1)–Nb–N(2), N(2)–Nb–O(3), O(3)–Nb–N(3),
and O(1)–Nb–N(3): total 360.97°] against the O(in
OC6F5)–Nb–N(in HN=CtBu2) axis [O(2)–Nb–N(1):
178.35(14)°]. The Nb–O bond distances [1.950(3)–1.976(3)
Å] are within the range of those introduced above, and the Nb–N
bond distances in the ketimide ligands [1.965(3) and 2.098(4) Å]
are shorter than the Nb–(H)N=CtBu2 bond distance [2.234(4) Å], clearly suggesting
a difference of nature of anionic donor or neutral donor ligand.
Figure 3 ORTEP
drawings for Nb(N=CtBu2)2(OC6F5)3(HN=CtBu2) (7). Thermal
ellipsoids are drawn at the 50% probability level, and H atoms are
omitted for clarity. Detailed analysis data are shown in the Supporting Information. Selected bond distances
in 7 (Å): Nb(1)–N(1) 1.965(3), Nb(1)–N(2)
2.098(4), Nb(1)–N(3) 2.234(4), Nb(1)–O(1) 1.950(3),
Nb(1)–O(2) 1.996(3), Nb(1)–O(3) 1.976(3). Selected bond
angles in 7 (deg): Nb(1)–N(1)–C(1) 178.7(3),
Nb(1)–N(2)–C(10) 167.1(3), Nb(1)–N(3)–C(19)
163.0(3), Nb(1)–O(1)–C(28) 168.3(3), Nb(1)–O(2)–C(34)
177.3(3), Nb(1)–O(3)–C(40) 173.3(3), N(1)–Nb(1)–N(2)
96.51(15), N(1)–Nb(1)–N(3) 95.04(14), N(2)–Nb(1)–N(3)
168.32(12), O(1)–Nb(1)–N(1) 87.80(13), O(1)–Nb(1)–N(2)
91.66(14), O(1)–Nb(1)–N(3) 90.48(13), O(1)–Nb(1)–O(2)
93.10(12), O(1)–Nb(1)–O(3) 172.10(14), O(2)–Nb(1)–O(3)
91.66(12), O(2)–Nb(1)–N(1) 178.35(14), O(2)–Nb(1)–N(2)
84.84(13), O(2)–Nb(1)–N(3) 83.58(13), O(3)–Nb(1)–N(1)
87.29(13), O(3)–Nb(1)–N(2) 95.04(14), O(3)–Nb(1)–N(3)
83.79(13).
Exploration for Reaction
Mechanisms of Nb(NAr)(N=CtBu2)3 (3a) and Nb(NAr)(N=CtBu2)2(O-2,6-iPr2C6H3) (4a) with Phenols
As
described above, the reaction of Nb(NAr)(N=CtBu2)3 (3a) with 1.0 or 2.0
equiv of 2,6-iPr2C6H3OH in n-hexane afforded Nb(NAr)(N=CtBu2)2(O-2,6-iPr2C6H3) (4a) or Nb(NAr)(N=CtBu2)(O-2,6-iPr2C6H3)2 (5), respectively, as the
sole isolated product, whereas similar reactions with 2,6-tBu2C6H3OH (2.0 equiv)
afforded Nb(NAr)(N=CtBu2)2(O-2,6-tBu2C6H3) (4b, Scheme 6) upon heating. On the basis of reactions
of 3a with fluorinated alcohols (and C6F5OH under dilute conditions), these reactions would proceed
via coordination of phenol (or alcohol) to Nb through the N(arylimido)–N(ketimide)–N(ketimide)
face in 3a and the subsequent proton transfer from the
phenol (or alcohol) to the ketimide (N=CtBu2) ligand, without accompanying protonolysis of
the N=CtBu2 group with
the alcohols (phenols). Although, as described in Introduction, this is the similar hypothesis confirmed in
the reactions of V(NAr)Me(N=CtBu2)2 with phenols affording another methyl complex54 and the reaction of V(CHSiMe3)(NAd)(CH2SiMe3)(PMe3)2 with phenol;57 however, the reaction chemistry in the niobium
complexes have never been reported. We thus conducted reaction of 4a with a different phenol (2,4,6-Me3C6H2OH) to get some information concerning the mechanism.
Scheme 6 Reactions of Nb(N-2,6-Me2C6H3)(N=CtBu2)3 (3a) with 2.0 equiv of Phenols (Detailed Synthetic Procedures Are Shown
in the Supporting Information)a
It turned out that
the reaction of 3a with 2.0 equiv
of 2,4,6-Me3C6H2OH in n-hexane afforded the corresponding bis(phenoxide) with coordination
of HN=CtBu2, Nb(NAr)(N=CtBu2)(O-2,4,6-Me3C6H2)2(HN=CtBu2) (12, Scheme 6), identified by NMR spectra and elemental
analysis.a As observed in 9, treatment
of the complex 12 with NiBr2 (ca. 3 equiv)
in toluene (at 25 °C for 3 days) would afford Nb(NAr)(N=CtBu2)(O-2,4,6-Me3C6H2)2 (13) due to disappearance
of resonances ascribed to methyl protons in the 1H NMR
spectrum of the reaction mixture (after filtration and removal of
toluene, Figure S1-32, SI).a
We note that the reaction mixture of 4a with 1.0 equiv
of 2,4,6-Me3C6H2OH in n-hexane (after 2 h) afforded a 1:1 mixture of 5 and 12 (and residual 4a) without the formation of
Nb(NAr)(N=CtBu2)(O-2,6-iPr2C6H3)(O-2,4,6-Me3C6H2) (Scheme 7 and Figure 4); the reaction seemed complete and further stirring
did not improve the conversion of 4a even after 1 day
(1H NMR spectra are shown in Figures S2-17–19, SI). The fact clearly indicates not only that
certain disproportionation (phenoxy exchange reactions) proceeded
in situ, but also that the reaction should proceed via fast coordination
(shown in bracket in Scheme 7), proton transfer, and dissociation of phenols. We do not
have a clear explanation of why the reaction only afforded the disproportionation
products (5 and 12) at this moment.
Figure 4 1H NMR spectra (in C6D6 at 25
°C) for (a) Nb(NAr)(N=CtBu2)(O-2,4,6-Me3C6H3)2(HN=CtBu2) (12), (b) Nb(NAr)(N=CtBu2)(O-2,6-iPr2C6H3)2 (5), (c) Nb(NAr)(N=CtBu2)2(O-2,6-iPr2C6H3) (4a), and (d) the reaction mixture of 4a with
1.0 equiv of 2,4,6-Me3C6H2OH. Detailed
conditions are shown in the Supporting Information. (More spectra are shown in Figures S2-17–19.)a
Scheme 7 Reactions of Nb(N-2,6-Me2C6H3)(N=CtBu2)2(O-2,6-iPr2C6H3) (4a) with 1.0 equiv of 2,4,6-Me3C6H2OH (Detailed Synthetic Procedures Are Shown
in the Supporting Information)a
Concluding Remarks
We have prepared a series of four-, five-, and six-coordinate (arylimido)niobium(V)
complexes containing ketimide (N=CtBu2), phenoxide, or fluorinated alkoxide ligands. Unique
reactivities of the tris(ketimide) analogue, Nb(NAr)(N=CtBu2)3 (3a), with various phenols (2,6-iPr2C6H3OH, 2,6-tBu2C6H3OH, 2,4,6-Me3C6H2OH, and C6F5OH), (CF3)2CHOH, and (CF3)3COH have
been demonstrated as summarized below.
Reactions of Nb(NAr)(N=CtBu2)3 (3a) with 1.0, 2.0, or 3.0 equiv
of 2,6-iPr2C6H3OH afforded Nb(NAr)(N=CtBu2)2(O-2,6-iPr2C6H3), Nb(NAr)(N=CtBu2)(O-2,6-iPr2C6H3)2, or Nb(NAr)(O-2,6-iPr2C6H3)3, respectively (in n-hexane at 25 °C),
whereas a similar reaction with 1.0 equiv of 2,6-tBu2C6H3OH afforded a mixture
of 3a and Nb(NAr)(N=CtBu2)2(O-2,6-tBu2C6H3) (4b) (even after
overnight) and the reaction with 2.0 equiv of 2,6-tBu2C6H3OH at 70 °C in
C6D6 (or 100 °C in toluene-d8) afforded 4b without the formation of the
bis(phenoxide); the reaction with 2.0 equiv of 2,4,6-Me3C6H2OH afforded Nb(NAr)(N=CtBu2)(O-2,4,6-Me3C6H3)2(HN=CtBu2) with coordination of HN=CtBu2. Similar reactions of 3a with 1.0 equiv of (CF3)3COH or 2.0 equiv of
(CF3)2CHOH afforded Nb(NAr)(N=CtBu2)2[OC(CF3)3](HN=CtBu2)
or Nb(NAr)(N=CtBu2)[OCH(CF3)2]2(HN=CtBu2), respectively. In addition to the structural
analyses data, it was assumed that these reactions proceeded via coordination
of phenol (alcohol) to Nb and the subsequent proton transfer to the
ketimide ligand.
In contrast, the reaction of 3a with 1.0 or 2.0 equiv
of C6F5OH afforded Nb(N=CtBu2)2(OC6F5)3(HN=CtBu2) (7) as the sole isolated product (with reaction of
the arylimido ligand). It turned out that the careful dropwise addition
of C6F5OH to 3a under diluted conditions
afforded Nb(NAr)(N=CtBu2)2(OC6F5)(HN=CtBu2) (by reaction of 3a with
the ketimide) and subsequent treatment with C6F5OH afforded 7.
The reaction of Nb(NAr)(N=CtBu2)2(O-2,6-iPr2C6H3) with 1.0
equiv of 2,4,6-Me3C6H2OH afforded
the disproportionation
products Nb(NAr)(N=CtBu2)(O-2,6-iPr2C6H3)2 and Nb(NAr)(N=CtBu2)(O-2,4,6-Me3C6H2)2(HN=CtBu2) with 1:1 ratio, clearly indicating that the reaction proceeded
via coordination of phenol to Nb and the subsequent fast proton transfer
(between ketimide and phenoxide), not by protonation.
As described
in Introduction, the synthesis
and reaction chemistry of (arylimido)niobium(V) complexes containing
monodentate anionic donor ligands were less compared to those in vanadium
complexes and (tert-butylimido)niobium complexes
containing β-diketiminate ligand. Therefore, the results introduced
here should provide important information in the reaction chemistry
of niobium for better understanding. We are now exploring another
route for the synthesis of the four-coordinate (arylimido)niobium(V)
dichloride or dialkyl complexes as promising catalyst precursors for
olefin polymerization and promising precursors for the alkylidene
complexes for olefin metathesis.
Experimental Section
General
Procedures
All experiments were carried out
under nitrogen atmosphere in a vacuum atmosphere dry box unless otherwise
specified. All chemicals used were of reagent grade and were purified
by the standard purification procedures. Anhydrous-grade n-hexane, dichloromethane, diethyl ether, and toluene (Kanto Chemical
Co., Inc.) were transferred into bottles containing molecular sieves
(mixture of 3 Å 1/16 and 4 Å 1/8, and 13× 1/16) under
a nitrogen stream in the dry box and used without further purification.
Nb(N-2,6-Me2C6H3)Cl3(dme),40 Nb(N-2,6-iPr2C6H3)Cl3(dme),33 and Nb(NAd)Cl3(dme)33 (Ad = 1-adamantyl) were
prepared according to a published procedure.33,40 Ethylene for polymerization was of polymerization grade (purity
>99.9%, Sumitomo Seika Co., Ltd.) and was used as received. Elemental
analyses were performed using EAI CE-440 CHN/O/S Elemental Analyzer
(Exeter Analytical, Inc.). All 1H and 13C NMR
spectra were recorded on a Bruker AV500 spectrometer (500.13 MHz for 1H NMR, 125.77 MHz for 13C NMR). All spectra were
obtained in the solvent indicated at 25 °C unless otherwise noted.
Chemical shifts are given in parts per million and are referenced
to SiMe4 (δ 0.00 ppm, 1H NMR, 13C NMR) and CFCl3 (δ 0.00, 19F NMR). Coupling
constants are given in hertz.
Synthesis of (Imido)niobium(V)
Dichloride Complexes Containing
Phenoxy Ligands
A series of (imido)niobium(V) dichloride
complexes, Nb(NR)Cl2(OAr′)(dme) [Ar′ = 2,6-iPr2C6H3,
R = 2,6-Me2C6H3 (1a);
2,6-iPr2C6H3 (1b); 1-adamantyl (1c); R = 2,6-Me2C6H3, Ar′ = 2,6-Ph2C6H3 (1d); dme = 1,2-dimethoxyethane],
were prepared from Nb(NR)Cl3(dme) by treating with 1.0
equiv of LiOAr′ in Et2O. These complexes were identified
by NMR spectra and elemental analysis, and some structures were determined
by X-ray crystallography.
Synthesis of Nb(N-2,6-Me2C6H3)Cl2(O-2,6-iPr2C6H3)(dme) (1a)
To an Et2O solution
(70 mL) containing
Nb(N-2,6-Me2C6H3)Cl3(dme) (1501 mg, 3.674 mmol), 2,6-iPr2C6H3OLi (677 mg, 3.674
mmol) was added at −30 °C. The reaction mixture was warmed
slowly to room temperature and then the mixture was stirred for 17
h. Volatiles were removed under reduced pressure to give an orange
solid. The residue was extracted with toluene (ca. 40 mL) to afford
an orange solution. The solution was filtered through a Celite pad,
and the filter cake was washed by toluene. The combined filtrate and
the wash were removed in vacuo. Recrystallization from CH2Cl2/pentane at 30 °C gave yellow microcrystals. Yield
1546 mg (76%). 1H NMR (CDCl3): δ 7.05
(d, J = 7.60 Hz, 2H, Ar-H), 6.93
(t, J = 7.60 Hz, 1H, Ar-H), 6.82
(d, J = 7.46 Hz, 2H, Ar-H), 6.70
(t, J = 7.46 Hz, 1H, Ar-H), 4.13,
4.11 (br, 4H, −OCH2), 4.02 (br,
3H, −OCH3), 3.92 (m, 2H, −CH(CH3)2), 3.82 (br, 3H, −OCH3), 2.49 (s, 6H, −CH3), 1.08 (d, J = 6.90 Hz, 12H, −CH(CH3)2). 13C NMR (CDCl3): δ 159.9, 152.8, 138.0, 136.6, 127.3, 125.0, 123.5,
122.8, 74.0, 70.9, 67.6, 61.8, 25.8, 24.2, 19.1. Anal. Calcd for C24H36Cl2NNbO3: C, 52.38; H,
6.59; N, 2.55. Found: C, 52.60; H, 6.61; N, 2.55.
Synthesis
of Nb(N-2,6-iPr2C6H3)Cl2(O-2,6-iPr2C6H3)(dme)
(1b)
In a dry box, to an
Et2O solution (10 mL) in a round-bottom flask containing
Nb(N-2,6-iPr2C6H3)Cl3(dme) (250 mg, 0.54 mmol),
Et2O solution (5 mL) containing Li(O-2,6-iPr2C6H3)
(83 mg, 0.57 mmol) was added slowly at −30 °C. The reaction
mixture was warmed slowly to room temperature and stirred overnight.
The volatiles were then evaporated in vacuo, the resultant mixture
was extracted with toluene, and the toluene solution was filtered
through a Celite pad. The filtrate was placed in a rotary evaporator
under vacuum. The resultant mixture was then dissolved in minimum
amount of CH2Cl2, and the solution was placed
in a freezer (−30 °C). The chilled solution afforded an
orange-yellow solid. Yield: 209 mg (80.0%). 1H NMR (CDCl3): δ 7.02 (d, 2H, J = 7.6 Hz, Ar), 6.96 (d, 2H, J = 8.0 Hz, Ar), 6.90 (t, 1H, J = 8.0 Hz, Ar),
6.89 (t, 1H, J = 8.2 Hz, Ar), 4.13
(b, 2H, CH2OCH3), 4.11 (b,
2H, CH2OCH3), 4.01 (m, 2H, CH(CH3)2), 3.96 (s, 3H, CH2OCH3), 3.89 (m, 2H, CH(CH3)2), 3.81 (s, 3H, CH2OCH3), 1.07 (t, 24H, J = 5.4 Hz, CH(CH3)2). 13C NMR (CDCl3): δ 159.3, 150.0, 146.8, 137.8, 125.6,
123.5, 122.8, 122.7, 74.0, 70.9, 67.1, 61.7, 28.0, 25.9, 24.6, 24.3.
Synthesis of Nb(NAd)Cl2(O-2,6-iPr2C6H3)(dme)
(1c)
In a dry box, to an Et2O solution
(6 mL) in a round-bottom flask containing Nb(NAd)Cl3(dme)
(30 mg, 0.07 mmol), Et2O solution (4 mL) containing Li(O-2,6-iPr2C6H3) (13 mg, 0.07 mmol) was added slowly at −30
°C. The reaction mixture was warmed slowly to room temperature
and stirred overnight. The volatiles were then evaporated in vacuo,
the resultant mixture was extracted with toluene, and the toluene
solution was filtered through a Celite pad. The filtrate was placed
in a rotary evaporator under vacuum. The resultant mixture was dissolved
in minimum amount of CH2Cl2 and layered by n-hexane, and the solution was placed in a freezer (−30
°C). The chilled solution afforded a fresh yellow solid. Yield:
33 mg (84.0%). 1H NMR (CDCl3): δ 7.08
(d, 2H, J = 7.3 Hz, Ar), 6.93 (d,
2H, J = 7.3 Hz, Ar), 4.04 (b, 6H,
CH2OCH3), 3.88 (m, 2H, CH(CH3)2), 3.70 (b, 3H, CH2OCH3), 1.90 (s, 3H, Ad),
1.69 (s, 6H, Ad), 146 (m, 6H, Ad), 1.20 (d, 12H, J = 6.7 Hz, CH(CH3)2). 13C NMR (CDCl3): δ 160.7, 137.4, 123.3, 122.0, 73.7, 71.8, 70.8, 67.8,
61.2, 43.4, 36.1, 29.3, 26.1, 24.1. Anal. Calcd. for C26H42Cl2NNbO3: C, 53.80; H, 7.29;
N, 2.41. Found(1): 53.39; H, 7.60; N, 2.38. Found(2): 53.99; H, 7.65;
N, 2.38.
Synthesis of Nb(N-2,6-Me2C6H3)Cl2(O-2,6-Ph2C6H3)(dme) (1d)
To an
Et2O solution (40 mL) containing Nb(N-2,6-Me2C6H3)Cl3(dme) (333 mg, 0.815
mmol), Li(O-2,6-Ph2C6H3) (206 mg, 0.815 mmol) was added at −30 °C. The
reaction mixture was warmed slowly to room temperature and then the
mixture was stirred for 17 h. Volatiles were removed under reduced
pressure to give an orange solid. The residue was extracted with toluene
(ca. 40 mL) to afford an orange solution. The solution was filtered
through a Celite pad, and the filter cake was washed by toluene. The
combined filtrate and the wash were removed in vacuo. Recrystallization
from CH2Cl2/pentane at 30 °C gave orange
solids. Microcrystals suitable for X-ray crystallographic analysis
were obtained by recrystallization in benzene at room temperature.
Yield 340 mg (67%). 1H NMR (CDCl3): δ
7.41 (d, J = 7.30 Hz, 4H, Ar-H),
7.17 (m, 8H, Ar-H), 7.03 (t, J =
7.45 Hz, 1H, Ar-H), 6.77 (d, J =
7.34 Hz, 2H, Ar-H), 6.71 (t, J =
7.34 Hz, 1H, Ar-H), 3.79 (br, 4H, −OCH2), 3.66 (br, 3H, −OCH3), 3.18 (br, 3H, −OCH3), 2.23 (s, 6H, −CH3). 13C NMR (CDCl3): δ 160.3, 152.5, 139.2, 137.2, 133.1,
131.1, 130.6, 127.7 127.0, 126.5, 124.9, 122.3, 73.7, 70.5, 67.0,
61.3, 19.0. Anal. Calcd for C30H32Cl2NNbO3: C, 58.27; H, 5.22; N, 2.27. Found: C, 58.51; H,
5.52; N, 2.35.
Synthesis of Nb(N-2,6-Me2C6H3)(CF3SO3)2(O-2,6-iPr2C6H3)(dme) (2a)
To a chilled CH2Cl2 (12 mL, −30 °C)
solution containing
Nb(N-2,6-Me2C6H3)Cl3(dme) (100 mg, 0.182 mmol), AgOTf (94 mg, 0.363 mmol)
was added. The reaction was warmed slowly to room temperature (25
°C) and stirred for 3 h. After the reaction, the volatiles were
evaporated in vacuo and the resultant mixture was extracted with toluene.
The solution was filtered through a Celite pad. The filtrate was placed
in a rotary evaporator under vacuum. The resultant mixture was dissolved
in minimum amount of Et2O layered with hexane, and the
solution was placed in a freezer (−30 °C). The resultant
orange solids were isolated as an analytically pure orange precipitate.
Yield: 86 mg (61%). 1H NMR (C6D6):
δ 7.07 (d, J = 7.64 Hz, 2H, Ar-H), 6.95 (t, J = 7.64 Hz, 1H, Ar-H), 6.61 (d, J = 7.53 Hz, 2H, Ar-H), 6.52 (t, J = 7.53 Hz, 1H, Ar-H), 3.71 (s, 3H, −OCH3), 3.69 (m,
2H, −CH(CH3)2), 3.51
(t, 2H, −OCH2), 3.22 (s, 3H, −OCH3), 3.21 (t, 2H, −OCH2), 2.41 (s, 6H, −CH3), 1.21 (d, J = 6.80 Hz, 12H, −CH(CH3)2). 19F NMR (C6D6): δ −76.89. 13C NMR (C6D6): δ 160.7, 153.4, 137.5, 136.4, 127.0,
124.7, 124.3, 120.1 (q, 1JCF = 317.9 Hz), 73.8, 70.5, 70.3, 62.6, 26.4, 24.2, 18.4. Anal. Calcd
for C26H36F6NNbO9S2: C, 40.16; H, 4.67; N, 1.80. Found: C, 40.29; H, 4.60; N,
1.75.
Synthesis of Nb(N-2,6-Me2C6H3)(CF3SO3)3(dme) (2b)
In a dry box, to a dichloromethane solution (18 mL) in
a round-bottom flask containing Nb(N-2,6-Me2C6H3)Cl3(dme) (490 mg, 1.20 mmol), a dichloromethane
solution (8 mL) containing AgOTf (OTf = CF3SO3, 925 mg, 3.60 mmol) was added slowly at −30 °C. The
reaction mixture was warmed slowly to room temperature and stirred
overnight. The volatiles were then evaporated in vacuo, and the resultant
mixture was extracted with toluene. The toluene solution was filtered
through a Celite pad. The filtrate was placed in a rotary evaporator
under vacuum. The resultant mixture was dissolved in minimum amount
of CH2Cl2 and layered by n-hexane
and the solution was placed in a freezer (−30 °C). The
chilled solution afforded a purple solid. Yield: 550 mg (61.2%). 1H NMR (CDCl3): δ 6.99 (d, 2H, J = 7.6 Hz, Ar), 6.91 (t, 1H, J =
7.1 Hz, Ar), 4.71 (t, 2H, J = 5.1
Hz, CH2OCH3), 4.58 (s, 3H,
CH2OCH3), 4.26 (t, 2H, J = 4.9 Hz, CH2OCH3), 3.80 (s, 3H, CH2OCH3),
2.64 (s, 6H, ArCH3). 19F NMR
(CDCl3): δ −75.82(s), −76.29(s). 13C NMR (CDCl3): δ 152.6, 139.9, 130.03, 127.94,
122.84, 120.40, 120.31, 117.79, 115.26, 78.26, 73.56, 70.38, 63.89,
53.56, 18.71.
Synthesis of Nb(N-2,6-Me2C6H3)(N=CtBu2)3 (3a)
To a toluene solution
(14 mL) containing
Nb(N-2,6-Me2C6H3)Cl3(dme)
(100 mg, 0.25 mmol), a toluene solution (6 mL) containing Li(N=CtBu2) (110 mg, 0.75 mmol) was added
slowly at −30 °C. The reaction mixture was warmed slowly
to room temperature and stirred overnight. The volatiles were then
evaporated in vacuo, and the resultant mixture was extracted with
toluene. The toluene solution was filtered through a Celite pad. The
filtrate was placed in a rotary evaporator under vacuum. The resultant
mixture was dissolved in minimum amount of n-hexane,
and the solution was placed in a freezer (−30 °C). The
chilled solution afforded an orange solid. Yield: 61 mg (39.0%). 1H NMR (C6D6): δ 7.08 (d, 2H, J = 7.9 Hz, Ar), 6.80 (t, 1H, J = 7.6 Hz, Ar), 2.63 (s, 6H, ArCH3), 1.30 (s, 54H, CCH3). 13C NMR (CDCl3): δ 195.3, 131.5, 128.4, 126.8,
119.5, 44.6, 30.8, 19.9. Anal. Calcd. for C35H65N4Nb: C, 66.43; H, 10.04; N, 8.85. Found: C, 64.22; H,
10.13; N, 8.57. Rather low C value would be due to incomplete combustion
during analysis run.
Synthesis of trans-NbCl2(N=CtBu2)3 (3b)
To a toluene solution (40 mL)
containing NbCl5 (600 mg, 2.22 mmol), a toluene solution
(18 mL) containing Li(N=CtBu2) (982 mg, 6.67 mmol) was added
slowly at −30 °C. The reaction mixture was warmed slowly
to room temperature and stirred overnight. The volatiles were then
evaporated in vacuo, the resultant mixture was extracted with toluene,
and the toluene solution was filtered through a Celite pad. The filtrate
was placed in a rotary evaporator under vacuum. The resultant mixture
was dissolved in minimum amount of n-hexane, and
the solution was placed in a freezer (−30 °C). The chilled
solution afforded an orange solid. Yield: 213 mg (16.4%).1H NMR (C6D6): δ 1.36 (s, 54, C(CH3)3). 13C NMR (C6D6): δ 188.9, 46.0, 31.1. Anal. Calcd. for C27H54Cl2N3Nb: C, 55.48; H,
9.31; N, 7.19. Found: C, 55.70; H, 9.12; N, 6.97.
Synthesis
of Nb(N-2,6-Me2C6H3)(N=CtBu2)2(O-2,6-iPr2C6H3) (4a)
To an n-hexane
solution (34 mL) containing Nb(NAr)(N=CtBu2)3 (3a) (560 mg, 0.89
mmol), an n-hexane solution (8 mL) containing 2,6-iPr2C6H3OH
(158 mg, 0.89 mmol) was added slowly at −30 °C. The reaction
mixture was warmed slowly to room temperature and stirred for 2 h.
The volatiles were then evaporated in vacuo, and the resultant mixture
was dissolved in minimum amount of n-pentane. The
solution was then placed in a freezer (−30 °C), and the
chilled solution afforded a yellow solid. Yield: 408 mg (69.0%). 1H NMR (CDCl3): δ 6.99 (d, 2H, J = 7.7 Hz, Ar), 6.92 (d, 2H, J =
7.4 Hz, Ar), 6.80 (t, 1H, J = 7.6
Hz, Ar), 6.70 (t, 1H, J = 8.8 Hz, Ar), 3.45 (m, 2H, CH(CH3)2), 2.40 (s, 6H, ArCH3), 1.28 (s,
36H, CCH3), 1.05 (d, 12H, J = 6.9 Hz, CH(CH3)2). 13C NMR (CDCl3): δ 158.1, 137.0,
131.8, 127.0, 122.8, 121.6, 119.6, 53.6, 45.1, 30.7, 28.6, 26.7, 23.4,
19.5, 14.3. Microcrystals suitable for X-ray crystallographic analysis
were prepared by recrystallization.
Synthesis of Nb(N-2,6-Me2C6H3)(N=CtBu2)2(O-2,6-tBu2C6H3OH) (4b)
To a sealed Schlenk glass tube
containing Nb(NAr)(N=CtBu2)3 (3a) (1095 mg, 1.73 mmol) and toluene
(25 mL), a toluene solution (18 mL) containing 2,6-tBu2C6H3OH (375 mg, 1.82 mmol)
was added slowly at −30 °C. The reaction mixture was stirred
at 70 °C overnight under N2. The volatiles were then
evaporated in vacuo, and the resultant mixture was extracted by minimum
amount of n-hexane. The solution was then filtered
through a filter paper for removal of remaining 2,6-tBu2C6H3OH. The resultant solution
was placed in a freezer (−30 °C), and the chilled solution
afforded a yellow solid. Yield: 531 mg (44.0%). 1H NMR
(C6D6): δ 7.28 (d, 2H, J = 8.3 Hz, Ar), 6.99 (d, 2H, J =
7.8 Hz, Ar), 6.84 (t, 1H, J = 7.8
Hz, Ar), 6.79 (t, 1H, J = 7.5 Hz, Ar), 2.60 (s, 6H, ArCH3), 1.53
(s, 18H, ArC(CH3)3), 1.27 (s,
36H, C(CH3)3). 13C NMR (C6D6): δ 197.9,
196.8, 138.7, 128.4, 127.6, 125.9, 122.6, 119.8, 44.7, 35.4, 31.8,
30.7, 20.0. Anal. Calcd. for C40H66N3NbO: C, 68.84; H, 9.53; N, 6.02. Found: C, 68.11; H, 9.53; N, 5.93.
Rather low C value would be due to incomplete combustion during analysis
run. Microcrystals suitable for the X-ray crystallographic analysis
were prepared by recrystallization.
Synthesis of Nb(N-2,6-Me2C6H3)(N=CtBu2)(O-2,6-iPr2C6H3)2 (5)
To an n-hexane
solution (12 mL) containing Nb(NAr)(N=CtBu2)3 (3a) (80 mg, 0.13
mmol), an n-hexane solution (5 mL) containing 2,6-iPr2C6H3OH
(46 mg, 0.26 mmol) was added slowly at −30 °C. The reaction
mixture was warmed slowly to room temperature and stirred for 2 h.
The volatiles were then evaporated in vacuo, and the resultant mixture
was dissolved in minimum amount of n-hexane. The
solution was placed in a freezer (−30 °C). The chilled
solution afforded a yellow solid. Yield: 74 mg (83.2%).1H NMR (C6D6): δ 7.12 (d, 4H, J = 7.4 Hz, Ar), 6.99 (t, 2H, J = 7.4 Hz, Ar), 6.87 (d, 2H, J =
6.9 Hz, Ar), 6.71 (t, 1H, J = 7.8
Hz, Ar), 3.88 (m, 4H, CH(CH3)2), 2.38 (s, 6H, ArCH3), 1.24 (m, 24H, CHCH3), 1.12 (s, 18H,
C(CH3)3). 13C NMR
(C6D6): δ 203.9, 158.2, 156.2, 137.5,
131.6, 127.6, 123.6, 123.2, 122.2, 44.8, 30.3, 27.2, 23.8, 23.7, 19.2.
Anal. Calcd. for C35H63N4Nb: C, 69.67;
H, 8.70; N, 3.96. Found: C, 69.49; H, 9.00; N, 3.92.
Synthesis
of Nb(N-2,6-Me2C6H3)(O-2,6-iPr2C6H3)3 (6)
Reaction with 2,6-iPr2C6H3OH
To an n-hexane
solution (18 mL) containing Nb(NAr)(N=CtBu2)3 (3a) (150 mg, 0.24
mmol), an n-hexane solution (8 mL) containing 2,6-iPr2C6H3OH
(128 mg, 0.72 mmol) was added slowly at −30 °C. The reaction
mixture was warmed slowly to room temperature and stirred for 2 h.
The volatiles were then evaporated in vacuo, and the resultant mixture
was dissolved in minimum amount of n-hexane. The
solution was placed in a freezer (−30 °C), and the chilled
solution afforded a yellow solid. Yield: 141 mg (79.0%).
Reaction
with Li(O-2,6-iPr2C6H3)
To an Et2O
solution (20 mL) containing Nb(N-2,6-Me2C6H3)Cl3(dme) (100 mg, 0.25 mmol), an
Et2O solution (6 mL) containing Li(O-2,6-iPr2C6H3)
(136 mg, 0.74 mmol) was added slowly at −30 °C. The reaction
mixture was warmed slowly to room temperature and stirred for 2 h.
The volatiles were then evaporated in vacuo, and the resultant mixture
was dissolved in minimum amount of n-hexane. The
solution was placed in a freezer (−30 °C), and the chilled
solution afforded a yellow solid. Yield: 162 mg (87.0%). 1H NMR (CDCl3): δ 7.11 (d, 6H, J = 7.7 Hz, Ar), 7.00 (t, 3H, J =
7.7 Hz, Ar), 6.78 (d, 2H, J = 7.0
Hz, Ar), 6.67 (t, 1H, J = 7.4 Hz, Ar), 3.54 (m, 6, CH(CH3)2), 1.88 (s, 6H, ArCH3), 1.13 (d,
36H, J = 6.8 Hz, CH(CH3)2). 13C NMR (CDCl3): 158.1, 155.4,
137.3, 132.0, 127.1, 123.7, 123.4, 122.8, 27.3, 23.6, 18.4. Anal.
Calcd. for C44H60NNbO3: C, 71.04;
H, 8.13; N, 1.88. Found(1): 70.43; H, 7.91; N, 1.73. Found(2): 70.59;
H, 7.90; N, 1.75. Rather low C value would be due to incomplete combustion
during analysis run.
Synthesis of Nb(N=CtBu2)2(OC6F5)3(HN=CtBu2) (7)
Reaction of 3a with 1 equiv of C6F5OH
To an n-hexane solution (12 mL)
containing Nb(NAr)(N=CtBu2)3 (3a) (80 mg, 0.13 mmol), an n-hexane solution (5 mL) containing C6F5OH (24
mg, 0.13 mmol) was added slowly at −30 °C. The reaction
mixture was warmed slowly to room temperature and stirred for 2 h.
The volatiles were then evaporated in vacuo, and the resultant mixture
was dissolved in minimum amount of n-hexane. The
solution was placed in a freezer (−30 °C), and the chilled
solution afforded an orange solid. Yield: 13 mg (9.6%). 1H NMR (C6D6): δ 9.67 (b, 1H, NH), 1.11 (s, 1H, C(CH3)3). 19F NMR (C6D6): δ
−160.19 (d), −165.5 (t), −169.6 (t). 13C NMR (C6D6): δ 204.4, 192.4, 141.0,
139.4, 139.0, 137.5, 137.4, 136.0, 134.0, 128.2, 127.8, 47.9, 41.6,
31.1, 29.8, 29.7. Anal. Calcd. for C45H55F15N3NbO3: C, 50.81; H, 5.21; N, 3.95.
Found: 50.94; H, 5.30; N, 4.07. Microcrystals suitable for X-ray crystallographic
analysis were prepared by recrystallization from the chilled n-hexane solution.
Reaction of 3a with 2 equiv of C6F5OH
To an n-hexane solution (6 mL)
containing Nb(NAr)(N=CtBu2)3 (3a) (44 mg, 0.07 mmol), an n-hexane solution (3 mL) containing C6F5OH (26
mg, 0.14 mmol) was added slowly at −30 °C. The reaction
mixture was warmed slowly to room temperature and stirred for 2 h.
The volatiles were then evaporated in vacuo, and the resultant mixture
was dissolved in minimum amount of n-hexane. Then,
the solution was placed in a freezer (−30 °C), and the
chilled solution afforded an orange solid identified as 7. Yield: 23 mg (33.0%).
Synthesis of Nb(N-2,6-Me2C6H3)(N=CtBu2)2[OC(CF3)3](HN=CtBu2) (8)
To a sealed Schlenk
glass tube containing Nb(NAr)(N=CtBu2)3 (3a) (150 mg, 0.24 mmol)
and n-hexane (16 mL), an n-hexane
solution (8 mL) containing (CF3)3COH (59 mg,
0.25 mmol) was added slowly at −30 °C. The reaction mixture
was then stirred at 40 °C overnight. The volatiles were evaporated
in vacuo, and the resultant residue was dissolved in minimum amount
of n-hexane. Then, the solution was placed in a freezer
(−30 °C), and the chilled solution afforded a yellow solid.
Yield: 62 mg (30.0%), and conversion of 3a was 50%. 1H NMR (C6D6): δ 9.66 (b, 1H, NH), 6.94 (d, 2H, J = 7.5 Hz, Ar), 6.76 (t, 1H, J = 7.5 Hz, Ar),
2.53 (s, 6H, ArCH3), 1.35 (s, 9H, C(CH3)3), 1.20 (s, 36H, C(CH3)3), 0.94 (s, 9H, C(CH3)3). 19F NMR (C6D6): δ −73.88 (s). Anal. Calcd. for C40H67F9N4NbO: C, 53.91; H, 7.42; N, 6.45.
Found(1): C, 52.90; H, 7.38; N, 6.28. Found(2): C, 52.27; H, 7.18;
N, 6.12. Rather low C value would be due to incomplete combustion
during analysis runs. Microcrystals suitable for the X-ray crystallographic
analysis were prepared by recrystallization of the chilled n-hexane solution.
