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Frontiers of Environmental Science & Engineering

ISSN 2095-2201

ISSN 2095-221X(Online)

CN 10-1013/X

Postal Subscription Code 80-973

2018 Impact Factor: 3.883

Front. Environ. Sci. Eng.    2021, Vol. 15 Issue (5) : 95    https://doi.org/10.1007/s11783-020-1341-y
RESEARCH ARTICLE
Experimental and computational assessment of 1,4-Dioxane degradation in a photo-Fenton reactive ceramic membrane filtration process
Shan Xue1,3, Shaobin Sun2,3, Weihua Qing3, Taobo Huang4, Wen Liu4, Changqing Liu1(), Hong Yao2, Wen Zhang3()
1. School of Environmental and Municipal Engineering, Qingdao University of Technology, Qingdao 266033, China
2. Beijing Key Laboratory of Aqueous Typical Pollutants Control and Water Quality Safeguard, Department of Municipal and Environmental Engineering, School of Civil Engineering, Beijing Jiaotong University, Beijing 100044, China
3. John A. Reif, Jr. Department of Civil and Environmental Engineering, New Jersey Institute of Technology, Newark, NJ 07102, USA
4. College of Environmental Sciences and Engineering, Peking University, Key Laboratory of Water and Sediment Sciences (Ministry of Education), Beijing 100871, China
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Abstract

• 1,4-Dioxane was degraded via the photo-Fenton reactive membrane filtration.

• Degradation efficiency and AQY were both enhanced in photocatalytic membrane.

• There is a tradeoff between photocatalytic degradation and membrane permeation flux.

• Degradation pathways of 1,4-Dioxane is revealed by DFT analysis.

The present study evaluated a photo-Fenton reactive membrane that achieved enhanced 1,4-Dioxane removal performance. As a common organic solvent and stabilizer, 1,4-Dioxane is widely used in a variety of industrial products and poses negative environmental and health impacts. The membrane was prepared by covalently coating photocatalyst of goethite (α-FeOOH) on a ceramic porous membrane as we reported previously. The effects of UV irradiation, H2O2 and catalyst on the removal efficiency of 1,4-Dioxane in batch reactors were first evaluated for optimized reaction conditions, followed by a systematical investigation of 1,4-Dioxane removal in the photo-Fenton membrane filtration mode. Under optimized conditions, the 1,4-Dioxane removal rate reached up to 16% with combination of 2 mmol/L H2O2 and UV365 irradiation (2000 µW/cm2) when the feed water was filtered by the photo-Fenton reactive membrane at a hydraulic retention time of 6 min. The removal efficiency and apparent quantum yield (AQY) were both enhanced in the filtration compared to the batch mode of the same photo-Fenton reaction. Moreover, the proposed degradation pathways were analyzed by density functional theory (DFT) calculations, which provided a new insight into the degradation mechanisms of 1,4-Dioxane in photo-Fenton reactions on the functionalized ceramic membrane.

Keywords Photo-Fenton      Ceramic membrane      1,4-Dioxane      Goethite     
Corresponding Author(s): Changqing Liu,Wen Zhang   
Issue Date: 18 January 2021
 Cite this article:   
Shan Xue,Shaobin Sun,Weihua Qing, et al. Experimental and computational assessment of 1,4-Dioxane degradation in a photo-Fenton reactive ceramic membrane filtration process[J]. Front. Environ. Sci. Eng., 2021, 15(5): 95.
 URL:  
https://academic.hep.com.cn/fese/EN/10.1007/s11783-020-1341-y
https://academic.hep.com.cn/fese/EN/Y2021/V15/I5/95
Fig.1  Schematic photo of the photo-Fenton reactive membrane filtration setup.
