浓差极化
电渗析
化学
膜
离子交换
废水
分析化学(期刊)
材料科学
环境工程
色谱法
离子
环境科学
生物化学
有机化学
作者
Sandali Panagoda,Younggy Kim
标识
DOI:10.1016/j.jenvman.2025.126864
摘要
The growing demand for lithium worldwide requires efficient and sustainable recovery strategies to reduce reliance on resource-intensive primary sources like conventional mining and brine extraction. Secondary sources, such as wastewater from spent lithium-ion batteries and industrial wastewater have emerged as viable alternatives for lithium extraction. This study investigates the concentration polarization (CP) near ion-exchange membranes (IEMs) for the selective separation of Li+ over K+ using the difference in the diffusion coefficient. The smaller diffusion coefficient of Li+ (1.03 × 10−9 m2/s) than that of K+ (1.96 × 10−9 m2/s) allowed the selective Li+ separation in shock electrodialysis (SED). A lab-scale SED reactor was built with two cation-exchange membranes (CEMs) to evaluate the effect of the applied voltage, flow rate, and intermembrane distance on Li+ selectivity. A successful Li+ selection (up to a 40.8% increase in the Li+ concentration) was demonstrated in the effluent of the concentrating boundary layer while the effluent of the diluting boundary layer showed a deselection of Li+ (up to a 30.4% decrease in the Li+ concentration). Mathematical model simulations of a ternary system (Li+, K+, Cl-) confirmed the selective Li+ separation in SED due to the diffusivity difference. In the model simulations, the Li+ selection was substantially enhanced with the selectivity of CEM, applied voltage and boundary layer thickness. These findings highlight the potential of SED as a scalable and energy-efficient approach for lithium recovery from secondary sources contributing to resource recycling in the circular economy.
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