Synthesis of Nb(N-2,6-Me2C6H3)(N=CtBu2)[OCH(CF3)2]2(HN=CtBu2) (9)
To an n-hexane solution (31 mL) containing
Nb(N-2,6-Me2C6H3)(N=CtBu2)3 (3a) (345 mg, 0.55
mmol), an n-hexane solution (9 mL) containing (CF3)2CHOH (184 mg, 1.09 mmol) was added slowly at
−30 °C. The reaction mixture was warmed slowly to room
temperature and stirred for 2 h. The volatiles were then evaporated
in vacuo, and the resultant mixture was dissolved in minimum amount
of dichloromethane. The solution was then placed in a freezer (−30
°C), and the chilled solution afforded an orange solid. Yield:
299 mg (66.0%). 1H NMR (C6D6): δ
9.77 (b, 1H, NH), 6.84 (d, 2H, J = 7.5 Hz, Ar), 6.70 (t, 1H, J =
7.8 Hz, Ar), 5.35 (m, 2H, CH(CF3)2), 2.52 (s, 6H, ArCH3), 1.27 (s, 9H, C(CH3)3),
1.16 (s, 18H, C(CH3)3), 0.98
(s, 9H, C(CH3)3). 19F NMR (C6D6): δ −75.1 (b). 13C NMR (C6D6): δ 199.6, 195.3,
124.6, 81.2, 44.4, 43.1, 41.4, 30.5, 30.3, 29.5, 26.9, 19.3. Anal.
Calcd. for C32H48F12N3NbO2: C, 46.44; H, 5.85; N, 5.08. Found: C, 46.30; H,
5.83; N, 5.01. Microcrystals suitable for the X-ray crystallographic
analysis were prepared by recrystallization.
Synthesis
of Nb(N-2,6-Me2C6H3)(N=CtBu2)[OCH(CF3)2]2 (10)
To a
sealed Schlenk glass tube containing Nb(N-2,6-Me2C6H3)(N=CtBu2)[OCH(CF3)2]2(HN=CtBu2) (9) (54 mg,
0.07 mmol) and toluene (5 mL), NiBr2 (43 mg, 0.20 mmol)
was added at low temperature (−30 °C). The reaction mixture
was stirred for 2 h. The mixture was filtered through a filter paper
for removal of the solid part. The solution was evaporated in vacuo,
and the removal of HN=CtBu2 was observed by NMR spectrum. 1H NMR (C6D6): δ 6.84 (d, 2H, J = 7.6 Hz, Ar), 6.70 (t, 1H, J = 7.5 Hz, Ar), 5.35 (m, 2H, CH(CF3)2),
2.52 (s, 6H, ArCH3),1.16 (s, 18H, C(CH3)3).
Synthesis of Nb(N-2,6-Me2C6H3)(N=CtBu2)2(OC6F5)(HN=CtBu2) (11)
Reaction
of 3a with 0.5 equiv of C6F5OH
An n-hexane solution (6.0 mL)
containing C6F5OH (15 mg, 0.08 mmol) was added
to an n-hexane solution (15.0 mL) containing 3a (103 mg, 0.16 mmol) at −30 °C. The reaction
mixture was warmed slowly to room temperature and stirred for 1 h.
The orange-yellow mixture was dried in vacuo, and the crude product
was measured by 1H and 19F NMR spectra (conversion
of 3a 45%). Microcrystals suitable for X-ray crystallographic
analysis were collected (in small amount) from the chilled n-hexane solution. 1H NMR (C6D6): δ 9.70 (b, 1H, NH), 6.93 (d, 2H, J = 6.8 Hz, Ar), 6.74 (t, 1H, J = 7.6 Hz, Ar), 2.57 (s, 6H, ArCH3), 1.34 (s, 9H, C(CH3)3), 1.20 (s, 36H, C(CH3)3), 0.95 (s, 9H, C(CH3)3). 19F NMR (C6D6): δ −162.01
(d), −166.28 (t), −173.05 (t). 13C NMR (CDCl3): 133.2, 126.9, 122.5, 44.9, 30.6, 19.2. These chemical shifts
were assigned from the mixture of 3a and 13 (different ratios shown below).
Synthesis of Nb(N-2,6-Me2C6H3)(N=CtBu2)(O-2,4,6-Me3C6H2OH)2(HN=CtBu2) (12)
To an n-hexane solution
(15 mL) containing Nb(NAr)(N=CtBu2)3 (3a) (100 mg, 0.16 mmol),
an n-hexane solution (5 mL)
containing 2,4,6-Me3C6H2OH (44 mg,
0.32 mmol) was added slowly at −30 °C. The reaction mixture
was warmed slowly to room temperature and stirred for 2 h. The volatiles
were then evaporated in vacuo, and the resultant mixture was dissolved
in minimum amount of n-pentane. The solution was
placed in a freezer (−30 °C), and the chilled solution
afforded a yellow solid. Yield: 36 mg (36.6%). 1H NMR (C6D6): δ 9.66 (b, 1H, NH),
6.90 (d, 2H, J = 7.6 Hz, Ar), 6.77
(s, 4H, Ar), 6.73 (t, 1H, J = 7.3
Hz, Ar), 2.43 (s, 12H, ArCH3), 2.41 (s, 6H, ArCH3), 2.15 (s,
6H, ArCH3), 1.35 (s, 9H, C(CH3)3), 1.12 (s, 18H, C(CH3)3), 0.94 (s, 9H, C(CH3)3). 13C NMR (C6D6):
δ 202.6, 192.5, 159.2, 132.0, 129.9, 129.5, 128.4, 126.3, 123.1,
44.9, 41.7, 41.6, 34.5, 31.2, 30.4, 29.9, 22.7, 20.8, 19.3, 17.7,
14.3. Anal. Calcd. for C44H68N3NbO2: C, 69.18; H, 8.97; N, 5.50. Found: C, 68.72; H, 9.17; N,
5.26. Rather low C value would be due to incomplete combustion during
analysis runs.
Synthesis of Nb(N-2,6-Me2C6H3)(N=CtBu2)(O-2,4,6-Me3C6H2)2 (13)
To a toluene solution (6 mL) containing
Nb(N-2,6-Me2C6H3)(N=CtBu2)(O-2,4,6-Me3C6H2)2(HN=CtBu2) (12a) (36 mg, 0.05 mmol), a toluene
solution (6 mL) containing
NiBr2 (31 mg, 0.14 mmol) was added slowly at −30
°C, and the mixture was stirred for 3 days. Color of the mixture
changed from orange to yellow, and the reaction profile was monitored
by 1H NMR spectrum. The solution was placed in vacuo, and
the residue was dissolved in minimum amount of n-pentane
and placed in a freezer (−30 °C). The chilled solution
afforded a yellow solid. Yield: 36 mg (68.0%). 1H NMR (C6D6): δ 6.90 (d, 2H, J =
7.5 Hz, Ar), 6.77 (s, 4H, Ar), 6.73
(t, 1H, J = 7. 7 Hz, Ar), 2.43 (s,
12H, ArCH3), 2.41 (s, 6H, ArCH3), 2.37 (s, 3H, ArCH3), 2.16
(s, 6H, ArCH3), 1.13 (s, 18H, C(CH3)3). Dissociation of HN=CtBu2 could be observed by 1H NMR spectrum.
Crystallographic Analysis
All measurements were made
on a Rigaku XtaLAB P200 diffractometer using multilayer mirror monochromated
Mo Kα radiation. The crystal collection parameters are listed
in Table S1. The data were collected and
processed using CrystalClear (Rigaku)62 or CrysAlisPro (Rigaku Oxford Diffraction),63 and the structure was solved by direct methods64 and expanded using Fourier techniques. The nonhydrogen
atoms were refined anisotropically, and the hydrogen atoms were refined
using the riding model. All calculations were performed using the
Crystal Structure65 crystallographic software
package, except for refinement, which was performed using SHELXL version
2014/7.66,67 Crystal data and the collection parameters
are shown in Tables S1 and S2 in the Supporting
Information, and structure reports and CIF and xyz files are also shown in the Supporting Information. CCDC numbers for complexes 1a, 1d, 4a, 4b, 7, 8, 9, and 11 are
1839646–1839653, respectively.
Supporting Information Available
The Supporting Information
is available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b01065.Experimental procedure
for some reactions with phenol,
tables for crystal data and collection parameters of 1a, 1d, 4a, 4b, 7, 8, 9, 11, and NMR spectra
for synthesized (arylimido)niobium complexes; NMR spectra monitoring
some reactions with phenols; ORTEP drawings and selected bond distances
and angles for 1a and 1d (PDF)
Structure reports and CIF
files for 1a, 1d, 4a, 4b, 7–9, and 11 (CIF)
Structure
reports and xyz files for 1a, 1d, 4a, 4b, 7–9,
and 11 (xyz)
Supplementary Material
ao8b01065_si_001.pdf
ao8b01065_si_002.cif
ao8b01065_si_003.xyz
The authors
declare no competing financial interest.
Acknowledgments
This project
was partly supported by Grant-in-Aid for Scientific
Research (B) from the Japan Society for the Promotion of Science (JSPS,
Nos. 15H03812 and H1801982). N.S. and K.W. acknowledge the Tokyo Metropolitan
government (Asian Human Resources Fund) for predoctoral fellowship.
The authors thank Profs. S. Komiya, A. Inagaki, and Dr. S. Sueki (Tokyo
Metropolitan University) for discussions.
a Selected NMR spectra
for (imido)niobium
complexes, and experimental procedure for some reactions with phenol
and the selected NMR spectra monitoring the reactions are shown in
the Supporting Information.
b Oak Ridge thermal ellipsoid plot (ORTEP)
drawings for NbCl2(N-2,6-Me2C6H3)(O-2,6-iPr2C6H3)(dme) (1a, CCDC 1839646) and NbCl2(N-2,6-Me2C6H3)(O-2,6-Ph2C6H3)(dme) (1d, CCDC 1839647),
selected bond distances and angles, and structure reports including CIF and xyz files
are shown in the Supporting Information.
c Activity by 1a: 23 kg
PE/(mol Nb h) (25 °C), 11 kg PE/(mol Nb h) (50 °C). Activity
by 1d: 12 kg PE/(mol Nb h) (25 °C). Conditions:
catalyst (1a or 1d), 5.0 μmol; toluene,
30 mL; ethylene, 8 atm; dry-MAO (prepared by removing toluene and
AlMe3 from the commercially available MAO),46−49 3.0 mmol; 1 h.
d The structure
reports including CIF and xyz files
for Nb(N-2,6-Me2C6H3)(N=CtBu2)2(O-2,6-iPr2C6H3) (4a, CCDC 1839648) and Nb(N-2,6-Me2C6H3)(N=CtBu2)2(O-2,6-tBu2C6H3OH) (4b, CCDC 1839649), Nb(N=CtBu2)2(OC6F5)3(HN=CtBu2) (7, CCDC 1839650), Nb(N-2,6-Me2C6H3)(N=CtBu2)2[OC(CF3)3](HN=CtBu2) (8, CCDC 1839651),
Nb(N-2,6-Me2C6H3)(N=CtBu2)[OCH(CF3)2]2(HN=CtBu2) (9, CCDC 1839652), and Nb(N-2,6-Me2C6H3)(N=CtBu2)2(OC6F5)(HN=CtBu2) (11, CCDC 1839653)
are shown in the Supporting Information.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145890610.1021/acsomega.8b00362ArticleDepolying Tunable Metal-Shell/Dielectric Core Nanorod
Arrays as the Virtually Perfect Absorber in the Near-Infrared Regime Chau Yuan-Fong
Chou †Chou Chao Chung-Ting ‡Lim Chee Ming †Huang Hung Ji §Chiang Hai-Pang *∥⊥† Centre
for Advanced Material and Energy Sciences, Universiti Brunei Darussalam, Tungku Link, Gadong BE1410, Negara Brunei Darussalam‡ Department
of Physics, Fu Jen Catholic University, New Taipei City 242, Taiwan§ Instrument
Technology Research Center, National Applied
Research Laboratories, Hsinchu, Taiwan∥ Institute
of Optoelectronic Sciences, National Taiwan
Ocean University, No.
2 Pei-Ning Road, 202 Keelung, Taiwan⊥ Institute
of Physics, Academia Sinica, Taipei 11529, Taiwan* E-mail: hpchiang@mail.ntou.edu.tw.09 07 2018 31 07 2018 3 7 7508 7516 28 02 2018 05 06 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
In
this paper, the coupled Ag-shell/dielectric-core nanorod for
sensor application is investigated and the different dielectric core
plasmonic metamaterial is adopted in our design. The operational principle
is based on the concept of combining the lattice resonance, localized
surface plasmon resonance (SPR), and cavity plasmon resonance modes
within the nanostructure. The underlying mechanisms are investigated
numerically by using the three-dimensional finite element method and
the numerical results of coupled solid Ag nanorods are included for
comparison. The characteristic absorptance/reflectance peaks/dips
have been demonstrated to be induced by different plasmonic modes
that could lead to different responses required for plasmonic sensors.
A nearly perfect absorptance and an approximate zero reflectance with
a sharp band linewidth are obtained from the proposed system, when
operated as an SPR sensor with the sensitivity and figure of merit
of 757.58 nm/RIU (RIU is the refractive index unit) and 50.51 (RIU–1), respectively. Our work provides a promising method
for the future developments of more advanced metamaterial absorber
for chemical sensing, thermal radiation tailoring, field enhanced
spectroscopy, and general filtering applications.
document-id-old-9ao8b00362document-id-new-14ao-2018-00362qccc-price
==== Body
1 Introduction
Plasmonic perfect absorbers
(PPAs) have fascinated increasing attention
in the field of nanophotonic devices because of their unusual capacity
of absorbing and enhancing electromagnetic (EM) waves to the nanometer-scale.1 It can be applied to different fields, such as
resonators,2 refractive index (RI) sensors,3 nanoantennas,4 plasmonic
solar cells,5 biosensing,6−10 and absorbers.11,12 Narrow-band plasmonic absorbers
using surface plasmon resonance (SPR) effects are widely used in thermal
radiation manipulation,13,14 detection, and sensors.15−18 On the basis of plasmonic nanostructures (PNSs) with the properties
of gap plasmon resonance (GPR),19 cavity
plasmon resonance (CPR),20 and metal–dielectric–metal
structure,11,12 perfect plasmonic absorbers21,22 can be achieved in the visible, infrared regime, and other EM regimes.
Recently, researchers have made many advancing efforts on PPAs
to achieve narrow band absorption11 for
plasmonic sensing applications. The narrow spectrum bandwidth is required
in medical sensing applications, for example the monitoring of chemical
reactions,23 the measurement of gas concentrations,24 as well as the detection of biomolecules.25 However, the general PPAs exhibit complicated
structure, and the resonance wavelength is at a fixed wavelength,
and this limits the diversification of their deployment. The various
approaches which have been reported to narrow the band linewidth giving
sharp spectrum feature12,26,27 are plasmonic gap resonance,28 surface
lattice resonance,29 and magnetic dipole
resonance.30 There are several metastructures
which have been studied for the purpose of absorption and they are
based on gap resonance;31,32 however, these literature
studies did not report on the design of sensors having perfect absorptance
and zero reflectance properties. PPAs need to be designed with simple
structure and tunable in the infrared regime if they are to be successfully
implemented in sensor applications.
The large band linewidth
of plasmon resonances causes strong radiative
damping in metals, which is a major problem because it reduces the
sensitivity and hence lowering the quality factor (Q-factor) of the sensor. An effective way to overcome this drawback
is to couple the plasmonic effects to a system with a narrow resonance.
There are several methods to narrow band tunability of PPAs, for example,
the use of stacked graphene-dielectric sheet,31 applying phase-change material (Ge2Sb2Te5),32 and deploying microelectromechanical
system.33 For practical applications, a
large intensity variation of the absorbed or reflected light at a
certain wavelength is desired, that is, sharp peaks/dips of absorptance/reflectance
with a large modulation depth are required. In contrast to the above
mentioned techniques, we proposed a dual band and tunability PPA consisting
of coupled Ag-shell/dielectric-core (ASDC) nanorod array arranged
in a square lattice. In our design, the PPA is made tunable by physically
modifying the PPA’s material and geometry. Each resonance obtained
from our proposed PPA has excellent correlation with respect to geometrical
and material parameters, and furthermore, it shows excellent tunability
for each resonant wavelength (λres). In the proposed
structure, an open cavity is introduced in ASDC nanorods such that
it is accessible to the surrounding medium, and this makes the ASDC
nanorods an attractive RI sensor. The ASDC nanorods and the bottom
Ag thin film layer provide an optical response of SPR and CPR, and
the positive–negative charge pairs will induce an electromotive
force on the metal surface, thus causing an effective coupled mode
which supports a nearly perfect absorptance and an approximate zero
reflectance. ASDC nanorods that are placed at a Bragg distance above
a metal mirror (i.e., 100 nm Ag bottom layer) form a Fabry–Pérot
nanocavity, and they constitute a coupled photonic–plasmonic
system. The influences of structure and material parameters on the
sensing performance are investigated by using the three-dimensional
(3-D) finite element method (FEM). In addition, we put to use the
strong localized enhancement of the EM wave in the gap and cavity
regions in the ASDC nanorods, and we examine the RI infrared sensing
performance. It is found that the absorptance bandwidth can be changed
by varying the dielectric core in the Ag-shell nanorods, and a nearly
perfect absorptance together with an approximate zero reflectance
with a sharp band linewidth are obtained from the proposed system.
The proposed structure can be operated as SPR sensors where the sensitivity
and figure of merit (FOM) of 757.58 nm/RIU and 50.51 (RIU–1), respectively, are observed. This narrow band linewidth and perfect
absorptance properties are required in sensing and filtering applications.34
2 Simulation Method and Models
To analyze the proposed plasmonic system, 3-D FEM is performed
using a commercially available software package (COMSOL multiphysics).
Because of the symmetry of the structures, a plane wave polarized
in x-axis is used as the incident light at normal
incidence from the top surface. Periodic boundary conditions are considered
in x- and y-directions, and perfectly
matching layers are applied along the z direction.
The Ag permittivity data cited in ref (35) is used. The absorptance (A) is calculated as 1 – reflectance (R) –
transmittance (T), with transmittance being nearly
zero in the infrared realm (i.e., the working region of the proposed
PPA) because of the thickness of the bottom Ag film is thicker than
the skin depth in the infrared region, the transmittance (T) channel is prevented, and the absorptance is reduced
to 1 – R. The sensing capability of the SPR
sensor is usually defined by the following definitions of sensitivity
(S) and FOM.3,4 1 where Δλ is the corresponding
central wavelength shift of the resonant dips and Δn is the difference of the RI. fwhm is the full width at half maximum
of the SPR spectrum, and it is defined as the corresponding λres width at half percentage of the reflectance dip. The Q factor can be calculated as the ratio of peak resonance
wavelength (λres) and the full width at half maximum,
that is, Q = λres/fwhm.36
The coupled ASDC nanorod array is arranged
in a square lattice. Figure 1 depicts a truncated
view of the periodic arrays of the coupled ASDC nanorods. The proposed
structure consists of periodic arrays of coupled ASDC nanorods placed
directly on the surface of a uniform Ag film. The value of the incident
EM wave is fixed at |E0|
= 1 V/m. The closely spaced ASDC nanorods have an outer radius (R) and inner radius (r) of 80 and 70 nm,
thickness (t = R – r) of 10 nm, and gap distance (g) of 20
nm. The filling medium in ASDC is set to air (ε = 1.00) and
silica (SiO2). The lattice constant (a) of the arrays is 470 nm, and the bottom silver film has a thickness
(s) of 100 nm. In addition, the whole structure is
placed on a silica substrate (i.e., glass), and the surrounding material
is assumed to be air or n, where n is the RI of the surrounding medium. The RI of silica is calculated
through the Sellmeier equation.37 All materials
are assumed to be nonmagnetic (i.e., μ = μ0).
Figure 1 Truncated view of the periodic arrays of coupled ASDC nanorods
placed directly on the surface of a uniform Ag film. The unit cell
repeats in the x and y direction
forming a square array with periodicity a. The origin
[(x, y, z) = (0,
0, 0)] of the coordinate system is positioned in the middle plane
of the simulation zone. The closely spaced ASDC nanorods have an outer
radius (R) and an inner radius (r) of 80 and 70 nm, thickness (t = R – r) of 10 nm, and gap distance (g) of 20 nm. The filling relative permittivity (ε)
in ASDC is set to air (ε = 1.00) and silica, respectively. The
lattice constant (a) of the arrays is 470 nm, and
the bottom silver film has a thickness (s) of 100
nm. In addition, the whole structure is placed on a silica substrate,
and the surrounding material is assumed to be air or n, where n is the RI of the surrounding medium.
Thanks to the rapid advances in
the fabrication technique of nanophotonic
structures, the proposed PNSs are compatible with the current fabrication
technology such as a manufacturing based on secondary electron lithography
generated by ion beam milling38−42 and other manufacturing processes.43 Superior
shell-to-shell uniformity with a well-ordered feature is established.40,42 Spacer lithography can construct uniformly patterned nanoshell arrays
with sub-10 nm thicknesses.40,44
3 Results
and Discussion
The EM wave coupling is mediated by diffraction
in the plane of
the ASDC nanorod arrays, which are composed of Ag-shell nanorods and
dielectric-core nanorods in a single structure. Upon the illumination
of the ASDC nanorod arrays with UV–visible–infrared
light, the hybrid modes are excited and exhibited as sharp spectral
peaks/dips in the optical absorptance/reflectance. These peaks/dips
are associated with a manifestation of light trapping in the ASDC
nanorod array system. The absorptance/reflectance spectra ascribe
to the lattice resonance and the coupling from the nanochannel waveguide
to the surface plasmon polariton (SPP) mode. Figure 2a,b shows the absorptance/reflectance spectra
of the coupled ASDC nanorods with different dielectric core, that
is, air and silica, where air and silica are the testing core materials
for the purpose of comparison and they can be replaced by other materials.
The top end of our proposed ASDC nanorod with air or silica core is
opened to the surrounding ambience and it can be realized by using
the fabrication processes as described in detail in ref (40). The solid Ag nanorods,
as counterpart for a solid or nonshell case, are also investigated
for the purpose of comparison. Because of the symmetry of the proposed
structures, polarization-insensitive absorptance/reflectance can be
easily realized.
Figure 2 (a) Absorptance and (b) reflectance spectra of the coupled
ASDC
nanorods with different dielectric core (air and silica). The results
include the data obtained for solid Ag nanorods which serves as a
counterpart (solid case) for the purpose of comparison.
As displayed in Figure 2a,b, there is one peak/dip with the maximum
absorptance and
minimum reflectance of 60.524 and 39.463% at λres of 955 nm for the solid case, and there are two peaks/dips with
the maximum absorptance and minimum reflectance of 93.656 and 6.323%
at λres of 855 nm for ASDC with air core and 98.489
and 1.496% at λres of 910 nm for ASDC with silica
core for peak/dip 1, respectively. For cases involving ASDC nanorods,
the absorptance/reflectance curves show two significant peaks/dips
with extremely high/small values. They represent two distinct types
of resonances, that is, the two narrow peaks/dips are result from
the surface lattice resonance and gap and cavity plasmonic resonance,
respectively.12 The number of absorptance/reflectance
peak/dip is dependent on the resonant modes in the PNS, that is, only
the SPR mode occurs in solid case, and for cases involving ASDC nanorods
both the SPR and CPR modes occur simultaneously. It is noteworthy
to point out that the corresponding peaks/dips of the absorptance/reflectance
spectra have the same λres. As the dielectric core
in the ASDC cases is changed from air to silica, the λres is red-shifted, which is in accord with previous literature studies.45 These resonances peaks and dips are attributed
to (1) the vertical GPR mode among incident EM wave, Ag/ASDC nanorod
arrays and the bottom Ag thin film (i.e., 100 nm thickness of Ag film
on the silica substrate) and (2) the transverse CPR mode between the
incident EM wave and the dielectric cores in the Ag shells. The vertical
Fabry–Pérot cavities of the ASDC nanorods waveguide
are formed by the dielectric cores, and the air gaps between metal
nanorods behave as the dielectric interfaces.3 With the help of the Ag film of the ASDC nanorods and the bottom
Ag thin film, the vertical GPR and transverse CPR modes can be well-excited.
As is well-known, the λres of PNSs is dependent on
the changing RI of the surrounding dielectric medium, a characteristic
that has been widely used for sensing applications. The case for ASDC
with ε = 1.00 (air) can be regarded as an SPR sensor, where
the change of ε in the cavity of the ASDC nanorods (e.g., ASDC
nanorods with silica core) causes a spectral shift and a large near-field
intensity variation.
To better understand the above-mentioned
phenomena, we calculate
the electric field intensity (|E|, V/m, Figure 3a), magnetic field
intensity (|H|, A/m, Figure 3b), absorbed power density
(Qe, W/m2, Figure 3c,d), and the surface charge
density distributions (coulomb/m2, Figure 3e) at the corresponding λres extracted from peak 1 for the solid case and peak 1 and peak 2 for
the ASDC case with silica core. From Figure 3, it is evident that the distribution profiles
of each resonance have good correspondence with each PNS structure.
It is obvious that the distribution profiles of |E|, |H|, and Qe are strongly confined in the gap region (i.e., gap enhancement)
at peak 1 and peak 2 for all the cases, while only the case of ASDCs
with silica core at peak 1 shows an enhanced distribution profile
of |E|, |H|, and Qe around their outer sides (i.e.,
edge enhancement). The gap enhancement profiles indicate that the
SPPs (i.e., GPR modes) were stimulated by the incident EM waves coupled
with the Ag/ASDC nanorods and the bottom Ag thin film.46,47 The localized distribution profiles of |E|, |H|, and Qe around the Ag MNPs, show that Peak 1 was induced by
the constructive interference, and this has enhanced the Ag MNP absorptance.48,49 The distribution profiles of |E|,
|H|, and Qe for the case of ASDC with silica core at peak 2 is localized between
the Ag MNPs and the Ag film, which indicates a stronger gap plasmon
mode occurring between the gap of Ag MNPs and also between the Ag
MNPs and bottom Ag film. They govern the absorptance and reflectance,33,46 hence resulting in stronger gap enhancement than that of the other
cases.
Figure 3 (a) Electric field intensity (|E|,
V/m), (b) magnetic field intensity (|H|, A/m), absorbed power density (Qe,
W/m2) in (c) x–y sectional plane and (d) x–z sectional plane, and (e) surface charge density (Coulomb/m2) distributions at the corresponding λres extracted
from peak 1 and peak 2 of the solid case and the ASDC case with silica
core.
The mechanism of these distributions
profiles in Figure 3a–d can be explained
by the surface charge density distributions, as shown in Figure 3e. The surface current
on the metal surface could be enhanced by the positive–negative
charge pairs and they induced the electromotive force. The surface
charge pairs of the solid case at peak 1 (λres =
955 nm) shows the same sign with an aggregation of (+ +) and (−
−) charges at the opposite sides of the Ag nanorods, and there
also is a weaker distribution of (+ +) (− −) on the
surface of the bottom Ag thin film. These surface charges exhibit
a typical dipole-like charge pattern, whose resonance is governed
by the GPR mode. For the ASDC with silica core at peak 1 (λres = 910 nm), the charge pairs distribute strongly and uniformly
in the form of (+ −) (+ −) on the rims and on the surface
of the Ag-shell nanorods, and (− −) (+ +) distribution
is observed on the surface of the bottom Ag thin film. There is also
a strong dipole-like charge pattern on the surface of inner/outer
rims and the bottom, which is governed by the vertical GPR mode. This
gives rise to a stronger dipolar effect and enhances the field pattern
around the gap and edge regions. Besides the GPR mode occurring on
the MNP-dielectric interface, the SPP waves are also included in the
light–electron interactions which happens between the incident
EM waves and the dielectric cores (or cavities) region. This produces
a strong coupling between the incident light and the electrons on
the inner and outer Ag-shell walls, hence bringing about the transverse
CPR mode in the nanocavities.48,50 A straightforward qualitative
understanding to this is that the inner electric field in the ASDC
is screened by the inner Ag-shell wall itself while the electric field
skin effect makes its coupling to the outer Ag-shell wall dominant.
As for the ASDC with silica core at peak 2 (λres =
1152 nm), the charge pairs distribute in the form of (− −)
(+ +) at the opposite sides of Ag-shell nanorods and (+ +) (−
−) on the surface of the bottom Ag thin film. In this case,
the distribution of the GPR mode is larger than that of the CPR mode
and this is due to the surface charge density in the gap region being
denser than that of the lateral sides. This can be verified by the
distribution profiles of |E|, |H|, and Qe, which
show stronger field patterns in the gap region than those of the cases
obtained from peak 1. This implies that the eigenmodes of peak 1 originate
mainly from hybrid plasmon mode of the neighboring Ag-shell wall,
which is caused by their strong mutual inductance and capacitive coupling
but not from the individual ring resonator.16 Its near perfect absorption and approximately zero reflectance utilizes
the Ohmic loss in the metal of the ASDC case. The resonance on the
surface and in the cavity of the ASDC can be tuned by changing the
geometric parameters of the structure, and this will be discussed
latter.
These lattice resonances can be tailored over a wide
spectral range
by changing the array lattice constant (i.e., period).11 The lattice constant, a, indicates
the density of the ASDC nanorods in the period arrays along x- and y-axis, and it has a significant
influence on the absorptance/reflectance spectra. To investigate the
influence of the lattice constant, a, the absorptance/reflectance
spectra for the case of ASDC (with silica core) nanorod arrays with a values in the range of [360, 370, 380, 400, 470, 500]
nm were examined, see Figure 4a,b. As can be seen that the peak 1 has a noticeable blue
shift with a stable magnitude of absorptance/reflectance as a is set in the range of [360, 370, 380, 400, and 470] nm,
whereas the absorptance/reflectance have a slight blue shift and a
decreasing (increasing) magnitude of absorptance (reflectance) as a is at 500 nm, indicating that the stronger coupling effect
occurred as a in the range of [360, 370, 380, 400,
and 470] nm. Note that the peak 2 and dip 2 of all cases possess the
resonance wavelength around λres = 1150 nm.
Figure 4 (a) Absorptance
and (b) reflectance spectra for the case of ASDC
(with silica core) nanorod arrays with different lattice constant, a = [360, 370, 380, 400, 470, and 500] nm. The other parameters
are the same as the ASDC (with silica core) used in Figure 2.
The absorptance and reflectance spectra can be also tuned
by t, h, R, and r, respectively. To better understand both the characteristics
of
the GPR and CPR modes, the effects of the thickness (t = R – r) of the Ag-shell
nanorods, outer radius (R), inner radius (r), and the height (h) of the ASDC nanorods
on the absorptance/reflectance spectra are examined. The results of
varying shell-thickness t in ASDC nanorods are shown
in Figure 5a,b, respectively.
The interaction between incident EM wave and ASDC nanorods could result
in the splitting of SPR modes that are hybridized from an outer Ag-shell
surface GPR mode and an inner Ag-shell surface CPR mode. The behavior
of absorptance/reflectance spectra ascribed by varying Ag-shell thicknesses
originates from capacitive coupling of the induced surface charges
at the side wall of the ASDC nanorod gaps. As the thickness of the
ASDCs increases from 8 to 13 nm, the λres is blue-shifted,
which is consistent with previous studies.51 As the outer dimensions of ASDC nanorods remain intact, the λres is sensitive to the thickness of the Ag nanoshell (i.e., t = R – r), which
blue-shifts from 940 to 820 nm for the case of peak/dip 1 and from
1220 to 1050 nm for the case of peak/dip 2, as the thickness is increased
from 8 to 13 nm. The stronger CPR can be obtained from increasing
the transverse cavity resonance using smaller t (e.g., t = 8, 9 and 10 nm) for peak/dip 1 while increasing the
transverse cavity resonance using larger t (e.g., t = 11, 12 and 13 nm) for peak/dip 2. The λres is blue-shifted with decreasing cavity size in ASDC nanorods. This
implies that, by adopting with a proper size of Ag shell-thickness,
one can carve out a cavity region to generate a contour PPA with tailored
absorptance/reflectance spectra at the desired λres. The key lies in the combination of the PNS with the photonic cavity
in ASDC nanorods. The cavity in ASDC nanorods dramatically influences
the resonance performance in PPA.
Figure 5 (a) Absorptance and (b) reflectance spectra
for the case of ASDC
(with silica core) nanorod arrays with different shell-thickness of t = [8, 9, 10, 11, 12, and 13] nm. The other parameters
are the same as the ASDC (with silica core) used in Figure 2.
The absorptance/reflectance spectra for the case of ASDC
(with
silica core) nanorod arrays with varying outer radius (R), inner radius (r), and height (h) are investigated as shown in Figures 6 and 7, respectively.
As it is shown in Figures 6 and 7, different cavity dimensions
along transverse and vertical directions are demonstrated to be induced
by different plasmonic modes that could lead to different responses
required for plasmonic sensors. Being cavity in ASDC nanorods, the
cavity channel can provide inner resonant modes with a localized electric
field confinement far below the Abbe diffraction limit.40 The λres red-shifts with the
increasing R, r (i.e., increasing
the transverse cavity volume), and h (i.e., increasing
the vertical cavity volume). The varying R, r, and h would yield a change of the cavity
volume in ASDC and result in the change of the surface charge density
on the Ag-shell surface, which is related to the number of positive–negative
charge pairs, that is, varying electron density distributed on the
inner and outer Ag-shell of the ASDC,51 thus forming a strong-coupled mode which favors the near perfect
absorption with proper cavity volume in the ASDC nanorods. In particular,
the strong-coupled modes induce efficient broad band absorptance and
reflectance, whose spectral width and position can be manipulated
by changing ASDC nanorods radius (R–r) and height (h). This suggests that the
CPR with respect to the cavity volume of ASDC nanorods can be affected
by the coupling from R, r, and h. As the Ag-shell thickness of ASDC nanorods remains intact,
the λres red-shifts from 820 to 1020 nm with the
increasing R(r) in the range of
[60(50), 70(60), 80(70), 90(80), and 100(90)] (Figure 6a,b) and from 850 to 1000 nm with the increasing h in the range of [ 80, 90, 100, 110, 120, and 130] (Figure 7a,b) for peak/dip
1 cases. It is worth mentioning that the performance of absorptance/reflectance
spectra are significantly affected by the size of R(r) for the peak/dip 1 cases and by the size of h for peak/dip 2 cases. In Figure 7a,b, the trend of absorptance/reflectance
spectra is quite different between peak/dip 1 and 2. There is a maximum/minimum
at h = 110 nm for the peak/dip 1, whereas the peak/dip
2 is monotone growing/declining with the increasing h. The discrepancies in the observed trends are attributable to the
difference of coupling effect arising from the vertical CPR corresponding
to the incident wavelength of EM wave and the length (i.e., h) of nanocavity channels in ASDC nanorods. Here, the band
linewidth of the coupled photonic–plasmonic resonance is associated
with the ASDC with cavity, which is linked to the Q-factor because of the modified photonic density of states and hence
the modified radiative damping rate. From the Figures 4–7, we observe
that the more the coupling effect on the SPRs and CPRs, the more absorptance
and less reflectance of the ASDC PPA exhibits. This implies that the
resonance arising from the ASDC PPA can be easily tuned by adjusting
its geometrical parameters.
Figure 6 (a) Absorptance and (b) reflectance spectra
for the case of ASDC
(with silica core) nanorod arrays with the outer radius of R = [60, 70, 80, 90, and 100] nm and the inner radius of r = [50, 60, 70, 80, and 90] nm. The thickness of ASDC is
kept at t = 10 nm. The other parameters are the same
as the ASDC (with silica core) used in Figure 2.
Figure 7 (a) Absorptance and (b) reflectance spectra for the case of ASDC
(with silica core) nanorod arrays with different height of h = [80, 90, 100, 110, 120, and 130] nm. The other parameters
are the same as the ASDC (with silica core) used in Figure 2.
For the nanoscale sensor applications, the ambient medium
is referred
to as the variation of RI. The testing sample surrounds the ASDC nanorods,
and the testing medium is usually in liquid or gaseous states.48,49 Calculating the absorptance and reflectance spectra for the proposed
structure, we investigated the ASDC (with silica core) nanorod arrays,
to the environmental RI perturbations. The sensitivity of the sensor
is dependent on the variation of the environmental RI surrounding
the PNSs. To verify the sensitivity of the proposed ASDC (with silica
core) nanorod array, the ambient RI of air (n = 1.00),
water (n = 1.33), and phosphate buffer saline52 are used, and the corresponding absorptance/reflectance
spectra are depicted in Figure 8a,b. A noticeable red shift in the position of the λres from 910 to 1160 nm is observed with the increasing RI
of the surrounding ambience. These features in the absorptance/reflectance
spectra indicate the superior sensing properties. The sensitivity
of RI sensors depends critically on the local electric field intensity
around the ASDC nanorods and the overlap of hot spots with the RI
of the surrounding ambience. This is shown in Figure 8a,b, where the absorptance/reflectance spectra
of the metasurface varies in response to the environmental perturbations.