Reaction condition Regression equation* k (min1) R2
α-FeOOH/H2O2/UV y = –(2.0x + 1.1) × 101 2.0 × 101 0.99
UV/H2O2 y = –(1.5x + 0.60) × 101 1.5 × 101 0.96
UV y = –(8.4x-0.51) × 102 8.4 × 102 0.94
α-FeOOH/UV y = –(8.1x + 3.9) × 102 8.1 × 102 0.99
α-FeOOH/H2O2 y = –(5.5x + 1.5) × 102 5.5 × 102 0.97
α-FeOOH y = –(4.2x + 5.8) × 102 4.2 × 102 0.95
H2O2 y = –(6.2x + 31) × 103 6.2 × 103 0.69
Tab.1  Rate constants obtained from linear regression analysis of 1,4-Dioxane removal data in Fig. 2
Fig.2  The ratio of the residual concentration (C) to the initial concentration (C0) of 1,4-Dioxane (a) and TOC after 12 h (b) under different reaction conditions. Initial 1,4-Dioxane concentration: 10.8 mg/L; Initial TOC concentration: 5.3 mg/L; UV365 intensity: 2000 µW/cm2; H2O2 concentration: 2 mmol/L; and catalyst dosage: 1 g/L. (c) First order plot for 1,4-Dioxane. Line is fitting curve. The red solid lines in Fig. 2(b) show the comparison pairs with the corresponding p values. p values of<0.05 indicate significant differences.
Fig.3  The ratio of the remaining concentration (C) to the initial concentration (C0) of 1,4-Dioxane (a) and TOC after 12 h (b) under different initial H2O2 concentration. Initial 1,4-Dioxane concentration: 10.8 mg/L; Initial TOC concentration: 5.3 mg/L; UV365 intensity: 2000 µW/cm2; and catalyst dosage: 1 g/L. The red solid lines in Fig. 3(b) show the comparison pairs with the corresponding p values. p values of<0.05 indicate significant differences.
Fig.4  The ratio of the remaining concentration (C) to the initial concentration (C0) of 1,4-Dioxane (a) and TOC after 12 h (b) under different initial 1,4-Dioxane concentration. UV365 intensity: 2000 µW/cm2; H2O2 concentration: 2 mmol/L; and catalyst dosage: 1 g/L. The black solid lines in Fig. 4(b) show the comparison pairs with the corresponding p values. p values of<0.05 indicate significant differences.
Fig.5  The ratio of the residual concentration (C) to the initial concentration (C0) of 1,4-Dioxane and TOC under different filtration conditions. Initial 1,4-Dioxane concentration: 10.8 mg/L; Initial TOC concentration: 5.3 mg/L; UV intensity: 2000 µW/cm2; H2O2 concentration: 2 mmol/L; and the catalyst coating density on the ceramic membrane was 2 µg/g. CM denotes for coated membrane, and UCM denotes for uncoated membrane. The black solid lines (1,4-Dioxane concentration) and blue solid lines (TOC concentration) show the comparison pairs with the corresponding p values. p values of<0.05 indicate significant differences.
Fig.6  (a) The theoretical and actual removal rates of 1,4-Dioxane and actual removal rates of TOC of coated ceramic membranes under different influent flux. (b) The 1,4-Dioxane removal rates under different initial 1,4-Dioxane concentration. Initial 1,4-Dioxane concentration: 10.8 mg/L; Initial TOC concentration: 5.3 mg/L; UV intensity: 2000 µW/cm2; H2O2 concentration: 2 mmol/L; and the catalyst coating density on the ceramic membrane was 2 µg/g.
Catalyst Initial 1,4-Dioxane concentration (mg/L) Removal performance Specific removal rate (mg/(g·h)) Specific removal rate (mg/(L·h)) AQY (%)* Reference
NF-TiO2/TiO2 140 <100% in 10 h 11.29 14 2.41 × 104 Barndõk et al., 2016b
TiO2/P25 0.85 100% in 100 min 0.051 0.51 18.2 Lee et al., 2015
Fe0 10 >89% in 4 h 0.445 2.23 Son et al., 2009
Hybridization of TiO2 0.1 100% in 1 h in a batch reactor 0.1 0.1 0.323 Lee and Choo, 2013
>60% in 39 min in a continuous flow reactor 2.1 0.09 0.291
Au/TiO2 500 59% in 4 h 73.8 7.64 × 103 Youn et al., 2010
Commercial ZnO 20 100% in 12 h 1.67 1.67 Hwangbo et al., 2019
α-FeOOH 10.8 90% in 12 h in a batch reactor 0.9 0.81 0.792 This work
α-FeOOH coated ceramic membrane 10.8 16% in 6 min in a continuous flow reactor 0.43 17.28 2.76 This work
Tab.2  Comparison of 1,4-Dioxane removal rates in different photocatalytic systems
Fig.7  Predicted Gibbs free energy changes of 1,4-Dioxane that underwent the hypothetical degradation pathway.
