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Article

Optimization of Degradation Kinetics towards O-CP in H3PW12O40/TiO2 Photoelectrocatalytic System

School of Environment, Northeast Normal University, Changchun 130117, China
*
Authors to whom correspondence should be addressed.
These authors contributed equally.
Sustainability 2019, 11(13), 3551; https://doi.org/10.3390/su11133551
Submission received: 18 April 2019 / Revised: 13 June 2019 / Accepted: 22 June 2019 / Published: 28 June 2019
(This article belongs to the Section Sustainable Chemical Engineering and Technology)

Abstract

:
Kinetics is crucial for photoelectrocatalytic degradation of organic contaminants. A 12-tungstophosphoric acid/titania (H3PW12O40/TiO2) composite film was prepared by the sol-gel-hydrothermal route to investigate the optimal conditions and degradation kinetics of o-chlorophenol (o-CP). The photoelectrocatalytic degradation efficiency of o-CP was 96.6% after 180 min under optimum conditions (impressed voltage: 0.5 V, solution pH: 6.3, and initial concentration: 5 mg·L−1), and the apparent kinetics constant (K’) was a 6.0-fold increase compared to the photocatalytic system. Furthermore, the photoeletrocatalytic reaction rate of o-CP by H3PW12O40/TiO2 and TiO2 film was 0.090 and 0.020 mg·L−1·min−1, respectively, and a higher apparent quantum yield (Φ = 32.14%) of H3PW12O40/TiO2 composite film was attained compared to TiO2 film (Φ = 10.00%), owing to the fact that more photo-generated carriers were produced and effectively separated. Intermediate products identified during o-CP degradation by liquid chromatography-mass spectrometer (LC-MS) were 2-Chlorohydroquinone (CHQ), catechol (CT), and hydroxyl-hydroquinone (H-HQ). The H3PW12O40/TiO2 photoelectrocatalytic system exhibited outstanding potential for the removal of chlorinated organic contaminants in wastewater.

1. Introduction

As the most promising and widespread semiconducting material in photocatalysis and photoelectrocatalysis [1,2,3], TiO2 is a remarkably stable photoactive material, which can be incorporated and immobilized in a photocatalytic system [4,5,6,7]. Consequently, an electrical potential can be directly applied to a conductive support, leading to a synergistic effect between the photocatalytic and electrocatalytic process. However, the photoexcitation and quantum efficiency is limited due to the wide band gap (3.2 eV for anatase) [8]. Due to their unoccupied W 5d orbit, polyoxometallates (POMs) can trap the photoelectron on the surface of TiO2, which effectively restrains the recombination of the electrons and holes [9,10]. Moreover, high light harvesting efficiency can be attained through the hybridization of Ti 3d and W 5d orbits [11,12]. POMs–TiO2 composite catalyst showed excellent photocatalytic activity towards various organic contaminants, including dyes and endocrine disrupters [13,14,15,16]. However, its photoeletrocatalytic activity was not exploited.
Kinetics is crucial for the degradation of organic contaminants in the reaction system [17,18]. Degradation kinetics can reveal the maximum catalytic capability of a heterogeneous reaction system, identify the limiting steps, and optimize the degradation rate of organic compounds [19,20]. Furthermore, the photo-generated electrons and holes of semiconductors can facilitate the degradation reactions based on the formation of radicals [21,22,23] in addition to the factors of impressed voltage, pH, and initial concentration of the targeted organic compound. The study of the separation of photo-generated electrons and holes is attracting increasing attention, with investigations of quantum efficiency, carrier density, and so on [24,25,26,27,28], that may further reveal in-depth information on photocatalytic and photoelectrocatalytic reaction mechanisms.
Thus, in the current study, o-CP, listed as a priority pollutant by the United States Environmental Protection Agency (US EPA), was selected to reveal the kinetics of photoelectrocatalytic degradation in the POMs-TiO2 system. In addition, the intermediate products were determined and the degradation path was studied. This study could provide essential information on the photoeletrocatalytic degradation of chloro-organic contaminants in wastewater.

