Preparation of PVDF/SiC hydrophobic/hydrophilic Janus composite membrane and its performance in the treatment of acidic wastewater by membrane distillation |
Authors: JIAN Kejie, FANG Minfeng, WU Xin, LI Jun, SUN Yiran, RAO Pinhua, LI Guanghui |
Units: 1. Innovation Center for Environment and Resources, College of Chemistry and Chemical Engineering, Shanghai University of Engineering Science, Shanghai 201620, China; 2. Petroleum and Chemical Industry Key Laboratory of Silicon Carbide Ceramic Membrane, Shanghai University of Engineering Science, Shanghai 201620, China; 3. Zhejiang Motonghuihai Technology Development Co., Ltd., Huzhou 313000, China |
KeyWords: Janus composite membrane; silicon carbide microfiltration membrane; poly(vinylidene fluoride); non-solvent induced phase separation; direct contact membrane distillation; acidic wastewater |
ClassificationCode:TQ028.3; TQ09; X703.1 |
year,volume(issue):pagination: 2024,44(4):157-169 |
Abstract: |
This article focuses on the treatment and resource reuse of acidic wastewater using direct contact membrane distillation (DCMD) technology. In response to the problems of low mechanical stability and low flux of traditional distillation membranes, a hydrophobic polyvinylidene fluoride (PVDF) porous thin layer was constructed on the surface of hydrophilic silicon carbide (SiC) microfiltration membrane using tape casting and non-solvent induced phase separation (NIPS) methods, and a PVDF/SiC hydrophobic/hydrophilic bilayer Janus composite membrane with asymmetric wettability was prepared for the study of its performance in DCMD. Using N, N-dimethylacetamide (DMAc) as the solvent and a water-ethanol system as a non-solvent coagulation bath, the effects of factors during the membrane preparation process such as PVDF casting solution concentration, the coagulation bath composition, and the coagulation bath temperature on the surface morphology and wetting properties of the PVDF layer were investigated. The performance of the composite membrane in concentrating dilute sulfuric acid and treating synthetic mine drainage by DCMD were studied. The results show that the optimal fabrication conditions are 10% PVDF casting solution by weight and pure ethanol as coagulation bath. The resulting composite membrane had a water contact angle of 140°, a separation layer porosity of 45%, an average pore size of 0.6 μm, and a strong adhesion between the PVDF layer and the SiC support. Using the composite membrane in DCMD, the permeation flux of water in the concentration of 10% by weight (107 g/L) dilute sulfuric acid solution and the treatment of synthetic mine drainage both reached above 10 L/(m2?h), and the rejection rate of non-aqueous components both reached nearly 100% as well. It also showed long-term operational stability, demonstrating potential application for treating acidic wastewater by DCMD. |
Funds: |
国家自然科学基金青年项目(22306025);上海市地方院校能力建设项目(21010501400);上海市“科技创新行动计划”启明星项目(扬帆专项)(23YF1415400)。 |
AuthorIntro: |
菅珂婕(1998-),女,河南省商丘人,硕士研究生,研究方向为膜材料和膜分离技术;E-mail:18339186637@163.com |
Reference: |
[1] Ballester A, Castro L, Costa M C, et al. Design of remediation pilot plants for the treatment of industrial metal-bearing effluents (BIOMETAL DEMO project): Lab tests[J]. Hydrometallurgy, 2017, 168: 103-115. [2] Ji R, Liu T J, Kang L L, et al. A review of metallurgical slag for efficient wastewater treatment: Pretreatment, performance and mechanism[J]. J Clean Prod, 2022, 380:135076. [3] 袁加巧, 柏少军, 毕云霄等. 国内外矿山酸性废水治理与综合利用研究进展[J]. 有色金属工程, 2022, 12(4): 131-139. [4] Hajihashemi S, Rajabpoor S, Schat H. Acid mine drainage (AMD) endangers pomegranate trees nearby a copper mine[J]. Sci Total Environ, 2023, 889: 164269. [5] Xia S, Song Z, Zhao X, et al. Review of the recent advances in the prevention, treatment, and resource recovery of acid mine wastewater discharged in coal mines[J]. J Water Process, 2023, 52: 103555. [6] 杜实之. 矿山酸性废水处理技术的研究进展[J]. 当代化工研究, 2022(14) : 58-63. [7] Kesieme U, Chrysanthou A, Catulli M, et al. A review of acid recovery from acidic mining waste solutions using solvent extraction[J]. J Chem Technol Biotechnol, 2018, 93 (12): 3374-3385. [8] Range B M K, Hawboldt K A. Review: Removal of thiosalt/sulfate from mining effluents by adsorption and ion exchange[J]. Miner Process Extr Metall Rev, 2018, 40 (2): 79-86. [9] Qasim M, Samad I U, Darwish N A, et al. Comprehensive review of membrane design and synthesis for membrane distillation[J]. Desalination, 2021, 518:115168. [10] 唐浩铭, 孙国富, 王卫东等. 膜蒸馏用疏水膜材料的研究进展[J]. 