1 D T Adamson, E A Piña, A E Cartwright, S R Rauch, R H Anderson, T Mohr, J A Connor (2017). 1,4-Dioxane drinking water occurrence data from the third unregulated contaminant monitoring rule. Science of the Total Environment, 596: 236–245
https://doi.org/10.1016/j.scitotenv.2017.04.085
2 R Ahmad, J K Kim, J H Kim, J Kim (2019). Diethylene glycol-assisted organized TiO2 nanostructures for photocatalytic wastewater treatment ceramic membranes. Water, 11(4): 750
3 N H Alias, J Jaafar, S Samitsu, T Matsuura, A Ismail, M Othman, M A Rahman, N H Othman, N Abdullah, S H Paiman (2019). Photocatalytic nanofiber-coated alumina hollow fiber membranes for highly efficient oilfield produced water treatment. Chemical Engineering Journal, 360: 1437–1446
4 R Aryal, C Xia, J Liu (2019). 1,4-Dioxane-contaminated groundwater remediation in the anode chamber of a microbial fuel cell. Water Environment Research, 91(11): 1537–1545
https://doi.org/doi.org/10.1002/wer.1155
5 A Aziz, S Ibrahim (2018). Preparation of activated carbon/N-doped titania composite for synergistic adsorption-photocatalytic oxidation of batik dye. MS&E, 358(1): 012014
https://doi.org/10.1088/1757-899X/358/1/012014
6 H Barndõk, L Blanco, D Hermosilla, Á Blanco (2016a). Heterogeneous photo-Fenton processes using zero valent iron microspheres for the treatment of wastewaters contaminated with 1,4-dioxane. Chemical Engineering Journal, 284: 112–121
https://doi.org/10.1016/j.cej.2015.08.097
7 H Barndõk, D Hermosilla, C Han, D D Dionysiou, C Negro, Á Blanco (2016b). Degradation of 1,4-Dioxane from industrial wastewater by solar photocatalysis using immobilized NF-TiO2 composite with monodisperse TiO2 nanoparticles. Applied Catalysis B: Environmental, 180: 44–52
https://doi.org/10.1016/j.apcatb.2015.06.015
8 H Barndõk, L Cortijo, D Hermosilla, C Negro, Á Blanco (2014). Removal of 1,4-Dioxane from industrial wastewaters: Routes of decomposition under different operational conditions to determine the ozone oxidation capacity. Journal of Hazardous Materials, 280: 340–347
https://doi.org/10.1016/j.jhazmat.2014.07.077
9 M A Beckett, I Hua (2000). Elucidation of the 1,4-Dioxane decomposition pathway at discrete ultrasonic frequencies. Environmental Science & Technology, 34(18): 3944–3953
https://doi.org/10.1021/es000928r
10 M A Beckett, I Hua (2003). Enhanced sonochemical decomposition of 1,4-Dioxane by ferrous iron. Water Research, 37(10): 2372–2376
https://doi.org/10.1016/S0043-1354(03)00005-8
11 T Berger, C Regmi, A Schäfer, B Richards (2020). Photocatalytic degradation of organic dye via atomic layer deposited TiO2–ceramic membranes in single-pass flow-through operation. Journal of Membrane Science: 118015
12 P Biniaz, M A Makarem, M R Rahimpour (2019). Membrane reactors. In: Benaglia M, Puglisi A, eds. Catalyst Immobilization: Methods and Applications. Hoboken: Wiley, 307–324
13 M B Chabalala (2016). Preparation of doped nanotitanium dioxide (TIO2) immobilized on polyethersulphone (PES) nanofiberes for photocatalytic degradation of water pollutants. Master’s thesis. Johannesburg: University of Johannesburg
14 S Chakraborty, S Loutatidou, G Palmisano, J Kujawa, M O Mavukkandy, S Al-Gharabli, E Curcio, H A Arafat (2017). Photocatalytic hollow fiber membranes for the degradation of pharmaceutical compounds in wastewater. Journal of Environmental Chemical Engineering, 5(5): 5014–5024
15 N P Cheremisinoff (2017). Groundwater Remediation: A Practical Guide for Environmental Engineers and Scientists. Hoboken: John Wiley & Sons