In Figure 8a,b, the
two groups of resonant peaks and dips are both highly sensitive, although
the different plasmonic modes produce the different λres responses. The physical inference for these red shifts is due to
the effective increase in capacitance of the resonant structure attributed
to the increase in the RI of the analyte.10 The trend of peak (dip) of the absorptance (reflectance) spectra
shows a decreasing (increasing) with an increasing RI of the surrounding
ambience. This is caused by the lesser SPR and CPR effects when higher
RI of the surrounding medium is introduced into the PPA system. According
to the absorptance and reflectance spectra at peak/dip 1, the calculated
sensitivity, FOM, and Q factor can be achieved to
the values of 757.58 nm/RIU, 50.51 (RIU–1), and
60.67, respectively. Noting that the near perfect absorptance and
near zero reflectance resonant with a sharp band linewidth narrower
corresponding to their SPR and CPR modes in Figure 8a,b are upright to each other and well-separated
in wavelengths and in spatial distributions. Indeed, we find that
the absorbing bands of peak 1 in Figure 8a displays good Lorentzian line shapes, and
they are well-matched to the couple mode theory.10
Figure 8 (a) Absorptance and (b) reflectance spectra of ASDC (silica core)
nanorod arrays with the surrounding RI of air (n =
1.00), water (n = 1.33) and phosphate buffer saline.
A comparison of the (c) electric field intensity distributions (at
cross-section across the ASDC nanorods center at z = 0 nm and y = 90 × 10–9 nm, respectively) and (d) surface charge density (including
the 3-D profiles of electric force lines (pink lines) and energy flows
(cyan arrows) of the proposed ASDC (silica core) nanorod arrays exposed
to air (n = 1.00) and a surrounding medium water
(n = 1.33). The other parameters are the same as
the ASDC (with silica core) used in Figure 2.
In an infrared absorptance (reflectance) spectra, the peaks
(dips)
correspond to the molecular groups which absorb (reflect) the infrared
light at specific wavelengths, that is, it regulates the dipole moment
by all (or some) number of its vibration normal coordinates, and it
will surely result in some considerable infrared absorption bands.
Therefore, all sensors have to be examined with respect to their sensitivity
on marginal variations in the surrounding medium. The next sets of
data are derived from the testing of the responsiveness of the proposed
ASDC nanorod array under marginal conditions of the test sample (surrounding
medium of the ASDC nanorod array). Figure 8c,d shows a comparison of the electric field
intensity distributions (at the cross section across the ASDC nanorods
center at z = 0 nm and y = 90 ×
10–9 nm, respectively) and the surface charge density (including the 3-D profiles of electric force lines (pink lines)
and the energy flows (cyan arrows) of the proposed ASDC (with silica
core) nanorod arrays exposed to air (n = 1.00) and
a surrounding medium of RI, n = 1.33 (water). After
the ASDC nanorods adsorbed by the surrounding RI medium, a remarkable
gap enhancement and localization of electric field intensity distributions
can be found along the x axis because of the x-polarization of the incident EM wave. The electric force
lines and energy flow arrows of n = 1.33 (Figure 8d) exhibit an irregular
profile compared to that of n = 1.00 (Figure 8c), when the environmental
RI perturbation influences the ASDC nanorods system. The proposed
ASDC structure has a larger overspread capacity of the hot spots and
the ambient media, which is approachable to the variation of surrounding
medium, and would be applied not only for very sensitive RI sensing
but also for improving most monolayer sensitivity, making it a greatly
attractive PPA structure. More potentially, the localized electric
field enhancement of the lattice resonance mode combined with the
SPR and CPR modes is concentrated on the ASDC nanorod surface thus
easily attainable for the measuring target biomolecules in the near
infrared region.
4 Conclusions
We have
proposed a novel approach to the design of PPA which could
support both tunability and sensitivity for highly sensitive RI sensor
application. The influence of structure and material parameters, the
SPRs and CPRs on the sensing performance have been investigated by
3-D FEM. The mechanisms of absorptance and reflectance spectra have
been demonstrated to be induced by the different plasmonic modes generated
on the periodic ASDC nanorods grating. In our design, the PPA is tuned
by changing or modifying the device material and geometry. The proposed
ASDC PNSs with a Fabry–Pérot nanocavity is shown to
provide a means for reducing the band linewidth of the resonances,
and therefore ameliorating the sensing properties of PNSs. The optical
spectrum can be changed by varying the dielectric core of the ASDC,
and a near perfect absorptance and an approximate zero reflectance
having a sharp band linewidth can be obtained from the proposed system.
The proposed ASDC PNS can be operated as SPR sensor with the sensitivity
and FOM of 757.58 nm/RIU and 50.51 (RIU–1), respectively.
In addition, the open cavity of our proposed ASDC nanorod system is
accessible to the surrounding medium, and this makes it attractive
for RI sensor and filtering applications.
The authors
declare no competing financial interest.
Acknowledgments
This work was supported by the University Research
Grant of Universiti Brunei Darussalam (grant no. UBD/OVACRI/CRGWG
(004) /170101) and Ministry of Science and Technology of Taiwan (MOST
106-2112-M-019-005-MY3, and 105-2221-E-492-036).
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145807510.1021/acsomega.8b02283ArticleEvaluating the Creaming of an Emulsion via Mass Spectrometry
and UV–Vis Spectrophotometry Shinoda Ryo Uchimura Tomohiro *Department of Materials Science
and Engineering, Graduate School of Engineering, University of Fukui, 3-9-1 Bunkyo, Fukui 910-8507, Japan* E-mail: uchimura@u-fukui.ac.jp. Phone/Fax: +81-776-27-8610.22 10 2018 31 10 2018 3 10 13752 13756 05 09 2018 11 10 2018 Copyright © 2018 American Chemical
Society2018American Chemical
SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
The creaming behavior of a turbid
oil-in-water emulsion was observed
via the processes of multiphoton ionization time-of-flight mass spectrometry
(MPI-TOFMS) and ultraviolet–visible spectrophotometry (UV–vis),
and the results were compared. The transmittance measurement by UV–vis
showed that the turbidity of the toluene emulsion was decreased with
time. However, non-negligible errors are common in the measurement
of a sample with high turbidity. The online measurement by MPI-TOFMS
detected many spikes in the time profile, which revealed the existence
of toluene droplets in the emulsion. A smooth time profile suggested
that the signal intensity had initially increased, and then decreased
with time; the initial concentration of toluene was 3 g/L, which had
decreased by half after 60 min. The signal behavior obtained using
MPI-TOFMS differed only slightly from that obtained using UV–vis.
Since a change in turbidity is not the same as a change in the local
concentration of an oil component, MPI-TOFMS is useful for the analysis
of a turbid emulsion and offers additional information concerning
the creaming phenomenon of an emulsion.
document-id-old-9ao8b02283document-id-new-14ao-2018-02283zccc-price
==== Body
Introduction
An emulsion is a system
in which one liquid is dispersed with another
and both are immiscible. Emulsions are applied in a wide variety of
fields; many types of emulsion products are commercialized such as
inks, paints, foods, cosmetics, and pesticide spraying agents.
An emulsion has several specific characteristics that differentiate
it from a so-called normal solution. For example, differences in the
preparation conditions affect the properties even if the concentrations
of the constituents are the same. Moreover, several collapse processes
exist in an emulsion such as creaming, aggregation, coalescence, and
Ostwald ripening. These processes are sensitive to the constituents
and their concentrations, as well as to the preparation conditions.
Among the collapse processes, creaming is a phenomenon wherein the
emulsion droplets are moved to the upper or lower portions according
to the differences in density between the dispersed phase and the
continuous phase. The rate of creaming is affected by the droplet
size, the viscosity of the dispersed phase, and so on. In any case,
the condition of an emulsion changes with time. Also, collapse processes
change the qualities of an emulsion product.
Recent analytical
studies of emulsions include evaluations of collapse
processes,1,2 analysis of the interface of droplets,3−5 and analysis of emulsion products.6 Turbidity
measured by ultraviolet–visible spectrophotometry (UV–vis)
has normally been used for the evaluation of emulsion stability.7−10 For instance, the time profile of turbidity was studied to evaluate
the coalescence and/or solubilization kinetics of oil in microemulsion
droplets11,12 and for determining the phase-inversion
temperature.13,14 However, when an incident light
insufficiently passes through an emulsion with rather high turbidity,
it is difficult to obtain reliable data. In the case of an oil-in-water
(O/W) emulsion, a higher concentration of an oil constituent generally
causes higher turbidity, although several other factors can also affect
the turbidity. In a normal solution with higher absorbance due to
a higher concentration, the solution should be normally diluted when
measuring transmittance and absorbance. However, in the case of an
emulsion, the size of droplets and the emulsion properties are changed
by dilution. As a result, the original behavior of a collapse process
cannot be evaluated.
Multiphoton ionization time-of-flight mass
spectrometry (MPI-TOFMS)
has several notable and practical characteristics. The ionization
method uses ultraviolet laser pulses with high optical selectivity
and less contamination, although soot is often produced by electron
ionization sources. Moreover, TOFMS can detect all of the induced
ions in principle, and is a robust and reasonably easy way to accomplish
design and handling.15−18 MPI-TOFMS is normally applied to atomic/molecular spectroscopy19−21 and to the trace analysis of compounds in real samples such as in
an environmental setting.22−27 Although MPI is generally an ionization method for analytes in a
gas phase, several vaporization methods for liquid samples have also
been studied.28−30
Recently, we applied MPI-TOFMS to the online
analysis of an emulsion.31−37 We developed a sample introduction technique for an emulsion, and
the online mass analysis of an oil phase in an O/W emulsion without
pretreatment was achieved.31 We reported
the time profile of a peak area of an analyte, which was constructed
by plotting the peak areas of the corresponding ions in a series of
mass spectra. Spikes often appear in time profiles, particularly when
measuring an emulsion with a white turbidity. Such spikes derive from
oil droplets, and, in the case of a toluene O/W emulsion, we calculated
the minimum diameter of a toluene droplet that could be detected as
a spike.35,36 We also reported an online analysis of multiple
components in an O/W emulsion34 and that
of a multiple emulsion.33 We recently used
a styrene O/W emulsion to achieve a quantitative analysis of the oil
component in an O/W emulsion, and obtained a linear calibration curve
of styrene in a concentration of as much as 5 g/L.37
Thus far, the possibility of using MPI-TOFMS to evaluate
the creaming
of an emulsion has only been suggested.31 In the present study, the time profiles of an O/W emulsion exhibiting
a creaming phenomenon were measured by UV–vis and MPI-TOFMS,
and the monitoring of an emulsion in a cuvette via these two types
of measurement was aligned. Comparable results established the utility
of MPI-TOFMS for the evaluation of creaming.
Experimental Section
Materials
and Sample Preparation
Toluene and sodium
dodecyl sulfate (SDS), as an oil phase and an emulsifier, respectively,
were purchased from WAKO Pure Chemical Industries (Osaka, Japan) and
were used without further purification. Purified water was prepared
in our laboratory.
For the sample preparation, first, water
(20 mL) and SDS were added to a vial that was shaken manually until
the solid SDS was dissolved. Then, toluene was added and stirred with
a homogenizer (AHG-160D, AS ONE, Osaka) at a speed of 5000 rpm for
10 min. The concentrations of both toluene and SDS were 3 g/L with
respect to the water. After stirring, 3.5 mL of the prepared sample
was transferred to a 5 mL cuvette.
UV–Vis
To establish the degree of turbidity,
UV–vis transmittance was measured with a spectrophotometer
(Shimadzu, UV-160, Japan). To suppress the vaporization of toluene,
a cuvette with a lid was placed on the holder of the spectrophotometer.
As will be described later, a local region of the sample in a cuvette
was monitored by MPI-TOFMS. Therefore, when measuring turbidity, a
horizontal slit (2 mm in width) was placed in the front of the cuvette,
as shown in Figure 1a, in a region where the transmittance measurement was limited in
terms of height. As a result, the incident light passed through the
region 1.8–2.0 cm from the bottom of the cuvette.
Figure 1 Experimental
setup. (a) Horizontal slit (2 mm in width) was placed
in the front of a cuvette when using UV–vis. The incident light
was passed through a region 1.8–2.0 cm from the bottom of the
cuvette. (b) Emulsion in a cuvette with a lid that had a small hole
(φ 1 mm) was monitored by MPI-TOFMS. The tip of the capillary
column was set at the same height as that of the transmittance measurement,
i.e., ca. 2 cm from the bottom of the cuvette.
The wavelengths of the incident light were set to 600 and
266 nm.
While each constituent in an emulsion had no absorption in terms of
its former wavelength, the absorption for toluene was in the latter
wavelength, which approximated the wavelength of the laser pulse for
MPI. In the present study, the turbidity was expressed by −log I/I0, where I and I0 were the incident light intensity
and the transmitted light intensity, respectively.
MPI-TOFMS
MPI-TOFMS used in the present study is described
in detail elsewhere,31 and only briefly
discussed here. The sample introduction port was composed of a pair
of concentric capillary columns. An emulsion was placed in a cuvette
with a lid that had a small hole (1 mm in diameter) to suppress the
vaporization of toluene as much as possible. An inner capillary column
was inserted through the hole to introduce an emulsion. The tip of
the capillary column was set at the same height as the region of the
transmittance measurement described previously, i.e., ca. 2 cm from
the bottom of the cuvette. Ambient air flowed through an outer capillary
column, and the flow rate was adjusted to 2 mL/min via a flow meter
(RK-1250, Kofloc, Kyoto, Japan). The pressure of the vacuum chamber
was ca. 1 × 10–2 Pa.
The linear-type
TOFMS used in the present study was developed at Kyushu University,
Japan. The fourth-harmonic of a Nd:YAG laser (GAIA II, 266 nm, 4 ns,
10 Hz, Rayture Systems, Tokyo, Japan) was used for ionization. The
laser pulse, which was adjusted to ca. 20 μJ, was focused with
a plano-convex lens (f = 200 mm). The ion signals
were acquired without averaging every 0.1 s via a 1 GHz digitizer
(AP240, 1 GS/s, Acqiris/Agilent Technologies, Tokyo, Japan). The mass
resolution was typically 220 at m/z 92 when measuring a toluene O/W emulsion with a white turbidity
(see Figure S1 in the Supporting Information).
The time profile for toluene shown in Figure 4a was constructed by plotting the sum of
the peak areas of m/z 92 (a molecular
ion) and m/z 91 (a fragment ion)
on a series of mass spectra. Figure 4b shows the time profile for the average of every 1200
plots, which corresponded to every 120 s, applied in the three experiments
including that in Figure 4a. It should be noted that the flow of ambient air did not
influence the time profile of the peak area of toluene, as shown in Figure 4, but was used simply
to stably introduce an emulsion into TOFMS.
Results and Discussion
Features
of an Emulsion
The features of the emulsion
prepared in a cuvette with time are shown in Figure 2. Just after the preparation, the emulsion
developed a white turbidity, the lower portion of which turned slightly
transparent with time, while the turbidity in the middle portion,
monitored using UV–vis and MPI-TOFMS in the present study,
seemed unchanged.
Figure 2 Photograph of an O/W emulsion with time.
Time Profile of Turbidity by UV–Vis
Figure 3 shows the
results
of transmittance measurement obtained by UV–vis where the wavelength
of the incident light was 600 nm. This indicates the turbidity of
an emulsion because the three constituents of the present emulsion,
i.e., toluene, water, and SDS, each had no absorption. In this study,
the turbidity of the first 5 min was seldom unchanged or was slightly
decreased, and was then clearly decreased with time at the height
of the monitoring position, although the change in turbidity could
not be confirmed by the naked eye (Figure 2). In this manner, the UV–vis time
profile measurement of turbidity was useful for evaluating the creaming
in an emulsion. However, as shown in Figure 3, the value of turbidity (−log I/I0) was more than 1.0 during
the first 35 min. That is, the transmittance was less than 10%, which
means that the incident light was seldom transmitted through the emulsion.
In conventional UV–vis spectroscopy, such an experimental condition
often results in an increase in the incidence of errors. That is,
non-negligible errors easily occur in the measurement of a sample
with turbidity such as the one in this study.
Figure 3 Time profile of the turbidity
of an O/W emulsion measured by UV–vis
at 600 nm. The error indicates the standard deviation (n = 3).
Incidentally, the value of −log I/I0 obtained at 266 nm was
saturated
at 2.1 throughout the measurement time because, in addition to the
presence of turbidity, toluene has absorption at this wavelength.
As a result, the creaming of the present emulsion could not be evaluated
using the transmittance at this wavelength. Therefore, it is quite
difficult to use UV–vis to explain the relationship between
the local concentration of a constituent of a dispersed phase and
the creaming phenomenon. The proper absorbance might have been obtained
by adding water to dilute toluene and also to reduce the turbidity,
but the properties of the resultant diluted emulsion, including any
creaming behavior, would surely be changed. A shortening of the light
path is one possible experimental condition that could enhance transmittance,
which could allow an estimation of the concentration. However, the
use of a thinner cuvette would be impractical and would likely influence
the creaming phenomenon of the emulsion because situations such as
convection differ between a thin cuvette and the rather large storage
containers that are used in practical situations.
Time Profile
of the Concentration of the Oil Phase by MPI-TOFMS
A time
profile of the peak area of toluene obtained by online MPI-TOFMS
is shown in Figure 4. Figure 4a shows the results of a time profile without averaging.
In this measurement, the recording began at the same time that the
capillary column was inserted into an emulsion. In Figure 4a, although the signal for
toluene was very small, it was surely found after ca. 100–113
s in three measurements and was then adopted as the time required
for sample introduction. After that, many spikes appeared on the time
profile, which decreased both in number and intensity with time. The
appearance of spikes suggested the existence of highly concentrated
toluene, i.e., toluene droplets.31,35 In the present
study, the number and size of the toluene droplets seemed to decrease
at the monitoring position in the cuvette with the occurrence of the
creaming of an emulsion.
Figure 4 Time profile of the peak area of toluene in
an O/W emulsion measured
by MPI-TOFMS. (a) Time profile recorded without averaging (by every
0.1 s). (b) Time profile of an average of every 1200 plots, which
corresponds to every 120 s, was applied in three experiments including
that in (a). The first plot (corresponding to the average of the first
120 s) was ignored because a time from 0 to ca. 120 s was required
to pass the sample through the capillary column (see the text). The
intensity of the second plot was set to 100%, and the right-hand scale
indicates the concentration of toluene where an intensity of 100%
is compatible with 3 g/L of toluene (see the text). The error indicates
the standard deviation (n = 3).
Next, an average of every 1200 plots, which corresponded
to every
120 s, was re-plotted. The time profile is shown in Figure 4b. The first plot (corresponding
to the average value of the first 120 s) was ignored (masked) because
a time that ranged from 0 to ca. 120 s was required for the sample
to pass through the capillary column. In addition, the average intensity
of the second plot was set to 100% in Figure 4b.
Previously, we reported the quantitative
analysis of an O/W emulsion
wherein a linear calibration curve of the oil phase of styrene in
an emulsion with up to 5 g/L was obtained.37 Although toluene was used in the present study, the results in Figure 4b suggest a change
in the concentration of toluene at the sampling position. The concentration
of toluene at the beginning of the measurement was 3 g/L. In this
figure, the right-hand scale indicates the concentration of toluene
where a signal intensity of 100% is compatible with 3 g/L of toluene.
Interestingly, the concentration increased ca. 25% during the first
few minutes, which could have been due to the introduction of a large
number of, and/or a large size of, toluene droplets. After that, the
concentration of toluene decreased at a rate of ca. 0.2 g/(L min)
from 8 to 16 min. Finally, the signal intensity was decreased by half
compared with the initial (at 2 min) signal intensity, which amounted
to a decrease of ca. 1.5 g/L after 60 min. These toluene concentrations
were still rather high and not suitable for the measurement of absorbance
by UV–vis at 266 nm, and, of course, the decrease in transmittance
that was caused by turbidity should also be taken into account. In
this manner, the creaming behavior can be quantitatively evaluated
using MPI-TOFMS, which can demonstrate the advantage of the present
method.
The changes in the signal intensities obtained by UV–vis
(Figure 3) and MPI-TOFMS
(Figure 4b) differed
slightly. That is, the turbidity was either almost constant or slightly
decreased for the first few minutes when using UV–vis, while
the concentration was somewhat increased when using MPI-TOFMS. Although
further studies are needed, one conceivable reason is as follows.
The present emulsion had a white turbidity and was polydispersed,
and at the monitoring point in the middle part of the cuvette, relatively
large oil droplets, which were moved from a lower position, were first
detected by MPI-TOFMS. Therefore, the local concentration in the middle
portion was increased first. This concentration change, however, only
scarcely contributed to the turbidity. In addition, assuming that
the latter part of the results (from 14 min or later) of Figures 3 and 4b were a single exponential decay, the decay time constants
were calculated to be 34 and 10 min, respectively. In this manner,
the differences in behavior between the turbidity and the concentration
could be detected.
MPI-TOFMS directly provides information concerning
the concentration
of an oil component in an emulsion. This method can also be used to
monitor the multiple constituents in an emulsion.33,34 Therefore, the influence of creaming on each constituent would be
evaluated. We are now studying the formulation for the signal behavior
obtained by MPI-TOFMS for a quantitative evaluation of the creaming
of an emulsion.
Conclusions
In the present study,
an O/W emulsion that showed creaming was
measured via UV–vis and MPI-TOFMS. Transmittance measurement
provided information concerning turbidity, but the measurement of
emulsions with higher levels of turbidity is difficult in principle.
On the other hand, with online mass analysis using MPI-TOFMS, the
change in the concentration of an oil phase accompanied by creaming
could be evaluated. The tendency of the change in the signal intensities
obtained from both methods was slightly different, which suggested
that the two methods provided different information, i.e., the turbidity
and the local concentration of an oil phase. The information for a
local concentration that was obtained by MPI-TOFMS would be difficult
to obtain via conventional UV–vis, which makes MPI-TOFMS a
useful tool for the evaluation of the collapse process of an emulsion.
Supporting Information Available
The Supporting
Information
is available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b02283.Mass spectrum
of toluene of a toluene O/W emulsion (Figure
S1) (PDF)
Supplementary Material
ao8b02283_si_001.pdf
The authors
declare no competing financial interest.
Acknowledgments
T.U. thanks
the University of Fukui for the financial support.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145811610.1021/acsomega.8b02298ArticleMicrowave-Assisted aza-Friedel–Crafts
Arylation of N-Acyliminium Ions: Expedient
Access to 4-Aryl 3,4-Dihydroquinazolinones Sawant Rajiv
T. †Stevens Marc Y. ‡Odell Luke R. *Department of Medicinal Chemistry,
Uppsala Biomedical Center, Uppsala University, P.O. Box 574, SE-751 23 Uppsala, Sweden* E-mail: luke.odell@ilk.uu.se.29 10 2018 31 10 2018 3 10 14258 14265 06 09 2018 12 10 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
A one-pot
microwave-assisted aza-Friedel–Crafts
arylation of N-acyliminium ions, generated in situ
from o-formyl carbamates and different amines, is
reported. This metal-free protocol provides rapid access to diverse
4-aryl 3,4-dihydroquinazolinones in excellent yield without any aqueous
workup. A solvent-directed process for the selective aza-Friedel–Crafts arylation of electron-rich aryl/heteroaryl/butenyl-tethered N-acyliminium ions is also described.
document-id-old-9ao8b02298document-id-new-14ao-2018-02298xccc-price
==== Body
Introduction
N-Acyliminium
ions1−5 are versatile electrophiles that provide direct access to α-substituted
amino derivatives via the intra- or intermolecular addition of various
nucleophiles. In particular, in situ-generated N-acyliminium
ions have been widely exploited in the synthesis of bioactive nitrogen-containing
heterocycles, especially in the preparation of alkaloid natural products.1,2,6,7 Accordingly,
the development of rapid, convenient, and high-yielding protocols
for the selective intra- or intermolecular nucleophilic addition to
cyclic N-acyliminium ions remains a field of considerable
interest.8−11 The C4-substituted quinazolinone framework is known to exhibit a
wide range of biological properties. For example, SM-15811 is a potent
Na+/Ca2+ exchanger inhibitor,12−14 proquazone
is an anti-inflammatory drug,15,16 and 4-disubstituted
3,4-dihydroquinazolinones are T-type channel selective calcium blockers
with in vivo central nervous system efficacy in epilepsy and tremor
models17,18 (Figure 1). Finally, the 3,4-dihydroquinazolinones DPC 961 and
DPC 083 and related analogs are potent human immunodeficiency virus
non-nucleoside reverse transcriptase inhibitors.19,20
Figure 1 Structures
of pharmaceutically important 4-aryl quinazolinones.
The known methods for the synthesis of 4-aryl substituted
3,4-dihydroquinazolinones
include a two-step condensation of aldehyde, urea, and carboxylic
acid,21 and a three-step synthesis from o-amino acetophenones12−14,17,18 and the organocatalytic asymmetric synthesis
of trifluoromethyl 3,4-dihydroquinazolinones based on the aza-Friedel–Crafts reaction of indoles with cyclic N-acylketimines using a chiral phosphoric acid catalyst.22 Xie and co-workers reported the enantioselective aza-Friedel–Crafts reaction of naphthols/phenols
with cyclic N-acylketimines using a chiral quinine-squaramide
catalyst.23 Despite these elegant approaches,
the existing methods require either lengthy reaction sequences or
isolation of cyclic N-acylketimines, which limits
their utility in the generation of diverse 3,4-dihydroquinazolinone
libraries.
During the preparation of this manuscript, Chandrasekharam
and
co-workers reported a water-mediated multicomponent synthesis of 4-aryl
substituted 3,4-dihydroquinazolinones under conventional heating.24 However, it is important to highlight that the
use of water as a reaction medium demanded long reaction times, and,
in many cases, chromatographic purification was required, both of
which detract from its appeal as a green protocol. Moreover, the scope
of this method is restricted to indole and mono-functional amine nucleophiles,
limiting its utility in library generation. In this context, an environmentally
benign and expedient method for the rapid synthesis of 4-aryl 3,4-dihydroquinazolinone
libraries is highly desirable.
As part of our ongoing research
program, we recently reported a
highly efficient solvent-directed diversity-oriented synthesis of
skeletally diverse 3,4-dihydroquinazolinones scaffold libraries based
on N-acyliminium ion chemistry under environmentally
benign reaction conditions.25−29 Our recent findings demonstrated that the intramolecular cyclization
of aryl/heteroaryl tethered nucleophiles with N-acyliminium
ions27 leads to the formation of 3,4-dihydroquinazolinone-embedded
polyheterocycles (Scheme 1). With the aim of developing an expedient approach to 4-aryl/heteroaryl
3,4-dihydroquinazolinones, we were encouraged to investigate the intermolecular
functionalization of N-acyliminium ions (I) with indoles and arenes to produce 4-aryl 3,4-dihydroquinazolinone
scaffold libraries based on a cascade imine/cyclization/aza-Friedel–Crafts reaction sequence. Herein, we present one-pot
microwave-assisted metal-free sequential N-acyliminium
ion/aza-Friedel–Crafts arylation that provides
rapid access to 4-aryl/heteroaryl 3,4-dihydroquinazolinones from readily
available precursors (Scheme 1).
Scheme 1 Proposed Reaction Sequence for the aza-Friedel–Crafts
Arylation of N-Acyliminium Ions
Results and Discussion
We started
our investigation by optimization of the reaction conditions
for the aza-Friedel–Crafts arylation of the N-acyliminium ion generated in situ from o-formyl carbamate 1a and NH4OAc 2a (Scheme 2). We were
pleased to observe that the reaction proceeded in either AcOH or EtOH/AcOH
as the solvent. The reaction between o-formyl carbamate 1a and NH4OAc 2a (2 equiv) in AcOH
under microwave heating at 130 °C for 10 min provided N-acyliminium ion intermediate Ia (confirmed
by liquid chromatography/mass spectrometry (LC/MS)), which upon subsequent
treatment with indole 3a (1.3 equiv) and an additional
20 min of heating at 130 °C produced 4-indolyl 3,4-dihydroquinazolinone 4a in excellent yield (95%). Similarly, the two-step reaction
sequence in EtOH/AcOH (9:1) afforded dihydroquinazolinone 4a in a slightly reduced yield (91%) under optimal protic solvent/Brønsted
acid combinations (Scheme 2).
Scheme 2 Optimization Studies for the aza-Friedel–Crafts
Arylation of an N-Acyliminium Ion
With the optimized reaction conditions in hand,
we first explored
the scope of the aza-Friedel–Crafts arylation
of different cyclic N-acyliminium ions generated
in situ from o-formyl carbamates 1b–1h and NH4OAc 2a with indole 3a in AcOH (Scheme 3). N-Acyliminium ions 1b–1h derived from aldehydes 1b–1h containing electron-donating/withdrawing and halogen substituents
reacted smoothly with indole to afford the corresponding 4-indolyl
3,4-dihydroquinazolinones 4b–4f in
good to excellent yields (86–92%). The introduction of an o-substituent and N-1-benzyl substituent
was also well-tolerated, giving 3,4-dihydroquinazolinones 4g and 4h in good yield. Next, the scope of the indole
nucleophile was explored and indole derivatives containing electron-donating/withdrawing,
and halogen substituents furnished the corresponding 4-indolyl 3,4-dihydroquinazolinones 4i, 4j, and 4n in good to excellent
yield (83–92%). Sterically hindered o-substituted
indoles reacted smoothly, producing 3,4-dihydroquinazolinones 4k–4m in good to excellent yield. The
protocol also worked well with N-methylindole and
7-azaindole to afford 3,4-dihydroquinazolinones 4o and 4p in 84 and 90% yield, respectively (Scheme 3).
Scheme 3 Scope of aza-Friedel–Crafts
Arylation of N-Acyliminium Ions with Indoles
Isolated yield. All reactions
were performed with 1 equiv o-formyl carbamate (1b–1h), 2 equiv NH4OAc (2a) in 1 mL AcOH, 130 °C, MW, 10 min, and then 1.3 equiv
indole (3a–3i) 130 °C, MW, 20–30
min.
Next, to further expand the scope and
applicability of microwave-assisted aza-Friedel–Crafts
arylation of N-acyliminium ions, we investigated
the effect of varying the arene
and amine components (Scheme 4). Our protocol tolerated a wide range of amine nucleophiles,
affording the corresponding 3,4-dihydroquinazolinone in up to 95%
yield. Primary alkyl amines such as benzylamine 2a and
2-thiophenemethylamine 2b worked well to afford N-3-functionalized 3,4-dihydroquinazolinones 6a, 6b in excellent yields (>94%). A one-step three-component
reaction between aldehyde 1a, benzylamine 2b, and indole 3a afforded 6a in reduced
yield (85%) confirming that the two-step sequential approach is preferable. N-Acyliminium ions also reacted smoothly with 1,3-dimethoxybenzene 5a to produce 4-aryl 3,4-dihydroquinazolinones 6c–6e in moderate to good yields. It is important
to highlight that the branched amine N-methyl 4-amino
piperidine 2d was efficiently transformed into 6e, an analog of SM-15811 in satisfactory yield. Finally, m-cresol 5b underwent chemoselective C-functionalization
to produce 6f in 52% yield (Scheme 4).
Scheme 4 Scope of aza-Friedel–Crafts
Arylation of N-Acyliminium Ions with Arenes,
Isolated
yield. Unless otherwise
stated, reactions were performed with 1 equiv o-formyl
carbamate (1b–1h), 2 equiv NH4OAc (2a) and 1.3 equiv amine (2b–2d) in 1 mL AcOH, 130 °C, MW, 10 min, and
then 1.3 equiv Nu (3a/5a/5b) 130 °C, MW, 20–30 min.
One-step reaction in AcOH, MW, 130 °C, 20 min.
Next, we sought to expand the scope of the selective
cascade arylation
reaction using challenging amine nucleophiles bearing pendant electron-rich
aryl/alkenyl moieties (2e–2j, Scheme 5). Gratifyingly,
electron-rich aryl/heteroaryl/butenyl-tethered N-acyliminium
ions were generated in situ from o-formyl carbamate
and amines 2e–2h in EtOH/AcOH (9:1)
and reacted smoothly with indole 3a to afford N-3-aryl/heteroaryl/butenyl-tethered 4-aryl 3,4-dihydroquinazolinones 7a–7d in excellent yield (Scheme 5). However, with indole tethered N-acyliminium ions, intramolecular aza-Friedel–Crafts
cyclization was more favored under the optimized reaction conditions.
The N-acyliminium ion derived from 4-aminomethyl
indole 2i gave 7e in 36% yield along with
the polycyclic product 7e′, whereas the tryptamine
derivative gave only traces of 7f (Scheme 5). It is important to highlight that by changing
the solvent composition the reaction can be paused at the N-acyliminium ion stage, followed by selective functionalization
at the C-4 position with an external indole nucleophile, despite the
presence of a pendant electron-rich aryl, thiophene, indole, or alkene
nucleophile. Thus, the two-step protocol using a minimum of acetic
acid can effectively suppress competing intramolecular aza-Friedel–Crafts27 and aza-Prins cyclization28 reactions, allowing
the selective C-4 functionalization by an indole nucleophile.
Scheme 5 Solvent-Directed Selective 4-Arylation of Aryl/Alkenyl Tethered N-Acyliminium Ions,
Isolated yield. All reactions
were performed with 1 equiv o-formyl carbamate (1a), 1.3 equiv amine (2e–2j) in 1 mL EtOH/AcOH (9:1), 130 °C, MW, 10 min, and then 1.5
equiv Nu (3a) 130 °C, MW, 20 min.
Product not isolated.
Conclusions
In conclusion, we have developed a highly
efficient, metal-free
microwave-assisted aza-Friedel–Crafts arylation
of N-acyliminium ions. The solvent-directed selective aza-Friedel–Crafts arylation of challenging aryl/heteroaryl/butenyl-tethered N-acyliminium ions was achieved to produce 4-aryl 3,4-dihydroquinazolinones.
This protocol offers a rapid and direct approach to generate polyfunctionalized
4-aryl 3,4-dihydroquinazolinone libraries in excellent yields under
environmentally benign reaction conditions and in a short reaction
time. Moreover, the protocols utilize readily available and stable o-formyl carbamate precursors and are compatible with a
broad scope of amine and aryl/heteroaryl nucleophiles. Further investigations
to expand the scope of this approach and explore the biological activity
of these compounds are underway in our laboratory.
Experimental
Section
All reagents and solvents were obtained from commercial
suppliers
and used without further purification. The yields stated refer to
homogenous and spectroscopically pure isolated material. Thin layer
chromatography (TLC, 0.25 mm E. Merck silica plates, 60F-254) was
used to assess reaction progress and the plates were visualized with
254 nm UV light. Silica gel chromatography was performed using E.
Merck silica gel (60 Å pore size, particle size 40–63
nm). 1H NMR spectra were recorded at 400 MHz and 13C NMR spectra at 100 MHz. The chemical shifts for 1H NMR
and 13C NMR were referenced to tetramethylsilane via residual
solvent signals (1H, CDCl3 at 7.26 ppm; 13C, CDCl3 at 77.16 ppm; 1H, DMSO-d6 at 2.45 ppm; 13C, DMSO-d6 at 39.43 ppm; 1H, CD3OD at 3.31 ppm; and 13C, CD3OD at 49.0 ppm).
Microwave reactions were performed in an Initiator single mode reactor
producing controlled irradiation at 2450 MHz and the temperature was
monitored using the built-in online IR sensor. LC/MS was performed
on an instrument equipped with a CP-Sil 8 CB capillary column (50
× 3.0 mm2, particle size 2.6 μm, pore size 100
Å) operating at an ionization potential of 70 eV using a CH3CN/H2O gradient (0.05% HCOOH). High-resolution
mass values were determined using a 7-T hybrid ion trap and a time
of flight detector and an electrospray ionization source. All reactions
were performed in sealed Pyrex microwave-transparent process vials
designed for 0.5–2 mL reaction volumes, unless otherwise stated.
Preparation
of o-Formyl Carbamates
The required known
compounds 1a–1h were prepared from
the corresponding amino alcohols following the
literature procedure.25,26
General Procedure A
One-Pot,
Two-Step Preparation of 4-Aryl 3,4-Dihydroquinazolinones
(4a–4p and 6a–6f) Exemplified by 4a
A 0.5–2
mL Pyrex process vial was charged with aldehyde 1a (40
mg, 224 μmol), NH4OAc 2a (34 mg, 448
μmol), and acetic acid (1 mL). The vial was sealed and subjected
to microwave irradiation at 130 °C for 10 min, after which indole
(3a, 34 mg, 290 μmol) was added. The vial was re-sealed
and heated by microwave at 130 °C for 20 min, and thereafter
the reaction mixture was concentrated in vacuo. Silica gel chromatography
(2–5% MeOH in dichloromethane (DCM) or 30–85% EtOAc
in n-pentane) provided the title compound as a white
solid (56 mg, 95%).
