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电场作用下有机污垢向阴离子交换膜的迁移行为。

Migration behavior of organic foulants toward anion exchange membrane under the electric field.

作者信息

Guo Tiecheng, Xu Daliang, Li Guibai, Tang Xiaobin, Liang Heng

机构信息

State Key Laboratory of Urban Water Resource and Environment, School of Environment, Harbin Institute of Technology, Harbin 150090, China.

State Key Laboratory of Urban Water Resource and Environment, School of Environment, Harbin Institute of Technology, Harbin 150090, China.

出版信息

Water Res. 2025 Sep 1;283:123809. doi: 10.1016/j.watres.2025.123809. Epub 2025 May 11.

Abstract

Anion exchange membrane (AEM) fouling has sparked extensive research, especially on the interaction of foulants with the AEM. However, there is still a lack of clear explanation about how foulants migrate from feedwater to the AEM surface. This study systematically investigated the migration of foulants and influencing factors in electrodialysis (ED). The behavior of negatively charged foulants in ED was found to occur in three stages according to the variety of the rate of diluate conductivity change: blocking by boundary layer, approaching, and arriving at the AEM surface. The results revealed that the membrane was rarely fouled in the first stage, whereas the fouling level significantly increased in the second and stabilized in the third. A limiting conductivity was identified, marking the point where the fouling level began to rise, indicating the transition from the first to subsequent stages. The current value was found to be highly responsible for limiting conductivity (contribution >95 %). Based on that, an operation strategy with low energy consumption and high desalination efficiency was proposed by adjusting the current according to feed water conductivity. This study brings insights into completing the whole fouling behavior and developing anti-fouling strategies for AEM by mitigating foulants' migration, which increases ED desalination performance facing fouling.

摘要

阴离子交换膜(AEM)污染引发了广泛研究,尤其是关于污染物与AEM之间的相互作用。然而,对于污染物如何从给水迁移到AEM表面,仍缺乏清晰的解释。本研究系统地研究了电渗析(ED)中污染物的迁移及影响因素。根据稀释液电导率变化速率的不同,发现ED中带负电荷污染物的行为发生在三个阶段:被边界层阻挡、接近和到达AEM表面。结果表明,在第一阶段膜很少被污染,而在第二阶段污染程度显著增加,并在第三阶段稳定下来。确定了一个极限电导率,它标志着污染程度开始上升的点,表明从第一阶段到后续阶段的转变。发现电流值对极限电导率高度负责(贡献率>95%)。基于此,提出了一种根据进水电导率调整电流的低能耗、高脱盐效率的运行策略。本研究为全面了解整个污染行为以及通过减轻污染物迁移来制定AEM的防污策略提供了见解,这提高了ED面对污染时的脱盐性能。

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