16 C H Chiou, C Y Wu, R S Juang (2008). Influence of operating parameters on photocatalytic degradation of phenol in UV/TiO2 process. Chemical Engineering Journal, 139(2): 322–329
https://doi.org/10.1016/j.cej.2007.08.002
17 S Chitra, K Paramasivan, M Cheralathan, P K Sinha (2012). Degradation of 1,4-Dioxane using advanced oxidation processes. Environmental Science and Pollution Research International, 19(3): 871–878
https://doi.org/10.1007/s11356-011-0619-9
18 J Y Choi, Y J Lee, J Shin, J W Yang (2010). Anodic oxidation of 1,4-Dioxane on boron-doped diamond electrodes for wastewater treatment. Journal of Hazardous Materials, 179(1–3): 762–768
https://doi.org/10.1016/j.jhazmat.2010.03.067
19 H Coleman, V Vimonses, G Leslie, R Amal (2007). Degradation of 1,4-Dioxane in water using TiO2 based photocatalytic and H2O2/UV processes. Journal of Hazardous Materials, 146(3): 496–501
https://doi.org/10.1016/j.jhazmat.2007.04.049
20 L De Angelis, M M F De Cortalezzi (2016). Improved membrane flux recovery by Fenton-type reactions. Journal of Membrane Science, 500: 255–264
https://doi.org/10.1016/j.memsci.2015.11.042
21 J De Clercq, E Van De Steene, K Verbeken, M Verhaege (2010). Electrochemical oxidation of 1,4-Dioxane at boron-doped diamond electrode. Journal of Chemical Technology and Biotechnology (Oxford, Oxfordshire), 85(8): 1162–1167
https://doi.org/10.1002/jctb.2415
22 Y Ding, W Sun, L Cao, J Yang (2016). A spontaneous catalytic membrane reactor to dechlorinate 2,4,6-TCP as an organic pollutant in wastewater and to reclaim electricity simultaneously. Chemical Engineering Journal, 285: 573–580
https://doi.org/10.1016/j.cej.2015.10.034
23 U.S. EPA, (2006). Treatment Technologies for 1,4-Dioxane: Fundamentals and Field Applications. Cincinnati: Office of Solid Waste and Emergency Response, EPA
24 EPA, U.S. (2017). Technical Fact Sheet for 1, 4-dioxane: EPA 505-F-17-011. Washington: Federal Facilities Restoration and Reuse Office, EPA
25 W Fu, W Zhang (2018). Microwave-enhanced membrane filtration for water treatment. Journal of Membrane Science, 568: 97–104
https://doi.org/10.1016/j.memsci.2018.09.064
26 Y Gu, I Favier, C Pradel, D L Gin, J F Lahitte, R D Noble, M Gómez, J C Remigy (2015). High catalytic efficiency of palladium nanoparticles immobilized in a polymer membrane containing poly (ionic liquid) in Suzuki–Miyaura cross-coupling reaction. Journal of Membrane Science, 492: 331–339
https://doi.org/10.1016/j.memsci.2015.05.051
27 Y Guo, B Xu, F Qi (2016). A novel ceramic membrane coated with MnO2–Co3O4 nanoparticles catalytic ozonation for benzophenone-3 degradation in aqueous solution: fabrication, characterization and performance. Chemical Engineering Journal, 287: 381–389
https://doi.org/10.1016/j.cej.2015.11.067
28 J He, W Ma, W Song, J Zhao, X Qian, S Zhang, C Y Jimmy (2005). Photoreaction of aromatic compounds at α-FeOOH/H2O interface in the presence of H2O2: Evidence for organic-goethite surface complex formation. Water Research, 39(1): 119–128
https://doi.org/10.1016/j.watres.2004.09.006
29 M Hwangbo, E C Claycomb, Y Liu, T E Alivio, S Banerjee, K H Chu (2019). Effectiveness of zinc oxide-assisted photocatalysis for concerned constituents in reclaimed wastewater: 1,4-Dioxane, trihalomethanes, antibiotics, antibiotic resistant bacteria (ARB), and antibiotic resistance genes (ARGs). Science of the Total Environment, 649: 1189–1197
https://doi.org/10.1016/j.scitotenv.2018.08.360