2. Material and Methods

2.1. Catalyst Preparation

As a typical POMs, H3PW12O40 was employed to prepare the H3PW12O40/TiO2 composite film by the easily-operated sol-gel-hydrothermal route. First, 2 mL titanium tetraisopropoxide (TTIP) was dissolved in 6 mL isopropanol and 0.03 mmol H3PW12O40 was dissolved with 1.6 mL isopropanol under ultrasonic for 10 min. The resulting H3PW12O40 solution was then dropped into the TTIP solution. An adequate acetic acid solution was added to slow down the hydrolysis rate of TTIP, and 2 mol·L−1 HCl was used to adjust the solution to pH 2–3. Stirring was continued until a white transparent sol was obtained. The sol was heated to 200 °C at a rate of 2 °C·min−1 in a Teflon-lined autoclave (Jinan Henghua Technology Co., LT, China, 316-type steel material 8mm lined with Teflon 8 mm). The resulting hydrogel was spin-coated on conductive glass (50 mm × 15 mm × 1 mm) and aged 7 days. The composite film obtained was denoted as H3PW12O40/TiO2 and pure TiO2 film was prepared by using the current method in the absence of H3PW12O40 for comparison.

2.2. Photoelectrocatalytic Degradation

A PLS-SXE300 Xe lamp (300 W, Beijing Trusttech Co. Ltd., Beijing, China) with an IR-cut filter to remove most of IR irradiation (780–1100 nm), produced light that matched well with natural solar light, with the wavelength ranging from 320 to 780 nm and light intensity of 200 mW/cm2, as measured by a PD300-1Wradiometer (OPHIR, Newport, RI, USA). An CHI700E electrochemical workstation (Shanghai Chenhua Instrument Co. LTD, China) was used to provide an electric field in the reaction system and H3PW12O40/TiO2, Pt wire, and Ag/AgCl were employed as working electrode, counter electrode, and reference electrode, respectively. Photoluminescence spectra were recorded with a HR800 instrument (Jobin-Yvon, Paris, France) in macroscopic configuration with a 325 nm line of He-Cd laser. The immobilized composite film (ca. 4.5 mg) was immersed in a self-designed quartz reactor with o-CP aqueous solution (100 mL). The photoelectrocatalytic reaction system (Figure 1) consisted of light source, electrochemical workstation, quartz reactor, and o-CP aqueous solution.
The adsorption–desorption equilibrium experiment was carried out prior to irradiation and power-up and the o-CP solution was stirred in the dark for 30 min to ensure the o-CP molecules contacted adequately with the catalyst. During the photoelectrocatalysis reaction, fixed amounts of o-CP solution was taken out at given intervals of reaction time, and analyzed by high performance liquid chromatograph (HPLC) equipped with a Waters 2489 UV/visible detector (Shanghai Dexiang Technology Co., LTD, China) and symmetry C18 (4.6 × 250 mm, particle size 5 μm), using a mobile phase of acetonitrile (40%) and H2O (60%, containing 0.1% acetic acid) at a flow rate of 0.7 mL·min−1 and wavelength of 254 nm.

3. Results and Discussion

3.1. Optimization of Photoelectrocatalytic Degradation Kinetics

The influence of impressed voltage (U = 0.3 V, 0.5 V, 0.8 V, and 1.0 V) on the photoelectrocatalytic degradation towards o-CP in the H3PW12O40/TiO2 system is shown in Figure 2a. After 180 min, the degradation efficiency reached 96.6% under 0.5 V which was comparably higher than that under 0.3 V (89.4%), 0.8 V (94.3%), and 1.0 V (87.3%). This was mainly attributed to the maximum amounts of photo-generated electrons in the case of the fixed light intensity (200 mW/cm2) and catalyst amount (ca. 4.5 mg) [29], and the degradation efficiency increased as voltage increased. However, the excess voltage may have caused the reallocation of the space charge layer and the Hector–Helmholtz layer, which would reduce the number of photogenerated carriers [30].
As illustrated in Figure 2b, the degradation efficiency achieved the maximum value (96.6%) at pH = 6.3 (its natural condition), due to the highest adsorption capacity of o-CP (11.2%) onto the composite film. Additionally, the photocatalytic activity of TiO2 also peaked at 6.2 (pHpzc) [31]. The degradation efficiency decreased in both alkaline conditions (79.70% at pH = 8.1 and 73.80% at pH = 10.0) and acid condition (78.3% at pH = 4.2).
The degradation efficiency was 86.3%, 96.6%, 77.3%, 69.4%, and 64.0% with initial concentrations of 2.5 mg·L−1, 5.0 mg·L−1, 10.0 mg·L−1, 15.0 mg·L−1, and 20.0 mg·L−1, respectively (Figure 2c). With a fixed catalyst amount, the highest efficiency was achieved when initial o-CP concentration was 5 mg·L−1, due to the ratio of catalytic active sites to substrate molecules [32].

