电渗析
膜
材料科学
卤水
化学工程
单体
离子交换
离子
多孔性
制作
选择性
离子运输机
半透膜
大规模运输
聚合物
分离过程
反应性(心理学)
醛
工作(物理)
正渗透
膜结构
多孔介质
聚合膜
焊剂(冶金)
溶解
纳滤
纳米技术
合成膜
无机化学
反向电渗析
色谱法
作者
Dingdong Chai,Wenguang Wang,Fengqi Yu,Tengfang Zhang,Dehao Yu,Yuhao Chen,Yang Zhang,Haixiang Sun
摘要
ABSTRACT Electric‐driven membranes featuring precise ion transport are extensively employed in energy and environmental science. Although separation performance has been significantly improved, the structural requirements for treating high‐salinity salt‐lake brines via selective electrodialysis (S‐ED) remain ambiguous. Herein, we exploit the differential reactivity of carboxyl and aldehyde groups in D‐glucuronic acid toward the abundant amino groups of polyethyleneimine. Combined with the monomer sustained‐release effect of the porous TpPa interlayer, this approach enables the construction of a biomimetic separation layer that possesses a dense surface and continuous internal Li + ‐conducting channels. These continuous pathways, rich in carboxyl moieties, enlarge the activation free‐energy barrier difference for Li + and Mg 2+ transport from 4.03 to 4.94 kJ·mol −1 . Such energetic differentiation emulates biological ion channels, wherein carboxyl groups selectively promote Li + transit while imposing a pronounced energetic penalty on heavily hydrated Mg 2+ . Consequently, the membrane exhibits cell‐membrane‐mimetic selectivity, delivering a Li + /Mg 2+ perm‐selectivity of 22.7 and a Li flux of 4.88 × 10 −8 mol·cm −2 ·s −1 , outperforming the current upper‐bound benchmark. Notably, the step‐current S‐ED process attains 78.45% Li + recovery from a simulated brine containing 106.74 g/L Mg 2+ and a Mg/Li mass ratio of 31.58. This work provides new insights into S‐ED membrane fabrication and process design for practical scalability.
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