30 J R Jasmann, T Borch, T C Sale, J Blotevogel (2016). Advanced electrochemical oxidation of 1,4-Dioxane via dark catalysis by novel titanium dioxide (TiO2) pellets. Environmental Science & Technology, 50(16): 8817–8826
https://doi.org/10.1021/acs.est.6b02183
31 M M Johns, W E Marshall, C A Toles (1998). Agricultural by-products as granular activated carbons for adsorbing dissolved metals and organics. Journal of Chemical Technology & Biotechnology Biotechnology, 71(2): 131–140
https://doi.org/10.1002/(SICI)1097-4660(199802)71:2<131::AID-JCTB821>3.0.CO;2-K
32 R Kamaludin, A S M Puad, M H D Othman, S H S A Kadir, Z Harun (2019). Incorporation of N-doped TiO2 into dual layer hollow fiber (DLHF) membrane for visible light-driven photocatalytic removal of reactive black 5. Polymer Testing, 78: 105939
33 U Karges, J Becker, W Püttmann (2018). 1,4-Dioxane pollution at contaminated groundwater sites in western Germany and its distribution within a TCE plume. Science of the Total Environment, 619: 712–720
https://doi.org/10.1016/j.scitotenv.2017.11.043
34 G M Klečka, S J Gonsior (1986). Removal of 1,4-Dioxane from wastewater. Journal of Hazardous Materials, 13(2): 161–168
https://doi.org/10.1016/0304-3894(86)80016-4
35 J Kleine, K V Peinemann, C Schuster, H J Warnecke (2002). Multifunctional system for treatment of wastewaters from adhesive-producing industries: Separation of solids and oxidation of dissolved pollutants using doted microfiltration membranes. Chemical Engineering Science, 57(9): 1661–1664
36 K C Lee, H J Beak, K H Choo (2015). Membrane photoreactor treatment of 1, 4-Dioxane-containing textile wastewater effluent: Performance, modeling, and fouling control. Water Research, 86: 58–65
https://doi.org/10.1016/j.watres.2015.05.017
37 K C Lee, K H Choo (2013). Hybridization of TiO2 photocatalysis with coagulation and flocculation for 1,4-Dioxane removal in drinking water treatment. Chemical Engineering Journal, 231: 227–235
https://doi.org/10.1016/j.cej.2013.07.023
38 S Li, G Zhang, W Peng, H Zheng, Y Zheng (2016). Microwave-enhanced Mn-Fenton process for the removal of BPA in water. Chemical Engineering Journal, 294: 371–379
https://doi.org/10.1016/j.cej.2016.03.006
39 Y Li, K L Yeung (2019). Polymeric catalytic membrane for ozone treatment of DEET in water. Catalysis Today, 331: 53–59
https://doi.org/10.1016/j.cattod.2018.06.005
40 L Liang, J Zhang, P Feng, C Li, Y Huang, B Dong, L Li, X Guan (2015). Occurrence of bisphenol A in surface and drinking waters and its physicochemical removal technologies. Frontiers of Environmental Science & Engineering, 9(1): 16–38
https://doi.org/10.1007/s11783-014-0697-2
41 G Liu, D Zhu, W Zhou, S Liao, J Cui, K Wu, D Hamilton (2010). Solid-phase photocatalytic degradation of polystyrene plastic with goethite modified by boron under UV-vis light irradiation. Applied Surface Science, 256(8): 2546–2551
https://doi.org/10.1016/j.apsusc.2009.10.102
42 H Liu, T Chen, R L Frost (2014). An overview of the role of goethite surfaces in the environment. Chemosphere, 103: 1–11
https://doi.org/10.1016/j.chemosphere.2013.11.065
43 W J Lyman, W F Reehl, D H Rosenblatt (1990). Handbook of Chemical Property Estimation Methods.Washington, DC: American Chemical Society
44 J Maekawa, K Mae, H Nakagawa (2016). Degradation of 1,4-Dioxane by the ferrioxalate-mediated photo-Fenton process using UV or white LED irradiation. Journal of Chemical Engineering of Japan, 49(3): 305–311
https://doi.org/10.1252/jcej.14we272