3.2. The Photoelectrocatalytic Degradation Kinetics

Photoelectrocatalytic degradation kinetics is well described by the Langmuir–Hinshelwood (L-H)-type kinetic model (Equation (1)) assuming the rate is controlled by Langmuir-type adsorption [33].
r = −dCt/dt = krKaCt/(1 + KaCt)
where r is reaction rate, Ct is the process concentration of the target compound, t is the reaction time, kr is rate constant, and Ka is the apparent adsorption equilibrium constant.
When the concentration is very low, and KaCt is much lower than 1, the above equation can be simplified as:
rkrKaCt i.e., −dCt/dt = krKaCt
Thus,
ln(C0/Ct) = krKaCt = Kt
where K’ is the apparent reaction constant and C0 is the initial concentration.
The kinetics under different conditions are described and summarized in Figure 3 and Table 1. K’ and r reached 0.018 min−1 and 0.090 mg·L−1·min−1, respectively, in the H3PW12O40/TiO2 photoelectrocatalytic reaction system under optimal conditions (impressed voltage: 0.5 V, solution pH: 6.3, and initial concentration: 5 mg·L−1). This was an excellent result, with a limited catalyst amount (ca. 4.5 mg) compared with related, photocatalytic research (Table 2). The degradation rate (r) of o-CP in the photoelectrocatalytic system had the greatest effect on the variation of the impressed voltage, which was 0.055 mg·L−1·min−1 (0.3 V), 0.090 mg·L−1·min−1 (0.5 V), 0.071 mg·L−1·min−1 (0.8 V), and 0.035 mg·L−1·min−1 (1.0 V), indicating that this factor may exert an essential influence on the kinetics. Compared with the photocatalytic system (degradation efficiency of o-CP was 33.7%), the efficiency increased significantly to 96.6% with optimum impressed voltage (Figure 4), and K’ was enhanced by 6.0-fold in the H3PW12O40/TiO2 photoeletrocatalytic system (Figure 5 and Table 3).

3.3. The Kinetics of H3PW12O40/TiO2 Composite Film and TiO2 Film in the Photoeletrocatalytic System

In the photoeletrocatalytic system, r of o-CP by H3PW12O40/TiO2 and TiO2 film was 0.090 and 0.020 mg·L−1·min−1, respectively (Figure 6, Figure 7, and Table 3). The apparent quantum yield (Φ) was directly derived from r to the effective photon flux (I0) under 420 nm illumination: Φ (%) = 100 × r/I0 [36]. A higher apparent quantum yield (Φ = 32.14%) of H3PW12O40/TiO2 composite film was attained in comparison with TiO2 film (Φ = 10.00%) under optimal conditions (Table 4).
As-prepared H3PW12O40/TiO2 composite film showed an excellent photoeletrocatalytic property because more photo-generated carriers were produced and separated efficiently based on the capability of accepting electrons of H3PW12O40. This was confirmed by the higher photocurrent intensity (6.2 μA) than that of TiO2 film (3.0 μA), together with excellent stability of recycling (Figure 8) in the photocurrent response experiment, and the considerably lower photoluminescence (PL) intensity of the broad emission (with a wavelength range of 350–800 nm) in the TiO2/H3PW12O40 system compared with that of the TiO2 system (Figure 9). Furthermore, Mott–Schottky plots (Figure 10) of both the TiO2 film and TiO2/H3PW12O40 composite film showed a positive slope, thus their carrier densities can be estimated by the following equation:
Nd = (2/e0εε0)[d(1/C2)/dV]−1
where Nd, e0, ε, ε0, and d(1/C2)/dV represent the carrier density, electron charge, the dielectric coefficient (about 170), the permittivity of vacuum, and the straight slope obtained from the plot, respectively [37]. Consequently, the carrier density of H3PW12O40/TiO2 composite film was 5.92 × 1022 cm−1 which was higher than that of TiO2 film (4.86 × 1022).

