膜
渗透
化学
乙二醇
甲醇
Nafion公司
乙酸钠
离子交换
化学工程
无机化学
高分子化学
色谱法
有机化学
离子
电化学
电极
物理化学
生物化学
工程类
作者
Jung Min Kim,Breanna M. Dobyns,Rong Zhao,Bryan S. Beckingham
标识
DOI:10.1016/j.memsci.2020.118486
摘要
Multicomponent transport through hydrated dense membranes is utilized in many applications, including photoelectrochemical CO2 reduction cells. One of the main challenges in these devices is to design an ion exchange membrane that minimizes crossover of CO2 reduction products, such as methanol and acetate, while maintaining sufficient ionic conductivity. Previously, the transport behavior of a sulfonated cation exchange membrane, Nafion® 117, to methanol and sodium acetate was investigated and an increase in permeability to sodium acetate was noticed in co-permeation with methanol. To further investigate this transport behavior, a charge-neutral membrane (PEGDA) and a series of sulfonated cation exchange membranes (PEGDA-AMPS) were prepared by varying the poly(ethylene glycol) diacrylate to 2-acrylamido-2-methylpropanesulfonic acid ratio. A distinct increase in permeability to sodium acetate in co-permeation with methanol is observed in co-permeation experiments compared to single solute permeation experiments. We attribute this transport behavior to the shielding of electrostatic repulsion, in which methanol interferes with electrostatic repulsion between acetate and membrane-bound sulfonate anions.
科研通智能强力驱动
Strongly Powered by AbleSci AI