钴基光芬顿蒸馏膜处理实际垃圾渗滤液应用研究
作者:卢振宇,杨麒臻,蒋宇铃,瞿芳术,鄢忠森
单位: 1. 福州大学 土木工程学院,福州 350108;2. 福州水务集团有限公司,福州 350001;3. 广州大学 土木工程学院,广州 510006
关键词: 膜蒸馏;垃圾渗滤液;光芬顿;膜污染;自清洁
DOI号:
分类号: TQ028;X52
出版年,卷(期):页码: 2024,44(3):106-114

摘要:
垃圾渗滤液包含高浓度污染物质,对人类健康和生态环境构成威胁。尽管膜蒸馏(MD)具有截留效率高和操作压力低等优点,在垃圾渗滤液的处理中展现出一定的潜力。然而在MD的实际应用过程中,有机物和无机物引起的络合污染降低了水的净化效率,从而限制了其潜在的应用。为了解决这一难题,本研究将基于硫酸盐自由基的高级氧化技术(SR-AOPs)集成到MD技术中,以加强膜污染的控制。本研究采用直接水热法结合真空过滤合成了四氧化三钴/氮修饰的碳量子点/聚偏氟乙烯(Co3O4/NCDs/PVDF,简称CN-PVDF)光芬顿蒸馏膜,并首次用于直接接触式膜蒸馏(DCMD)中处理垃圾渗滤液。在1.9 kW/m2的可见光照射下,其活化20 mmol/L的过氧一硫酸盐(PMS),能够缓解DCMD处理实际垃圾渗滤液废水过程的膜污染,减少Ca2+、Mg2+和有机物在膜面的沉积。此外,CN-PVDF膜能实现光芬顿自清洁效果,经清洗后膜比通量由0.449显著恢复至0.928。本研究为MD膜抗污染能力提升提供了新的思路。
 Landfill leachate contains all kinds of harmful substances, which pose a threat to human health and ecological environment. Although membrane distillation (MD) has the advantages of high interception efficiency and low operating pressure, it shows certain potential in the treatment of landfill leachate. However, in the practical application of MD, the membrane complexation fouling caused by organic and inorganic substances reduces the efficiency of water purification, thus limiting its potential application. To solve this problem, this study integrated sulfate radical based advanced oxidation process (SR-AOPs) into MD technology to enhance the control of membrane fouling. Co3O4/NCDs/PVDF (CN-PVDF) photo-Fenton distillation membrane was synthesized by direct hydrothermal method combined with vacuum filtration, and it was first used in direct contact membrane distillation (DCMD) to treat landfill leachate. Under visible light irradiation of 1.9kW/m2 and activation of 20 mmol/Lol/L peroxymonosate (PMS), which could alleviate membrane fouling during DCMD treatment of actual landfill leachate wastewater, and reduce the deposition of Ca2+, Mg2+, and organic matter on the membrane surface during water production. In addition, CN-PVDF membrane can realize the self-cleaning effect of photo-Fenton, and the specific flux of CN-PVDF membrane can recover significantly from 0.449 to 0.928 after cleaning. In conclusion, this study proposes an innovative method to improve the anti-pollution ability of MD membranes.

基金项目:
国家自然科学基金资助项目(52370069,52000034),广东省自然科学基金杰出青年项目(2023B1515020057)