3.4. The Photoelectrocatalytic Degradation Path

Under the attack of OH which was the primary radical in the TiO2/H3PW12O40 system [14], the intermediate products including 2-chlorohydroquinone (CHQ), catechol (CT), and hydroxyl-hydroquinone (H-HQ) were identified by LC-MS (Table 5). Furthermore, the parent and intermediate species underwent a ring-opening reaction and were finally mineralized. The possible photoelectrocatalytic degradation pathways of o-CP were as follows (Figure 11).

4. Conclusions

The as-prepared H3PW12O40/TiO2 photoeletrocatalytic system showed an outstanding potential for o-CP degradation with an efficiency of 96.6% after 180 min under optimum conditions, and K was enhanced 6.0-fold compared with the photocatalytic system. Meanwhile, more photo-generated carriers were produced and separated efficiently in H3PW12O40/TiO2 composite film compared with TiO2 film in the photoeletrocatalytic system. It is worth noting that the catalyst amount and the impressed voltage were only ca. 4.5 mg and 0.5 V, respectively, which together were an excellent property, indicating that this technique is more environmentally-friendly and energy-efficient and has great advantages over other techniques. It could be also be applied in the treatment of organochlorine wastewater.

Author Contributions

L.L. designed the research and wrote the paper; L.J. performed measurements and analyzed the data; L.Y. analyzed the data; J.L. and J.W. collected samples; N.L. wrote the paper; and J.Q. contributed to writing.

Funding

This research and APC were funded by the National Natural Science Foundation of China [51408109], Science and Technology Project of Changchun City [18DY009].

Conflicts of Interest

The authors declare that they have no competing interests.