General Procedure B
One-Pot, Two-Step Preparation
of 4-Aryl 3,4-Dihydroquinazolinones
(7a–7e) Exemplified by 7b
A 0.5–2 mL Pyrex process vial was charged with aldehyde 1a (40 mg, 224 μmol), amine 2f (53 mg,
290 μmol), and ethanol/acetic acid (9:1, 1 mL). The vial was
sealed and subjected to microwave irradiation at 130 °C for 10
min, after which indole (3a, 39 mg, 334 μmol) was
added. The vial was re-sealed and heated by microwave at 130 °C
for 20 min, and thereafter the reaction mixture was concentrated in
vacuo. Silica gel chromatography (2–5% MeOH in DCM or 55–70%
EtOAc in n-pentane) provided the title compound as
a white solid (85 mg, 90%).
4-(1H-Indol-3-yl)-3,4-dihydroquinazolin-2(1H)-one (4a)24
Prepared following the general procedure (A), starting
from aldehyde 1a (40 mg, 224 μmol), amine 2a (34 mg, 448 μmol), and nucleophile 3a (34 mg, 290 μmol). Yield: 56 mg (95%); white solid. 1H NMR (DMSO-d6, 400 MHz): δ 10.99–10.90
(m, 1H), 9.27–9.22 (m, 1H), 7.50 (d, J = 7.9
Hz, 1H), 7.35 (d, J = 8.1 Hz, 1H), 7.18–7.14
(m, 2H), 7.11–7.02 (m, 2H), 6.96–6.87 (m, 2H), 6.86–6.81
(m, 1H), 6.79–6.73 (m, 1H), 5.80 (d, J = 2.2
Hz, 1H). 13C NMR (DMSO-d6,
100 MHz): δ 154.1, 137.6, 137.1, 127.9, 127.0, 125.3, 123.5,
122.2, 121.6, 121.2, 119.6, 119.0, 118.7, 114.0, 112.0, 50.9. High
resolution mass spectrometry HRMS (electrospray ionization, ESI):
calcd for C18H17N4O [M + MeCN + H]+ 305.1402; found 305.1418. TLC (SiO2): Rf = 0.06 (60% EtOAc in n-pentane).
4-(5-Methoxy-2-methyl-1H-indol-3-yl)-3,4-dihydroquinazolin-2(1H)-one (4b)
Prepared following the
general procedure (A), starting from aldehyde 1b (40 mg, 191 μmol), amine 2a (29 mg, 376 μmol),
and nucleophile 3a (29 mg, 248 μmol). Yield: 52
mg (92%); white solid. 1H NMR (DMSO-d6, 400 MHz): δ 10.98 (d, J = 2.5 Hz,
1H), 9.12 (d, J = 1.9 Hz, 1H), 7.66–7.48 (m,
1H), 7.37 (m, 1H), 7.18 (d, J = 2.5 Hz, 1H), 7.11
(m 1H), 7.07 (ddd, J = 8.1, 7.0, 1.2 Hz, 1H), 6.94
(ddd, J = 8.0, 7.0, 1.1 Hz, 1H), 6.79 (d, J = 8.7 Hz, 1H), 6.73 (dd, J = 8.7, 2.7
Hz, 1H), 6.56 (d, J = 2.7 Hz, 1H), 5.79 (d, J = 2.3 Hz, 1H), 3.58 (s, 3H). 13C NMR (DMSO-d6, 100 MHz): δ 153.9, 153.7, 136.7, 130.8,
124.9, 123.0, 122.9, 121.2, 119.2, 118.6, 118.2, 114.4, 112.9, 112.2,
111.6, 55.2, 50.6. HRMS (ESI): calcd for C19H19N4O2 [M + MeCN + H]+ 335.1508; found
335.1517. TLC (SiO2): Rf =
0.13 (5% MeOH in DCM).
6-Bromo-4-(1H-indol-3-yl)-3,4-dihydroquinazolin-2(1H)-one (4c)
Prepared following the
general procedure (A), starting from aldehyde 1c (40 mg, 155 μmol), amine 2a (24 mg, 311 μmol),
and nucleophile 3a (47 mg, 292 μmol). Yield: 48
mg (91%); white solid. 1H NMR (DMSO-d6, 400 MHz): δ 11.19–10.92 (m, 1H), 9.56–9.44
(m, 1H), 7.50 (d, J = 7.9 Hz, 1H), 7.39 (d, J = 8.1 Hz, 1H), 7.35–7.31 (m, 1H), 7.28 (dd, J = 8.5, 2.3 Hz, 1H), 7.25 (d, J = 2.5
Hz, 1H), 7.13–7.05 (m, 2H), 7.00–6.93 (m, 1H), 6.81
(d, J = 8.5 Hz, 1H), 5.92–5.82 (m, 1H). 13C NMR (DMSO-d6, 100 MHz): δ
153.3, 136.7, 136.6, 130.3, 129.0, 124.7, 124.3, 123.3, 121.3, 119.0,
118.8, 117.7, 115.7, 112.0, 111.8, 50.1. HRMS (ESI): calcd for C18H16BrN4O [M + MeCN + H]+ 383.0507; found m/z 383.0516.
TLC (SiO2): Rf = 0.15 (5% MeOH
in DCM).
6-Fluoro-4-(1H-indol-3-yl)-3,4-dihydroquinazolin-2(1H)-one (4d)
Prepared following the
general procedure (A), starting from aldehyde 1d (40 mg, 203 μmol), amine 2a (31 mg, 402 μmol),
and nucleophile 4a (31 mg, 265 μmol). Yield: 50
mg (88%); white solid. 1H NMR (DMSO-d6, 400 MHz): δ 11.01 (s, 1H), 9.31 (s, 1H), 7.65–7.48
(m, 1H), 7.48–7.31 (m, 1H), 7.24 (s, 1H), 7.22–7.19
(m, 1H), 7.13–7.04 (m, 1H), 7.01–6.92 (m, 2H), 6.91–6.82
(m, 1H), 6.82–6.75 (m, 1H), 5.84 (s, 1H). 13C NMR
(DMSO-d6, 100 MHz): δ 156.4 (d, 1JCF = 236.1 Hz), 153.2, 136.3,
133.3 (d, 4JCF = 1.9 Hz), 124.3,
123.1 (d, 3JCF = 7.0 Hz), 122.8,
120.8, 118.7, 118.3, 117.1, 114.4 (d, 3JCF = 7.7 Hz), 113.9 (d, 2JCF = 22.7 Hz), 112.50 (d, 2JCF = 23.6 Hz), 111.3, 49.9. HRMS (ESI): calcd for C16H13FN4O [M + H]+ 282.1043;
found 282.1054. TLC (SiO2): Rf = 0.16 (5% MeOH in DCM).
7-Chloro-4-(1H-indol-3-yl)-3,4-dihydroquinazolin-2(1H)-one (4e)
Prepared following the
general procedure (A), starting from aldehyde 1e (40 mg, 187 μmol), amine 2a (29 mg, 376 μmol),
and nucleophile 3a (29 mg, 248 μmol). Yield: 49
mg (88%); white solid. 1H NMR (CD3OD, 400 MHz):
δ 7.41 (m, 1H), 7.35 (m, 1H), 7.19 (s, 1H), 7.09 (ddd, J = 8.2, 7.0, 1.1 Hz, 1H), 6.94 (ddd, J = 8.0, 7.0, 1.1 Hz, 1H), 6.88 (d, J = 2.0 Hz, 1H),
6.82 (dd, J = 8.3, 0.9 Hz, 1H), 6.76 (dd, J = 8.3, 2.0 Hz, 1H), 5.92 (s, 1H). 13C NMR (CD3OD, 100 MHz): δ 153.8, 139.4, 137.4, 132.3, 128.9, 125.4,
123.9, 121.8, 121.4, 121.1, 119.7, 119.3, 118.2, 113.6, 112.3, 50.7.
HRMS (ESI): calcd for C18H16ClN4O
[M + MeCN + H]+ 339.1013; found 339.1029. TLC (SiO2): Rf = 0.09 (5% MeOH in DCM).
4-(1H-Indol-3-yl)-7-(trifluoromethyl)-3,4-dihydroquinazolin-2(1H)-one (4f)
Prepared following the
general procedure (A), starting from aldehyde 1f (40 mg, 162 μmol), amine 2a (25 mg, 324 μmol),
and nucleophile 3a (25 mg, 213 μmol). Yield: 46
mg (86%); white solid. 1H NMR (DMSO-d6, 400 MHz): δ 11.17–10.91 (m, 1H), 9.85–9.48
(m, 1H), 7.54–7.48 (m, 1H), 7.45–7.41 (m, 1H), 7.41–7.36
(m, 1H), 7.28–7.22 (m, 1H), 7.20–7.14 (m, 2H), 7.14–7.05
(m, 2H), 6.99–6.93 (m, 1H), 5.94 (s, 1H). 13C NMR
(DMSO-d6, 100 MHz): δ 152.7, 137.5,
136.3, 127.9 (q, 2JCF = 31.8
Hz), 127.2, 125.7 (q, 4JCF =
1.2 Hz), 123.6 (q, 1JCF = 272.1
Hz), 124.3, 123.0, 120.9, 118.6, 118.4, 116.9, 115.95 (q, 3JCF = 4.5 Hz), 111.3, 109.5 (q, 3JCF = 4.2 Hz), 49.9. HRMS (ESI):
calcd for C19H16F3N4O
[M + MeCN + H]+ 373.1276; found 373.1281. TLC (SiO2): Rf = 0.15 (5% MeOH in DCM).
4-(1H-Indol-3-yl)-8-methoxy-3,4-dihydroquinazolin-2(1H)-one (4g)
Prepared following the
general procedure (A), starting from aldehyde 1g (40 mg, 191 μmol), amine 2a (29 mg, 376 μmol),
and nucleophile 3a (29 mg, 248 μmol). Yield: 45
mg (80%); white solid. 1H NMR (CDCl3/CD3OD, 400 MHz): δ 7.31–7.24 (m, 1H), 7.23–7.16
(m, 1H), 7.03 (s, 1H), 6.97–6.90 (m, 1H), 6.82–6.76
(m, 1H), 6.68–6.64 (m, 2H), 6.46–6.37 (m, 1H), 5.82
(s, 1H), 3.76 (s, 3H). 13C NMR (CDCl3/CD3OD, 100 MHz): δ 156.2, 146.5, 138.3, 126.1, 126.0, 124.2,
123.1, 122.9, 122.5, 120.0, 119.7, 117.8, 56.3, 52.5. HRMS (ESI):
calcd for C19H19N4O2 [M
+ MeCN + H]+ 335.1508; found 335.1524. TLC (SiO2): Rf = 0.16 (5% MeOH in DCM).
1-Benzyl-4-(1H-indol-3-yl)-3,4-dihydroquinazolin-2(1H)-one (4h)
Prepared following the
general procedure (A), starting from aldehyde 1h (40 mg, 149 μmol), amine 2a (23 mg, 298 μmol),
and nucleophile 3a (23 mg, 196 μmol). Yield: 45
mg (86%); white solid. 1H NMR (CDCl3, 400 MHz):
δ 8.34 (s, 1H), 7.66–7.49 (m, 1H), 7.42–7.29 (m,
6H), 7.25–7.17 (m, 1H), 7.15–7.05 (m, 3H), 6.98–6.90
(m, 1H), 6.88–6.81 (m, 2H), 6.00 (s, 1H), 5.55 (s, 1H), 5.29
(d, J = 16.6 Hz, 1H), 5.21 (d, J = 16.6 Hz, 1H). 13C NMR (CDCl3, 100 MHz):
δ 155.5, 137.8, 137.6, 137.0, 128.8, 128.3, 127.1, 126.9, 126.6,
125.4, 124.0, 123.4, 122.7, 122.4, 120.2, 119.7, 117.0, 114.3, 111.7,
51.0, 46.2. HRMS (ESI): calcd for C23H20N3O [M + MeCN + H]+ 354.1606; found 354.1606. TLC
(SiO2): Rf = 0.13 (5% MeOH
in DCM).
4-(5-Methyl-1H-indol-3-yl)-3,4-dihydroquinazolin-2(1H)-one (4i)
Prepared following the
general procedure (A), starting from aldehyde 1a (40 mg, 224 μmol), amine 2a (34 mg, 441 μmol),
and nucleophile 3b (38 mg, 290 μmol). Yield: 57
mg (92%); yellow solid. 1H NMR (DMSO-d6, 400 MHz): δ 10.87 (s, 1H), 9.29 (s, 1H), 7.36–7.33
(m, 1H), 7.31–7.26 (m, 1H), 7.20–7.17 (m, 1H), 7.16–7.10
(m, 2H), 7.01–6.87 (m, 3H), 6.84–6.78 (m, 1H), 6.10–5.68
(m, 1H), 2.35 (s, 3H). 13C NMR (DMSO-d6, 100 MHz): δ 153.8, 137.2, 135.1, 127.5, 126.9,
126.5, 125.2, 123.2, 122.8, 121.9, 120.8, 118.8, 117.5, 113.6, 111.3,
50.5, 21.4. HRMS (ESI): calcd for C19H19N4O [M + MeCN + H]+ 319.1559; found m/z 319.1575. TLC (SiO2): Rf = 0.16 (5% MeOH in DCM).
4-(5-Bromo-1H-indol-3-yl)-3,4-dihydroquinazolin-2(1H)-one (4j)
Prepared following the
general procedure (A), starting from aldehyde 1a (40 mg, 224 μmol), amine 2a (34 mg, 441 μmol),
and nucleophile 3c (57 mg, 291 μmol). Yield: 70
mg (91%); white solid. 1H NMR (DMSO-d6, 400 MHz): δ 11.17 (br s, 1H), 9.29 (br s, 1H), 7.67
(d, J = 1.9 Hz, 1H), 7.33 (d, J =
8.6 Hz, 1H), 7.21–7.14 (m, 2H), 7.11–7.08 (m, 1H), 6.93
(d, J = 7.5 Hz, 1H), 6.85 (dd, J = 8.0, 1.2 Hz, 1H), 6.79 (ddd, J = 7.5, 7.5, 1.2
Hz, 1H), 5.80 (s, 1H). 13C NMR (DMSO-d6, 100 MHz): δ 153.7, 137.2, 135.4, 127.7, 126.7,
126.5, 124.8, 123.7, 121.5, 121.4, 121.0, 118.1, 113.7, 111.4, 50.1.
HRMS (ESI): calcd for C18H16BrN4O
[M + MeCN + H]+ 383.0507; found 383.0502. TLC (SiO2): Rf = 0.16 (5% MeOH in DCM).
4-(2-Methyl-1H-indol-3-yl)-3,4-dihydroquinazolin-2(1H)-one (4k)
Prepared following the
general procedure (A), starting from aldehyde 1a (40 mg, 224 μmol), amine 2a (34 mg, 441 μmol),
and nucleophile 3d (38 mg, 290 μmol). Yield: 58
mg (93%); white solid. 1H NMR (DMSO-d6, 400 MHz): δ 10.93 (s, 1H), 9.28 (s, 1H), 7.34–7.26
(m, 1H), 7.26–7.20 (m, 1H), 7.11 (m, 1H), 7.01–6.96
(m, 1H), 6.89–6.81 (m, 2H), 6.77–6.72 (m, 2H), 5.95
(s, 1H), 2.46 (s, 3H). 13C NMR (DMSO-d6, 100 MHz): δ 153.7, 137.7, 135.8, 133.2, 127.9,
127.0, 126.7, 121.9, 121.2, 120.5, 118.8, 113.9, 113.7, 110.9, 49.9,
11.8. HRMS (ESI): calcd for C19H19N4O [M + MeCN + H]+ 319.1551; found 319.1559. TLC (SiO2): Rf = 0.16 (5% MeOH in DCM).
4-(2-Phenyl-1H-indol-3-yl)-3,4-dihydroquinazolin-2(1H)-one (4l)
Prepared following the
general procedure (A), starting from aldehyde 1a (40 mg, 224 μmol), amine 2a (34 mg, 441 μmol),
and nucleophile 3e (56 mg, 290 μmol). Yield: 69
mg (91%); yellow solid. 1H NMR (DMSO-d6, 400 MHz): δ 11.43 (s, 1H), 9.35 (d, J = 1.9 Hz, 1H), 7.81–7.73 (m, 2H), 7.63–7.55 (m, 2H),
7.54–7.47 (m, 1H), 7.45–7.41 (m, 1H), 7.37–7.32
(m, 1H), 7.29–7.24 (m, 1H), 7.17–7.05 (m, 2H), 6.98–6.91
(m, 1H), 6.89 (dd, J = 8.0, 1.1 Hz, 1H), 6.70 (m,
1H), 6.61–6.54 (m, 1H), 5.99 (s, 1H). 13C NMR (DMSO-d6, 100 MHz): δ 153.8, 137.6, 136.8, 136.8,
132.6, 129.3, 129.2, 128.5, 128.1, 126.7, 126.5, 122.0, 121.6, 121.3,
120.3, 119.3, 114.0, 113.5, 111.8, 50.5. HRMS (ESI): calcd for C24H21N4O [M + MeCN + H]+ 381.1715;
found 381.1730. TLC (SiO2): Rf = 0.20 (5% MeOH in DCM).
4-(5-Methoxy-1H-indol-3-yl)-3,4-dihydroquinazolin-2(1H)-one (4m)
Prepared following the
general procedure (A) starting from aldehyde 1a (40 mg, 224 μmol), amine 2a (34 mg, 441 μmol),
and nucleophile 3f (47 mg, 292 μmol). Yield: 52
mg (76%); pink solid. 1H NMR (DMSO-d6, 400 MHz): δ 10.76 (s, 1H), 9.34 (d, J = 1.9 Hz, 1H), 7.17 (d, J = 8.7 Hz, 1H), 7.15–7.09
(m, 1H), 7.01–6.96 (m, 1H), 6.90–6.85 (m, 1H), 6.81–6.74
(m, 3H), 6.65 (dd, J = 8.7, 2.5 Hz, 1H), 5.90 (d, J = 1.7 Hz, 1H), 3.64 (s, 3H), 2.43 (s, 3H). 13C NMR (DMSO-d6, 100 MHz): δ 153.8,
153.2, 137.8, 133.8, 130.8, 127.9, 127.2, 127.1, 121.8, 121.3, 114.0,
113.8, 111.4, 109.5, 101.7, 55.5, 49.9, 11.9. HRMS (ESI): calcd for
C20H21N4O2 [M + MeCN +
H]+ 349.1665; found 349.1669. TLC (SiO2): Rf = 0.16 (5% MeOH in DCM).
Methyl 3-(2-oxo-1,2,3,4-Tetrahydroquinazolin-4-yl)-1H-indole-4-carboxylate (4n)
Prepared
following the general procedure (A), starting from aldehyde 1a (40 mg, 224 μmol), amine 2a (34 mg,
441 μmol), and nucleophile 3g (51 mg, 291 μmol).
Yield: 60 mg (83%); white solid. 1H NMR (DMSO-d6, 400 MHz): δ 11.46 (s, 1H), 9.28 (s, 1H), 7.75–7.66
(m, 2H), 7.27–7.20 (m, 1H), 7.19–7.14 (m, 1H), 7.03–6.97
(m, 1H), 6.93–6.88 (m, 1H), 6.87–6.83 (m, 1H), 6.84–6.73
(m, 2H), 6.27 (d, J = 2.5 Hz, 1H), 3.93 (s, 3H). 13C NMR (DMSO-d6, 100 MHz): δ
168.7, 154.1, 137.8, 137.6, 127.6, 126.9, 126.4, 123.1, 122.8, 122.6,
122.3, 121.1, 120.3, 118.8, 117.0, 113.8, 52.2, 49.8. HRMS (ESI):
calcd for C18H16N3O3 [M
+ H]+ 322.1192; found 322.1202. TLC (SiO2): Rf = 0.17 (5% MeOH in DCM).
4-(1-Methyl-1H-indol-3-yl)-3,4-dihydroquinazolin-2(1H)-one (4o)24
Prepared
following the general procedure (A), starting from aldehyde 1a (40 mg, 224 μmol), amine 2a (34 mg,
441 μmol), and nucleophile 3h (38 mg, 290 μmol).
Yield: 52 mg (84%); white solid. 1H NMR (DMSO-d6, 400 MHz): δ 9.27 (d, J = 1.9
Hz, 1H), 7.56 (m, 1H), 7.40 (m, 1H), 7.21 (t, J =
2.2 Hz, 1H), 7.15 (s, 1H), 7.17–7.07 (m, 1H), 7.13–7.06
(m, 1H), 6.99 (ddd, J = 8.0, 7.0, 1.0 Hz, 1H), 7.00–6.93
(m, 1H), 6.86 (dd, J = 8.0, 1.2 Hz, 1H), 6.78 (m,
1H), 5.82 (d, J = 2.2 Hz, 1H), 3.74 (s, 3H). 13C NMR (DMSO-d6, 100 MHz): δ
153.7, 137.1, 127.6, 127.2, 126.5, 125.3, 121.7, 121.3, 120.8, 119.4,
118.8, 117.6, 113.7, 109.8, 50.2, 32.3. HRMS (ESI): calcd for C19H19N4O [M + MeCN + H]+ 319.1559;
found m/z 319.1567. TLC (SiO2): Rf = 0.08 (60% EtOAc in n-pentane).
4-(1H-Pyrrolo[2,3-b]pyridin-3-yl)-3,4-dihydroquinazolin-2(1H)-one (4p)
Prepared following the
general procedure (A), starting from aldehyde 1a (40 mg, 224 μmol), amine 2a (34 mg, 441 μmol),
and nucleophile 3i (34 mg, 288 μmol). Yield: 53
mg (90%); white solid. 1H NMR (DMSO-d6, 400 MHz): δ 11.53 (s, 1H), 9.31 (s, 1H), 8.19 (d, J = 4.6 Hz, 1H), 7.85 (d, J = 7.9 Hz, 1H),
7.33–7.26 (m, 2H), 7.17–7.08 (m, 1H), 7.05–6.95
(m, 2H), 6.91–6.84 (m, 1H), 6.83–6.78 (m, 1H), 6.07–5.61
(m, 1H). 13C NMR (DMSO-d6,
100 MHz): δ 153.7, 148.9, 142.7, 137.1, 127.7, 127.3, 126.6,
123.3, 121.3, 121.0, 117.2, 117.2, 115.2, 113.7, 50.5. HRMS (ESI):
calcd for C15H13N4O [M + H]+ 265.1089; found 265.1076. TLC (SiO2): Rf = 0.09 (5% MeOH in DCM).
3-Benzyl-4-(1H-indol-3-yl)-3,4-dihydroquinazolin-2(1H)-one (6a)24
Prepared following
the general procedure (A), starting
from aldehyde 1a (40 mg, 224 μmol), amine 2b (36 mg, 336 μmol), and nucleophile 3a (34 mg, 290 μmol). Yield: 75 mg (95%); yellow solid. 1H NMR (CDCl3/CD3OD, 400 MHz): δ
11.14 (d, J = 2.5 Hz, 1H), 9.70 (s, 1H), 7.53–7.48
(m, 1H), 7.47–7.45 (m, 1H), 7.44–7.35 (m, 3H), 7.34–7.27
(m, 3H), 7.15–7.07 (m, 2H), 7.04–6.94 (m, 2H), 6.92
(dd, J = 8.0, 1.1 Hz, 1H), 6.78 (m, 1H), 5.75 (s,
1H), 5.17 (d, J = 15.5 Hz, 1H), 3.77 (d, J = 15.4 Hz, 1H). 13C NMR (CDCl3/CD3OD, 100 MHz): δ 155.8, 138.5, 138.3, 136.6, 129.5, 128.9,
128.7, 128.3, 128.1, 126.1, 124.7, 123.0, 122.8, 122.5, 120.3, 119.9,
117.0, 114.7, 112.6, 56.5, 47.8. HRMS (ESI): calcd for C23H20N3O [M + H]+ 354.1606; found
354.1613. TLC (SiO2): Rf =
0.20 (40% EtOAc in n-pentane).
4-(1H-Indol-3-yl)-3-(thiophen-2-ylmethyl)-3,4-dihydroquinazolin-2(1H)-one (6b)
Prepared following the
general procedure (A), starting from aldehyde 1a (40 mg, 224 μmol), amine 2c (33 mg, 292 μmol),
and nucleophile 3a (34 mg, 290 μmol). Yield: 76
mg (94%); white solid. 1H NMR (CDCl3/CD3OD, 400 MHz): δ 7.44 (m, 1H), 7.38 (m, 1H), 7.35 (s,
1H), 7.31 (dd, J = 4.8, 1.6 Hz, 1H), 7.14–7.07
(m, 2H), 6.99–6.95 (m, 2H), 6.95–6.91 (m, 1H), 6.91–6.86
(m, 2H), 6.79 (m, 1H), 5.86 (s, 1H), 5.29 (dd, J =
15.5, 0.9 Hz, 1H), 4.07 (d, J = 15.5 Hz, 1H). 13C NMR (CDCl3/CD3OD, 100 MHz): δ
156.1, 141.8, 139.4, 137.3, 129.8, 129.1, 128.7, 128.4, 127.2, 127.1,
126.0, 123.9, 123.8, 123.3, 121.3, 120.9, 117.5, 115.6, 113.6, 57.1,
43.7. HRMS (ESI): calcd for C21H18N3OS [M + H]+ 360.1171; found 360.1168. TLC (SiO2): Rf = 0.16 (5% MeOH in DCM).
3-Benzyl-4-(2,4-dimethoxyphenyl)-3,4-dihydroquinazolin-2(1H)-one (6c)
Prepared following the
general procedure (A) but with 30 min of heating in the
second step, starting from aldehyde 1a (40 mg, 224 μmol),
amine 2b (36 mg, 336 μmol), and nucleophile 5a (40 mg, 289 μmol). Yield: 72 mg (86%); yellow solid. 1H NMR (CDCl3, 400 MHz): δ 8.96 (s, 1H), 7.51
(m, 5H), 7.45–7.40 (m, 1H), 7.30 (m, 1H), 7.22–7.15
(m, 1H), 7.08–6.93 (m, 2H), 6.77–6.57 (m, 2H), 6.05
(s, 1H), 5.62 (d, J = 15.1 Hz, 1H), 4.01 (s, 6H),
3.93 (d, J = 15.1 Hz, 1H). 13C NMR (DMSO-d6, 100 MHz): δ 160.1, 157.0, 153.4, 137.8,
136.4, 128.4, 127.9, 127.7, 127.4, 127.1, 125.9, 122.9, 121.6, 121.1,
113.6, 105.7, 98.6, 55.6, 55.2, 54.6, 46.8. HRMS (ESI): calcd for
C23H23N2O3 [M + H]+ 375.1709; found 375.1711. TLC (SiO2): Rf = 0.26 (40% EtOAc in n-pentane).
4-(2,4-Dimethoxyphenyl)-3,4-dihydroquinazolin-2(1H)-one (6d)
Prepared following the general procedure
(A) but with 30 min of heating in the second step, starting
from aldehyde 1a (40 mg, 224 μmol), amine 2a (34 mg, 441 μmol), and nucleophile 5a (40 mg, 289 μmol). Yield: 35 mg (55%); white solid. 1H NMR (DMSO-d6, 400 MHz,): δ 9.21
(s, 1H), 7.17–7.07 (m, 1H), 7.05–6.95 (m, 3H), 6.86–6.79
(m, 2H), 6.64–6.59 (m, 1H), 6.54–6.48 (m, 1H), 5.80
(d, J = 2.4 Hz, 1H), 3.86 (s, 3H), 3.76 (s, 3H). 13C NMR (DMSO-d6, 400 MHz,): δ
159.4, 156.2, 153.6, 136.7, 127.3, 127.2, 125.8, 124.9, 121.2, 120.6,
113.3, 104.6, 98.1, 55.2, 54.8, 50.2. HRMS (ESI): calcd for C18H20N3O3 [M + MeCN + H]+ 326.1505; found 326.1508. TLC (SiO2): Rf = 0.21 (5% MeOH in DCM).
4-(2,4-Dimethoxyphenyl)-3-(1-methylpiperidin-4-yl)-3,4-dihydroquinazolin-2(1H)-one (6e)
Prepared following the
general procedure (A) but with 30 min of heating the
second step, starting from aldehyde 1a (40 mg, 224 μmol),
amine 2d (33 mg, 289 μmol), and nucleophile 5a (68 mg, 492 μmol). Yield: 43 mg (50%); white solid. 1H NMR (CDCl3, 400 MHz): δ 7.47 (s, 1H), 7.24–7.20
(m, 2H), 7.08–6.96 (m, 1H), 6.86–6.76 (m, 1H), 6.65–6.58
(m, 1H), 6.40–6.31 (m, 1H), 6.29 (dd, J =
8.5, 2.4 Hz, 1H), 5.95 (s, 1H), 4.41–4.14 (m, 1H), 3.84 (s,
3H), 3.67 (s, 3H), 2.95 (d, J = 10.7 Hz, 1H), 2.79
(d, J = 11.7 Hz, 1H), 2.24 (s, 3H), 2.21–1.97
(m, 4H), 1.59 (d, J = 12.1 Hz, 1H), 1.45 (m, 2H). 13C NMR (CDCl3, 100 MHz): δ 160.0, 155.3,
154.9, 135.0, 127.5, 127.0, 125.3, 125.0, 123.2, 121.8, 113.3, 104.4,
98.2, 55.2, 55.0, 54.9, 54.8, 52.2, 51.4, 45.2, 29.4, 28.7, 21.8.
HRMS (ESI): calcd for C22H28N3O3 [M + H]+ 382.2131; found 382.2132. TLC (SiO2): Rf = 0.23 (10% MeOH in DCM).
4-(4-Hydroxy-2-methylphenyl)-3,4-dihydroquinazolin-2(1H)-one (6f)
Prepared following the
general procedure (A) but with 30 min in heating the
second step, starting from aldehyde 1a (40 mg, 224 μmol),
amine 2a (33 mg, μmol), and nucleophile 5b (31 mg, 289 μmol). Yield: 30 mg (52%); white solid. 1H NMR (DMSO-d6, 400 MHz): δ 9.62
(s, 1H), 9.15 (s, 1H), 7.07 (t, J = 7.9 Hz, 2H),
6.95 (s, 1H), 6.89 (d, J = 7.8 Hz, 1H), 6.81–6.74
(m, 2H), 6.63 (s, 1H), 6.55 (d, J = 7.8 Hz, 1H),
5.79 (d, J = 2.3 Hz, 1H), 2.17 (s, 3H). 13C NMR (DMSO-d6, 100 MHz): δ 154.0,
153.4, 137.5, 137.0, 128.5, 127.5, 126.9, 126.3, 121.9, 120.9, 119.9,
115.9, 113.6, 50.7, 20.7. HRMS (ESI): calcd for C15H15N2O2 [M + H]+ 255.1143;
found 255.1134. TLC (SiO2): Rf = 0.22 (5% MeOH in DCM).
4-(1H-Indol-3-yl)-3-(3-methoxyphenethyl)-3,4-dihydroquinazolin-2(1H)-one (7a)
Prepared following the
general procedure (B), starting from aldehyde 1a (40 mg, 224 μmol), amine 2e (43 mg, 290 μmol),
and nucleophile 3a (39 mg, 334 μmol). Yield: 82
mg (92%); off-white solid. 1H NMR (CDCl3, 400
MHz): δ 8.33–8.20 (m, 1H), 7.99 (s, 1H), 7.56 (m, 1H),
7.34 (m, 1H), 7.20–7.13 (m, 3H), 7.13–7.04 (m, 2H),
6.91–6.86 (m, 1H), 6.79 (ddd, J = 14.3, 7.7,
1.1 Hz, 2H), 6.74 (dd, J = 7.9, 2.1 Hz, 2H), 6.67–6.63
(m, 1H), 5.59 (s, 1H), 4.01 (ddd, J = 14.0, 9.0,
5.0 Hz, 1H), 3.66 (s, 3H), 3.22 (ddd, J = 13.8, 8.7,
7.1 Hz, 1H), 2.95 (ddd, J = 13.2, 9.0, 7.1 Hz, 1H),
2.71 (ddd, J = 13.4, 8.6, 5.0 Hz, 1H). δ 13C NMR (CDCl3, 100 MHz): δ 159.7, 154.1,
141.3, 136.7, 135.7, 129.6, 128.2, 126.8, 125.4, 122.8, 122.6, 122.1,
121.6, 121.3, 120.3, 119.4, 117.5, 114.3, 113.8, 112.2, 111.6, 56.9,
55.2, 47.3, 34.6. HRMS (ESI): calcd for [M + H]+ 398.1869;
found 398.1873. TLC (SiO2): Rf = 0.13 (50% EtOAc in n-pentane).
3-(3,4-Dimethoxyphenethyl)-4-(1H-indol-3-yl)-3,4-dihydroquinazolin-2(1H)-one (7b)
Prepared following the
general procedure (B), starting from aldehyde 1a (40 mg, 224 μmol), amine 2f (53 mg, 290 μmol),
and nucleophile 3a (39 mg, 334 μmol). Yield: 85
mg (90%); white solid. 1H NMR (CDCl3/CD3OD, 400 MHz): δ 7.33–7.24 (m, 2H), 7.21–7.13
(m, 1H), 7.03–6.95 (m, 1H), 6.96–6.87 (m, 2H), 6.85–6.76
(m, 1H), 6.71–6.53 (m, 4H), 6.50–6.36 (m, 2H), 5.40
(s, 1H), 3.70–3.56 (m, 4H), 3.47 (s, 3H), 3.07–2.87
(m, 1H), 2.73–2.61 (m, 1H), 2.52–2.37 (m, 1H). 13C NMR (CDCl3/CD3OD, 100 MHz): δ
154.6, 148.9, 147.6, 137.1, 135.4, 132.4, 128.2, 127.0, 125.4, 123.6,
122.5, 122.2, 121.8, 121.0, 119.8, 119.0, 116.5, 113.9, 112.3, 111.9,
111.7, 57.2, 56.0, 55.7, 47.6, 33.9. HRMS (ESI): calcd for C26H26N3O3 [M + H]+ 428.1974;
found 428.1977. TLC (SiO2): Rf = 0.10 (50% EtOAc in n-pentane).
4-(1H-Indol-3-yl)-3-(2-(thiophen-2-yl)ethyl)-3,4-dihydroquinazolin-2(1H)-one (7c)
Prepared following the
general procedure (B), starting from aldehyde 1a (40 mg, 224 μmol), amine 2g (37 mg, 290 μmol),
and nucleophile 3a (39 mg, 334 μmol). Yield: 80
mg (96%); light yellow solid. 1H NMR (CDCl3,
400 MHz): δ 8.32–8.24 (m, 1H), 8.15 (s, 1H), 7.58 (m,
1H), 7.35 (m, 1H), 7.21–7.13 (m, 2H), 7.14–7.03 (m,
3H), 6.94–6.85 (m, 2H), 6.83–6.70 (m, 3H), 5.67 (s,
1H), 4.01 (ddd, J = 13.3, 8.4, 5.2 Hz, 1H), 3.34–3.15
(m, 2H), 3.00–2.84 (m, 1H). 13C NMR (CDCl3, 100 MHz): δ 154.1, 141.8, 136.7, 135.6, 128.2, 127.1, 126.8,
125.4, 125.3, 123.8, 122.9, 122.7, 122.2, 121.5, 120.4, 119.4, 117.5,
113.9, 111.6, 57.2, 47.5, 28.5. HRMS (ESI): calcd for C22H29N3OS [M + H]+ 374.1327; found
374.1324. TLC (SiO2): Rf =
0.15 (50% EtOAc in pentane).
3-(But-3-en-1-yl)-4-(1H-indol-3-yl)-3,4-dihydroquinazolin-2(1H)-one (7d)
Prepared following the
general procedure (B), starting from aldehyde 1a (40 mg, 224 μmol), amine 2h (21 mg, 290 μmol),
and nucleophile 3a (39 mg, 334 μmol). Yield: 68
mg (96%); off-white solid. 1H NMR (CDCl3, 400
MHz): δ 8.32 (s, 1H), 8.05 (s, 1H), 7.63 (dd, J = 7.9, 1.1 Hz, 1H), 7.35 (m, 1H), 7.22–7.14 (m, 2H), 7.09
(m, 2H), 7.01 (ddd, J = 7.7, 1.5, 0.7 Hz, 1H), 6.85–6.72
(m, 2H), 5.88 (s, 1H), 5.78 (m, 1H), 5.15–4.88 (m, 2H), 3.91
(ddd, J = 13.9, 8.7, 6.4 Hz, 1H), 3.04 (ddd, J = 14.2, 8.6, 5.9 Hz, 1H), 2.47–2.35 (m, 1H), 2.33–2.20
(m, 1H). 13C NMR (CDCl3, 100 MHz): δ 154.2,
136.7, 135.7, 135.6, 128.2, 126.8, 125.4, 122.7, 122.6, 122.1, 121.5,
120.3, 119.4, 117.6, 116.7, 113.9, 111.6, 56.4, 44.7, 32.2. HRMS (ESI):
calcd for [M + H]+ 318.1606; found 318.1606. TLC (SiO2): Rf = 0.2 (50% EtOAc in n-pentane).