作者简介:
卢振宇(1997-),男,福建福州人,硕士,从事膜蒸馏废水处理技术研究

参考文献:
 [1]Mandal P, Dubey B K, Gupta A K. Review on landfill leachate treatment by electrochemical oxidation: Drawbacks, challenges and future scope[J]. Waste Manage, 2017,69:250-273.
[2]Bolyard S C, Reinhart D R. Application of landfill treatment approaches for stabilization of municipal solid waste[J]. Waste Manage, 2016,55:22-30.
[3]Liu Z, Wu W, Shi P, et al. Characterization of dissolved organic matter in landfill leachate during the combined treatment process of air stripping, Fenton, SBR and coagulation[J]. Waste Manage, 2015,41:111-118.
[4]Chen G, Wu G, Li N, et al. Landfill leachate treatment by persulphate related advanced oxidation technologies[J]. J  Hazard Mater, 2021,418:126355.
[5]Reshadi M A M, Bazargan A, McKay G. A review of the application of adsorbents for landfill leachate treatment: Focus on magnetic adsorption[J]. Sci Total Environ, 2020,731:138863.
[6]Baderna D, Caloni F, Benfenati E. Investigating landfill leachate toxicity in vitro: A review of cell models and endpoints[J]. Environ Int, 2019,122:21-30.
[7]Zoungrana A, Zengin 0 H, Elcik H, et al. The treatability of landfill leachate by direct contact membrane distillation and factors influencing the efficiency of the process[J]. Desalin Water Treat, 2017,71:233-243.
[8]Zhou Y, Huang M, Deng Q, et al. Combination and performance of forward osmosis and membrane distillation (FO-MD) for treatment of high salinity landfill leachate[J]. Desalination, 2017,420:99-105.
[9]Zarebska A, Nieto D R, Christensen K V, et al. Ammonia recovery from agricultural wastes by membrane distillation: Fouling characterization and mechanism[J]. Water Res, 2014,56:1-10.
[10]Yan Z, Lu Z, Chen X, et al. Membrane distillation treatment of landfill leachate: Characteristics and mechanism of membrane fouling[J]. Sep  Purif  Technol, 2022,289:120787.
[11]Yan Z, Chen X, Chang H, et al. Feasibility of replacing proton exchange membranes with pressure-driven membranes in membrane electrochemical reactors for high salinity organic wastewater treatment[J]. Water Res, 2024, 254:121340.
[12]Giannakis S, Lin K A, Ghanbari F. A review of the recent advances on the treatment of industrial wastewaters by Sulfate Radical-based Advanced Oxidation Processes (SR-AOPs)[J]. Chem Eng J, 2021,406:127083.
[13]Ji B, Bilal Asif M, Zhang Z. Photothermally-activated peroxymonosulfate (PMS) pretreatment for fouling alleviation of membrane distillation of surface water: Performance and mechanism[J]. Sep Purif  Technoly, 2023,309:123043.
[14]Asif M B, Ji B, Maqbool T, et al. Algogenic organic matter fouling alleviation in membrane distillation by peroxymonosulfate (PMS): Role of PMS concentration and activation temperature[J]. Desalination, 2021,516:115225.
[15]Lou M, Li J, Zhu X, et al. Difunctional MOF-wrapped graphene membranes for efficient photothermal membrane distillation and VOCs interception[J]. J  Membr  Sci, 2023,676:121592.
[16]Yan Z, Chen X, Bao S, et al. Integration of in situ Fenton-like self-cleaning and photothermal membrane distillation for wastewater treatment via Co-MoS2/CNT catalytic membrane[J]. Sep Purif Technol, 2022,303:122207.
[17]Seng R X, Tan L, Lee W P C, et al. Nitrogen-doped carbon quantum dots-decorated 2D graphitic carbon nitride as a promising photocatalyst for environmental remediation: A study on the importance of hybridization approach[J]. J Environ Manag, 2020,255:109936.
[18]肖  萍, 肖  峰, 赵锦辉, 等. 采用膜污染指数评估天然有机物在低压超滤膜中的污染行为[J]. 环境科学, 2012,33(12):4322-4328.
[19]Nguyen A H, Tobiason J E, Howe K J. Fouling indices for low pressure hollow fiber membrane performance assessment[J]. Water Res, 2011,45(8):2627-2637.
[20]Yan Z, Jiang Y, Chen X, et al. Evaluation of applying membrane distillation for landfill leachate treatment[J]. Desalination, 2021,520:115358.
[21]Li B, He X, Wang P, et al. Opposite impacts of K(+) and Ca(2+) on membrane fouling by humic acid and  cleaning process: Evaluation and mechanism investigation[J]. Water Res, 2020,183:116006.
[22]Mi X, Wang P, Xu S, et al. Almost 100 % Peroxymonosulfate Conversion to Singlet Oxygen on Single-Atom  CoN(2+2) Sites[J]. Angew Chem Int Ed Engl, 2021,60(9):4588-4593.
[23]Wiszniowski J, Robert D, Surmacz-Gorska J, et al. Landfill leachate treatment methods: A review[J]. Environ chem lett, 2006,4(1):51-61.
[24]Zhu R, Diaz A J, Shen Y, et al. Mechanism of humic acid fouling in a photocatalytic membrane system[J]. J membr sci, 2018,563:531-540.
[25]姜艳丽. TiO2/Ti催化剂改性及光电催化降解水中腐殖酸的研究[D]. 哈尔滨工业大学, 2007.
[26]Borisover M, Graber E R. Hydration of Natural Organic Matter:  Effect on Sorption of Organic Compounds by Humin and Humic Acid Fractions vs Original Peat Material[J]. Environ sci technol, 2004,38(15):4120-4129.
[27]Miao R, Li X, Wu Y, et al. A comparison of the roles of Ca2+ and Mg2+ on membrane fouling with humic acid: Are there any differences or similarities?[J]. J Membr Sci, 2018,545:81-87.
[28]Yan Z, Yang H, Qu F, et al. Application of membrane distillation to anaerobic digestion effluent treatment: Identifying culprits of membrane fouling and scaling[J]. Sci Total Environ, 2019,688:880-889.
[29]Shao J, Hou J, Song H. Comparison of humic acid rejection and flux decline during filtration with negatively charged and uncharged ultrafiltration membranes[J]. Water res (Oxford), 2011,45(2):473-482.
[30]Zhang L, Tang C, Li M, et al. Identification of key surfactant in municipal solid waste leachate foaming and its influence mechanism[J]. Water Res, 2023,231:119487.
[31]刘锋平, 王占生, 李  薇, 等. 基于三阶段划分的微滤膜污染数学模型[C]// 智能信息技术应用学会, 2011.
张月苗, 冉茂贵, 刘  畅. 膜蒸馏污水处理过程中的有机膜污染行为机制研究[J]. 广东化工, 2023,50(6):63-66.

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