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Figure 1. Photoelectrocatalytic reaction system.
Figure 1. Photoelectrocatalytic reaction system.
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Figure 2. The influence of impressed voltage (a), pH (b), and initial concentration (c) on the photoelectrocatalytic performance of H3PW12O40/TiO2 film towards o-chlorophenol (o-CP) degradation.
Figure 2. The influence of impressed voltage (a), pH (b), and initial concentration (c) on the photoelectrocatalytic performance of H3PW12O40/TiO2 film towards o-chlorophenol (o-CP) degradation.
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Figure 3. The influence of impressed voltage (a), pH (b), and initial concentration (c) on the kinetics of o-CP degradation.
Figure 3. The influence of impressed voltage (a), pH (b), and initial concentration (c) on the kinetics of o-CP degradation.
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Figure 4. The degradation efficiency of o-CP in photocatalytic and photoeletrocatalytic systems.
Figure 4. The degradation efficiency of o-CP in photocatalytic and photoeletrocatalytic systems.
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Figure 5. The reaction kinetics of o-CP in photocatalytic and photoeletrocatalytic systems.
Figure 5. The reaction kinetics of o-CP in photocatalytic and photoeletrocatalytic systems.
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Figure 6. The degradation efficiency of o-CP by H3PW12O40/TiO2 and TiO2 film in the photoeletrocatalytic system.
Figure 6. The degradation efficiency of o-CP by H3PW12O40/TiO2 and TiO2 film in the photoeletrocatalytic system.
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Figure 7. The reaction kinetics of o-CP by H3PW12O40/TiO2 and TiO2 film in the photoeletrocatalytic system.
Figure 7. The reaction kinetics of o-CP by H3PW12O40/TiO2 and TiO2 film in the photoeletrocatalytic system.
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Figure 8. Photocurrent density of H3PW12O40/TiO2 composite film and TiO2 film.
Figure 8. Photocurrent density of H3PW12O40/TiO2 composite film and TiO2 film.
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Figure 9. Photoluminescence (PL) spectra of TiO2 film and TiO2/H3PW12O40 composite film.
Figure 9. Photoluminescence (PL) spectra of TiO2 film and TiO2/H3PW12O40 composite film.
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Figure 10. Mott–Schottky plots of TiO2 film and TiO2/H3PW12O40 composite film.
Figure 10. Mott–Schottky plots of TiO2 film and TiO2/H3PW12O40 composite film.
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Figure 11. The possible photocatalytic degradation pathways of o-CP by H3PW12O40/TiO2 composite film.
Figure 11. The possible photocatalytic degradation pathways of o-CP by H3PW12O40/TiO2 composite film.
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Table 1. The kinetics equations of o-CP photoelectrocatalytic degradation.
Table 1. The kinetics equations of o-CP photoelectrocatalytic degradation.
Influence FactorConditionsInitial Rate r0 (mg·L−1·min−1)Apparent Constant K’ (min−1)Kinetics Equations ln(C0/C) = K’tR2
Impressed voltage0.3 V0.0550.011y = 0.011x0.991
0.5 V0.0900.018y = 0.018x0.991
0.8 V0.0710.014y = 0.0140.983
1.0 V0.0350.008y = 0.007x0.973
Solution pHpH = 4.20.0450.009y = 0.009x0.982
pH = 6.30.0900.018y = 0.018x0.991
pH = 8.10.0450.009y = 0.009x0.996
pH = 10.00.0550.011y = 0.011x0.995
Initial concentration2.5 mg·L−10.0280.011y = 0.010x0.988
5.0 mg·L−10.0900.018y = 0.018x0.991
10.0 mg·L−10.0900.009y = 0.009x0.987
15.0 mg·L−10.1200.008y = 0.008x0.977
20.0 mg·L−10.1200.006y = 0.006x0.977
Table 2. Comparison of degradation dynamics under various systems.
Table 2. Comparison of degradation dynamics under various systems.
Pollution Concentration CatalystLampReaction RateReferences
5 mg·L−1H3PW12O40/TiO2
ca. 0.045 g·L−1
300 W
Xenon lamp
0.087 mg·L−1·min−1Our work
5 mg·L−1ZnO-ZnS@Polyaniline
0.5 g·L−1
104 W
White visible light lamp
0.008 mg·L−1·min−1[34]
10 mg·L−1TiO2
2 g·L−1
1000 W
Xenon lamp
0.478 mg·L−1·min−1[35]
Table 3. The kinetics equations of o-CP degradation.
Table 3. The kinetics equations of o-CP degradation.
ConditionsInitial Rate
r (mg·L−1·min−1)
Apparent Constant
K’(min−1)
Kinetics Equations ln(C0/C) = K’tR2
Photocatalytic degradation0.0150.003y = 0.003x0.993
Photoelectrocatalytic degradation0.0900.018y = 0.018x0.991
TiO2 film0.0200.004y = 0.004x0.975
H3PW12O40/TiO2 composite film0.0900.018y = 0.018x0.991
Table 4. The apparent quantum yield (Φ) of photoelectrocatalytic degradation.
Table 4. The apparent quantum yield (Φ) of photoelectrocatalytic degradation.
Catalyst TypeI0 (mW/cm2)r (mg·L−1·min−1)Φ
TiO2 film200.02010.00%
H3PW12O40/TiO2 composite film280.09032.14%
Table 5. The structure of o-CP and the main intermediate products.
Table 5. The structure of o-CP and the main intermediate products.
m/zStructure
o-CP126.8 Sustainability 11 03551 i001
Main intermediate products142.8 Sustainability 11 03551 i002
108.3 Sustainability 11 03551 i003
124.3 Sustainability 11 03551 i004

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Li, L.; Jiang, L.; Yang, L.; Li, J.; Lu, N.; Qu, J. Optimization of Degradation Kinetics towards O-CP in H3PW12O40/TiO2 Photoelectrocatalytic System. Sustainability 2019, 11, 3551. https://doi.org/10.3390/su11133551

AMA Style

Li L, Jiang L, Yang L, Li J, Lu N, Qu J. Optimization of Degradation Kinetics towards O-CP in H3PW12O40/TiO2 Photoelectrocatalytic System. Sustainability. 2019; 11(13):3551. https://doi.org/10.3390/su11133551

Chicago/Turabian Style

Li, Lu, Liyan Jiang, Liu Yang, Ju Li, Nan Lu, and Jiao Qu. 2019. "Optimization of Degradation Kinetics towards O-CP in H3PW12O40/TiO2 Photoelectrocatalytic System" Sustainability 11, no. 13: 3551. https://doi.org/10.3390/su11133551

APA Style

Li, L., Jiang, L., Yang, L., Li, J., Lu, N., & Qu, J. (2019). Optimization of Degradation Kinetics towards O-CP in H3PW12O40/TiO2 Photoelectrocatalytic System. Sustainability, 11(13), 3551. https://doi.org/10.3390/su11133551

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