电渗析
缩放比例
海水淡化
能源消耗
化学
离子
选择性
体积流量
膜
限制电流
工艺工程
膜技术
电流密度
化学物理
材料科学
限制
水溶液
反渗透
石膏
分析化学(期刊)
过程(计算)
流量(数学)
环境科学
热力学
测距
高效能源利用
能量(信号处理)
化学工程
能量密度
离子键合
消散
作者
Weiyi Pan,Kaiyue Li,Junwei Zhang,Yanghua Duan,Ruoyu Wang,J.E. Dykstra,Menachem Elimelech
标识
DOI:10.1021/acs.est.5c16084
摘要
Electrodialysis (ED) is an electrically driven separation technology that has been widely applied in various industrial sectors (e.g., desalination and food processing). While recent research has focused on developing novel ion-exchange membrane (IEM) materials, the detrimental effects of inorganic scaling in ED systems, particularly on energy consumption and ion selectivity, remain largely overlooked. In this study, we systematically investigated the impact of inorganic scaling (i.e., gypsum) on ED performance under varying operating conditions, including applied current densities ranging from 20% to 100% of the limiting current density and flow rates ranging from 4 to 12 mL min –1 (linear velocities from 0.33 to 1 cm min –1 ). Through precise measurements of input energy, solution composition evolution, and solid-phase characterization, we found that scaling not only increased energy consumption (up to 3-fold compared to nonscaling conditions) but also significantly changed selectivity. Specifically, we found that sodium–calcium and chloride–sulfate selectivities exhibited up to a 7-fold change relative to the initial value when the salt removal from the diluate solution reached approximately 30%. By integrating process modeling with experimental data, we confirmed that these changes in selectivity were directly attributable to gypsum formation on the surface of the IEM. These findings advance our understanding of inorganic scaling effects in ED and offer valuable guidance for optimizing real-world ED operation.
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