3-((1H-Indol-4-yl)methyl)-4-(1H-indol-3-yl)-3,4-dihydroquinazolin-2(1H)-one (7e)
Prepared following the general procedure
(B), starting from aldehyde 1a (40 mg, 224
μmol),
amine 2i (42 mg, 290 μmol), and nucleophile 3a (39 mg, 334 μmol). Yield: 32 mg (36%); off-white
solid. 1H NMR (DMSO-d6, 400
MHz): δ 11.13 (d, J = 13.2 Hz, 2H), 9.66 (s,
1H), 8.28 (s, 1H), 7.48 (d, J = 8.0 Hz, 1H), 7.42–7.23
(m, 4H), 7.05 (m, 3H), 6.90 (m, 4H), 6.68 (m, 1H), 6.45 (s, 1H), 5.60
(s, 1H), 5.50 (d, J = 15.0 Hz, 1H), 3.83 (d, J = 15.0 Hz, 2H). 13C NMR (DMSO-d6, 100 MHz): δ 152.9, 137.1, 136.3, 136.2, 128.4,
127.8, 127.1, 126.7, 125.3, 124.7, 124.0, 121.6, 121.3, 121.2, 121.0,
119.2, 119.0, 118.5, 116.3, 113.6, 112.1, 111.0, 99.8, 54.6, 44.7.
HRMS (ESI): calcd for [M + H]+ 393.1715; found 393.1729.
TLC (SiO2): Rf = 0.1 (50% EtOAc
in n-pentane).
Supporting Information Available
The Supporting Information
is available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b02298.Copies of 1H and 13C NMR spectra
for all compounds (PDF)
Supplementary Material
ao8b02298_si_001.pdf
Author Present Address
‡ Department of Radiology, Stanford University, Stanford, California
94306, United States (M.Y.S.).
Author Present Address
† Beactica
AB, Uppsala Business Park, Virdings allé 2, 75450
Uppsala, Sweden (R.T.S.).
The authors
declare no competing financial interest.
Acknowledgments
This research
was supported by Uppsala University. The authors
thank Dr Lisa Haigh (Imperial College London) for assistance with
HRMS determination.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145894110.1021/acsomega.8b00985ArticleHexagon Flower Quantum Dot-like Cu Pattern Formation during Low-Pressure
Chemical Vapor Deposited Graphene Growth on a Liquid Cu/W Substrate Pham Phuong V. *SKKU Advanced Institute of Nano Technology
(SAINT), SKKU, Suwon, Gyeonggi-do 440-746, Republic of KoreaCenter for Multidimensional Carbon
Materials, Institute for Basic Science, Ulsan 44919, Republic of Korea* E-mail: pvphuong@skku.edu.18 07 2018 31 07 2018 3 7 8036 8041 12 05 2018 09 07 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under a Creative Commons Attribution (CC-BY) License, which permits unrestricted use, distribution and reproduction in any medium, provided the author and source are cited.
The
H2-induced etching of low-dimensional materials is of significant
interest for controlled architecture design of crystalline materials
at the micro- and nanoscale. This principle is applied to the thinnest
crystalline etchant, graphene. In this study, by using a high H2 concentration, the etched hexagonal holes of copper quantum
dots (Cu QDs) were formed and embedded into the large-scale graphene
region by low-pressure chemical vapor deposition on a liquid Cu/W
surface. With this procedure, the hexagon flower-etched Cu patterns
were formed in a H2 environment at a higher melting temperature
of Cu foil (1090 °C). The etching into the large-scale graphene
was confirmed by optical microscopy, atomic force microscopy, scanning
electron microscopy, and Raman analysis. This first observation could
be an intriguing case for the fundamental study of low-dimensional
material etching during chemical vapor deposition growth; moreover,
it may supply a simple approach for the controlled etching/growth.
In addition, it could be significant in the fabrication of controllable
etched structures based on Cu QD patterns for nanoelectronic devices
as well as in-plane heterostructures on other low-dimensional materials
in the near future.
document-id-old-9ao8b00985document-id-new-14ao-2018-00985accc-price
==== Body
Introduction
Graphene, a honeycomb crystal
carbon lattice, has attracted huge research interest during the past
few years due to its anomalous properties, including very high carrier
mobility, extremely high mechanical strength and optical transparency,
electrical conductivity, etc.1−25 As a result, graphene is considered to be an ideal nanomaterial
for next-generation semiconductors to replace silicon.
The etching
of material is the block removal from a material matrix by chemical
or physical methods—the reverse of the growth process. Understanding
the etching mechanism is necessary for material design as well as
the realization of its capabilities. Material growth/etching requires
a high-energy barrier nucleation process. Controlling the etching/growing
parameters may originate from the formation of a thermodynamic and
stably ordered structure with the ability to form a different kinetically
controlled metastable structures with high-energy crystal facets and
edges.
The material growth systems have been controlled with
different scales (nanometer to micrometer).26−28 The family
of snow-crystal-like graphene with patterns is formed by a nonlinear
process in nature.29 In contrast, the highly
crystalline materials (e.g., Si) are etched via an anisotropic rule,30 leading to stable etched patterns with Euclidean
geometries. The underlying mechanism is attributed to various etching
rates on various crystalline directions and surfaces related to various
free energies. However, the etched structures of low-dimensional materials
beyond Euclidean geometries have not been investigated.
The
high crystal C atom single-layer supplies a simple model to study
the fundamental growth and/or etching process via the chemical vapor
deposition (CVD) method. Significant efforts have been created to
develop graphene growth strategies with controlled size, crystallinity,
and edge structures via CVD.31−34 In addition, several reports on graphene etching
have been carried out utilizing various etchants, such as plasma H2,35−38 H2,39,40 and metallic nanoparticles.41−43 Recently, graphene crystal patterns were well-controlled through
inert gases and a H2 source.44
Those discoveries inspired us to additionally examine the
fundamental issue of the graphene etching mode. In this work, we report
the first observation of a new kind of etched geometry of a large-scale
grown graphene region that is beyond known Euclidean geometries to
date. The hexagon quantum dot (QD)-like etched Cu pattern is a new
morphology that has not yet been revealed.
Results and Discussion
For the etched graphene growth procedure on a liquid Cu/W substrate,
a schematic of the hexagon QD-like Cu pattern formation during low-pressure
CVD graphene growth onto a liquid Cu/W substrate is illustrated in Figure 1. Low-pressure chemical
vapor deposition (LPCVD) is investigated at low pressure (6 Torr)
using Cu (thickness of 250 μm) as a catalytic substrate located
on a W foil (thickness of 80 μm). First, a Cu/W substrate was
heated in the H2 environment (100 sccm) for 30 min to the
melting point of Cu (1090 °C) and then annealed in H2 (100 sccm) for 30 min. The integrated etching/growth proceeded via
the LPCVD approach with hexagon flower-etched Cu patterns, embedded
into the large-scale graphene located on a liquid Cu/W substrate using
a CH4/H2 ratio of 6/100 sccm in 30 min. Finally,
the furnace was opened and CH4 gas was turned off; H2 flow was continued for fast cooling to 100 °C.
Figure 1 (a) Schematic
of the formation of a hexagon flower QD-like Cu pattern during low-pressure
CVD graphene growth on a liquid Cu/W substrate.
There have been several investigations on the controlled
diffusive etching modes for crystal growth of low-dimensional materials
that are responsible for etched graphene pattern formation,1−4,39 generating an effective engineering
method for etched patterns on other 2D and 3D material systems. However,
etching to form flower QD-like Cu patterns embedded into the large-scale
graphene region is quite new, strange, and intriguing in the field
of etching at the micro- and nanoscale. To date, there is no scientific
report in terms of theory and simulation investigations that detail
the relationship of the hexagonal-shaped etching mode and the underneath
graphene structure.
For morphology investigations of solid Cu,
liquid Cu, and graphene before and after the CVD process, scanning
electron microscopy (SEM), atomic force microscopy (AFM), and optical
microscopy (OM) were carried out, as shown in Figure 2a–f. Here, Figure 2a exhibits the morphology of bare Cu foil
(250 μm) through the SEM image before the CVD process. Figure 2b reveals the SEM
image of liquid Cu at 1090 °C after being resolidified. Figure 2c is the micrograph
photo of etched large-scale graphene on the liquid Cu/W substrate. Figure 2d reveals the AFM
image of the surface liquid Cu after being resolidified on W foil
with a liquid Cu thickness of 150 nm after 1090 °C and resolidified
as shown in Figure 2e, corresponding to the blue line in Figure 2d. Figure 2f is the OM images of liquid Cu located on W foil after
being resolidified, corresponding to the AFM image in Figure 2d.
Figure 2 (a) OM image of bare
Cu foil (thick 250 μm). (b) SEM image of liquid Cu at 1090 °C
after being resolidified. (c) Micrograph photo of etched large-scale
graphene on liquid Cu/W. (d) AFM of liquid Cu on W foil after being
resolidified. (e) Thickness of liquid Cu at 1090 °C and resolidified
at about 150 nm, corresponding to the blue line in (d). (f) OM images
of liquid Cu on W foil after being resolidified, corresponding to
the AFM image in (d).
Figure 3 and
Figures S1 and S2 in the Supporting Information reveal a new Euclidean geometry of the QD-like Cu patterns which
are partially etched Cu hexagons at the center of six edge sites and
embedded into the large-scale graphene located on the liquid Cu/W
surface after a higher melting point of Cu foil (1090 °C). Because
the melting temperature for W foil was 3422 °C, its morphology
did not change after treatment at 1090 °C. Similarly, the SEM
images at various magnifications were taken for hexagon flower-etched
Cu patterns embedded into large-scale graphene located on a liquid
Cu/W substrate, as shown in Figure 4 and Figures S3 and S4 in the Supporting Information.
Figure 3 OM images of hexagon flower-etched Cu patterns embedded
into the large-scale graphene located on a liquid Cu/W substrate.
Figure 4 SEM images of hexagon flower-etched Cu patterns
embedded into the large-scale graphene located on a liquid Cu/W substrate
at different magnifications.
For further demonstrations, the AFM data were applied to
observe the hexagon flower-etched Cu patterns embedded into large-scale
graphene located on a liquid Cu/W substrate, as shown in Figure 5 and Figure S5 in
the Supporting Information for two-dimensional
(2D) and three-dimensional (3D) images at different corners. In addition,
their phase images, which are characterized for softness, stiffness,
and the adhesion between the AFM cantilever tip with the specimen
surface, are shown in Figure 5d and Figure 5Sd.
Figure 5 AFM images of hexagon
flower-etched Cu patterns embedded into large-scale graphene located
on a liquid Cu/W substrate, (a,b) 3D AFM mapping image, (c) 3D AFM
mapping image at different views of (a), and (d) phase image of (a).
To investigate the existence of
graphene on liquid Cu/W and the Cu pattern etching effect, Raman spectroscopy
was carried out at two regions: graphene and Cu pattern (see Figure 6). At the Cu pattern
regions, the Raman peaks in Figure 6c,d correspond to the OM images that are directly captured
by the Raman analysis instrument, with the red cross in Figure 6a and the black cross in Figure 6b. They showed the
presence of some peaks of CuO, Cu2O, and Cu(OH)2, which are already well-known from a previous report.45 On the other hand, in the blue and green graphene
regions in Figure 6c and the red region in Figure 6d, corresponding blue and green crosses in Figure 6a and red cross in Figure 6b show clearly the
D, G, and 2D peaks of Raman data as the fingerprints of the graphene
structure on liquid Cu/W substrates. The Raman mapping of Figure 6b was also obtained
for the etched Cu pattern at a wavelength scan range from 0 to 800
nm for the typical existence of CuO, Cu2O, and Cu(OH)2 peaks (Figure 6g), which was proven in a previous report.45Figure 6a,f shows
the zoomed-in images of Figure 6c,d, respectively.
Figure 6 (a,b) OM images captured from Raman spectroscopy
of hexagon flower-etched Cu patterns embedded into the large-scale
graphene located on a liquid Cu/W substrate. (c,d) Raman data of different
positions marked as blue, green, and red crosses in (a,b). (e,f) Zoomed-in
image of graphene in (c,d), respectively. (g) Raman mapping with a
scan range from 0 to 800 nm of region (b).
For an explanation about the mechanism of etched Cu pattern
formation embedded into large-area graphene film, see Figure 7. It is believed that the etching
mode occurred due to the diffusion of etchants (H2 molecules
or H radicals) at the graphene/liquid Cu interface and the diffusion
on the graphene surface. Consequently, the etching effect formed at
the defects sites or grain boundaries was embedded into the large-scale
graphene to create the hexagon QD-like Cu patterns. Here, the diffusion
at the graphene/liquid Cu interface might be the key role for formation
of the etched Cu pattern. The high etching rate is because of high
H2 etchant concentration as well as hindered diffusion
at the graphene/liquid Cu interface. H2 diffusion on isotropic
liquid Cu indicates the physical origin of the high symmetry of etched
Cu patterns. Also, it is a key factor for visualizing the etched line
mode because controlled diffusive etching varies with nanoparticle
etching from previous reports.41−43
Figure 7 Mechanism of etched Cu patterns embedded
into the large-area graphene film with diffusion of etchants (H2 molecules or H radicals) underneath and above the liquid
Cu surface, which could be mostly responsible for the formation of
etched Cu patterns.
Conclusions
The
resulting hexagon flower QD-like etched Cu patterns have revealed
a new kind of unknown Euclidean geometry during large-scale CVD graphene
growth. Here, we have established the first observation of etched
Cu patterns on large-scale graphene that can form a new etched hexagon
shape. The experimental results provide clear proof of this etching
mode. Etching to form the hexagon QD-like Cu pattern was induced at
high H2 concentration. This study is expected to be further
computationally and experimentally examined for in situ observation
of integrated graphene etching/growth in the future. This new integrated
growth/etching effect shows an unknown graphene etching mode that
enables other nanomaterial structures to be formed. In addition, further
investigation of the graphene etching mode on new substrates (e.g.,
Ni/W) is another intriguing phenomenon which will be discovered in
the near future.
Supporting Information Available
The Supporting Information is available free of
charge on the ACS Publications
website at DOI: 10.1021/acsomega.8b00985.OM, SEM, and AFM
images of hexagon flower QD-etched patterns embedded into the large-scale
graphene located on the liquid Cu/W foil (PDF)
Supplementary Material
ao8b00985_si_001.pdf
The author declares no competing
financial interest.
Abbreviations
OMoptical microscopy
SEMscanning electron microscopy
AFMatomic force microscopt
QDsquantum dots
CVDchemical vapor deposition
LPCVDlow-pressure chemical
vapor deposition
2Dtwo-dimensional
3Dthree-dimensional
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145899510.1021/acsomega.8b01331ArticleLocal Domain Size in Single-Chain Polymer Nanoparticles Pomposo José A. *†‡§Moreno Angel J. †∥Arbe Arantxa †Colmenero Juan †‡∥† Centro
de Física de Materiales (CSIC, UPV/EHU) and Materials Physics
Center MPC, Paseo Manuel
de Lardizabal 5, E-20018 San Sebastián, Spain‡ Departamento
de Física de Materiales, Universidad
del País Vasco (UPV/EHU), Apartado 1072, E-20800 San Sebastián, Spain§ IKERBASQUE—Basque
Foundation for Science, María Díaz de Haro 3, E-48013 Bilbao, Spain∥ Donostia
International Physics Center (DIPC), Paseo Manuel de Lardizabal 4, E-20018 San Sebastián, Spain* E-mail: Josetxo.pomposo@ehu.eus.02 08 2018 31 08 2018 3 8 8648 8654 13 06 2018 20 07 2018 Copyright © 2018 American Chemical
Society2018American Chemical
SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
Single-chain polymer nanoparticles
(SCNPs) obtained through chain
collapse via intramolecular cross-linking are attracting significant
interest for nanomedicine and biomimetic catalysis applications, among
other fields. This interest arises from the possibility to bind active
species (e.g., drugs and catalysts)—either temporally or permanently—to
the SCNP local pockets formed upon chain collapse. However, direct
quantification of the size and number of such local domains in solution—even if highly desirable—is currently
highly demanding from an experimental point of view because of the
small size involved (<5 nm). On the basis of a scaling analysis,
we establish herein a connection between the global compaction degree
(R/R0) and the size (ξ)
and number (n) of the “collapsed domains” generated upon SCNP formation at high dilution from a linear
semiflexible precursor polymer. Results from molecular dynamics simulations
and experimental data are used to validate this scaling analysis and
to estimate the size and number of local domains in polystyrene SCNPs
synthesized through a “click” chemistry procedure, as
a representative system, as well as for relevant catalytic SCNPs containing
Cu, Pt, and Ni atoms. Remarkably, the present work is a first step
toward tuning the local domain size of the next generation of SCNPs
for nanomedicine and bioinspired catalysis applications.
document-id-old-9ao8b01331document-id-new-14ao-2018-01331cccc-price
==== Body
1 Introduction
Intramolecular cross-linking
of individual polymer chains in a
good solvent at high dilution produces single-chain polymer nanoparticles
(SCNPs) via intrachain collapse.1−5 The compaction of a single chain to a SCNP resembles—in some
way—the conformational rearrangement needed by some biomacromolecules
to reach its functional state.6−8 Depending on the specific nature
of the intramolecular cross-links formed, dynamic or permanent SCNPs
result by involving reversible or irreversible intrachain interactions,
respectively.9,10 These soft nano-objects have
attracted significant interest for a variety of applications, including
nanomedicine and biomimetic catalysis uses.3 The possibility to bind active species (e.g., drugs and catalysts)—either
temporally or permanently—to the SCNP local pockets formed
upon intrachain chain collapse remains as a driving force toward bioinspired
applications.6,8 To understand the possibilities
that SCNPs offer for nanomedicine and biomimetic catalysis, the reader
is referred to several illustrative works11−25 and a recent book.26
Significant
theoretical effort27−32 has been recently devoted to understand how the nature of the intramolecular
cross-links (both reversible and irreversible interactions), the amount
of functional reactive groups, x, and the precursor
molecular weight, Mw, determine the global
collapse degree upon intramolecular cross-linking, R/R0, where R0 and R are the linear precursor polymer size and
the SCNP size, respectively. However, to our best knowledge, no attempt
has been yet carried out to establish a connection between the global
compaction degree (R/R0) and the size (ξ) and number (n) of local
pockets (domains) generated upon SCNP formation at high dilution.
It is worthy of mention that a direct visualization/quantification
of such local domains in solution—even if highly desirable—is
currently highly demanding from an experimental point of view.26
We use herein the analogy of chain confinement
into a spherical
cavity33 to the collapse of a linear chain
to a SCNP to perform a scaling analysis34,35 allowing to
establish a connection between the global compaction degree (R/R0) and the size (ξ)
and number (n) of “collapsed domains” generated upon SCNP formation at high dilution. It is worthy
of mention that the case of confinement of a linear semiflexible polymer
chain into a cavity under good solvent conditions has recently attracted
significant theoretical and computer simulations efforts.36−39 Remarkably, the present work provides a solid basis to understand
the effect of (i) the strength of the intramolecular interactions,
(ii) the amount of functional groups, (iii) the precursor molecular
weight, and (iv) the precursor chain stiffness on the size and number
of local domains of SCNPs in solution.
The article is organized
as follows. In Section 2, we first introduce two expressions for
the change in free energy upon collapse based, respectively, on the
analogy of SCNP formation to the case of chain confinement into a
spherical cavity under good solvent conditions and on the number of
new intramolecular bonds formed and the change in free energy per
each new bond formed. Next, useful scaling expressions for the global
compaction degree and the size and number of local domains are derived.
Validation of the scaling analysis with results from molecular dynamics
(MD) simulations and reliable experimental data, as well as an estimation
of the size and number of local domains for relevant catalytic SCNPs
in solution containing Cu, Pt, and Ni atoms, is provided in Section 3 and, finally, the
conclusions of the work are given in Section 4.
2 Scaling Analysis
2.1 Free Energy of Collapse
Let us assume
that the change in free energy, ΔFc, upon collapse of a linear precursor polymer of size R0 to a SCNP of size R in a good solvent
under high dilution conditions follows an expression similar to that
corresponding to chain confinement into a spherical cavity under good
solvent conditions35−39 1 where kB is the
Boltzmann’s constant, T the absolute temperature,
and α is the scaling exponent of the resulting collapsed
domains upon SCNP formation (see below). It is reasonable
to assume that SCNPs with different chain stiffness will show different
values of the exponent in eq 1, as observed in computer simulations of semiflexible chains
confined in a spherical cavity.36
Because the free energy of collapse comes from all of the new intramolecular
bonds formed, we can additionally write 2 where xN/2 is the number
of new intramolecular bonds formed, x is the fraction
of reactive groups in the linear precursor polymer of total number
of monomers N, and |Δfc| is the absolute value of the change in free energy per each
new bond formed. Implicit in eq 2 is the assumption that by means of dimerization of the corresponding
reactive monomers the maximum number of intrachain bonds (xN/2) is obtained. Experimentally, this is expected to be
the case for SCNPs prepared through highly reactive cross-linking
procedures (e.g., “click” chemistry reactions10) but not for SCNPs prepared by means of weak,
dynamic interactions9 (e.g., hydrogen bonds).
For real systems, Δfc is expected
to contain a favorable enthalpic contribution, Δhc < 0, because of (exothermic) bond formation and an
unfavorable entropic contribution, Δsc < 0, because of severe configurational restriction upon chain
collapse.
2.2 Global Compaction Degree
By combining eqs 1 and 2, we obtain an analytical expression for the compaction degree (R/R0) as a function of x and N such as 3a 3b
Taking into account that the size of
a semiflexible linear chain in a good solvent is given37 (to a first approximation) by R0 ≃ bC∞1/5Nν0, where b is the monomer size, C∞ is the characteristic ratio,34 and ν0 is the Flory exponent (ν0 ≈ 3/5), eq 3a can be rewritten as 4a 4b
Consequently, according to the present scaling
analysis, the exponents
of the dependence of SCNP size R on x and N are actually connected through eq 4b.
2.3 Local
Domain Size
Similar to the
case of a linear chain confined in a spherical cavity,35−39 we introduce herein the concept of“cross-linked blobs” or collapsed domains upon SCNP formation
via chain collapse. The average number of such domains (n) each one having associated a free energy around kBT and a size ξ can be estimated
from the free energy of collapse such as37,39 5 Therefore, by using eqs 1 and 2, we obtain the
following expressions for the domain size 6a 6b whereas the number of monomers in each collapsed
blob (g) is just given by37,39 7
It is worthy of mention that α
in eq 6a is related to the scaling exponent
of the cross-linked blobs, so its value gives an idea of compaction
at local level (i.e., at domain size ξ). Conversely,
the value of ν in eq 4a gives an indication of chain compaction at global scale (i.e., at SCNP size R). In general, one expects
1/3 ≤ (α, ν) ≤ 1 where the lower value is
expected for globule-like compaction, whereas the upper value corresponds
to rod-like compaction.34
It is instructive
to rewrite eqs 5 and 7 by using eq 6b, such as 8 and 9
Hence, according to the present
scaling analysis n depends linearly on x, N, and
|Δfc|, whereas g depends inversely on x and |Δfc| but it is independent on N.
3 Results and Discussion
3.1 Scaling Analysis Validation
with Data from
MD Simulations
Analysis of R/R0 and xN/2 data from MD simulations of
semiflexible SCNPs in terms of eq 3a allows one to determine the scaling exponent β
(and hence α from eq 3b) as well as the absolute value of the change in free energy
per each new bond formed, |Δfc|. Figure 1 shows such an analysis
for SCNPs having different chain stiffness, as characterized by the
value of the bending constant k employed in the coarse-grained
MD simulations.40 Note that k is related to the well-known characteristic ratio, C∞, and it was previously reported that C∞ ≈ 1.7, 5, 9, and 15 for k = 0 (fully flexible case), 3, 5, and 8, respectively.40 The dependences of β, the exponent of
the free energy of collapse 3/(3α – 1), and |Δfc| on chain stiffness are illustrated in Figure 2 for semiflexible
SCNPs. Upon increasing the SCNP characteristic ratio, the value of
β was found to decrease nearly linearly with C∞ (see Figure 2A). Concerning the exponent of the free energy of collapse,
it decreases abruptly on increasing C∞ toward a plateau value for the stiffer SCNPs (Figure 2B). This behavior is in agreement with that
reported by Cifra and Bleha36 in computer
simulations of the confinement of a semiflexible linear chain in a
closed spherical cavity reaching a limiting value of 2.6 upon increasing
chain stiffness. Interestingly, |Δfc| also reaches a plateau value upon increasing SCNP stiffness (Figure 2C). As noted by Cifra
and Bleha,36 for semiflexible linear chains,
the free-energy penalty on chain compaction is maximum for the fully
flexible case when compared with the case of stiffer systems. According
to the data in Figure 2C, there is a difference in |Δfc| between the fully flexible and stiffer SCNPs around 3.7 kBT. An estimation of the free
energy of collapse as a function of SCNP stiffness at identical compaction
degree can be obtained from eq 1. As an example, at a compaction degree R/R0 = 0.65, we obtain =
218.0, 14.8, 7.1, and 4.4 for SCNPs with C∞ = 1.7, 5, 9, and 15, respectively.
Figure 1 MD simulations data of compaction degree
(R/R0) as a function
of new intramolecular bonds
formed (xN/2) for SCNPs having different chain stiffness:40 (A) C∞ =
1.7, (B) C∞ = 5, (C) C∞ = 9, and (D) C∞ = 15 (see text for details).
Figure 2 Dependence of (A) scaling exponent β, (B) scaling exponent
3/(3α – 1), and (C) change in free energy per new bond
formed, |Δfc|, on chain stiffness
for semiflexible SCNPs with different values of characteristic ratio, C∞, according to MD simulations (see eqs 1–3a and text for details).
Table 1 shows
a
comparison of the values of ν = ν0 + β
and , as derived from the present scaling
analysis,
to those previously reported for semiflexible SCNPs with different C∞ values as estimated directly from MD
simulations data.40 As stated previously
in Section 2, ν
gives an indication of chain compaction at global scale (i.e., at SCNP size R) whereas the value
of α is indicative of chain compaction at local level (i.e., at domain size ξ). In general, a good agreement
is observed between the values of ν from the present scaling
analysis and MD simulations. Concerning the values of α, the
MD simulations provide values that are systematically larger than
those derived from the scaling analysis, although both data sets follow
the general trend of a higher value of α on increasing C∞.
Table 1 Comparison of ν
and α
Values from the Scaling Analysis of This Work to Estimations from
MD Simulations of SCNPs with Different C∞ Values40
C∞ β ν α νMDsim. αMDsim.
1.7 –0.08 0.52 0.41 0.50 0.63
5 –0.16 0.44 0.49 0.47 0.74
9 –0.22 0.38 0.55 0.42 0.81
15 –0.29 0.31 0.62 0.30 0.84
Figure 3 shows the
evolution of the collapsed domain size, ξ (in σ units,
where σ is the bead size) and the number of beads in a domain, g, as a function of SCNP stiffness, for SCNPs with a fraction
of reacting monomers of x = 0.2 and N = 400, as calculated from eqs 4a–5 with data from Figure 1 and Table 1. Inspection of Figure 3 reveals that a minimum SCNP stiffness is
required for the scaling analysis to provide consistent values of
ξ and g. As a matter of fact, the domain size
of fully flexible SCNPs in Figure 3A approaches the bead size which invalidates the scaling
analysis for this case. Inasmuch C∞ ≥ 5, consistent values of ξ, n, and g are obtained showing a collapsed domain size around 3.7σ,
about 33 collapsed blobs per SCNP and ∼12 beads per blob for
semiflexible SCNPs (x = 0.2, N =
400) with C∞ = 5, 9, and 15 because
of the similar values of |Δfc| (refer
to eqs 6bb, 8, and 9).
Figure 3 Dependence of (A) collapsed
domain size, ξ (in σ units,
where σ is the bead size) and (B) number of beads per collapsed
domain, g, on chain stiffness for semiflexible SCNPs
(x = 0.2, N = 400) as calculated
from eqs 6bb and 9 with data from Figure 1 and Table 1.
Figure 4 illustrates
the dependence of ξ and g on the fraction of
reacting monomers, x, for SCNPs with N = 400 and C∞ = 9. Chain collapse
from a linear precursor with low amount of reacting monomers (e.g., x = 0.05) produces a few collapsed domains (∼8) of
relatively large size (∼8.4σ) containing a large amount
of beads per blob (∼51). Upon increasing x, both collapsed domain size and number of beads per blob reduce
notably (refer to eqs 6bb and 9), whereas the number of blobs is found
to increase linearly with x (refer to eq 8).
Figure 4 Dependence of (A) collapsed domain size,
ξ, and (B) number
of beads in a collapsed domain, g, on the fraction
of reacting monomers x for SCNPs with N = 400 and C∞ = 9, as calculated
from eqs 6bb and 9 with data from Figure 1 and Table 1.
3.2 Scaling
Analysis Validation with Experimental
Data
Complementary to the analysis based on MD simulations
data, we have also analyzed data for real SCNPs in terms of eq 3a. In this sense, compaction
data from well-defined polystyrene (PS)-SCNPs synthesized via “click”
chemistry,41 covering from x = 0.025 to x = 0.3 and three different values of
weight-average molecular weight (Mw ≈
44, 111, and 232 kDa) were found to merge into a single master curve
with β ≈ −0.20 and |Δfc| ≈ 0.16, when plotted according to eq 3a (see Figure 5).
Figure 5 Compaction degree (R/R0) as a function of new intramolecular bonds
formed (xN/2) for PS-SCNPs (C∞ ≈
9.5 for PS34) of different molecular weight:41Mw = 44 kDa (solid
blue points), Mw = 111 kDa (solid red
points), and Mw = 232 kDa (solid green
points).
Apparently, the experimental data
best follow the scaling behavior
at large values of N. From ν = ν0 + β and , we obtain
ν = 0.4 and α =
0.53 based on the value of β ≈ −0.20. Note that
the values of β and ν for PS-SCNPs (C∞ ≈ 9.5 for PS34) are in excellent agreement with those predicted by a model of elastic
SCNPs recently developed by our group27 (β = −1/5, ν = 2/5).
When compared with
MD simulations of SCNPs prepared from a precursor
polymer of C∞ = 9, the value of
|Δfc| was found to be about fivefold
lower for real PS-SCNPs. However, it is worth stressing that similar
values should not be expected even at a qualitative level. Thus, though
one finds similar scaling properties for the molecular size and may
expect similar entropy loss per monomer because of network formation
in the coarse-grained and in the real SCNPs, this is not the case
for the associated enthalpy change, Δhc, because the bonded and nonbonded interactions in the simplified
bead-spring model of the simulations40 are
of different nature than that in the real polymers.10
Figure 6 illustrates
the dependence of ξ and g on the fraction of
reacting monomers, x, for PS-SCNPs of Mw ≈ 44, 111, and 232 kDa, as calculated form eqs 6bb and 9 with data from Figure 5. On increasing the amount of functional monomers from x = 0.1 to x = 0.3, a decrease in the domain
size is observed from ξ ≈ 4 nm to ξ ≈ 2
nm. According to the results displayed in Figure 6A, the domain size in PS-SCNPs shows a weak
dependence on Mw. Remarkably, on the basis
of the present scaling analysis, the number of monomers in each local
domain is expected to be independent of Mw, as illustrated in Figure 6B. By taking into account that for real systems σ ≈
0.64 nm and each bead in the MD simulations comprises ∼5 monomers,
the results shown in Figure 6 are in good agreement with those displayed in Figure 4.
Figure 6 Dependence of (A) collapsed
domain size, ξ, and (B) number
of monomers in a collapsed domain, g, on the fraction
of reacting monomers, x, for PS-SCNPs (C∞≈ 9.5 for PS34) of Mw = 44 kDa (solid blue points), Mw = 111 kDa (solid red points) and Mw = 232 kDa (solid green points) as calculated from eqs 6bb and 9 with data from Figure 5.
3.3 Estimation
of Local Domain Size in Pt-, Cu-
and Ni-Containing Catalytic SCNPs in Solution
Data about
the local domain size, number of domains, and number of monomers per
domain for relevant metal-containing catalytic SCNPs20,22,42 in solution are given in Table 2. The precursor polymers
were based on either PS or poly(methyl methacrylate) (PMMA), both
having a similar value of chain stiffness34 (C∞(PS) = 9.5, C∞(PMMA) = 9.0). Estimations were carried out based
on experimental R/R0 data
by assuming α ≈ 0.53 in eq 6aa, for PtII-, CuII-, and NiII-containing SCNPs employed with success in amination of allyl
alcohol,20 selective alkyne homo-coupling
reactions,22 and photoreduction of carbon
dioxide,42 respectively.
Table 2 Local Domain Size (ξ), Number
of Domains (n), and Number of Monomers per Domain
(g) in Relevant Metal-Containing Catalytic SCNPs
(See Text)
catalyst reaction R0 (nm) R (nm) ξ (nm) n g refs
PtII@PS-SCNPs amination of allyl alcohol 7.4 4.9 2.4 9 40 (20)
CuII@PMMA SCNPs selective alkyne homo-coupling 26 15 5.9 16 125 (22)
NiII@PMMA SCNPs photoreduction of carbon dioxide 4.2 3.7 3.0 1.9 241 (42)
As stated previously, direct
quantification of the size and number
of SCNP local domains in solution is currently highly
demanding from an experimental point of view, so there are no experimental
data available. Nevertheless, experimental evidence of the presence
of local compact domains in isolated SCNPs is provided
in Figure 7, as revealed
by transmission electron microscopy (TEM) measurements performed to
Cu-containing SCNPs upon solvent removal and deposition onto a carbon
grid.22 Obviously, upon solvent removal
the dimensions of the SCNPs change and often a pancake morphology
is observed for isolated SCNPs deposited onto solid substrates. Moreover,
the SCNP size is found to depend to a large extent on the surface
energy of the substrate.27
Figure 7 TEM image showing the
presence of local compact domains in a Cu-containing
SCNP in the dry state.22
4 Conclusions
Quantification
of the size and number of local domains of SCNPs
in solution is currently of great interest because of the possibilities
that offer such local pockets to bind—either temporally or
permanently—active species to them (e.g., drugs and catalysts)
rendering the resulting SCNPs highly attractive for applications in
nanomedicine and catalysis, among other fields. A scaling analysis
was performed to establish a connection between the global compaction
degree (R/R0) and the
size (ξ) and number (n) of collapsed domains
generated upon SCNP formation at high dilution from a linear semiflexible
precursor polymer. The scaling analysis was validated with results
from MD simulations and reliable experimental data. On the basis of
the scaling equations here proposed, we have estimated—as an
example of application—the size and number of local domains
for relevant catalytic SCNPs in solution containing Cu, Pt, and Ni
atoms. Remarkably, this work is a first step toward tuning the local
domain size of the next generation of SCNPs for nanomedicine and bioinspired
catalysis applications.
The authors
declare no competing financial interest.
Acknowledgments
The
financial support by the Spanish Ministry “Ministerio
de Economia y Competitividad”, MAT2015-63704-P (MINECO/FEDER,
UE), the Basque Government, IT-654-13, and the Gipuzkoako Foru Aldundia,
RED 101/17, is acknowledged.
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145799310.1021/acsomega.8b01680ArticleSimple Preparation of Porous Carbon-Supported Ruthenium:
Propitious Catalytic Activity in the Reduction of Ferrocyanate(III) and a Cationic Dye Veerakumar Pitchaimani *†‡Salamalai Kamaraj §Thanasekaran Pounraj ∥Lin King-Chuen *†‡† Department
of Chemistry, National Taiwan University, Taipei 10617, Taiwan‡Institute of Atomic and Molecular
Sciences and ∥Institute of Chemistry, Academia Sinica, Taipei 11529, Taiwan§ Department
of Mechanical Engineering, PSN Institute
of Technology and Science, Tamil Nadu, Tirunelveli 627152, India* E-mail: spveerakumar@gmail.com (P.V.).* E-mail: kclin@ntu.edu.tw. Phone: +866-2-33661162 (K.-C.L.).04 10 2018 31 10 2018 3 10 12609 12621 17 07 2018 20 09 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
The present study
involves the synthesis, characterization, and
catalytic application of ruthenium nanoparticles (Ru NPs) supported
on plastic-derived carbons (PDCs) synthesized from plastic wastes
(soft drink bottles) as an alternative carbon source. PDCs have been
further activated with CO2 and characterized by various
analytical techniques. The catalytic activity
of Ru@PDC for the reduction of potassium hexacyanoferrate(III), (K3[Fe(CN)6]), and new fuchsin (NF) dye by NaBH4 was performed under mild conditions. The PDCs had spherical
morphology with an average size of 0.5 μm, and the Ru NP (5
± 0.2 nm) loading (4.01 wt %) into the PDC provided high catalytic
performance for catalytic reduction of ferrocyanate(III) and NF dye.