45 J Mao, X Quan, J Wang, C Gao, S Chen, H Yu, Y Zhang (2018). Enhanced heterogeneous Fenton-like activity by Cu-doped BiFeO3 perovskite for degradation of organic pollutants. Frontiers of Environmental Science & Engineering, 12(6): 10
https://doi.org/10.1007/s11783-018-1060-9
46 A V Marenich, C J Cramer, D G Truhlar (2009). Universal solvation model based on solute electron density and on a continuum model of the solvent defined by the bulk dielectric constant and atomic surface tensions. Journal of Physical Chemistry B, 113(18): 6378–6396
https://doi.org/10.1021/jp810292n
47 B J Martijn, A L Fuller, J P Malley, J C Kruithof (2010). Impact of IX-UF pretreatment on the feasibility of UV/H2O2 treatment for degradation of NDMA and 1,4-Dioxane. Ozone Science and Engineering, 32(6): 383–390
https://doi.org/10.1080/01919512.2010.515507
48 V Maurino, P Calza, C Minero, E Pelizzetti, M Vincenti (1997). Light-assisted 1,4-dioxane degradation. Chemosphere, 35(11): 2675–2688
https://doi.org/10.1016/S0045-6535(97)00322-6
49 A C Mcelroy, M R Hyman, D R Knappe (2019). 1,4-Dioxane in drinking water: Emerging for forty years and still unregulated. Current Opinion in Environmental Science & Health, 7: 117–125
https://doi.org/doi.org/10.1016/j.coesh.2019.01.003
50 M J Mcguire, I H Suffet, J V Radziul (1978). Assessment of unit processes for the removal of trace organic compounds from drinking water. Journal-American Water Works Association, 70(10): 565–572
https://doi.org/doi.org/10.1002/j.1551-8833.1978.tb04244.x
51 N Merayo, D Hermosilla, L Cortijo, Á Blanco (2014). Optimization of the Fenton treatment of 1,4-Dioxane and on-line FTIR monitoring of the reaction. Journal of Hazardous Materials, 268: 102–109
https://doi.org/10.1016/j.jhazmat.2014.01.008
52 X Miao, H Dai, J Chen, J Zhu (2018). The enhanced method of hydroxyl radical generation in the heterogeneous UV-Fenton system with α-FeOOH as catalyst. Separation and Purification Technology, 200: 36–43
https://doi.org/10.1016/j.seppur.2018.02.012
53 Y Miao, N W Johnson, P B Gedalanga, D Adamson, C Newell, S Mahendra (2019). Response and recovery of microbial communities subjected to oxidative and biological treatments of 1,4-Dioxane and co-contaminants. Water Research, 149: 74–85
https://doi.org/10.1016/j.watres.2018.10.070
54 T K Mohr, J A Stickney, W H Diguiseppi (2016). Environmental investigation and remediation: 1,4-Dioxane and other solvent stabilizers. Florida: CRC Press
55 N Moustakas, F Katsaros, A Kontos, G E Romanos, D Dionysiou, P Falaras (2014). Visible light active TiO2 photocatalytic filtration membranes with improved permeability and low energy consumption. Catalysis Today, 224: 56–69
56 Y Nomura, S Fukahori, T J J O H M Fujiwara (2020). Removal of 1,4-Dioxane from landfill leachate by a rotating advanced oxidation contactor equipped with activated carbon/TiO2 composite sheets. Journal of Hazardous Materials, 383: 121005
https://doi.org/doi.org/10.1016/j.jhazmat.2019.121005
57 T A Otitoju, D Jiang, Y Ouyang, M A M Elamin, S Li (2020). Photocatalytic degradation of Rhodamine B using CaCu3Ti4O12 embedded polyethersulfone hollow fiber membrane. Journal of industrial and engineering chemistry, 83: 145–152
58 M Otto, S Nagaraja (2007). Treatment technologies for 1,4-Dioxane: Fundamentals and field applications. Remediation Journal: The Journal of Environmental Cleanup Costs, Technologies & Techniques, 17(3): 81–88
https://doi.org/doi.org/10.1002/rem.20135
