电渗析
膜
电容去离子
化学
电解质
化学工程
结垢
图层(电子)
离子交换
镁
二价
无机化学
基质(水族馆)
色谱法
离子
海水淡化
电极
有机化学
生物化学
海洋学
物理化学
工程类
地质学
作者
Young Woo Choi,Naeun Kang,Namjo Jeong,Chan-Soo Kim
出处
期刊:Meeting abstracts
日期:2018-04-13
卷期号:MA2018-01 (30): 1799-1799
标识
DOI:10.1149/ma2018-01/30/1799
摘要
Membrane fouling is one of fatal barriers in electrochemical water treating technologies using ion exchange membranes (IEM) such as electrodeionization (EDI), Electrodialysis (ED), capacitive deionization (CDI), and reverse electrodialysis (RED). Calcium and Magnesium ions are representative foulants which make cake-like scale on the IEMs, leading to high resistance and low durability. In order to minimize membrane fouling in systems using IEMs, we are having developed monovalent cation selective membranes prepared by a layer-by-layer pore-filled technique. Anion exchangeable electrolytes are pore-filled on both surfaces of a semi-pore-filled cation exchange membrane (layer-by-layer). A porous PE substrate (<20 um) is used to be filled with electrolytes and crosslinking agents and to be polymerized. Monovalent cation selectivity against divalent ions, calcium and magnesium ions, of the resulting membranes was evaluated using 1N MgCl 2 , CaCl 2 and NaCl solutions.
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