This catalyst can be recycled more than six times with only a minor
loss of its catalytic activity. In addition, the stability and reusability
of the Ru@PDC catalyst are also discussed.
document-id-old-9ao8b01680document-id-new-14ao-2018-016802ccc-price
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Introduction
Over the past few years,
biowastes and non-biodegradable plastic
waste materials as low-cost feedstock have been utilized for the production
of value-added carbon nanomaterials with a wide range of applications.1 Until now, enormous amounts of plastic wastes
were generated because of increased demand of plastic-related production.2 These plastics are not biodegradable and thus
generate extremely troublesome components for landfilling. Handling
and managing these plastic wastes is a huge task, because a large
amount of these wastes are generally dumped into landfill or disposed
in the ocean, thereby causing a very serious environmental issue.3 Therefore, a large number of methods have been
investigated to convert plastic wastes into useful products.4 For instance, they have been transformed into
different kinds of carbon-based nanostructures including nanotubes,5 spheres,6 hollow spheres,7 nanosheets,8 activated
carbons,9 and graphene flake/foil10 for sustainable energy applications.11
Carbon-based nanostructure materials,
particularly biowaste activated
carbon spheres (CSs), have gained a wide range of interests because
of their excellent energy storage ability, good electrical conductivity,
biocompatibility, and electrical properties, and thus, they have received
a wide attention.12 In recent years, active
metals supported on the porous carbon substrate such as Rh,13 Re,14 Ru,15 Os,16 Ir,17 and Pt18 have been
used as active catalysts for organic/inorganic transformations. Among
them, Ru-based nanomaterials are widely explored as nanocatalysts19 because of their low cost and attractive feature
of superior catalytic activity and stability.
Generally, potassium
hexacyanoferrate(III), (K3[Fe(CN)6]), is well-known
as one of the most common pollutants, which
is found in contaminated air, water, and soil in the environment.
It can easily accumulate inside humans, aquatic animals, and other
living organisms through food chains20 and
has been proved to have mutagenicity, acute toxicity, carcinogenicity,
and high environmental mobility, even in a trace level.21 In contrast, Fe(II) is considered as an essential
nutrient required in metabolic pathways for humans and animals. The
most common type of anemia is caused by the iron deficiency whereas
some diseases such as hemochromatosis can be due to iron overload;
the United States Recommended Daily Allowance (USRDA) for iron is
18 mg.22 Besides, the conversion of Fe(III)
into Fe(II) offers several important advantages and attractive applications
including possibilities for (i) tin purification, (ii) separation
of copper out of molybdenum ore, (iii) wine and citric acid in large-scale
preparation, (iv) serving as a benchmark for electron transfer reaction,
and (v) medical diagnosis for diabetic patients and designing of amperometric
biosensor for electrochemical applications.23
Recently, Pastoriza-Santos et al.24 carried
out the reduction of Fe(CN)63– with NaBH4, using gold nanorods containing metallodielectric hollow
shells of SiO2 or TiO2. However, these catalytic
supports are expensive compared to the carbon nanostructure. Remarkably,
these supports are difficult to remove from the active phase, but
the carbon support can be easily burnt to separate the active metallic
phase. Carregal-Romero’s group fabricated spherical Au NP heterostructures25 and have used them for catalytic reduction of
Fe(CN)63– by NaBH4 in aqueous
solution; however, this catalyst rate was 4 times higher than that
of the uncatalyzed reaction. Despite their successful results, low
stability and inconvenient recovery restrict practical application
of the materials. Jana et al.26 prepared
mesoporous Au-boehmite film catalyst for reduction Fe(CN)63–. However, this catalyst achieved large rate
constant and was four times recycled but required high loadings, harsh
conditions, and high-boiling-point aprotic solvents for the catalytic
methods. Likewise, Miao et al.27 used Fe3O4@GNSs as the catalyst for the reduction of Fe(CN)63– in aqueous media. This magnetic composite was used as an ideal catalyst and shows recyclability
along with persistent catalytic activity even after being recycled
six times. Chen et al.28 developed the
submicron-sized PEGDMA@Au NP microsphere catalyst for the reduction
of Fe(CN)63– by NaBH4 in aqueous
solution, but they failed to report recyclability and leaching experiments.
Likewise, Yang et al.29 used 2,6-pyridinedicarboxylic
acid-protected Au NP as a catalyst for the same reduction. However,
the catalyst exhibits poor rate constant and lack of recyclability
and stability. Wu et al.30 have demonstrated
an ionic liquid-based synthesis of hollow and porous platinum nanotubes
as a new catalyst, however required harsh preparation conditions,
exhibited poor stability, and produced silica waste after etching.
Recently, Jiang demonstrated a new approach for the one-pot synthesis
of gold hollow nanospheres exhibiting excellent catalytic activity
toward the reduction of Fe(CN)63– by
NaBH4 in water.31 Being stable
in air and water, this catalyst could be reused 10 times. However,
a long time period was required for completion of reduction. Therefore,
the above-mentioned catalysts are less advantageous with limited practical
applications in catalysis, owing to some unique natures, such as great
chemical stability, low corrosive capability, high thermal stability,
hydrophobic feature, easy recovery, and low price.32
On the other hand, clean water is the major topic
of the current
research because it is an important source for humans and the environment.33 Discharge of effluents containing toxic dyes
and heavy metal ions from manufacturing industries such as cosmetic,
leather, paper, textile, pharmaceuticals, and so on into nearby water
bodies is highly detrimental to the human health and environment.34 Hence, the development of robust and smart functionalized
nanomaterials with practical feasibility and biocompatibility is necessitated
to act as an effective adsorbent for removal of toxic dyes.35 In particular, metals or metal oxide-containing
carbon nanomaterials have been reported as inexpensive nano-adsorbents
for the adsorption/removal of heavy metals and dyes.34,35 Thus, utilization of inexpensive nano-adsorbents for the treatment
of industrial dye effluents could be helpful in resolving the human
and environment problems.36,37
In this work,
small-sized Ru NPs were decorated on the PDC support
by the microwave-assisted (MW) reduction method, which has been popularly
employed over the past few years for its advantageous nature, such
as easy control of particle size and surface area, purity and high
production yield, quick operation time, desirable temperature regulation,
and tenability for the carbonaceous structure. Herein, we report a
novel preparation to fabricate Ru NPs supported on porous PDC (Ru@PDC)
by converting waste plastics into porous carbons. We adopted plastic
wastes as the primary carbon rich precursor and ruthenium(III) acetylacetonate
[Ru(acac)3] as a metal precursor. A more detailed description
for the preparation procedure of Ru@PDC catalyst is shown in Scheme 1.
Scheme 1 Schematic Diagram
for the Preparation and Application of the Ru@PDC
Catalyst
Results and Discussion
Phase
Structure
The phase structures of the as-prepared
samples were examined using powder X-ray diffraction (PXRD) and Raman
spectroscopy. Analyzing the XRD of carbon samples exhibits two broad
peaks with low intensities at 2θ ≈ 23.5° and 43.6°
corresponding to the (002) and (100) diffraction planes ascribed to
the graphitic and amorphous carbon structure, respectively (Figure 1a). Upon increasing
the temperature, the diffraction peaks of PDC-600, PDC-700, and PDC-800
samples become broader slightly with larger intensities, indicating
that the carbon structure is characteristic of a more extent of graphitic
nature implying a trend of polymer aggregation into large polyaromatic
structures. Aggregation reactions proceed progressively with temperature
at 600 °C and higher until the carbonaceous materials are formed
showing nanometer-scale morphology containing highly organized carbons.38 On the other hand,
additional sharp diffraction peaks were observed for the Ru@PDC composite
at 2θ ≈ 38.4°, 42.3°, 44.1°, 58.5°,
69.6°, and 78.2° corresponding to the (100), (002), (101),
(102), (110), and (103) planes of the hexagonal close-packed Ru (JCPDS
06-0663), in excellent agreement with the reported values.31 The XRD pattern of Ru@PDC shows a broad peak
located at 44.1° composed of overlap between both C(100) and
Ru(101) diffractions, thus suggesting that the catalyst contains smaller
size ruthenium particles with diameters ≈5 nm. Additionally,
the low C(002) peak intensity in the catalyst was observed, because
of general lack of graphitic ordering. Scherrer formula (eq 1) in the following was adopted to
calculate the apparent crystallite size for a given reflection. 1 where D denotes the mean
size of the crystallite perpendicular to the planes (hkl) and K is a Scherrer parameter adopted as 1.84
for (100) and 0.94 for (002) for half-widths. λ is equal to
0.15406 nm, the used wavelength of the X-ray radiation, β is
the breadth at half maximum intensity in radians, and θ is the
Bragg angle for the reflection concerned. The average particle size
of Ru NP was evaluated to be 5–6 nm, consistent with the high
resolution transmission electron microscopy (HR-TEM) results (vide
infra).
Figure 1 (a) PXRD patterns, (b) Raman spectra, (c) N2 sorption-isotherms,
and (d) TGA curves of the as-prepared PDC and Ru@PDC materials.
Raman Analysis
Raman spectroscopy is used to inspect
the structure defects and disorder nature of carbonaceous materials.
Raman spectra for all the samples (Figure 1b) exhibited two marked peaks at around 1344
and 1601 cm–1, which were ascribed to the D band
and G band, respectively.39 The G band
at 1592–1601 cm–1 is due to the E2g C–C stretching mode of sp2-bonded two-dimensional
hexagonal lattice of graphite layers, while the D-band at 1323–1344
cm–1 is attributed to the A1g vibrational
mode and is characteristic of the disorder nature. The intensity ratio
of ID/IG is
used to evaluate the defects of carbon-based samples; a smaller ratio
suggests more significant defects on graphitic carbons. As such, the
band intensity ratios (ID/IG) for PDC-600 and PDC-700 are 0.48 and 0.51, respectively,
both indicative of low graphitization.40 However, the peak area ratio of ID/IG for pristine PDC and Ru@PDC increased to 0.78
and 0.83, respectively, indicating graphitization enhancement of the
PDC-800 after the high-temperature treatment; the fact agrees with
the XRD measurements (see Figure 1a). The resulting ID/IG ratios of all samples were calculated and
are listed in Table 1. This consequence is in agreement with those by the XPS and HR-TEM
analyses (vide infra).
Table 1 Textural Properties
of the As-Prepared
PDC and Ru@PDC Materials
sample STota (m2 g–1) SMicrob (m2 g–1) SMesoc (m2 g–1) VTota (cm3 g–1) DPd (nm) Dme (%) ID/IG
PDC-600 97.6 31.2 66.4 0.032 7.8 0.48
PDC-700 294.2 103.1 191.1 0.071 7.5 0.51
PDC-800 466.7 217.2 249.5 0.086 7.5 0.78
Ru@PDC 396.5 184.6 211.9 0.082 7.3 6.01 0.83
a Surface area (STot) from the BET method and total pore volume (VTot) calculated at P/P0 = 0.99.
b Microporous
surface areas (SMicro) obtained from t-plot
analyses.
c SMeso (SMeso = STot – SMicro).
d Average pore size (DP) derived by BJH adsorption branches of isotherms.
e Metal dispersion measured by H2 chemisorption at 323 K.
Textural Property
The nitrogen adsorption/desorption
isotherms at 77 K of PDC and Ru@PDC samples are shown in Figure 1c. The isotherms
exhibited a type-IV curve with hysteresis loop associated with capillary
condensation in the range of P/P0 from 0.45 to 0.99. This finding indicated that the porosity
of the obtained PDC and Ru@PDC was essentially made up of micropores/mesopores,
and it may be generated by the CO2 activation. The textural
properties including BET total surface area (STot), micropore surface area (SMicro), mesopore surface area (SMeso), total
pore volume (VTot), and average pore diameter
(DP) are summarized in Table 1. The BET surface area of Ru@PDC
(SBET = 396.5 m2 g–1) sample significantly decreased compared to PDC-800 (466.7 m2 g–1), indicating that Ru NPs blocked the
pores of the CSs and thus diminished the surface area and the total
pore volume of the Ru@PDC.41 These results
verified that the Ru NPs were impregnated on the surface of the PDC
matrix. The Ru NPs were well dispersed on the surface and no obvious
aggregation was observed, whereas unsupported Ru NPs were likely to
aggregate immediately.42a The Ru@PDC catalysts
were characterized and are listed in Table 1. It seems that a higher BET specific surface
area tends to favor a higher Ru dispersion. Masthan et al. have reported
the H2 dispersion measurement for Ru/γ-Al2O3, the H2 absorption equilibrium was much
faster at a higher temperature (373 K) rather than ambient temperature.42b The value of Ru dispersion and average crystallite
size for Ru-based catalysts based on H2 chemisorption method
is provided in Table S1, (Supporting Information).
The Barrett–Joyner–Halenda (BJH) model was
adopted to evaluate the pore size distributions in terms of the adsorption
branches of the isotherms (Figure S1 of the Supporting Information).
Thermal Stability
Thermal properties
of the samples
thus prepared were further examined by thermogravimetric analysis
(TGA), as displayed in Figure 1d. The weight loss below 200 °C (12–18% for all
samples) can be attributed to the adsorbed water evaporation. The
other weight losses began at around 558 °C, which are mainly
due to the burning of the carbon structures. It indicated the high
purity of the prepared PDC. However, a trace amount of residues was
also observed after complete decomposition of carbon samples. Inductively
coupled plasma–atomic emission spectroscopy (ICP–AES)
was further employed to analyze the elemental contents, obtaining
the Zn species present in the carbon material with a content of 1017
ppm (i.e., ca. 0.10 wt %). The impregnation of ZnCl2 during
the process tended to cause dehydration of the carbon substrate and
subsequently to result in charring and aromatization along with the
creation of porosities. The mobile liquid ZnCl2 (mp ≈
283 °C) was expected to occur in the earlier stage of the activation.
Sometimes, the
Zn ions are expected to be strongly intercalated between the carbon
interlayers, when the activation temperature is increased beyond 700
°C (bp of ZnCl2 ca. 730 °C), and a strong interaction
between carbon atoms and Zn species between the carbon interlayers
might leave trace Zn residue unvaporized.21
The burning of PDC in the Ru@PDC sample began at around 561
°C because of the interaction between Ru NP and carbon atoms
inducing defects in the graphitic carbon structure of PDC.43 While further heating, no weight loss was found
significantly, verifying that the particle crystallinity took place
at 800 °C. Moreover, according to the data from TG measurements,
the content of Ru in Ru@PDC was evaluated to be 4.01 wt %. This experiment
evidences additionally that Ru NPs are successfully incorporated onto
the PDC support.
Morphology and Microstructure
The
CSs were prepared
by using plastic wastes as carbon sources without any catalysts under
hydrothermal conditions, as reported earlier.44 According to this method, the SEM images of PDC-800 spheres exhibited
uniform spherical shapes ranging from 300 to 500 nm in diameter, as
displayed in the Figure S2, Supporting Information. As can be seen, a minor agglomeration bonding between spheres can
be ascribed to polymerization interruption or structure collapse.
Additionally, the microstructures of PDC-600 and PDC-700 were further
examined using HR-TEM as displayed in Figure S3 Supporting Information, which shows appearance of smooth surface
with perfect spheres. HR-TEM observation at different magnifications
(Figure 2a,b) and enlarged
portions (Figure 2c–g)
shows the shape of the PDC-800 particle, which has sizes of few hundred
nanometers along with porous microstructure. Moreover, the selected
area electron diffraction (SAED) reveals that the PDC-800 has a typical
amorphous carbon microstructure (Figure 2h), which preserves the structural integrity
and spherical morphology.
Figure 2 (a–g) HR-TEM images of the as-prepared
bare PDC-800 with
different magnifications and (h) electron diffraction pattern of the
representative image of PDC-800. The bars represent (a) 0.5 μm,
(b) 200 nm, (c) 100 nm, (d) 50 nm, (e) 20 nm, (f) 10 nm, and (g) 5
nm.
As shown in Figure 3, HR-TEM images of the Ru@PDC catalyst showed
that Ru NP had an average
size of 5 ± 0.2 nm, which are apparently distributed smoothly
on the surface of PDC. A representative histogram of particle size
distribution of Ru NP in Ru@PDC catalyst is shown in Figure S4 (Supporting Information). Energy-dispersive spectrometry
analysis evidenced the presence of Ru, C, and O elements in the Ru@PDC
catalyst (Figure S5, Supporting Information). Again, it is believed that Ru NPs have been successfully planted
on the surface of PDC matrix.
Figure 3 (a–f) Typical HR-TEM images of the Ru@PDC
catalyst with
different magnifications.
As displayed in Figure 4a–c, the additional filed emission TEM (FE-TEM)
images
of Ru@PDC verify a uniform distribution of the Ru NP on the surface
of PDC carbon matrix. The Ru presence was confirmed from SAED pattern
of Ru NPs (Figure 4d). It was found that some Ru NPs aggregate to form small clusters
with a maximum size of 6 nm. The images also indicate that some Ru
NPs are successfully planted in the PDC carbon matrix.
Figure 4 (a–c) Additional
HR-TEM images of the Ru@PDC catalyst and
(d) SAED pattern.
Surface Element Composition
Analysis
The surface element
compositions of PDC-800 and Ru@PDC samples were characterized using
XPS. Figure 5a shows
the XPS survey spectra of PDC-800 and Ru@PDC, containing C, O, and
Ru elements. The C 1s XPS spectrum (Figure 5b) exhibits a strong peak at 284.3 eV, ascribed
to the C–C/C=C bonds, and two relatively weaker peaks
with the binding energies (B.E) at about 285.1 and 288.7 eV, attributed
to the C–H and C=O species, respectively. It is notable
that the two bands with B.E at 284.3 and 280.4 eV can be readily assigned
to Ru 3d3/2 and 3d5/2, respectively, in the
nanoparticles by referring to the values of Ru metal at 285 and 280
eV, respectively.45 As shown in Figure 5c for the O 1s spectrum,
a broad band is found and deconvoluted into four peaks with a B.E
ca. 529.9 eV (C=O), 530.7 (COOH), 532.6 (O–C–O),
and 534.2 eV (C–OH). The Ru 3p signal of Ru@PDC (Figure 5d) is fitted into a pair with
the B.E of ca. 461.1 (Ru 3p3/2) and 483.2 eV (Ru 3p1/2), corresponding to the photoemission of metallic Ru.46 Additionally, the elemental analysis by the
ICP–AES technique evidenced the presence of the Ru element
in the Ru@PDC catalyst material with a content of 4.01 wt % (see Table
S4, Supporting Information).
Figure 5 (a) XPS survey
spectra of the pristine PDC-800 and the Ru@PDC samples,
and the corresponding core-level spectrum of (b) C 1s + Ru 3d, (c)
O 1s, and (d) Ru 3p.
FT-IR Study
FT-IR spectra were recorded for PDC and
Ru@PDC samples, and the results are shown in Figure S6, Supporting Information. The appearance of a weakly
broad band at ∼3345 cm–1 is attributed to
the hydroxyl group (−OH), and a weak band at 1638 cm–1 is attributed to the skeleton vibration of aromatic (−C=C−)
rings. The band at 2926 cm–1 is assigned to CH2 asymmetric stretching, while the band at 1442 cm–1 is ascribed to the C–H bending mode. Other bands at 1110–1258
cm–1 are due to the C–O stretching mode.11a After carbonization, most peaks disappear with
increase of temperature from 600 to 800 °C (Figure S6, Supporting Information). However, a small peak
at 1594 cm–1 remains, implying that some aromatic
rings in the carbonized samples still exist. Meanwhile, after the
carbonization process in conjunction with Ru NP immobilization, the
bands of −OH groups in the Ru@PDC nanocomposite decrease in
intensity. This is due to a strong interaction of the functional group
with Ru metal.44
In addition, different
types of plastic materials were utilized as carbon sources, including
high-density polyethylene (HDPE), low-density polyethylene (LDPE),
and polyacrylate (PC). The produced solid CSs had smooth surfaces
and the size of CSs is in the range from 3 to 8 μm (Figure S7, Supporting Information). In terms of TEM analysis
(Figure S8, Supporting Information), the
CSs produced with various plastic precursors are solid in nature,
and their spherical images of CSs can be clearly seen in all the cases
of carbon sources at 800 °C (Figure S8, Supporting Information). All samples are carbon-rich materials (∼68–69%)
as revealed by the elemental analysis and XRD patterns (Figure S9, Supporting Information), showing carbon content
on weight basis, and possession of trace amounts of heteroatoms (such
as N, S, and Cl Table S2, Supporting Information), whose presence should be beneficial to the preparation of active
carbons. Controlling of the carbonization conditions and activation
process is not the only key factor to determine porous structure of
CSs, which may also be affected by the structure and nature of the
precursors. It is important for starting plastics to possess high
content in hydrocarbons for the preparation of porous carbon by the
self-assembly approach with which hydrocarbons are aggregated into
higher poly-hydrocarbons resulting in the formation of carbon materials.
The elemental analysis (Table S3, Supporting Information) reveals that the hydrogen content is much greater in LDPE than
in HDPE and PC. As reported, it is well-known processes for the generation
of CSs from aromatic hydrocarbons and from degradation of plastic
materials to the mixture of hydrocarbons.44
Catalytic Study
Ruthenium-supported carbon materials
have been vastly envisaged for catalytic applications over the last
years.45,46 Because carbon-supported Ru NPs containing
mesoporous structures and large surface areas have been explored as
superior catalysts in the inorganic and organic fields.47 Therefore, the designed Ru@PDC catalysts can
serve as a novel catalyst for inorganic reduction reactions with a
highly efficient performance. The dispersibility of heterogeneous
catalysts in solution should play a key role in order to enhance the
catalytic activity. In this manner, the presence of functional groups
on the surface renders the catalyst to disperse fabulously in the
solution, as displayed in Figure S6b (Supporting Information).
The catalytic activities of Ru@PDC have
been tested for the reduction of [Fe(CN)6]3– using NaBH448 as a reducing
agent. Initially, we tested the blank experiment in the absence of
either reducing agent or Ru@PDC catalyst and found that the concentration
of [Fe(CN)6]3– did not change. It is
a fact that the reaction does not occur significantly in the presence
of either the reducing agent or Ru@PDC catalyst alone (Figures S10a,b, Supporting Information). Therefore, the combination
of all these reagents is required for the reduction reaction. The
catalytic activity of Ru@PDC with excess NaBH4 was performed,
showing that the characteristic yellow color (i.e., high catalytic
activity) in aqueous solution disappeared in inorganic reaction within
seconds, as shown in Figure 6a. We verified such an efficient reaction through analysis
of the catalyst effect on the kinetic reduction of K3[Fe(CN)6] in the presence of NaBH4, which is essentially
based on an electron-transfer process, and the kinetic change can
be easily monitored using UV–vis absorption spectroscopy. The
K3[Fe(CN)6] aqueous solution in light yellow
showed its absorption band at 420 nm. When NaBH4 was added,
the absorption intensity at 420 nm decreased gradually because of
the [Fe(CN)6]4– formation, indicating
that Fe(III) ions were reduced to Fe(II), along with the solution
color changed to colorless, as displayed in Figure 6b,c. Under the given conditions, we tested
the same reaction by NaBH4 in the presence of either the
Ru NP catalyst (Figure 5d) or available commercial Ru/C catalyst (Figure 6e); but both of them take a long period of
30 s (reaction was incomplete). These results indicated that both
Ru NP and Ru/C catalysts possess a less catalytic activity, when compared
with the Ru@PDC catalyst. This is due to insufficient porous features
to allow diffusion of reactants and products. When the concentration
of NaBH4 far exceeds [Fe(CN)6]3–, the kinetic reduction can be treated as a pseudo-first-order reaction,
and then the kinetic rate R can be expressed as eq 2(49) 2 where t is the reaction time; k is the pseudo-first-order
reaction rate constant; and Ct and C0 denote the concentration
of [Fe(CN)6]3– at time t and the initial time t0, respectively.
The Ct/C0 is proportional to the relative
intensity of At/A0, where At and A0 are the peak absorbance
at time t and t0, respectively.
Hence, the pseudo-first-order kinetic model is described as eq 3 3
Figure 6 UV–vis spectra
for the reduction of K3[Fe(CN)6] by NaBH4 in the presence of (a) Ru@PDC recorded
within 30 s, (b)1.0 mg, (c) 2.0 mg of Ru@PDC, (d) Ru NP, (e) Ru/C,
and (f) conversions vs catalysts.
The pseudo-first-order rate constant (k)
can be
estimated from the linear plot of ln(At/A0) versus the reduction
time (t). Accordingly, the rate constant (k) is calculated to be 0.0942, 0.1011, 0.0612, and 0.021
s–1, for Ru@PDC (1.0 mg; 2.0 mg), Ru NP, and ruthenium
black (Ru/C) catalysts, respectively. This plot ln(At/A0) versus
time reveals that the [Fe(CN)6]3– can
be converted completely into [Fe(CN)6]4–, as displayed in Figure 6f. Conversion of the catalytic products is determined by eq 4(50) 4
The calculated results demonstrated
that a good conversion (98%)
was observed for the Ru@PDC catalyst, while lower conversions were
obtained by unsupported Ru NP (65%) and commercial Ru/C (23%) catalysts;
however, both the Ru NP and Ru/C catalysts show slightly a lower catalytic
activity due to its lower surface area. The Ru@PDC was found to exhibit
a much better catalytic activity for [Fe(CN)6]3– reduction than that of ruthenium black (kRu@PDCs: 0.1011 s–1 vs kRublack: 0.021 s–1). Meanwhile, the k value of Ru@PDC (0.1011 s–1) is also higher than
those of Pd/GPDAP (kPd/GPDAP = 2.330 ×
10–2 s–1),48a Au@IFMC-100 (kAu@IFMC-100 = 3.07 × 10–2 s–1),49 ce-MoS2 (kce-MoS2 = 53 ± 7 × 10–2 s–1),51 and other unsupported noble metal
nanoparticles (see Table S7, Supporting Information) under the same reaction conditions, further demonstrating that
the Ru@PDC have excellent reactivity for the [Fe(CN)6]3– reduction.
In addition, we examined the catalytic
activity of the Ru@PDC catalyst
using Na2S2O3 as an alternative reducing
agent. At first, we tested the catalytic reduction reaction in the
absence of a catalyst, but the result showed that the reduction did
not proceed significantly in Na2S2O3 solution (Figure S11a, Supporting Information). Then, we added different dosages of catalyst into the reaction
mixture and found the depletion of [Fe(CN)6]3– peaking at 420 nm (Figure S11b,c, Supporting Information), revealing that the [Fe(CN)6]3– is converted into [Fe(CN)6]4–; the
corresponding kinetic plot is given in inset of Figure S11 Supporting Information. The linear plot of ln(At/A0) against time yielded the apparent rate constant to be 0.0932 s–1 (1.0 mg) and 0.1154 s–1 (2.0 mg)
at ambient temperature (Figure S8, Supporting Information). A few important studies reported previously based
on the Na2S2O3 reducing agent are
selected for comparison with our results, as summarized in Table S7. For instance, Ajit et al.52 have reported a porous platinum nanostructured
catalyst for the catalytic reduction of [Fe(CN)6]3–, yielding a smaller rate constant, kPt NNs = 1.52 × 10–4 s–1 for 60
min. Likewise, the Au/boehmite26 catalyst
yielded the reduction rate constant, kAu/boehmite, = 5.16 × 10–5 s–1 and
NiWO4 NP53 yielded kNiWO4 NP = 1.06 × 10–4 s–1. These catalytic results are less efficient
than those obtained with the Ru@PDC catalyst.
The reaction mechanism
invoked for the catalytic reduction of [Fe(CN)6]3– in the presence of reducing agents over
the Ru@PDC catalyst comprises two steps based on the earlier reports.24 They are (i) rapid polarization of the metal
NP by NaBH4 (fast) and (ii) transfer of excess surface
electrons to [Fe(CN)6]3– complex ions
(slow). That is, an electron-transfer process must be involved to
form the reduced [Fe(CN)6]4– ions. Hence,
the reduction reactions in an aqueous solution can be written as eq 5(48b) 5
To test the catalytic
activity of Ru@PDC, [Fe(CN)6]3– reduction
by Na2S2O3 was investigated involving
the following reaction eq 6(54) 6
Catalytic Activity
Catalytic activity depends significantly
on particle size and shape, and thus, how to synthesize colloidal
nanoparticles with well-controlled size and shape is urgent and challenging.31 Actually, the nanomaterial owns several catalytic
merits including crystal plane, crystal phase, and small size. Among
them, the size effect is an important parameter for both homogenous
and heterogeneous catalysis. The particle size effect of metal nanoparticles
on the catalysis has been thoroughly investigated.55 Regarding the particle size effect, the Ru@PDC catalyst
yielded higher activity because of the smaller size of Ru embedded,
resulting in a faster reaction (k = 0.1011 s–1), probably due to the larger surface area (particle
size 5 ± 0.2 nm), in contrast to the boehmite supported Au NP
(15–40 nm),26 which led to the k was 0.103 min–1 for the reduction of
K3[Fe(CN)6]. Likewise, the cases of Fe3O4@Au hollow sphere20 (Au NP:
25–30 nm, k: 36.55 × 10–3 s–1), graphene/Pd47b (Pd NP: 18.8 nm, k: 36.55 × 10–3 s–1) catalysts appear to have larger particle
size than our catalyst systems. The detailed data of various catalysts
with different sizes of metal nanoparticles and their rate constants
are listed (Table S6, Supporting Information). The results indicated that the smaller particle size may lead
to a larger surface area and subsequently was favorable for a good
catalyst with high efficiency. In other words, the small nanoparticles
are more effective catalysts than the larger NP, because an increase
in the electron density for the small metal atoms leads to an increased
reactivity on the surface of the catalysts. Moreover, PDC-supported
metal (Mn, Fe, Co, Cu, and Ni) catalysts for the reduction of K3[Fe(CN)6] were investigated, and the results given
in Table S6 (Supporting Information) shows
that the reaction is sensitive to the change of metals. Turnover frequency
(TOF) is used to quantify the catalytic activity of Ru@PDC and is
defined as the number of [Fe(CN)6]3– molecules
converted to [Fe(CN)6]4– with 1.0 mg
of catalyst per s. Typically, 3.0 mmol of [Fe(CN)6]3– solution was completely reduced in the presence of
Ru@PDC in 30 s, while Ru NPs and Ru/C exhibited lower catalytic activity
within the same reaction time. We can simply calculate TOF values
for a catalytic reaction using eq 7:56 7
The TOF
of Ru@PDC was up to 5.0 ×
10–5 s–1 for the [Fe(CN)6]3– reduction reaction, which was much larger than
those of other nanocatalysts reported previously and was comparable
with that of Ru NP and commercial Ru/C (see Table S7, Supporting Information).
Effect of Catalyst Dosage
Figure S12 Supporting Information shows
the k result
as a function of different amounts of catalyst (0.25–3.0 mg
mL–1). The k value is proportion
to the catalyst amount because of an increase in the number of reaction
sites.57 The obtained slope can be used
to evaluate the pseudo-first-order of kinetic rate constant. It becomes
feasible to understand why a large catalyst amount in the reaction
may result in a rapid reduction of [Fe(CN)6]3–. For instance, Reddy et al.58 have demonstrated
that gum acacia-stabilized gold nanoparticles (GA/Au NPs) for catalytic
reduction of [Fe(CN)6]3– showed a similar
dependence of the k value on catalyst dosages. Moreover,
the reaction orders and the rate constants were displayed in Table
S8 (Supporting Information). Hence, the
reaction constant and the order of the reaction are increasing linearly
with increase of Ru@PDC catalyst dosage.
Stability and Reusability
Stability and reusability
should be considered for the practical applications of catalysts.59 The Ru@PDC catalyst may be facilely recovered
by ultracentrifugation (10 000 rpm) after the reaction. As
a result, the catalyst was inspected up to six consecutive cycles
for the reduction of [Fe(CN)6]3– and
monitored by UV–vis spectroscopy. As shown in Figure 7a, the apparent rate constants
reveal that the catalyst preserves more than 85% of the initial catalytic
ability after six consecutive cycles. The reaction mixtures were also
analyzed by ICP–optical emission spectrometry to check if any
Ru was leached, but no significant leaching was found. Hence, the
reaction rate change cannot be caused by the loss of Ru from the catalyst.
The rational decrease of catalytic ability might be due to the trace
loss of catalyst after several times of use, as confirmed by HRTEM
images (Figure 7b,c).
The powder XRD pattern of the reused Ru@PDC catalyst demonstrates
to understand retention of the crystallinity after the catalytic reaction
as shown in Figure 7d. The energy-dispersive X-ray spectroscopy (EDX) analysis of the
Ru NP proved the existence of an elemental ruthenium signal. Other
EDX signals emitting from C, O, and Cu atoms were also noticed (Figure 7e). This result indicated
that the Ru species were successfully immobilized on the nanocomposite,
even after being recycled six times.
Figure 7 (a) Recycling test of the Ru@PDC catalyst
toward the [Fe(CN)6]3– reduction, (b,c)
FE-TEM images, (d)
XRD pattern, (e) EDX spectrum, (f) N2 sorption-isotherm,
and (g) corresponding pore size distribution of the reused Ru@PDC
catalyst.
Figure 7f shows
the nitrogen adsorption/desorption isotherms of the reused Ru@PDC
catalyst and pore-size distributions (Figure 7g) derived from the adsorption branch of
the isotherms according to the BJH method. We also noted that the
surface area of the spent Ru@PDC catalyst had shown slightly lower
surface area (SBET = 388.3 m2 g–1) than the fresh catalyst (SBET = 396.5 m2 g–1, Table 1) after six uses.
The catalytic activity decreased from the fourth to sixth cycles,
probably because of the loss of catalyst during the recycling process.
Notably, the reused catalyst exhibits a type-IV curve corresponding
to a mesoporous structure with pore volume (VTot = 0.080 cm3 g–1); hence, these
results demonstrated that the reused Ru@PDC catalyst remained stable
without any change in its porous structure after six runs.
Reduction
of New Fuchsin (NF)
In addition, we performed
the reduction of a cationic triarylmethane dye (new fuchsin, NF);
the chemical structure and characteristics of dye used in the study
is shown in Table S9, (Supporting Information). The reduction process of NF dye was monitored using UV–vis
spectrophotometry, as shown in Figure 8. Note that the reaction does not proceed significantly
in the absence of catalyst, indicating the indispensable role of the
catalyst for the NF reduction. As shown in Figure 8b–f, the absorbance peak of NF at
543 nm decreases to a different extent depending on the added amount
of 0.5, 1.0, 1.5, 2.0, and 3.0 mg of Ru@PDC catalyst. The NF solution
changes red color to colorless when the reduced NF is formed, confirming
the catalytic activities (inset of Figure 8b–f). As revealed in Figure 8g, the absorbance at 543 nm
disappears within 9 min after the introduction of 3.0 mg of Ru@PDC
catalyst. In contrast, 30, 18, 16, and 13 min are required to complete
the reduction by adding 0.5, 1.0, 1.5, and 2.0 mg of catalysts, respectively
(see Figure 8h). It
suggests that an increased catalyst dosage should result in fast diffusion
of dye molecules/reagents on the catalyst surface and thus enhance
the catalytic activity which may be reflected in the apparent rate
constant kapp measurements (Figure 8h). The kapp value is evaluated to be 0.1911, 0.3061, 0.4019, 0.6903,
and 0.7601 min–1 for addition of 0.5, 1.0, 1.5,
2.0, and 3.0 mg of catalyst, respectively (see Figure 8i). These results indicate that the reaction
follows a pseudo-first-order kinetics because of the presence of excessive
NaBH4. The kapp obtained for
Ru@PDC (0.7601 min–1) turns out to be much larger
than that of graphene quantum dots (kGQDs = 0.0263 min–1).60 The
fact may be caused by (i) a large surface area of Ru@PDC to effectively
adsorb a more amount of NF molecules and (ii) fast electron transfer
from NaBH4 to the adsorbed NF dye molecules via the catalyst.
Thus, it facilitates the reduction of organic pollutants absorbed
on the catalyst surface.
Figure 8 UV–vis spectra for the reduction of NF
dye in aqueous medium
in the (a) absence of catalyst, in contrast to the presence of (b)
0.5, (c) 1.0, (d) 1.5, (e) 2.0, and (f) 3.0 mg of Ru@PDC catalyst,
(g) plot of ln(At/A0) vs time for catalytic reduction of NF at
different catalyst dosages, (h) linear region of plot of ln(At/A0) vs time of catalytic reduction of NF used for calculation of kapp, and (i) dependence of kapp on catalyst dosage for reduction of NF.
Conclusions
In this work, a porous
and heterogeneous stable catalyst, Ru@PDC,
was successfully prepared and characterized. The catalyst exhibit
enhanced catalytic activity for the reduction of inorganic complex
and cationic dye with higher reaction kinetics as compared with other
catalysts. Furthermore, the as-prepared nanocatalyst possesses several
advantages: (i) it can be easily separated from the reaction mixture,
(ii) not much loss of catalytic activity is found even after several
cycles of reuse, (iii) it takes short time (∼30 s) to complete
the reaction showing superior activity, (iv) the catalyst was fabricated
using plastic as solid waste feedstock, and (v) moreover, the catalyst
has been used for perspective applications. The catalysts were found
to be stable and effective for more than 6 runs, with a conversion
efficiency of ∼98%. The decrease of conversion can be probably
attributed to a reduction in the surface active sites of the catalyst.
Experimental
Section
Materials
Ruthenium(III) acetylacetonate (Ru(acac)3, ≥99.9%), ruthenium black (Ru/C, ≥98%), potassium
ferricyanide (K3[Fe(CN)6], 99%), New Fuchsin
(NF), sodium borohydride (NaBH4, 99.99%), and sodium thiosulphate
(Na2S2O3, ≥98%) were purchased
from Sigma-Aldrich. All other chemicals belonged to analytical grade,
and all solutions were freshly prepared using Milli-Q water.
