In-situ interfacial polymerization of zwitterionic nanofiltration membranes with anti-scaling performance

Yue Shen , Gilles Van Eygen , Bin Wu , Chao Wu , Ming-Jie Yin , Yan Zhao , Bart Van der Bruggen , Quan-Fu An
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Abstract

Mineral scaling caused by multivalent metal ions can significantly hinder the long-term operation of nanofiltration membranes. In this study, in-situ interfacial polymerization including a posttreatment by using a citric acid solution was employed in order to mitigate scaling on the membrane surface. Under the optimal conditions (15 ​min of posttreatment with a 2 ​M citric acid solution), the membrane water permeance increased from 5.76 ​± ​0.2 to 15.1 ​± ​1.8 ​L⋅m−2⋅h−1·bar−1 for the pristine and the optimal membrane, respectively. The molecular weight cut-off of the optimal membrane was 399 ​Da, which allows for the removal of organic micropollutants in groundwater. Furthermore, the resulting membrane showed a Na2SO4 and CaCl2 rejection of 92.5 ​± ​1.9 and 11.4 ​± ​1.3%, respectively. During the anti-scaling tests, the membrane fabricated with this strategy exhibited a minor decline of the water permeance of 33.5% when subjected to the same water recovery process, opposed to 65.8% for the pristine membrane. This proposed fabricating procedure thus provides an effective strategy for retarding membrane scaling in desalination applications.

Abstract Image

具有抗缩放性能的原位界面聚合齐聚物纳滤膜
多价金属离子造成的矿物结垢会严重阻碍纳滤膜的长期运行。本研究采用了原位界面聚合技术,包括使用柠檬酸溶液进行后处理,以减轻膜表面的结垢。在最佳条件下(用 2 M 柠檬酸溶液进行 15 分钟的后处理),原始膜和最佳膜的透水性分别从 5.76 ± 0.2 升-m-2-h-1-bar-1 提高到 15.1 ± 1.8 升-m-2-h-1-bar-1。最佳膜的截留分子量为 399 Da,可以去除地下水中的有机微污染物。此外,所得膜对 Na2SO4 和 CaCl2 的去除率分别为 92.5 ± 1.9% 和 11.4 ± 1.3%。在防结垢测试中,与原始膜的 65.8% 相比,采用该策略制造的膜在进行相同的水回收过程时,透水性略有下降,降幅为 33.5%。因此,这种拟议的制造程序为海水淡化应用中阻止膜结垢提供了一种有效的策略。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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