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电流方向调控电渗析中逐层单面涂层离子交换膜的离子传输。

Current Direction Regulates Ion Transport Across Layer-by-Layer One-Side-Coated Ion-Exchange Membranes in Electrodialysis.

作者信息

Elozeiri Alaaeldin A E, Dykstra Jouke E, Lammertink Rob G H, Rijnaarts Huub H M

机构信息

Environmental Technology, Wageningen University & Research, Bornse Weilanden 9, 6708 WG Wageningen, The Netherlands.

Membrane Science and Technology, Faculty of Science and Technology (TNW), University of Twente, Drienerlolaan 5, 7522 NB Enschede, The Netherlands.

出版信息

ACS Appl Mater Interfaces. 2025 Apr 9;17(14):22004-22013. doi: 10.1021/acsami.5c00155. Epub 2025 Mar 30.

Abstract

Polyelectrolyte multilayer (PEM) modified membranes can attain selective ion separations in electrodialysis with several potential applications, such as sustainable brine management. To understand the ion transport across PEM-coated membranes, we coated six different commercial cation-exchange membranes (CEMs) with PEM via the layer-by-layer technique. Coating one side of the membrane with a PEM leads to an asymmetric current-voltage response in case of solutions containing Mg and Ca ions. When the coating faces the counterion transport direction (FT), the coated membrane reaches a limiting current density which does not occur if the applied current is reversed. We investigated these phenomena via several electrochemical techniques. After coating, the total membrane resistance increases significantly at solutions of Mg or Ca (relative to the bare membrane resistance). Furthermore, the transport characteristics of the PEM coating are highly influenced by the base membrane resistance and fixed-charge density. Regarding the counterion type, the resistance of the coated membrane increases in the same order as the bare membrane: K < Na< Ca < Mg. The higher the bare membrane resistance is, the higher the PEM resistance is. The co-ion valency (i.e., monovalent Cl or divalent SO) had limited to insignificant effects on the current-voltage response of the coated membranes. Therefore, dielectric exclusion is insignificant for these coated membranes at the tested concentrations, i.e., 0.25 M SO. Lastly, we employed an ion transport model to explain the observed effect of the current direction on the current-voltage response and analyze the effective properties of the PEM coating.

摘要

聚电解质多层(PEM)修饰膜可在电渗析中实现选择性离子分离,具有多种潜在应用,如可持续盐水管理。为了解离子在PEM涂层膜上的传输情况,我们通过层层技术用PEM涂覆了六种不同的商用阳离子交换膜(CEM)。在含有镁离子和钙离子的溶液中,在膜的一侧涂覆PEM会导致不对称的电流 - 电压响应。当涂层面向反离子传输方向(FT)时,涂覆膜会达到一个极限电流密度,而如果施加电流反向则不会出现这种情况。我们通过几种电化学技术研究了这些现象。涂覆后,在镁离子或钙离子溶液中,总膜电阻相对于裸膜电阻显著增加。此外,PEM涂层的传输特性受基膜电阻和固定电荷密度的影响很大。关于反离子类型,涂覆膜的电阻与裸膜按相同顺序增加:钾离子 < 钠离子 < 钙离子 < 镁离子。裸膜电阻越高,PEM电阻越高。同离子价态(即一价氯离子或二价硫酸根离子)对涂覆膜的电流 - 电压响应影响有限或不显著。因此,在测试浓度即0.25 M硫酸根离子下,介电排斥对这些涂覆膜不显著。最后,我们采用离子传输模型来解释观察到的电流方向对电流 - 电压响应的影响,并分析PEM涂层的有效性能。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/95ce/11986911/721bc8a71730/am5c00155_0001.jpg

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