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通过涉及环烷胺单体和均苯三甲酰氯的界面聚合形成的纳滤膜在染料脱盐过程中对氯表现出一定耐受性。

Nanofiltration Membranes Formed through Interfacial Polymerization Involving Cycloalkane Amine Monomer and Trimesoyl Chloride Showing Some Tolerance to Chlorine during Dye Desalination.

作者信息

Ang Micah Belle Marie Yap, Wu Yi-Ling, Chu Min-Yi, Wu Ping-Han, Chiao Yu-Hsuan, Millare Jeremiah C, Huang Shu-Hsien, Tsai Hui-An, Lee Kueir-Rarn

机构信息

R&D Center for Membrane Technology and Department of Chemical Engineering, Chung Yuan Christian University, Taoyuan 32023, Taiwan.

Research Center for Membrane and Film Technology, Department of Chemical Science and Engineering, Kobe University, Rokkodaicho 1-1, Nada, Kobe 657-8501, Japan.

出版信息

Membranes (Basel). 2022 Mar 17;12(3):333. doi: 10.3390/membranes12030333.

DOI:10.3390/membranes12030333
PMID:35323809
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC8954597/
Abstract

Wastewater effluents containing high concentrations of dyes are highly toxic to the environment and aquatic organisms. Recycle and reuse of both water and dye in textile industries can save energy and costs. Thus, new materials are being explored to fabricate highly efficient nanofiltration membranes for fulfilling industrial needs. In this work, three diamines, 1,4-cyclohexanediamine (CHD), ethylenediamine (EDA), and p-phenylenediamine (PPD), are reacted with TMC separately to fabricate a thin film composite polyamide membrane for dye desalination. Their chemical structures are different, with the difference located in the middle of two terminal amines. The surface morphology, roughness, and thickness of the polyamide layer are dependent on the reactivity of the diamines with TMC. EDA has a short linear alkane chain, which can easily react with TMC, forming a very dense selective layer. CHD has a cyclohexane ring, making it more sterically hindered than EDA. As such, CHD's reaction with TMC is slower than EDA's, leading to a thinner polyamide layer. PPD has a benzene ring, which should make it the most sterically hindered structure; however, its benzene ring has a pi-pi interaction with TMC that can facilitate a faster reaction between PPD and TMC, leading to a thicker polyamide layer. Among the TFC membranes, TFC exhibited the highest separation efficiency (pure water flux = 192.13 ± 7.11 L∙m∙h, dye rejection = 99.92 ± 0.10%, and NaCl rejection = 15.46 ± 1.68% at 6 bar and 1000 ppm salt or 50 ppm of dye solution). After exposure at 12,000 ppm∙h of active chlorine, the flux of TFC was enhanced with maintained high dye rejection. Therefore, the TFC membrane has a potential application for dye desalination process.

摘要

含有高浓度染料的废水对环境和水生生物具有高毒性。纺织工业中水和染料的回收再利用可以节约能源和成本。因此,人们正在探索新型材料来制造满足工业需求的高效纳滤膜。在这项工作中,三种二胺,1,4 - 环己二胺(CHD)、乙二胺(EDA)和对苯二胺(PPD),分别与均苯三甲酰氯(TMC)反应,制备用于染料脱盐的复合聚酰胺薄膜。它们的化学结构不同,差异位于两个端胺的中间。聚酰胺层的表面形态、粗糙度和厚度取决于二胺与TMC的反应活性。EDA具有短的直链烷烃链,能够轻松与TMC反应,形成非常致密的选择层。CHD有一个环己烷环,这使其空间位阻比EDA更大。因此,CHD与TMC的反应比EDA慢,导致聚酰胺层更薄。PPD有一个苯环,这应该使其具有最大的空间位阻结构;然而,其苯环与TMC存在π - π相互作用,这可以促进PPD与TMC之间更快的反应,导致聚酰胺层更厚。在这些复合膜中,TFC表现出最高的分离效率(在6巴压力和1000 ppm盐或50 ppm染料溶液条件下,纯水通量 = 192.13 ± 7.11 L∙m∙h,染料截留率 = 99.92 ± 0.10%,NaCl截留率 = 15.46 ± 1.68%)。在12,000 ppm∙h的活性氯暴露后,TFC的通量增加,同时保持了高染料截留率。因此,TFC膜在染料脱盐过程中具有潜在的应用价值。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/dc79/8954597/e5d9a63bc0b0/membranes-12-00333-g007.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/dc79/8954597/bb1c41e50f80/membranes-12-00333-g001.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/dc79/8954597/42d0f573ed85/membranes-12-00333-g002.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/dc79/8954597/f30bd7606248/membranes-12-00333-g003.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/dc79/8954597/44de10c04d33/membranes-12-00333-g004.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/dc79/8954597/7aa4fce3aeeb/membranes-12-00333-g005.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/dc79/8954597/7f5997094f95/membranes-12-00333-g006.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/dc79/8954597/e5d9a63bc0b0/membranes-12-00333-g007.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/dc79/8954597/bb1c41e50f80/membranes-12-00333-g001.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/dc79/8954597/42d0f573ed85/membranes-12-00333-g002.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/dc79/8954597/f30bd7606248/membranes-12-00333-g003.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/dc79/8954597/44de10c04d33/membranes-12-00333-g004.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/dc79/8954597/7aa4fce3aeeb/membranes-12-00333-g005.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/dc79/8954597/7f5997094f95/membranes-12-00333-g006.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/dc79/8954597/e5d9a63bc0b0/membranes-12-00333-g007.jpg

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