山东化工, 2021, 50( 3): 101-103+108. [11] Feng S, Zhong Z, Wang Y, et al. Progress and perspectives in PTFE membrane: Preparation, modification, and applications[J]. J Membr Sci, 2018, 549: 332-349. [12] Liu Y, Xiao T, Bao C, et al. Performance and fouling study of asymmetric PVDF membrane applied in the concentration of organic fertilizer by direct contact membrane distillation (DCMD)[J]. Membranes, 2018, 8 (1): 9. [13] Pagliero M, Comite A, Soda O, et al. Effect of support on PVDF membranes for distillation process[J]. J Membr Sci, 2021, 635: 119528. [14] Hotza D, Di Luccio M, Wilhelm M, et al. Silicon carbide filters and porous membranes: A review of processing, properties, performance and application[J]. J Membr Sci, 2020, 610:118193. [15] Ramlow H, Ferreira R K M, Marangoni C, et al. Ceramic membranes applied to membrane distillation: A comprehensive review[J]. Int J Appl Ceram Technol, 2019, 16 (6): 2161-2172. [16] Zou D, Fan Y. State-of-the-art developments in fabricating ceramic membranes with low energy consumption[J]. Ceram Int, 2021, 47 (11): 14966-14987. [17] 王俊伟, 徐鑫. 膜蒸馏用多孔陶瓷膜的疏水改性[J]. 现代技术陶瓷, 2020, 41( 3): 171-185. [18] Pagliero M, Bottino A, Comite A, et al. Silanization of tubular ceramic membranes for application in membrane distillation[J]. J Membr Sci, 2020, 601:117911. [19] Foureaux A F S, Moreira V R, Lebron Y a R, et al. Direct contact membrane distillation as an alternative to the conventional methods for value-added compounds recovery from acidic effluents: A review[J]. Sep Purif Technol, 2020, 236:116251. [20] Xiao T, Wang P, Yang X, et al. Fabrication and characterization of novel asymmetric polyvinylidene fluoride (PVDF) membranes by the nonsolvent thermally induced phase separation (NTIPS) method for membrane distillation applications[J]. Journal of Membrane Science, 2015, 489: 160-174. [21] 国家市场监督管理总局, 中国国家标准化管理委员会. GB/T 9286-2021, 色漆和清漆 划格试验[S]. 北京: 中国标准出版社, 2021. [22] Pagliero M, Bottino A, Comite A, et al. Novel hydrophobic PVDF membranes prepared by nonsolvent induced phase separation for membrane distillation[J]. Journal of Membrane Science, 2020, 596: 117575. [23] Venault A, Ballad M R B, Huang Y-T, et al. Antifouling PVDF membrane prepared by VIPS for microalgae harvesting[J]. Chem Eng Sci, 2016, 142: 97-111. [24] Jung J T, Kim J F, Wang H H, et al. Understanding the non-solvent induced phase separation (NIPS) effect during the fabrication of microporous PVDF membranes via thermally induced phase separation (TIPS)[J]. J Membr Sci, 2016, 514: 250-263. [25] Haponska M, Trojanowska A, Nogalska A, et al. PVDF membrane morphology-influence of polymer molecular weight and preparation temperature[J]. Polymers (Basel), 2017, 9 (12): 718. [26] Almarzooqi F A, Bilad M R, Arafat H A. Development of PVDF membranes for membrane distillation via vapour induced crystallisation[J]. Eur Polym J, 2016, 77: 164-173. [27] Zhang J, Ding Q, Xu Q, et al. An ultra-robust fabric-embedded PVDF membrane fabricated by NTIPS method and its application for monosodium glutamate concentration in membrane distillation[J]. Journal of Membrane Science, 2021, 635: 119448. [28] 国家环境保护总局. GB 8978-1996, 污水综合排放标准[S]. 北京: 中国标准出版社, 1996. [29] 环境保护部, 国家质量监督检验检疫总局. GB 25467-2010, 铜、镍、钴工业污染物排放标准[S]. 北京: 中国环境科学出版社, 2010. [30] Zoungrana A, Çakmakci M, Zengin ? H, et al. Treatment of metal-plating waste water by modified direct contact membrane distillation[J]. Chem Pap, 2016, 70 (9): 1185-1195. [31] Chen G, Tan L, Xie M, et al. Direct contact membrane distillation of refining waste stream from precious metal recovery: Chemistry of silica and chromium (III) in membrane scaling[J]. J Membr Sci, 2020, 598: 117803. [32] Jimenez Y P, Ulbricht M. Recovery of water from concentration of copper mining effluents using direct contact membrane distillation[J]. Ind Eng Chem Res, 2019, 58 (42): 19599-19610. [33] Hull E J, Zodrow K R. Acid rock drainage treatment using membrane distillation: impacts of chemical-free pretreatment on scale formation, pore wetting, and product water quality[J]. Environ. Sci. Technol, 2017, 51 (20): 11928-11934. [34] Afsari M, Jiang J, Phuntsho S, et al. Ammonia recovery from source-separated hydrolyzed urine via a dual-membrane distillation in-series process[J]. Chem Eng J, 2023: 144215. [35] Marques D S, Raynel G, Al-Saeed D, et al. Effects of sour oilfield produced water on direct contact membrane distillation systems[J]. Mater Chem Phys, 2022, 277: 125593. [36] Kesieme U K, Aral H. Application of membrane distillation and solvent extraction for water and acid recovery from acidic mining waste and process solutions[J]. J Environ Chem Eng, 2015, 3 (3): 2050-2056. [37] Foureaux A F S, Moreira V R, Lebron Y a R, et al. A sustainable solution for fresh-water demand in mining sectors: Process water reclamation from POX effluent by membrane distillation[J]. Sep Purif Technol, 2021, 256: 117797. |
Service: |
【Download】【Collect】 |
《膜科学与技术》编辑部 Address: Bluestar building, 19 east beisanhuan road, chaoyang district, Beijing; 100029 Postal code; Telephone:010-80492417/010-80485372; Fax:010-80485372 ; Email:mkxyjs@163.com
京公网安备11011302000819号