59 S Papageorgiou, F Katsaros, E Favvas, G E Romanos, C Athanasekou, K Beltsios, O Tzialla, P Falaras (2012). Alginate fibers as photocatalyst immobilizing agents applied in hybrid photocatalytic/ultrafiltration water treatment processes. Water Research, 46(6): 1858–1872
60 W Qing, X Li, S Shao, X Shi, J Wang, Y Feng, W Zhang, W Zhang (2019). Polymeric catalytically active membranes for reaction-separation coupling: A review. Journal of Membrane Science, 583: 118–138
https://doi.org/10.1016/j.memsci.2019.04.053
61 W Qing, F Liu, H Yao, S Sun, C Chen, W Zhang (2020). Functional catalytic membrane development: A review of catalyst coating techniques. Advances in Colloid and Interface Science, 282: 102207
https://doi.org/10.1016/j.cis.2020.102207
62 G Romanos, C Athanasekou, V Likodimos, P Aloupogiannis, P Falaras (2013). Hybrid ultrafiltration/photocatalytic membranes for efficient water treatment. Industrial & Engineering Chemistry Research, 52(39): 13938–13947
63 G E Romanos, C Athanasekou, F Katsaros, N Kanellopoulos, D Dionysiou, V Likodimos, P Falaras (2012). Double-side active TiO2-modified nanofiltration membranes in continuous flow photocatalytic reactors for effective water purification. Journal of Hazardous Materials, 211: 304–316
64 E J Rosenfeldt, K G Linden, S Canonica, U Von Gunten (2006). Comparison of the efficiency of OH radical formation during ozonation and the advanced oxidation processes O3/H2O2 and UV/H2O2. Water Research, 40(20): 3695–3704
https://doi.org/10.1016/j.watres.2006.09.008
65 G Scaratti, A Basso, R Landers, P J Alvarez, G L Puma, R F Moreira (2018). Treatment of aqueous solutions of 1,4-Dioxane by ozonation and catalytic ozonation with copper oxide (CuO). Environmental Technology, 39: 1–13
https://doi.org/10.1080/09593330.2018.1538259
66 H S Son, S B Choi, E Khan, K D Zoh (2006). Removal of 1,4-Dioxane from water using sonication: Effect of adding oxidants on the degradation kinetics. Water Research, 40(4): 692–698
https://doi.org/10.1016/j.watres.2005.11.046
67 H S Son, J K Im, K D Zoh (2009). A Fenton-like degradation mechanism for 1,4-Dioxane using zero-valent iron (Fe0) and UV light. Water Research, 43(5): 1457–1463
https://doi.org/10.1016/j.watres.2008.12.029
68 M I Stefan, J R Bolton (1998). Mechanism of the degradation of 1,4-Dioxane in dilute aqueous solution using the UV/hydrogen peroxide process. Environmental Science & Technology, 32(11): 1588–1595
https://doi.org/10.1021/es970633m
69 D K Stepien, P Diehl, J Helm, A Thoms, W Püttmann (2014). Fate of 1,4-Dioxane in the aquatic environment: From sewage to drinking water. Water Research, 48(1): 406–419
https://doi.org/10.1016/j.watres.2013.09.057
70 J H Suh, M Mohseni (2004). A study on the relationship between biodegradability enhancement and oxidation of 1,4-Dioxane using ozone and hydrogen peroxide. Water Research, 38(10): 2596–2604
https://doi.org/10.1016/j.watres.2004.03.002
71 M Sun, C Lopez-Velandia, D R Knappe (2016). Determination of 1,4-Dioxane in the Cape Fear River watershed by heated purge-and-trap preconcentration and gas chromatography–mass spectrometry. Environmental Science & Technology, 50(5): 2246–2254
https://doi.org/10.1021/acs.est.5b05875
72 S Sun, H Yao, W Fu, L Hua, G Zhang, W Zhang (2018). Reactive photo-Fenton ceramic membranes: Synthesis, characterization and antifouling performance. Water Research, 144: 690–698
https://doi.org/10.1016/j.watres.2018.08.002
73 S Sun, H Yao, W Fu, S Xue, W Zhang (2020). Enhanced degradation of antibiotics by photo-Fenton reactive membrane filtration. Journal of Hazardous Materials, 386: 121955