Preparation
of Porous Carbon
Plastic-derived carbon
(PDC) have been prepared from soft drink plastics collected from a
local market at Taipei, which were utilized as carbon sources according
to the methods reported previously.7−9 Typically, waste plastic
bottles shredded into small size of 30–50 mm pieces (∼2.0
g) were added in the 100 mL capacity Teflon-lined stainless steel
autoclave. The sealed autoclave was then heated to the temperature
(ramp at 20 °C min–1) in the muffle furnace
at ∼300 °C for 6 h. Subsequently, the carbonaceous material
was cooled slowly back to room temperature (RT), followed by thorough
washing with copious amounts of benzene and ethanol, and then air-dried
at 100 °C overnight. The PDC samples thus obtained were represented
to be PDC-x, where x denotes the
final carbonization temperature (in °C) used. To enhance their
porosities, the PDC substrates were pyrolyzed again under the condition
of flowing CO2 (flow rate 30 mL min–1) at 400 °C for 30 min. In comparison, the carbon sources generated
by other plastic materials such as HDPE, LDPE, PC, and polypropylene
showed the maximum extent of oil formation containing aromatic hydrocarbons
to form CSs. The mechanism of char formation in the thermal process
of polymer degradation was interpreted appreciably elsewhere.3,4 Furthermore, we have analyzed the chemical composition of plastic
wastes and their elemental composition of plastic-derived char (before
activation), PDC (after activation), and Ru@PDC as displayed in Tables
S2–S4, Supporting Information. In
addition, the yields of carbon after carbonization and activation
under different conditions were presented in Table S5, Supporting Information.
Physical Activation
In general, the endothermic reactions
for physical activation of the carbonaceous material by using water
vapor steam and CO2 are shown in eqs 8 and 9(61) 8 9 10 11
Besides, the C +
H2O reaction
in eq 8 is accompanied
by the formation of CO2 + H2, while catalyzed
on the carbon surface as shown in eq 10. Because of endothermic reactions for eqs 8 and 9, the
activation process may be controlled accurately in the heating furnace.
External heating to remain high temperature is required to drive.
In contrast to the reactions 8 and 9 which can be driven accurately at high temperature, the reaction 11 is extremely exothermic and its progression is
difficult to control. A decrease in the average particle size and
the product yield may happen as a result of over-heating the external
carbon surface.62
Preparation of the Ru@PDC
Catalyst
Ru@PDC nanocomposite
was obtained by immobilization of Ru NPs on the PDC-800 support. In
brief, 0.2 g of the as-prepared PDC-800 powdered sample was mixed
with Ru(acac)3 for 4.01 wt % loading in 5.0 mL tetrahydrofuran.
Then, the mixture was removed into a 50 mL Teflon-coated microwave
reactor for microwave irradiation at power of 300 W for 1 h. The Ru0 state was reduced effectively from the Ru3+ ions
upon irradiation and was dispersive on the mesoporous PDC carbon support.
Catalyzed Reduction of Ferrocyanate(III)
To conduct
the reduction reaction, we prepared 3.0 mL of 3 × 10–3 M [K3Fe(CN)6] into 1.0 mg mL–1 Ru@PDC catalyst and then added rapidly 0.2 mL of 0.04 M ice-cold
fresh NaBH4 or Na2S2O3. As the reaction proceeded, the solution in yellow faded to be colorless.
Subsequently, the kinetic measurements were carried out for K3Fe(CN)6 by using UV–vis spectroscopy fixed
at 420 nm to monitor the reduction reaction in a quartz cuvette. When
the reaction was complete, the catalyst was removed by using an ultracentrifuge
for further investigation of its reusability.
Catalyzed Reduction of
the Cationic Dye
Experimental
procedure for the cationic dye reduction is based on an earlier report.63 Typically, 1.0 mg mL–1 of
solid catalyst (Ru@PDC) was added into 3.0 mL of NF (5 mM) dye solution
at RT under vigorous magnetic stirring in dark condition for 5 min
to allow the dye molecules adsorbed physically onto the Ru@PDC composite.
Then, 0.1 mL of 0.04 M ice-cold NaBH4 was added and the
mixture was kept stirring under ambient conditions. Approximately,
3.0 mL of sample was taken from the mixture and the dye solution was
analyzed by UV–vis spectrophotometric measurements (at 553
nm) to follow the catalytic reduction reaction.
Supporting Information Available
The Supporting Information is
available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b01680.Additional experimental
details including catalyst characterization
and ruthenium dispersion measurements; results obtained from pore
size distribution; SEM, TEM, EDX, XRD, FT-IR, and UV–vis studies
of assorted samples; carbon yield calculation; chemical and elemental
composition analyses; comparison of catalytic activity reduction of
K3[Fe(CN)6] over the Ru@PDCs and other reported
catalyst; kinetic parameters for the Ru@PDC catalyst at different
dosages; and chemical structure and some properties of NF dye (PDF)
Supplementary Material
ao8b01680_si_001.pdf
The authors
declare no competing financial interest.
Acknowledgments
The authors are grateful for the financial
supports
(NSC 102-2113-M-002-009-MY3 to KCL) from the Ministry of Science and
Technology (MOST), Taiwan.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 3145888310.1021/acsomega.8b00596ArticleTwo-Dimensional
Double Hydroxide Nanoarchitecture with High Areal and Volumetric Capacitance Deshmukh Abhay D. *†Urade Akanksha R. †Nanwani Alisha P. †Deshmukh Kavita A. §Peshwe Dilip R. §Sivaraman Patchaiyappan ∥Dhoble Sanjay J. ‡Gupta Bipin Kumar *⊥†Energy
Materials and Devices Laboratory, Department of Physics and ‡Nanomaterials
Research Laboratory, Department of Physics, RTM Nagpur University, Nagpur 440033, India§ Department
of MME, Visvesvaraya National Institute
of Technology, Nagpur 440010, India∥ Polymer
Science and Technology Centre, Naval Materials
Research Laboratory (DRDO), Ambernath (E) 421506, India⊥ CSIR-National
Physical Laboratory, Dr. K.S. Krishnan Road, New Delhi 110012, India* E-mail: abhay.d07@gmail.com (A.D.D.).* E-mail: bipinbhu@yahoo.com (B.K.G.).02 07 2018 31 07 2018 3 7 7204 7213 29 03 2018 18 06 2018 Copyright © 2018 American Chemical
Society2018American Chemical
SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
The development of high volumetric
or areal capacitance energy
storage devices is critical for the future electronic devices. Hence,
the hunting for next-generation electrode materials and their design
is of current interest. The recent work in the two-dimensional metal
hydroxide nanomaterials demonstrates its ability as a promising candidate
for supercapacitor due to its unique structure and additional redox
sites. This study reports a design of freestanding high-mass-loaded
copper-cobalt hydroxide interconnected nanosheets for high-volumetric/areal-performance
electrode. The unique combination of hydroxide electrode with high
mass loading (26 mg/cm2) exhibits high areal and volumetric
capacitance of 20.86 F/cm2 (1032 F/cm3) at a
current density of 10 mA/cm2. This attributes to the direct
growth of hydroxides on porous foam and conductivity of copper, which
benefits the electron transport. The asymmetric supercapacitor device
exhibits a high energy density of 21.9 mWh/cm3, with superior
capacitance retention of 96.55% over 3500 cycles.
document-id-old-9ao8b00596document-id-new-14ao-2018-00596qccc-price
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Introduction
The proliferating demand
for green and clean energy has excited
tremendous research efforts in the design and fabrication of the energy
storage devices, in particular, supercapacitor. Recent research has
focused on improving the specific capacitance of supercapacitor, but
a typical challenge for such a system is to increase the volumetric
capacitance.1−3 The only way to increase the volumetric capacitance
is higher mass loading with three-dimensional (3D) porous network.
Nevertheless, the crucial disadvantage of higher mass loading per
cubic centimeter is increasing the dead mass of an electrode.4 The highest volumetric capacitance achieved for
hydrated ruthenium oxide5 is around 1000–1500
F/cm3, activated graphene6,7 can reach the
capacitance of 200–350 F/cm3, activated carbon8,9 can reach 60–100 F/cm3, and Mxene10,11 can reach 1000 F/cm3 but only with low mass loading or
in thin film.
The two-dimensional solids are gaining tremendous
attention, in
particular, layered double hydroxide (LDH) with a general formula
of [M12+–x M3+x(OH)2]12−22 (M2+and M3+, the bivalent and trivalent metal
cations, respectively), due to the double benefit of their large active
surface area23−25 and high density of redox active species. Metal hydroxides
had been studied and proved to be a promising candidate for supercapacitors
exhibiting gravimetric capacitance exceeds that of reported metal
oxide materials. However, volumetric capacitance is limited due to
lower mass loading of active material. With increasing mass loading
per centimeter cubic, metal oxide/hydroxides show decrease in cyclability
as well as capacitance owing to lower surface active sites and etching
of active material. To date, all oxide/hydroxides have been studied
in thin film with lower mass loading.26−30
Layered double hydroxide (LDH) nanosheets as
electrode for supercapacitor
application have raised particular interest.30,31 Several LDHs have been studied, including Ni–Co LDHs, Ni–Mn
LDHs, Ni–Fe LDHs, and Cu–Co LDHs.31−38 Although there are some publications on preparations39−43 and applications of Cu–Co LDHs, to our knowledge, the higher
mass loading of Cu–Co LDHs for high areal/volumetric supercapacitor
application has not been reported so far. The higher stability, good
conductivity, excellent electrochemical activity, and multiple functionality
over other metal hydroxides have let the Cu–Co LDHs to be an
ideal electrode for supercapacitor application. The copper-cobalt
double hydroxides reported in this study were prepared by growing
copper-cobalt double hydroxide higher mass loading on the nickel foam
with porous and layered nanostructures for supercapacitors. Here,
we report a two-dimensional copper-cobalt double hydroxide with different
mass loadings per centimeter square, demonstrating the improved electrochemical
properties when used as electrode material in a supercapacitor. The
unique combination of double hydroxide electrode with a high mass
loading of 26 mg/cm2 exhibits a high volumetric capacitance
of 1032 F/cm3 at a current density of 10 mA, which will
open up new opportunities to develop a high volumetric supercapacitor
and a new field in double hydroxide materials.
Results and Discussion
A schematic representation of the deposition process of high-density
layered copper-cobalt hydroxide (L-CCH) architecture is shown in Figure 1. The electrodeposited
L-CCH electrode results in the formation of a porous 3D-interconnected
two-dimensional layered framework with a large oxygen-containing functional
group, which was beneficial for increasing the electrochemical sites
within the network. The mass loading of the L-CCH can easily be tuned
with a variation of concentration of solute in the electrodeposition
process. The change in concentration of solute has been preferred
over time to have higher density of L-CCH electrode instead of growth
in the layered structure (Figure 1a). The growth mechanism and morphology of L-CCH network
is well understood from the field emission scanning electron microscopy
(FESEM) images that reveal the growth of 2D layered like interconnected
structure (Figure 1b). The insightful observation indicates the dense network of L-CCH
nanosheets that are approximately 100 nm in width and few microns
in length (Figure 1c). This interconnected structure can play an important role in increasing
the surface area and electrochemical sites for absorption. Further
energy-dispersive spectroscopy (EDS) analysis was carried out, which
confirms the presence of cobalt, copper, and oxygen, as shown in Figure 1f. The detailed spectroscopic
analysis of L-CCH structure was explored by Fourier transform infrared
spectroscopy (FTIR) (Figure 1d). The peaks at 3134 and 3438 cm–1 are
assigned to O–H stretching vibration of water molecules in
the interlayer and hydrogen-bonded hydroxyl group of copper-cobalt
hydroxide. The other absorption bands observed below 700 cm–1 are associated with metal oxygen stretching and bending modes. The
spectrum shows a distinct peak at 524 and 541 cm–1, indicating the absorptions associated with Cu–O stretching
and Cu–OH bending vibrations, whereas that at 511 cm–1 corresponds to the Co–O stretching vibration.44Figure 1e shows the X-ray diffraction (XRD) pattern of the L-CCH electrode,
which shows the 2θ values at 13°, 26°, 33°, and
36°, corresponding to (001), (002), (120), and (121) lattice
plane, corresponding to copper hydroxide (JCPDS 42-0746), and the
peaks observed at 43°, 51°, 59°, and 74° 2θ
values, corresponding to (200), (102), (003), and (311) lattice plane,
which are in good agreement with the XRD data of cobalt hydroxide
of JCPDS 300443. The average grain size was estimated by using the
Debye–Scherer formula: D = 0.9 λ/β cos(θ),
where λ is 1.54A° for the wavelength of Cu Kα radiation,
“β” is full width at half-maximum, and “θ”
is the Bragg angle. The average grain size was found to be in the
range of 100 nm, which is in agreement with the SEM results.
Figure 1 (a) Schematic
representation of the synthesis procedure of L-CCH
electrode showing different mass loadings. (b, c) Microscopic images
of L-CCH electrode confirm the high mass loading with interconnected
layered growth of double hydroxide. (d) Fourier transform infrared
spectra of L-CCH electrode shed the light on types of bonding and
surface groups. (e) X-ray diffraction spectra of L-CCH, which is a
combination of copper and cobalt hydroxide results in double hydroxide
electrode. (f) Energy-dispersive spectrum for L-CCH, which shows the
pure formation of double hydroxide.
Layered double hydroxides (LDHs) have been extensively studied
as pseudocapacitive material and acknowledged as superior to metal
oxides due to higher electrochemical activity. However, the performance
of hydroxides/oxides completely depends on the electrode film thickness,
which limits their use in requisite high volumetric or areal capacitance
devices. Moreover, thick-film electrode without insulating binder
deteriorates the performance of metal oxide/hydroxide due to collapse
of 3D architecture as well as limited ionic transport in the inner
volume of the thicker electrode. To enhance the volumetric capacitance
of L-CCH electrode, a higher mass loading of 26 mg/cm2 electrode
was examined. In the initial experiments, we found that the volumetric
capacitance of lower mass loading L-CCH1 is negligible
compared to volumetric capacitance of high mass loading of L-CCH3.
First, the electrochemical properties of different
areal density
L-CCH electrodes were tested in 2 M KOH electrolyte. The electrically
conductive layer allows the thicker film with the high mass loading
formation without any binder. The obtained cyclic voltammetry (CV)
curves in 2 M KOH from 0.0 to 0.45 V potential versus Ag/AgCl are
shown in Figure 2a.
It is clearly seen from the typical CV curves of L-CCH electrode that
the capacitance increases by a factor of 10 in the higher-areal-density
electrode. Galvanostatic charge/discharge measurement (Figure 2b) was carried out for the
L-CCH1, L-CCH2, and L-CCH3 electrode
at a current density of 20 mA/cm2, which shows the discharge
time of 12.63, 32.72, and 192 s, respectively, suggesting the formation
of more redox sites in higher mass loading, which is in agreement
with CV results. Figure 2c shows the CVs of L-CCH3 electrode at a scan rate ranging
from 5 to 100 mV/s showing the semirectangular shape retained even
at a very high scan rate of 100 mV/s. The semirectangular shape may
be explained by the existence of double-layer capacitance as well
as pseudocapacitive behavior. The possible electrochemical faradic
process of L-CCH electrodes in 2 M KOH as electrolyte is 1 2 To study the areal and volumetric capacitance
of the L-CCH3, electrode galvanostatic charge/discharge
measurements were performed at 10, 20, 30, 40, 50, 60, 80, 102, 122,
204, and 306 mA/cm2 in 2 M KOH, shown in Figure 2d. A plot of current density
verses areal/volumetric capacitance for the high mass loading (L-CCH3) electrode is shown in Figure 2e. The excellent volumetric capacitance of 1032 F/cm3 and areal capacitance of 20.86 F/cm2 were measured
at a current density of 10 mA/cm2. The capacitance of L-CCH3 electrode was found to be 18.04 F/cm2, which is
18 times higher than that of L-CCH1 electrode (1.06 F/cm2) at the current density of 20 mA/cm2 and retains
50% of capacitance even at a high current density of 100 mA/cm2 (shown in Supporting Information Tables S1 and S2). This high capacitance value at a high scan rate
is assumed due to the more porous nature of L-CCH3 electrode,
which increases the rate of intercalation/deintercalation of an electrolyte
ion in the L-CCH 2D-interconnected layered framework. In addition,
it also reveals that the volumetric/areal capacitance is dependent
on the mass loading of L-CCH electrode. The cyclic stability of the
electrode was examined for >2000 charge/discharge cycles at a very
high current density of 60 mA/cm2 (Figure 2f). Usually, at higher current density, the
electrode stability decreases rapidly. However, in this study, the
capacity retention of 80% was found after 2000 cycles at 60 mA/cm2.
Figure 2 (a) Cyclic voltammetry curve at 5 mV/s for different mass loadings.
(b) Galvanostatic charge/discharge curves of different mass loadings
at 20 mA/cm2 current density. (c) Cyclic voltammetry curves
recorded at various scan rates for higher areal density electrode.
(d) Galvanostatic charge/discharge curve of higher areal density electrode
at different current densities. (e) Variation of areal and volumetric
capacitance with current densities calculated from galvanostatic charge/discharge
curve. (f) Cyclic stability performance for 2000 charge/discharge
cycles; the inset figure shows last 10 charge/discharge cycles. (g)
Ragone plot of the estimated volumetric energy density and volumetric
power density at various charge/discharge rates.
To elucidate the charge/discharge kinetics and semirectangular
behavior of L-CCH electrode for lower and higher mass loading, the
method given by Trasatti45,46 et al. was employed.
According to this method, the total charge storage of an electrode
is a sum of contribution due to an inner surface, where faradic reaction
occurs from the slow H+ ion donating species, and the outer
surface, where redox reaction can occur from fast charge transfer.
The capacitive charge (including both pseudocapacitance and electric
double-layer capacitance) depends on the potential scan rate given
by Trasatti in a way as follows 3 4 where Q* is the total charge
obtained by integrating the CV curve at different scan rates.
The capacitive charge contribution and the total charge contribution
can be calculated from the graphs, as shown in Figure 3a,b. In this process, the total charge storage
can be calculated from the y-axis intercept of Q* verses V1/2 and the charge
stored on the outer surface of the electrode can be calculated from
the plot of Q* against V−1/2. Moreover, the difference between the total charge and the charge
stored on the outer surface will give the value of the charge stored
in the inner surface. As shown in Figure 3a, the value of the maximum total charge
stored is found to be 8.3486 C/cm2, which is equivalent
to the maximum areal capacitance ∼20.86 F/cm2 for
the potential window 0.45 V. Furthermore, the charge stored at the
outer surface, (Figure 3b) was found to be 1.606 C/cm2 (∼3.56 F/cm2) and the charge stored in the inner surface (diffusion-controlled
redox capacity) was found to be 6.7426 C/cm2 (∼14.98
F/cm2). From Figure 3c, it is clear that the diffusion-controlled redox capacity
increases on increasing the mass loading. The L-CCH3 electrode
exhibited 80.77% diffusion-controlled redox capacity, whereas L-CCH2 and L-CCH1 exhibited 45.94 and 43.66%, respectively.
Increase in the total charge might be the reason for the corresponding
higher areal and volumetric capacitance for L-CCH3 electrode
compared to that of L-CCH2 and L-CCH1. It is
speculated that the surface Grotthuss mechanism18 is responsible for the diffusion of H+ ions
to the inner region surface.
Figure 3 (a) Plot of 1/Q* against V1/2 to find the total charge (Q*) stored by
the electrode material. (b) Plot of Q* against V–1/2 to find the charge stored only on
the outer surface of the electrode material (Q*outer).
(c) Contributions of double-layer capacity and diffusion-controlled
redox capacity to the total capacity of the electrode. (d) Plot of
log I and log V to
find the value of b (b = 0.53, 0.75,
and 0.71 for L-CCH1, L-CCH2, and L-CCH3)
The total electrochemical charge
storage can be obtained by integrating
the CV curve, and this charge originates from two contributions: the
faradic contribution limited by ion diffusion together with fast charge-transfer
process at the surface and the non-faradic contribution from the fast
electric double-layer effect. This effect can be analyzed by the CV
curve at the different scan rates using the power law47−49i = aVb, where “a” and “b” are adjustable
parameters. b value can be determined by the slope
of log i against log V. Ideally, if b value is ∼0.5, then the capacity
response is diffusion controlled and it satisfies Cottrell’s
equation9i = V1/2 and b = 1 shows purely
capacitive response (including both double-layer capacitance and diffusion-controlled
redox capacitance). From Figure 3d, the b value of L-CCH3 is found to be 0.53, which demonstrates the dominancy of diffusion-controlled
redox capacitance, which agrees with our results. For L-CCH1 and L-CCH2, b values were 0.75 and 0.71,
respectively, which shows the capacitive response. This confirms the
higher mass of our L-CCH3 electrode increases the diffusion-controlled
redox activity and is dominant in this study.
The electrochemical
impedance spectroscopy (EIS) is an important
characterization tool to evaluate the resistive behavior of the electrode. Figure 4a shows the respective
Nyquist plots for three different electrodes from f = 0.01 to 10 000 Hz, where Z′ is
the real part and Z″ is the imaginary part
of the impedance, respectively. The Nyquist plots consist of three
characteristic regions:50,51 (1) a low-frequency
region that is represented by an inclined line along the imaginary
axis which shows capacitive behavior also known as double-layer capacitive
region; (2) a high-frequency region represented by a partial semicircle
which shows the blocking behavior of the supercapacitor (in this region,
the supercapacitor behaves as a pure resistor and the resistance values
determines the charge-transfer and series resistance of the electrode);
and (3) a middle-frequency range that shows the effect of electrode
thickness and the porosity on the diffusion of ions from electrolyte
to electrode. The inset of the Figure 4g shows the equivalent circuit [R(C{RQ})W] used for the
fitting curve of L-CCH3. Rs is the equivalent series resistance of an electrolyte, Rct is the charge-transfer resistance during the faradic
reaction, Cd is the electric double-layer
resistance, Zw is the Warburg impedance
that represents the impedance of the diffusion controlling process
in the electrolyte, and CPE is the constant-phase element. Electrochemical
impedance is defined as51,52ZCPE = [Y0(jω)n]−1, where the unit of Y0 is 1 S/cm2 and is independent of
frequency and n is the exponent whose values varies
between −1 and +1; when n = −1, the
CPE is pure inductor; when n = 0, the CPE behaves
as a pure resistor; and when n = 1, CPE is pure capacitor.
In our experiment, the CPE value for L-CCH3 is found to
be n = 1.0, which shows that CPE behaves like a pure
capacitor, which is in good agreement with our results. Nyquist plots
clearly show that in the high-frequency region, L-CCH3 has
a lower series resistance value (Rs =
0.59 Ω) than that of L-CCH1 and L-CCH2 (Supporting Information Figure S1), which
implies that the resistance of an electrolyte solution is lesser in
L-CCH3 electrode. Moreover, the impedance spectrum of L-CCH3 shows a smaller semicircle (Rct = 0.11 Ω) than that that of the L-CCH1 and L-CCH2, which suggests that the L-CCH3 has a good electrical
conductivity between the prepared electrode and current collecting
electrode, as well as lower charge-transfer resistance, which is attributed
to the significant increase in the capacitance value of L-CCH3. Additionally, in the low-frequency region, the ideal straight
line implies a higher rate of electrolyte diffusion
and mass transfer. Figure 4c shows the good access to the electrolyte and ionic diffusion
even after 2000 cycles attributed to the excellent electrical conductivity
and very low internal resistance (Figure 4b). The Bode plots show phase angle values
obtained for higher mass loading electrode is close to 74, which is
almost near to that of the ideal capacitor, suggesting that the prepared
material is suitable for the fabrication of low-leakage capacitor.
Moreover, no significant change occurs in the phase angle after 2000
cycles. The EIS data strongly supports the excellent electrochemical
activity and high rate capability.
Figure 4 (a) Nyquist plot (−Z″ vs Z′ plot) for the different areal
density electrodes
within the frequency range from 0.01 to 100 000 Hz. (b) Bode
phase angle plot (phase angle against frequency for different areal
density electrodes). (c) Plot of the real part of capacitance against
frequency for different areal density electrodes. (d) Plot of the
imaginary part of capacitance against frequency for different areal
density electrodes. (e) Normalized reactive power |Q|/|S| and reactive power |P|/|S| vs frequency plots (f) Nyquist plot (−Z″ vs Z′ plot) for L-CCH3 before and after 2000 cycles; the inset shows the equivalent
circuit used for fitting the data. (g) Bode phase angle plot before
and after cycles for L-CCH3
The relaxation time constant τ is a measure of how
fast the
device can discharge and obtained from the analysis of the complex
plots. The complex capacitance is expressed as C(ω)
= C′(ω) + jC″(ω),
where C′(ω) is the real part of the
capacitance that shows the amount of stored energy in farad and C″(ω) is the imaginary part of the capacitance
that shows the energy dissipation as a function of the angular frequency
and they are given by22 5 6 where Z′ and Z″ are
the real and imaginary part of the impedance,
ω = 2πf, and Z(ω)
= Z′(ω) + jZ″(ω),
where ω is the angular frequency.
The complex power is
defined as S(ω) = P(ω)
+ jQ(ω), where P(ω)
is the real part of complex power called active
power and Q(ω) is the imaginary part of the
complex power called reactive power, and they are given by 7 8 where ΔVrms = ΔVmax/√2 and
ΔVmax is the maximum value of the
potential (here,
0.45 V). From Figure 4e, the relaxation time constant (τ = 1/f)
can be calculated from either the frequency corresponding to the half
of the maximum value of the real part of capacitance, that is, from C′(ω) against the frequency plot or peak frequency
corresponding to the C″(ω) against frequency
plots. As shown in Figure 4c, the real part of the capacitance decreases as the frequency
increases, which is a characteristic of the electrode material and
the electrode/electrolyte interface. The more detailed characteristics
of relaxation time constant can be obtained from the normalized power
against frequency plot. Figure 4f shows the plot of the real part of power P/S and imaginary part Q/S against frequency plots. The power dissipated into the
systems can be analyzed from the active power P/S. The impedance behavior of the supercapacitor varies from
the ideal capacitive behavior at a low frequency where no power is
dissipated to the pure resistive behavior at a high frequency where P = 100%. In fact, P/S and Q/S show the opposite trend
with respect to the frequency. The crossing of the two plots P/S and Q/S appears at ϕ = 45° and will give the value of the frequency
corresponding to the relaxation time. It defines the capacitive behavior
at frequencies below 1/τ and resistive behavior at frequencies
above 1/τ. From the crossing point of the two plots, the relaxation
time has been calculated for higher and lower mass loading. The obtained
relaxation times for L-CH1, L-CCH2, and L-CCH3 were 1, 2, and 12 s, respectively.
Figure 5 (a) Cyclic voltammogram
of carbon cloth as a negative electrode
and L-CCH3 as positive electrode at 5 mV/sec. (b) Cyclic
voltammetry curves of an asymmetric L-CCH3//CC electrode
at different scan rates. (c) Galvanostatic charge/discharge curves
at different current densities from 3 to 10.5 mA/cm2. (d)
Plot of areal and volumetric capacitance as a function of current
densities. (e) Cyclic performance during 3500 charge/discharge cycles.
It is clearly seen from the figure that only 0.1% loss is observed
during cyclic performance; inset figure shows the last 10 charge/discharge
cycles. (f) Nyquist plot (−Z″ vs Z′ plot) of L-CCH3//activated carbon cloth
(ACC) electrode within the frequency range from 0.01 to 100 000
Hz. (g) Plot of real and imaginary capacitance against frequency.
(h) Normalized power against frequency. (i) Ragone plot showing the
relationship between the volumetric energy density and power density
of a typical electrolytic capacitor, supercapacitor, Li thin-film
batteries, and our prepared L-CCH3//ACC electrode.
To study the practical application
of high mass loading L-CCH3 architecture, an asymmetric
supercapacitor is fabricated
by using L-CCH3 as a positive electrode and the activated
carbon cloth (ACC) as a negative electrode. Figure 5a shows the CV curves of carbon cloth within
a 0.0 to 1.0 V and L-CCH3 electrode within a 0.0 to 0.45
V voltage window. The prepared L-CCH3//ACC asymmetric device
operates at a higher voltage window from 0.0 to 1.2 V at different
scan rates ranging from 10 to 200 mV/s, exhibiting the combined behavior
of carbon cloth and L-CCH electrode (Figure 5b). The CV curves show obvious reduction
oxidation peak within a 0 to 1.2 V potential window. Interestingly,
with the increasing scan rate, no major shifts are observed in the
oxidation reduction peak, which shows the device ability to sustain
a high charge/discharge rate and an excellent ability of ion diffusion
into the electrode surface. Figure 5c shows the galvanostatic charge/discharge curve of
L-CCH3//ACC at various current densities from 3 to 10.5
mA/cm2. The areal capacitance values calculated from charge-discharge
(CD) curves are 2.43, 2.32, 2.24, 2.18, 2.14, 2.04, and 1.98 F/cm2 and 109.73, 104.38, 100.81, 98.14, 96.35, 92.11, and 89.22
F/cm3 at the current densities of 3, 4.5, 6, 7.5, 9, 10.5,
and 12 mA, respectively (shown in Supporting Information Table S4). The comparative study of different
areal capacitance values and their energy densities is shown in Supporting
Information Table S5, which shows the highest
performance of L-CCH electrode in terms of area/volumetric capacitance
as well as energy density.
The electrochemical impedance spectroscopy
of an asymmetric device
is also studied to gain the understanding of electrochemical behavior. Figure 5d represents plot
of areal and volumetric capacitance as a function of current densities
and Figure 5e shows
the cyclic performance during 3500 charge/discharge cycles. Figure 5f shows the Nyquist
plot and the corresponding equivalent circuit. The asymmetric device
shows a very low series resistance Rs =
0.9 Ω and a charge-transfer resistance of 2.11 Ω. The
relatively low values of Rs and Rct represent the higher accessibility in the
diffusion of ions in the electrolyte to the electrode material during
charge/discharge cycles, which is responsible for an excellent electrochemical
performance of an asymmetric device. To study the stability of an
asymmetric device, the cycle stability tests were carried out at 8.33
mA/cm2 current density, shown in Figure 5e. The asymmetric device exhibits an excellent
cyclic stability with capacitive retention of 96.55% after 3500 cycles. Figure 5i shows the Ragone
plot of several commercially available energy storage devices. It
can be seen from the plot that the energy density of L-CCH3//ACC supercapacitor reached close to the energy density of Li thin-film
batteries and power density approached close to the power density
of the 25 mF supercapacitor. The imperative feature of this device
is a very small characteristic relaxation time constant τ0 (the minimum time required to discharge all energy from the
device), which is only 12 s. Thus, the areal/volumetric capacitance
values described above are probably near to the maximum values possible
for LDH materials in general. Thus, the fact is that high volumetric
and areal capacitance of L-CCH material may also enable LDHs use in
supercapacitors. Thus, this work opens up exciting possibilities of
developing higher mass loading of LDH electrode supercapacitor devices
using a large variety of combinations of metals and their chemistries.
Conclusions
In summary, a simple and reproducible method has been adopted to
demonstrate the electrochemical performance of copper-cobalt hydroxide
with higher mass loading in aqueous electrolyte. Benefits of the double
metal hydroxide and 2D structure contribute to the ultra-high volumetric/areal
pseudocapacitive performance. The 2D hydroxide structure reveals an
enhanced volumetric capacitance response of 1032 F/cm3.
The enhanced capacitance was due to the high mass loading layered
structure with porous structure leading to more electrochemical sites
for redox response, as well as high ionic diffusion and better electron
conductivity of copper in copper-cobalt hydroxide electrode. The prepared
asymmetric supercapacitor showed a high areal and volumetric capacitance
of 2.43 F/cm2 (109 F/cm3) at 2.41 mA/cm2 and exhibited an excellent cyclic stability with 96.55% capacitive
retention after 3500 cycles at the current density of 8.33 mA/cm2. Thus, this effective method of fabricating a freestanding
metal hydroxide/carbon asymmetric device paves the way for practical
application of an energy storage device.
Methods
Synthesis of
L-CCH/Ni-Foam Electrode
All chemicals
were of analytical grade and used without further purification. Before
depositing copper-cobalt LDHs, nickel foam was washed with 0.1 M HCl
solution for 3 min and cleaned with deionized water to remove NiO
layer from its surface. The cleaned nickel foam was dried in a vacuum
oven overnight at 60 °C and used as the working electrode (1.5
cm × 1 cm). Platinum and Ag/AgCl were used as the counter and
reference electrode, respectively. The Cu–Co LDHs were electrochemically
deposited by dissolving 4 mM Cu(NO3)2·3H2O and 8 mM of Co(NO3)2·6H2O in 30 mL of distilled water at a constant voltage of −1
V for 300 s. Further, the electrodeposited Cu–Co LHDs were
cleaned with distilled water and dried in vacuum oven overnight at
80 °C. The mass loading of the electrode was measured before
and after electrodeposition. The same procedure is repeated by taking
different concentrations of copper nitrate trihydrate and cobalt nitrate
hexahydrate to prepare a different mass loading electrode to compare
the results. The different mass loading electrode of 4.69, 8.77, and
26.53 mg/cm2 are denoted as L-CCH1, L-CCH2, and L-CCH3, respectively.
Characterization
Powder X-ray diffraction (PXRD) patterns
were recorded with a PAN-analytical diffractometer equipped with Cu
Kα (λ = 1.5405 Å) X-ray source in geometry and 0.5
s dwelling time with a proportional detector. An anti-scattering incident
slit (2 mm) and nickel filter were used. The tube voltage and current
were 40 kV and 40 mA, respectively. Scanning electron microscopy (SEM)
was performed on a JEOL JSM 7610F FESEM equipped with energy-dispersive
spectroscopy (EDS) Oxford instruments, X-Max with coating unit (make:
JEOL, model: JEC-3000FC). The EDS mapping was obtained at low magnification
at random points of the electrodeposited film. Fourier transform infrared
spectra were obtained from the Perkin Elmer Spectrum one instrument.
All electrochemical measurements were carried out using a Metrohm
Autolab 128N potentiostat (Netherland) with 2 M KOH aqueous electrolyte
in electrochemical cell. Ag/AgCl and platinum foil were used as pseudo
reference electrode and counter electrode, respectively, whereas electrodeposited
L-CCH was the working electrode.
Electrochemical Measurement
Electrochemical performance
of L-CCH electrodes was studied by using a three-electrode configuration
and 2 M KOH as an electrolyte. Platinum foil and silver/silver chloride
electrode are used as a counter and a reference electrode, respectively.
Cyclic voltammetry was performed on a Metrohm Autolab-128N potentiostat.
The electrodeposited L-CCH electrodes were used as a working electrode
in a three-electrode system. CV measurement was carried out at different
scan rates in the potential window 0 to 0.45 V. The charge/discharge
study was performed at different current densities of 10, 20, 30,
40, 50, 60, 80, 102, 122, 142, 204, and 306 mA/cm2 in a
potential window of 0 to 0.45 V.
Supporting Information Available
The Supporting Information
is available free of charge on the ACS Publications website at DOI: 10.1021/acsomega.8b00596.Performance data
for three independent CCH pseudocapacitive
electrodes, areal and volumetric capacitance at different current
densities from 10 to 122 mA/cm2, performance comparison
of copper-cobalt hydroxide pseudocapacitor with oxides, areal and
volumetric capacitance of an asymmetric device at different current
densities, performance comparison of L-CCH//ACC two-electrode pseudocapacitor,
equivalent circuit of L-CCH-1 and L-CCH-2, CV curves at different
cell voltages at a scan rate of 100 mV/s, CD curves at different cell
voltages, plot of the bode modulus and phase angle against frequency
for two-electrode, CV curve before and after 3500 cycles at a scan
rate of 10 mV/s (PDF)
Supplementary Material
ao8b00596_si_001.pdf
Author Contributions
All authors
contributed to the experimental design and data analyses. The manuscript
was written through contributions of all authors. All authors have
given approval to the final version of the manuscript
The authors
declare no competing financial interest.
Acknowledgments
A.D.D. acknowledges the financial support from
Naval Research
Board (NRB), DRDO New Delhi (NRB Sanctioned no: DRDO/NRB/4003/PG/338).
A.D.D. acknowledges ENVIRON Care Product for providing the activated
carbon cloth (ACC) for this research work. A.D.D. also acknowledges
Celgard, LLC, North Carolina for their support in making available
the material for our research.
