结垢
聚电解质
膜
化学
聚丙烯酰胺
电渗析
化学工程
膜污染
海水淡化
超滤(肾)
聚合物
纳滤
吸附
水处理
离子交换
离子交换膜
色谱法
离子
高分子化学
有机化学
工程类
生物化学
作者
P.A. Sosa-Fernandez,S.J. Miedema,Harry Bruning,Frans A. M. Leermakers,Jan A. Post,Huub H.M. Rijnaarts
标识
DOI:10.1016/j.jcis.2020.10.077
摘要
Cation exchange membranes (CEMs) are subject to fouling when utilized to desalinate wastewater from the oil and gas industry, hampering their performance. The kind and extent of the fouling are most likely dependent on the composition of the stream, which in practical applications can vary significantly. Fouling experiments were performed on commercial cation exchange membranes, which were used in electrodialysis runs to desalinate solutions of varying composition. The variations included ionic strength, type of ions, amount of viscosifying polyelectrolyte (partially hydrolyzed polyacrylamide), presence of crude oil, and surfactants. Performance parameters, like electric potential and pH, were monitored during the runs, after which the membranes were recovered and analyzed. Fouling was detected on most CEMs and occurred mainly in the presence of the viscosifying polyelectrolyte. Under normal pH conditions (pH ~ 8), the polyelectrolyte fouled the concentrate side of the CEMs, as expected due to electrophoresis. However, by applying a current in the opposite direction, the polyelectrolyte layer could be removed. Precipitation occurred mostly on the opposite side of the membrane, with different morphology depending on the feed composition.
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