https://doi.org/10.1016/j.jhazmat.2019.121955
74 G P Tian, Q Y Wu, A Li, W L Wang, H Y Hu (2017). Promoted ozonation for the decomposition of 1,4-Dioxane by activated carbon. Water Science and Technology: Water Supply, 17(2): 613–620
https://doi.org/10.2166/ws.2016.071
75 D H Tseng, L C Juang, H H Huang (2012). Effect of oxygen and hydrogen peroxide on the photocatalytic degradation of monochlorobenzene in aqueous suspension. International Journal of Photoenergy, 2012: 328526
https://doi.org/10.1155/2012/328526
76 L Varanasi, E Coscarelli, M Khaksari, L R Mazzoleni, D Minakata (2018). Transformations of dissolved organic matter induced by UV photolysis, Hydroxyl radicals, chlorine radicals, and sulfate radicals in aqueous-phase UV-Based advanced oxidation processes. Water Research, 135: 22–30
https://doi.org/10.1016/j.watres.2018.02.015
77 J Wang, Z Wu, T Li, J Ye, L Shen, Z She, F Liu (2018). Catalytic PVDF membrane for continuous reduction and separation of p-nitrophenol and methylene blue in emulsified oil solution. Chemical Engineering Journal, 334: 579–586
https://doi.org/10.1016/j.cej.2017.10.055
78 S Wei, C Zeng, Y Lu, G Liu, H Luo, R Zhang (2019). Degradation of antipyrine in the Fenton-like process with a La-doped heterogeneous catalyst. Frontiers of Environmental Science & Engineering, 13(5): 66
https://doi.org/10.1007/s11783-019-1149-9
79 T Westermann, T Melin (2009). Flow-through catalytic membrane reactors: Principles and applications. Chemical Engineering and Processing: Process Intensification, 48(1): 17–28
https://doi.org/10.1016/j.cep.2008.07.001
80 X Xu, S Liu, Y Cui, X Wang, K Smith, Y Wang (2019). Solar-driven removal of 1,4-Dioxane using WO3/ng-Al2O3 nano-catalyst in water. Catalysts, 9(4): 389
https://doi.org/10.3390/catal9040389
81 Y Yabuki, G Yoshida, T Daifuku, J Ono, A J J O W Banno, E Technology (2018). Biological treatment of 1,4-Dioxane in wastewater from landfill by indigenous microbes attached to flowing carriers. Journal of Water and Environment Technology, 16(6): 245–255
82 N K Youn, J E Heo, O S Joo, H Lee, J Kim, B K Min (2010). The effect of dissolved oxygen on the 1,4-Dioxane degradation with TiO2 and Au–TiO2 photocatalysts. Journal of Hazardous Materials, 177(1–3): 216–221
https://doi.org/10.1016/j.jhazmat.2009.12.020
83 Q Zeng, H Dong, X Wang, T Yu, W Cui (2017). Degradation of 1, 4-Dioxane by hydroxyl radicals produced from clay minerals. Journal of Hazardous Materials, 331: 88–98
https://doi.org/10.1016/j.jhazmat.2017.01.040
84 S Zhang, P B Gedalanga, S Mahendra (2017). Advances in bioremediation of 1,4-Dioxane-contaminated waters. Journal of Environmental Management, 204: 765–774
https://doi.org/10.1016/j.jenvman.2017.05.033
85 Y Zhao, D G Truhlar (2008). The M06 suite of density functionals for main group thermochemistry, thermochemical kinetics, noncovalent interactions, excited states, and transition elements: Two new functionals and systematic testing of four M06-class functionals and 12 other functionals. Theoretical Chemistry Accounts, 120(1–3): 215–241
https://doi.org/10.1007/s00214-007-0310-x
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[1] Wenyue Li, Min Chen, Zhaoxiang Zhong, Ming Zhou, Weihong Xing. Hydroxyl radical intensified Cu2O NPs/H2O2 process in ceramic membrane reactor for degradation on DMAc wastewater from polymeric membrane manufacturer[J]. Front. Environ. Sci. Eng., 2020, 14(6): 102-.
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