==== Refs
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ACS OmegaACS OmegaaoacsodfACS Omega2470-1343American Chemical Society 10.1021/acsomega.8b00488ArticleRegulating the Microstructure of Intumescent Flame-Retardant
Linear Low-Density Polyethylene/Nylon Six Blends for Simultaneously
Improving the Flame Retardancy, Mechanical Properties, and Water Resistance Zhao Pan Lu Chang *Gao Xi-ping Yao Da-Hu Cao Cheng-Lin Luo Yu-Jing Chemical Engineering & Pharmaceutics
School, Henan University of Science and
Technology, 263, Kaiyuan Avenue, Luoyang 471023, China* E-mail: luchang139@126.com (C.L.).27 06 2018 30 06 2018 3 6 6962 6970 15 03 2018 14 06 2018 Copyright © 2018 American Chemical Society2018American Chemical SocietyThis is an open access article published under an ACS AuthorChoice License, which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
A compatibilizer
was melt-blended with intumescent flame-retardant
linear low-density polyethylene/nylon six blends (LLDPE/PA6/IFR) by
different methods, and the effect of microstructure on the flame retardancy,
mechanical properties, and water resistance was investigated. Melt-blending
compatibilizers with LLDPE/PA6/IFR above the polyamide-6 (PA6) melt
temperature formed the microstructure with IFR dispersion in the LLDPE
matrix and good interphase adhesion between the PA6 phase and the
matrix. Compared with the blends with the lack of compatibilizers,
although good interphase adhesion improved the mechanical properties
and water resistance, IFR dispersion in the LLDPE matrix reduced the
flame retardancy sharply. To obtain the microstructure with IFR dispersion
in the PA6 phase and strong interface adhesion of the PA6 phase with
a matrix, a novel method in which a compatibilizer was melt-blended
with LLDPE/PA6/IFR between the melt temperatures of LLDPE and PA6
was employed. The results showed that the flame retardancy, mechanical
properties, and water resistance were improved simultaneously.
document-id-old-9ao8b00488document-id-new-14ao-2018-00488tccc-price
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1 Introduction
Intumescent flame retardants
are now being used more and more in
polymer flame retardants because they are more environmentally friendly
than traditional halogen-containing flame retardants. The characteristic
of intumescent flame retardants is that the combustion chamber can
form a honeycomb expansion carbon layer, which reduces the mass transfer
and heat transfer between the gas phase and the solidification phase.1−3 Acid source, carbon source, and blowing agent are the three elements
of chemically intumescent flame retardants.4−6 In general,
ammonium polyphosphate (APP as the acid source and blowing agent),
pentaerythritol (PER as the charring agent) and melamine (as the blowing
agent) form a traditional IFR system together.
However, IFR
has poor water resistance and compatibility with many
polymer matrices, resulting in the decrease of flame retardancy and
the damage to the mechanical properties of polymer composites. These
drawbacks will restrict their wide industrial applications. Microencapsulation
of IFR is regarded as an efficient method to get rid of these drawbacks
mentioned above.7−11 The microencapsulated IFR particles have a core–shell structure,
which allows the isolation of encapsulated substances from the surrounding
and thus improves their compatibility with the polymer matrix and
the water resistance. In general, the encapsulating shell, such as
polyurethane (PU), melamine–formaldehyde, melamine, silicon
resin, or urea–melamine–formaldehyde, was prepared by
the in situ polymerization method.12−17
Physics encapsulation technology was also employed to prepare
microencapsulated
IFR particles. Wang18,19 provided a novel method of preparing
microencapsulated IFR by the extrusion of melamine phosphate and PER,
together with a polypropylene (PP) carrier. The results showed that
the IFR encapsulated by the PP carrier improved flame retardancy and
water resistance. Zeng20 used PU as a carrier
resin to encapsulate melamine pyrophosphate/PER through melt blending,
and encapsulated IFR was adopted to flame-retard PP. The results showed
that encapsulated IFR endowed PP with better flame retardancy, water
resistance, and mechanical properties. Compared with the in situ polymerization
method, physics encapsulation technology has the advantages of a simple
process and less environmental problems.
Polymer blending has
gained considerable interest as a suitable
way to tailor the properties of polymeric materials without investing
in new chemistry.21 However, the flame
retardancy of polymer blends is more complex than that of pure polymers
because of the complicated microstructure caused by the dispersion
of IFR and their synergists in the multiphase.22−24 Lu25 reported that APP had a tendency to disperse
in the polyamide-6 (PA6) phase of polystyrene (PS)/PA6 blends. The
blends with cocontinuous phase structures have better flame retardancy
than that of the blends with the sea-island structure. For the blends
of PS/PA6 and acrylonitrile–butadiene–styrene/PA6 with
sea-island morphology, Lu26,27 found that blends with
organic montmorillonite and APP, respectively, distributed in the
phase interface and PA6 phase have better flame retardancy than that
of the blends with clay and APP dispersed in the PA6 phase. Jin28 employed the compatibilizer to adjust the microstructure
for improving the mechanical properties and flame retardancy of PP/ethylene-octene
copolymer/IFR. Along with the increase of compatibilizer content,
the blends exhibited different microstructures. The addition of compatibilizers
in a proper range caused the simultaneous improvement on mechanical
properties and flame retardancy.
IFR for flame-retardant polymer
blends also encounters the challenges
of poor water resistance and damage on mechanical properties. Although
the microstructure of polymer blends contributes to the augment of
the flame retardancy to a great extent, improving IFR water resistance
and decreasing its damage on mechanical properties with resorting
to regulating the microstructure have not been studied systematically.
In this paper, we attempted to regulate the microstructure of polymer
blends for the purpose of overcoming these disadvantages. The microstructure
in which IFR localizes in the dispersed phase can be regarded as the
microencapsulated IFR in which dispersed phase as the shell encapsulates
IFR to improve water resistance. Compatibilizers can be employed to
improve the compatibility. Moreover, char-forming polymers chosen
as dispersed phase to encapsulate IFR particles could endow the blends
with better flame retardancy.
The flammability of linear low-density
polyethylene (LLDPE)/PA6
blends has limited its applications in packaging and automotive fields.
In the LLDPE/PA6
blends, higher affinity of IFR for PA6 than for LLDPE should exhibit
the dispersion of IFR in the PA6 phase. Furthermore, it was reported
that PA6 acted as the charring agent of APP to enhance the charring
performance, resulting in better flame retardancy.29−31 Therefore,
the use of IFR as flame retardants was investigated for their potential
in improving the fire-retardant behavior of LLDPE/PA6. The IFR system
used consists of APP and PER. Meanwhile, maleic anhydride grafted
with LLDPE (LLDPE-g-MAH) was chosen as a compatibilizer
for enhancing the compatibility of LLDPE/PA6 blends. The compatibility
of LLDPE-g-MAH may prohibit the dispersion of IFR
in the PA6 phase, while LLDPE, PA6, and IFR are melt-blended with
LLDPE-g-MAH simultaneously. In order to prepare the
blends with IFR dispersion in the PA6 phase, a two-step processing
method was employed: PA6, LLDPE, and IFR were melted above the melting
temperatures of LLDPE and PA6 to first prepare blends of LLDPE/PA6/IFR,
and then LLDPE-g-MAH was melt-blended with LLDPE/PA6/IFR
between the melt temperatures of LLDPE and PA6. The effects of the
microstructure on the flame retardancy, mechanical properties, and
water resistance were investigated.
2 Results
and Discussion
2.1 Dispersion of APP and PER
in LLDPE/PA6 Blends
and Their Microstructure
In order to investigate the spontaneous
dispersion of APP or PER in the blends of LLDPE/PA6, PA6/LLDPE/APP
or PA6/LLDPE/PER prepared by method one was investigated by Fourier
transform infrared (FTIR) spectra, respectively. Figure 1 shows the FTIR spectra of
the remaining parts of the PA6/LLDPE/IFR or PA6/LLDPE/PER extracted
by formic acid or formic acid and ethyl alcohol, respectively. The
−CH2– asymmetric stretching (2919 cm–1), symmetric stretching (2849.5 cm–1), bending vibrations (1469 cm–1), and the wagging
vibration of C–H (719.4 cm–1) were observed,
indicating that the remaining parts consisted of PE. In these blends,
PA6 formed a continuous phase because of high PA6 content. The absence
of PA6 in the remaining parts indicated that continuous PA6 phase
was completely extracted by formic acid. The absence of APP or PER
in the remaining parts showed that APP or PER was also completely
extracted by formic acid or ethyl alcohol, respectively. If APP or
PER was localized in the LLDPE phase of blends, they could not be
extracted by formic acid or ethyl alcohol, with the result that APP
or PER could be detected in the remaining parts. Therefore, the results
that APP or PER was not detected in the remaining parts indicated
that APP or PER is localized in the PA6 phase. In the blends tested
by FTIR, APP or PER should disperse spontaneously in the polymer with
high affinity, due to which the processing temperature was higher
than the melting temperature of LLDPE and PA6. Therefore, the localization
of APP or PER in the PA6 phase indicated that the affinity of APP
or PER is higher for PA6 than for LLDPE because of similar polarity
between PA6 and IFR.
Figure 1 FTIR spectra of the (a) remaining part of LLDPE/PA6/APP
extracted
by formic acid and (b) remaining part of LLDPE/PA6/PER extracted by
formic acid and ethyl alcohol.
Scanning electron microscopy–energy-dispersive spectroscopy
(SEM–EDS) was employed to characterize the dispersion of IFR
in the blends and the microstructure of the blends, as shown in Figure 2. SEM results showed
that APP and PER were irregular particles. The spherical particles
with a large dimension were observed in the matrix of C-0. The results
of FTIR showed that IFR is spontaneously distributed in the PA6 phase.
Therefore, IFR particles were coated by the PA6 phase to form the
spherical particles. The EDS results showed that the P content was
1.83 wt %. Generally, the detected depth for the EDS measurement is
about 1000 nm, so small amounts of elemental P dispersed in the PA6
phase were detected. Some cavities were seen on the surface of C-0,
and there were clear interfaces between PA6 particles and LLDPE, indicating
poor compatibility between PA6 and LLDPE, which is due to the different
polarity between PA6 and LLDPE, exhibiting a weak interfacial adhesion.
The results showed that C-0 formed sea-island morphology in which
IFR localized in the dispersed PA6 phase and PA6 phase and the LLDPE
matrix exhibited poor interface adhesion.
Figure 2 SEM–EDS of IFR
and blends prepared by different methods.
For blends of C2-M1 and C8-M1, irregular cavities with lengths
of about some 10 μm and spherical particles with a dimension
of about 3–5 μm were observed. The exfoliation of IFR
particles from the LLDPE matrix formed larger irregular cavities,
while the PA6 phase formed the small spherical particles in the LLDPE
matrix. The results indicated that PA6 and IFR particles were both
dispersed in the LLDPE matrix. The EDS results of C2-M1 and C8-M1
also indicated that IFR was dispersed in the LLDPE matrix rather than
in the PA6 phase, due to which the percentages of elemental P and
O in C2-M1 and C8-M1, respectively, were higher than that of C-0.
The cavities formed by the exfoliation of IFR from the LLDPE matrix
and clear interfaces between IFR particles and the LLDPE matrix indicated
poor interfacial adhesion. Meanwhile, strong interfacial adhesion
between PA6 particles and the LLDPE matrix was observed because of
vague interface. The results indicated that the compatibilizer improved
the interfacial adhesion between the PA6 phase and the LLDPE matrix.
The different polarity between IFR and LLDPE caused a weak interfacial
adhesion. The SEM–EDS results showed that LLDPE/PA6/IFR/LLDPE-g-MAH blends prepared by method one formed the sea-island
morphology such that both IFR and PA6 localized in the LLDPE matrix
and LLDPE-g-MAH improved the interfacial adhesion
of the PA6 phase and the LLDPE matrix.
Interfacial tensions
between the filler and each polymer determine
the filler distribution in the filler-filled polymer blends.32,33 In the uncompatibilized blends, IFR dispersion in the PA6 phase
rather than in the LLDPE phase indicated that the interfacial tension
between IFR and PA6 was lower than that of IFR and LLDPE. When LLDPE-g-MAH was melt-blended with LLDPE/PA6/IFR, LLDPE-g-MAH was reacted with PA6 to form a copolymer. The copolymer
should migrate to the interface of PA6 and LLDPE to reduce the interfacial
tension and phase size, indicating that the interfacial tension between
LLDPE and PA6 was lower than that of IFR and PA6. As a result, IFR
particles were found to localize in the LLDPE matrix rather than in
the PA6 phase.
The blends of C2-M2 and C8-M2 were prepared via
a two-step process.
At the first step, IFR should disperse in the PA6 phase because of
similar polarity between PA6 and IFR. When LLDPE-g-MAH was melt-blended with LLDPE/PA6/IFR at the second step, LLDPE-g-MAH should not change the dispersion of IFR, due to which
the PA6 phase remained solid, exhibiting IFR dispersion in the PA6
phase. The typical empty holes and the exfoliation phenomenon that
appeared in C-0, C2-M1, and C8-M1 almost vanished, which suggested
good interfacial adhesion. The results indicated that LLDPE-g-MAH improved the compatibility between PA6 and LLDPE.
The PA6 phase remained solid when LLDPE-g-MAH was
melt-blended with LLDPE/PA6/IFR. Therefore, the improvement of interfacial
adhesion and compatibility between PA6 particles and LLDPE should
be attributed to the reaction between the maleic anhydride group in
the LLDPE-g-MAH melt and the amidogen on the surface
of solid PA6 particles. The EDS results showed that the percentages
of elemental P and O in C2-M2 and C8-M2, respectively, were lower
than that of C-0, indicating that LLDPE-g-MAH encapsulated
the PA6 phase, demonstrating that IFR dispersed in the PA6 phase was
hard to be detected by EDS. As the content of LLDPE-g-MAH increased from 2 to 8 wt %, the coating thickness of LLDPE-g-MAH on the surface was also increased, causing the percentages
of P and O to decrease from 14.88 and 1.03 to 14.12 and 0.6%, respectively.
Therefore, the sea-island morphology in which IFR localized in the
dispersed PA6 phase and LLDPE-g-MAH improved the
compatibility of the PA6 phase and the LLDPE matrix was formed in
LLDPE/PA6/IFR/LLDPE-g-MAH blends prepared by method
2.
In order to confirm the reaction between LLDPE-g-MAH and PA6 in the blends prepared by method 2, the blends of LLDPE/PA6
(85/15) or LLDPE/PA6/LLDPE-g-MAH (80/15/5) were extracted
by dimethylbenzene to remove LLDPE and LLDPE-g-MAH
and the remaining parts were tested by FTIR, as shown in Figure 3. The blend of LLDPE/PA6
was melt-blended above the melting temperature of LLDPE and PA6. LLDPE/PA6/LLDPE-g-MAH blend was prepared by method 2. The typical infrared
spectra of PA6 were shown, and no characteristic peaks of LLDPE were
found in the remaining part of LLDPE/PA6, indicating that whole LLDPE
was dissolved by dimethylbenzene and the remaining part consisted
of PA6. For the remaining part of LLDPE/PA6/LLDPE-g-MAH prepared by method 2, the peaks at 2934 and 2968 cm–1 shown in LLDPE/PA6 were replaced by 2918 and 2850 cm–1, respectively. The peaks at 2934, 2968 cm–1 in
the remaining part of LLDPE/PA6 were the −CH2–
asymmetric stretching and symmetric stretching of PA6, respectively.
From Figure 1, it was
observed that the peaks at 2918 and 2850 cm–1 were
the −CH2– asymmetric stretching and symmetric
stretching of LLDPE. The results indicated that the remaining part
of LLDPE/PA6/LLDPE-g-MAH contained LLDPE or LLDPE-g-MAH. LLDPE or unreacted LLDPE-g-MAH can
be extracted by dimethylbenzene, but LLDPE-g-MAH
reacted with PA6 should not dissolve in dimethylbenzene. Therefore,
it can be concluded that the maleic anhydride group in the LLDPE-g-MAH melt can react with the amidogen on the surface of
solid PA6 particles in the blends prepared by method 2.
Figure 3 FTIR spectra
of the remaining part of LLDPE/PA6 (a) or LLDPE/PA6/LLDPE-g-MAH (b) extracted by dimethylbenzene.
2.2 Flame Retardancy
The flame retardancy
of LLDPE/PA6/IFR and LLDPE/PA6/IFR/LLDPE-g-MAH prepared
by different methods was investigated by limiting oxygen index (LOI)
and UL-94 test, as shown in Table 1. For C-0, the LOI value was 29.7, and the samples
achieved a V-2 rating in UL94 testing because of the melt dripping
during combustion. Processing methods showed a remarkable influence
on the flame retardancy. Blends of LLDPE/PA6/IFR/LLDPE-g-MAH prepared by method 1 exhibited poor flame retardancy, and the
LLDPE-g-MAH content showed weak influence on the
flame retardancy. The LOI values were only 24–24.7% and had
no vertical rating in the UL-94 test. However, the flame retardancy
of the blends prepared by method 2 was significantly improved, compared
with the blends prepared by method 1. LOI values of C2-M2 and C5-M2
were both 28.6 and the samples passed the UL-94 V-2 rating, indicating
that their flame retardancy was close to C-0. The best flame retardancy
was exhibited in C8-M2. The LOI value reached 30.0%. The samples passed
the UL-94 V-0 rating, indicating that the dripping properties exhibited
in C-0, C2-M2, and C5-M2 were restrained in C8-M2.
Table 1 Flammability Characteristics of Blends
sample code LOI (%) UL-94 rating
C-0 29.7 V-2
C2-M1 24.0 no rating
C5-M1 24.0 no rating
C8-M1 24.7 no rating
C2-M2 28.6 V-2
C5-M2 28.6 V-2
C8-M2 30.0 V-0
The results showed that blends with IFR dispersion in the PA6 phase
(C-0, C2-M2, C5-M2, and C8-M2) exhibited better flame retardancy than
the blends with IFR dispersion in the LLDPE phase (C2-M1, C5-M1, and
C8-M1). It was reported that PA6 can act as the charring agent of
APP to enhance the charring performance and flame retardancy.29−31 Therefore, IFR dispersion in the PA6 phase was more beneficial for
the reaction between APP and PA6, exhibiting better flame retardancy,
compared with the blends with IFR dispersion in the LLDPE phase. C8-M2
samples had no melt dripping during combustion. The reason for this
may be the case that LLDPE-g-MAH increases the viscosity
of blends and enhances the antidripping property.
Melt flow
index (MFI) can relate to viscosity indirectly, which
indicates the dripping properties of flame-retardant LLDPE/PA6 blends.
MFI experiments were used to test the flow rate of flame-retardant
LLDPE/PA6 blends at different LLDPE-g-MAH contents,
as shown in Table 2. The highest MFI value observed in C-0 indicated the lowest melt
viscosity. Obviously, the melt dripping of C-0 should be attributed
to the low melt viscosity. MFI values of the LLDPE/PA6/IFR/LLDPE-g-MAH blends prepared by method 1 were lower than that of
C-0. Moreover, the increase of LLDPE-g-MAH contents
caused a sharp reduction of MFI values. The results indicated that
LLDPE-g-MAH increased the melt viscosity. The copolymer
formed by the reaction of LLDPE-g-MAH and PA6 can
entangle with PA6 and LLDPE molecular chains at the interface to increase
the flow resistance of melt, resulting in high melt viscosity. The
increase of LLDPE-g-MAH contents in the blends produced
more copolymers, resulting in higher melt viscosity. For the LLDPE/PA6/IFR/LLDPE-g-MAH blends prepared by method 2, the MFI values were also
lower than that of C-0 and the increase of LLDPE-g-MAH contents caused the reduction of MFI values. The MFI value of
C8-M2 was about one-third of C-0, indicating a sharp increase of melt
viscosity, resulting in the enhancement of antidripping property.
The increase of melt viscosity can also be attributed to the copolymer
formed by the reaction of LLDPE-g-MAH and PA6.
Table 2 Effect of LLDPE-g-MAH Contents on
the MFI of the Blends Prepared by Different Methods
sample code C-0 C2-M1 C5-M1 C8-M1 C2-M2 C5-M2 C8-M2
MFI (g/10 min) 105 71 52 25 67 43 34
2.3 Cone Calorimeter Analysis
The cone
calorimeter was also employed to evaluate the flame retardancy. Samples
of C-0, C8-M1, and C8-M2 were chosen for testing by cone calorimetry.
The heat release rate (HRR), total heat released (THR), and mass loss
curves recorded during cone calorimeter tests are presented in Figure 4. The related data
are presented in Table 3.
Figure 4 Relationship between (a) HRR, (b) THR, and (c) mass loss and time
of blends prepared by different methods.
Table 3 Cone Calorimeter Test Data of Blends
sample code PHHR (kW/m2) THR (kJ/m2) char
residues (wt %) MAHRE (kW/m2 s) FPI (m2 s/kW) FGI (kW/m2 s)
C-0 223 99 32 153 0.35 0.44
C8-M1 296 113 25 209 0.23 1.04
C8-M2 246 88 29 139 0.31 0.56
The peak HRR (PHRR) value of C8-M1 was higher than
that of C-0
and C8-M2, indicating that the flame retardancy of C8-M1 was poorer
than that of C-0 and C8-M2. The results showed that IFR dispersion
in the PA6 phase enhanced flame retardancy in comparison with IFR
dispersion in the LLDPE phase.
The HRR curves of C-0 and C8-M2
displayed two peaks: the first
peak was assigned to the formation of expandable char layers and the
second peak was assigned to the further decomposition of a carbonaceous
residue.34 The first PHHR and the HRR values
for the initial 250 s of C8-M2 were lower than that of C-0, indicating
that the char layer of C8-M2 formed in the initial period can provide
better protection against the combustion of the matrix than that of
C-0. Combustion experiments performed in the UL94 or LOI test were
similar to the scenario of cone calorimetry at the ignition stage.35−37 Therefore, the results that the LOI and the vertical combustion
level of C8-M2 were better than that of C-0 can be due to reduced
combustion intensity in the initial period. The second PHHR value
of C8-M2 was higher than that of C-0, indicating that the stability
of the carbonaceous residue in C8-M2 was poorer than that of C-0.
The THR of C-0 and C8-M2 was lower than that of C8-M1, and the
mass loss curve showed that the char residue of C-0 and C8-M2 was
higher than that of C-0, indicating that the dispersion of IFR in
the PA6 phase was more favorable to the formation of a carbonaceous
residue, resulting in the decrease of THR.
Fire performance
index (FPI) is defined as the proportion of TTI
and PHRR; fire growth index (FGI) is defined as the proportion of
PHRR and time to PHRR; MARHE is the maximum of the average rate of
heat emission. The values of MARHE, FPI, and FGI can evaluate the
fire hazard. It can be seen from Table 1 that the highest MAHRE and FGI values or the lowest
FPI was observed in C8-M1, suggesting that C8-M1 possessed the strongest
fire hazard in comparison with C-0 and C8-M2.
2.4 Characterizations
of Residue Char
Figure 5 shows the
residue of the blends at the end of the cone calorimeter test. Broken
char residue was observed in C8-M1. C-0 and C8-M2 formed a coherent
and dense char residue with high intumescentia. The formation of highly
intumescent, coherent, and dense char layer could provide a better
protective shield; thus, the heat and mass transfer between the gas
and condensed phase could be slowed, and the underlying materials
are protected from further burning. For this reason, C-0 and C8-M2
exhibited much lower PHRR values than C8-M1.
Figure 5 Photos of the aspect
of the crust of blends after the cone calorimeter
test.
Char residues of LLDPE/PA6/IFR
and LLDPE/PA6/IFR/LLDPE-g-MAH prepared by different
methods were examined by SEM,
as shown in Figure 6. The char residue of C2-M1 and C8-M1 was completely a loose structure;
many voids can be observed. A continuous and compact char residue
was formed in C-0, C2-M2, and C8-M2. Compared with the loose structure
displayed in C2-M1 and C8-M1, a continuous and compact char residue
can accumulate flammable gas and improve the blocking ability of heat
and gas, resulting in the improvement of flame retardancy.
Figure 6 SEM of intumescent
char residues for blends prepared by different
methods.
The different morphologies of
char residues should be attributed
to the different dispersion of IFR in polymer blends. Compared with
IFR dispersion in the LLDPE phase, IFR dispersion in the PA6 phase
was beneficial for the reaction between APP and PA6, forming a high
char residue, resulting in the formation of a continuous and compact
char residue. However, IFR dispersion in the LLDPE phase was against
the charring performance, forming loose char residues.
2.5 Water Resistance of Flame-Retardant LLDPE/PA6
Table 5 shows the
mass loss percentages, LOI, and the UL-94 test results of flame-retardant
LLDPE/PA6 after water immersion. The highest mass loss percentage
was exhibited in C-0. Mass loss percentages of LLDPE/PA6/LLDPE-g-MAH/IFR blends prepared by method 1 were higher than that
of blends prepared by method 2. The results indicated that LLDPE/PA6/LLDPE-g-MAH/IFR prepared by method 2 exhibited the best water
resistance.
The LOI and UL-94 test results were in accordance
with the mass loss results. After water immersion, the LOI value of
C-0 reduced from 29.7 to 24%, and the samples failed to pass the UL-94
test, indicating remarkable reduction in flame retardancy because
of poor water resistance. Blends of C2-M1, C5-M1, and C8-M1 had poor
flame retardancy before water immersion. Therefore, little change
in flame retardancy was observed after water immersion. Good water
resistance was exhibited in C2-M2, C5-M2, and C8-M2. After water immersion,
the LOI values were reduced slightly, and UL-94 rating grades were
unchanged.
The different water resistance exhibited in Table 4 should be attributed
to different microstructures
of the blends. The sample of C-0 had the microstructure in which IFR
dispersed in the dispersed PA6 phase and the interfacial adhesion
between the PA6 phase and the LLDPE matrix was poor. Poor interfacial
adhesion contained a number of microgaps, through which the water
entered to dissolve IFR, resulting in poor water resistance. Blends
of LLDPE/PA6/LLDPE-g-MAH/IFR prepared by method 1
possessed the microstructure in which IFR and PA6 phase both dispersed
in the LLDPE matrix and the interfacial adhesion between the PA6 phase
and the LLDPE matrix or IFR particles and the LLDPE matrix was strong
or poor, respectively. Although the compatibilization of LLDPE-g-MAH on LLDPE/PA6 decreased the microgaps, the dispersion
of IFR in the LLDPE matrix and the poor interfacial adhesion between
IFR particles and the LLDPE matrix were both against the improvement
of water resistance. In blends of LLDPE/PA6/LLDPE-g-MAH/IFR prepared by method 2, the microstructure in which IFR dispersed
in the dispersed PA6 phase and LLDPE-g-MAH improved
the interfacial adhesion between the PA6 phase and the LLDPE matrix
was formed. Good interfacial adhesion reduced the microgaps, indicating
that the water was hard to diffuse into the matrix. The PA6 phase
can protect the IFR component from attack by water. Accordingly, good
water resistance was observed in these blends.
Table 4 Mass Loss, UL-94, and LOI
Results of Blends after Water Treatment
at 70 °C for 168 h
sample code mass loss
percentage (%) LOI (%) UL-94 rating
C-0 3.2 ± 0.1 24 failed
C2-M1 1.7 ± 0.2 24 failed
C5-M1 1.9 ± 0.1 24.7 failed
C8-M1 1.6 ± 0.1 24 failed
C2-M2 0.9 ± 0.1 26.3 V-2
C5-M2 0.9 ± 0.1 27.1 V-2
C8-M2 0.7 ± 0.1 28.6 V-0
2.6 Mechanical Properties
The mechanical
properties of flame-retardant LLDPE/PA6 are compiled in Table 5. The tensile strength, elongation at break, and impact strength
of C-0 were 7.1 MPa, 9.4%, and 3.0 kJ/m2, respectively.
Poor compatibility between PA6 and LLDPE should be responsible for
the deteriorated mechanical properties. For the blends prepared by
method 1, compatibilizer LLDPE-g-MAH improved the
tensile strength and elongation at break. Introduction of LLDPE-g-MAH to C-0 through method 1 also improved the impact strength
except for C2-M1. The mechanical properties of the blends prepared
by method 2 were higher than that of C-0 and the blends prepared by
method 1. This phenomenon should be attributed to different morphologies.
For the blends prepared by method 1, PA6 phase and IFR were both dispersed
in continuous LLDPE phase. The compatibilizer elevated the interphase
adhesion of PA6 and LLDPE phases and decreased PA6 phase size. Therefore,
the tensile strength and elongation at break were increased from 7.1
MPa and 9.4% for C-0 to 9.0 MPa and 23.4% for C5-M1, respectively.
For the blends prepared by method 2, IFR was dispersed in the PA6
phase and the compatibilizer elevated the interphase adhesion between
the PA6 phase and the matrix. Therefore, the tensile strength, elongation
at break, and impact strength were increased about 60, 300, and 50%
in comparison with C-0, respectively.
Table 5 Mechanical
Properties of the Blends
Prepared by Different Methods
sample code tensile stress
(MPa) elongation
at break (%) impact strength (kJ/m2)
C-0 7.1 ± 0.9 9.6 ± 3.5 3.0 ± 0.08
C2-M1 8.3 ± 1.2 27.3 ± 8.3 2.0 ± 0.01
C5-M1 9.0 ± 1.5 23.4 ± 9.3 3.3 ± 0.98
C8-M1 9.0 ± 0.9 23.3 ± 10.2 3.5 ± 0.78
C2-M2 11.9 ± 0.5 28.9 ± 4.9 3.7 ± 0.06
C5-M2 11.7 ± 0.6 24.2 ± 8.2 4.3 ± 0.08
C8-M2 11.9 ± 0.6 29.4 ± 7.1 4.4 ± 0.02
It was observed that the compatibilizer contents exhibited a weak
effect on the mechanical properties of LLDPE/PA6/LLDPE-g-MAH/IFR prepared by different methods, due to which the increase
of compatibilizer contents caused little change of the mechanical
properties. For the blends prepared by method 1, although the increase
of LLDPE-g-MAH content reduced the PA6 phase size
and contributed to the augment of the mechanical properties to a certain
extent, the poor interphase adhesion between IFR and the LLDPE matrix
showed a greatly negative impact on mechanical properties, indicating
that the mechanical properties were not influenced remarkably along
with the increase of LLDPE-g-MAH content. In the
blends prepared by method 2, the PA6 phase remained solid when LLDPE-g-MAH was melt-blended with LLDPE/PA6/IFR. Therefore, LLDPE-g-MAH cannot reduce the PA6 phase size. The increase of
LLDPE-g-MAH content increased the coating thickness
of LLDPE-g-MAH on the PA6 particles surface rather
than increasing the interfacial strength. Therefore, the poor effect
of the compatibilizer contents on mechanical properties was exhibited.
3 Conclusions
Different processing methods
were employed to prepare LLDPE/PA6/IFR
blends with different microstructures, and the results showed that
the microstructure affected the flame retardancy, mechanical properties,
and water resistance greatly. Melt-blending IFR with LLDPE/PA6 simultaneously
formed the microstructure in which IFR was selectively dispersed in
the PA6 phase of LLDPE/PA6/IFR and the interphase adhesion between
PA6 and the LLDPE matrix was poor. Although IFR dispersion in the
PA6 phase was beneficial for the increase of flame retardancy, poor
interphase adhesion deteriorated the mechanical properties and water
resistance. When the compatibilizer LLDPE-g-MAH was
melt-blended with LLDPE/PA6/IFR simultaneously, a microstructure was
formed, indicating that IFR and PA6 particles were respectively dispersed
in the LLDPE matrix and that LLDPE-g-MAH strengthened
the interphase adhesion between the PA6 phase and the LLDPE matrix
rather than IFR particles and the LLDPE matrix. The improvement of
the interphase adhesion increased the mechanical properties and water
resistance, but IFR dispersion in the LLDPE matrix decreased the flame
retardancy sharply. A novel processing method that the IFR was first
melt-blended with LLDPE/PA6 and then LLDPE-g-MAH
was melt-blended with LLDPE/PA6/IFR between the melt temperatures
of LLDPE and PA6 was employed to obtain the microstructure with the
dispersion of IFR in the PA6 phase and strong interface adhesion of
the PA6 phase with the matrix. The flame retardancy, mechanical properties,
and water resistance were improved simultaneously. IFR dispersion
in the PA6 phase and high viscosity caused by the compatibilization
of LLDPE-g-MAH should be responsible for the improvement
of flame retardancy. Strong interface adhesion of the PA6 phase with
the matrix and IFR dispersion in the PA6 phase caused good water resistance.
Moreover, good mechanical properties were attributed to the strong
interface adhesion between the PA6 phase and the LLDPE matrix.
4 Experimental Section
4.1 Materials
The
materials used in this
study were LLDPE (LL6201XR, MI = 50 g/10 min, d =
0.926 g/cm3) supplied by ExxonMobil Corp. and PA6 (33500,
relative viscosity of 3.50, d = 1.14 g/cm3) supplied by Xinhui Meida-DSM Nylon Chips Co., Ltd. The IFR system
consists of APP and PER, and the weight ratio of APP to PER is 4:1.
APP [(NH4PO3)n,
purity level > 90%] was supplied by Zhejiang Longyou Gede Chemical
Factory (China). PER was supplied by Jinan Taixing Fine Chemicals
Co., Ltd. LLDPE-g-MAH (TRD200L, MI = 2 g/10 min, d = 0.92 g/cm3) was supplied by Wujiang Siruda
Plastic Industry Co., Ltd. The amount of maleic anhydride in LLDPE-g-MAH was 1 wt %.
4.2 Preparation of Composites
All the
materials were oven-dried for 12 h at 85 °C before extrusion
and injection. The blends were extruded via a corotating twin-screw
extruder with a barrel diameter of 20 mm and a barrel-length-to-diameter
ratio of 25. Then the extruded blends were molded into sheets of suitable
thickness at the injection pressure of 50 MPa via an injection molding
machine. The formula of the blend is listed in Table 6.
Table 6 Formulation of Blends
sample code LLDPE PA6 IFR LLDPE-g-MAH processing
method
C-0 64 16 20 0 method 1
C2-M1 62 16 20 2 method 1
C5-M1 59 16 20 5 method 1
C8-M1 56 16 20 8 method 1
C2-M2 62 16 20 2 method 2
C5-M2 59 16 20 5 method 2
C8-M2 56 16 20 8 method 2
Two processing
methods were employed for preparing the blends.
Method 1: all
the materials were melt-blended above the melt temperature
of LLDPE and PA6 for preparing the blends. The temperatures from hopper
to die were 140, 160, 190, 220, and 240 °C.
Method 2: two
steps were employed to prepare the blends. In the
first step, PA6 and LLDPE were melt-blended with IFR to prepare LLDPE/PA6/IFR,
and the processing temperature was higher than the melt temperature
of LLDPE and PA6. The temperatures from hopper to die were 140, 160,
190, 220, and 240 °C. In the second step, LLDPE/PA6/IFR was melted
with LLDPE-g-MAH, and the processing temperature
was between the melt temperatures of LLDPE and PA6. The temperatures
from hopper to die were 140, 150, 160, 160, and 160 °C.
4.3 Measurement and Characterization
LOI was measured according
to ASTM D2863-77. The apparatus used was
a JF-3 instrument (Chengde, China). The specimens used for the test
were of dimensions 120 × 6 × 3 mm3. The vertical
test was carried out according to the UL94 test standard. The specimens
used for the test were of dimensions 127 × 12.7 × 3 mm3.
The sample flammability performed on the cone calorimeter
(FTT, UK) test according to ISO 5660 standard procedures. The specimens
used for the test were of dimensions 100 × 100 × 3 mm3. The specimen was exposed horizontally at an incident flux
of 35 kW/m2.
FTIR spectra were recorded on a Bruker
Vector 33 spectrometer.
LLDPE/PA6/APP (24/56/20) or LLDPE/PA6/PER (27/63/10) in which LLDPE
was used as the matrix and PA6 formed dispersed phase was pressed
into disks with KBr. Before being pressed, the samples of LLDPE/PA6/APP
were extracted by formic acid for 48 h. The samples of LLDPE/PA6/PER
were extracted first by formic acid and later by alcohol. The sample
of LLDPE/PA6 (85/15) or LLDPE/PA6/LLDPE-g-MAH (80/15/5)
was extracted by dimethylbenzene at 120 °C to remove LLDPE and
LLDPE-g-MAH, and the residuum was pressed into disks
with KBr for the FTIR test.
A JEOL 6301F scanning electron microscope
was used to investigate
the morphology of residue char and molded specimens at an acceleration
voltage of 20 kV. The residue char was obtained from the specimen
left after the vertical test. The molded specimens were fractured
in liquid nitrogen.
To determine the water resistance of polymer
blends, specimens,
of the same size as used for the UL-94 test, were put in distilled
water at 70 °C and kept at this temperature for 168 h. The water
was replaced every 24 h, according to UL746C. The treated specimens
were subsequently dried in a vacuum oven at 80 °C for 72 h, and
the weight of the specimens was measured before water immersion and
after drying. The mass loss percentages were calculated in the following
equation18 where W0 is the
initial weight of the specimens before water immersion and W is the remaining weight of the specimens after water immersion
and drying.
The tensile strength was measured by a tensile tester
(LJ1000,
Guangzhou Test Instrument Factory, China) according to ASTM D638.
The MFI of melting polymer blends was measured by a melt index
instrument, and the measurement temperature was 225 °C; load
was 2.16 kg.
The authors
declare no competing financial interest.
Acknowledgments
The authors
gratefully acknowledge the financial
support of this work by the National Natural Science Foundation of
China (contract number: 51673059), Natural Science Foundation of Education
Department of Henan Province (contract number: 17A150009), and Student
Research Training Program of HAUST.
==== Refs
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