Ion migration mechanism of electrochemical water softening in dual-chamber reactors and their performance for real circulating cooling water

阳极 阴极 软化 电解 电化学 材料科学 化学 化学工程 分析化学(期刊) 电解质 电极 复合材料 工程类 物理化学 色谱法
作者
Wenda Kang,Jiyuan Xu,Yingxin Xie,Liming Yan,Kun Zhao,Xinying Gong,Hongtao Yu
出处
期刊:Journal of Cleaner Production [Elsevier BV]
卷期号:448: 141700-141700 被引量:1
标识
DOI:10.1016/j.jclepro.2024.141700
摘要

Electrochemical water softening studies often use ion exchange membrane (IEM) reactors. However, their practical application is limited because of inevitable cathodic scaling. To overcome this challenge, one necessary approach is to understand the ion migration mechanism in the typical IEM reactor. In this study, we used operando visualization to reveal that the divider such as IEM or nylon nets was essential to confine the neutralization reaction between H+ and OH−. Ca2+ and Mg2+ may transfer from the anode chamber through the divider into the cathode chamber via electromigration. Using mesh electrodes instead of plate electrodes, the total hardness removal in the cathode chamber and anode chamber was 94.2% and 92.5%, respectively. The high removal rate was attributed to H2 microbubbles produced by cathodic water electrolysis, which drove OH− ions diffusion into solution and sequentially strengthened the nucleation of scale crystals in solution rather than on the cathode surface. On the basis of the above ion migration mechanism, the revolutionized reactor with mesh electrode module and nylon-net divider exhibited good performance in softening real circulating cooling water, and the total hardness removal exceeded 93.1% during 30 h running. These results open new horizons for improving the practicability of electrochemical water softening.
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