Zwitterion membranes for selective cation separation via electrodialysis

被引:36
作者
Ul Afsar, Noor [1 ]
Ge, Xiaolin [1 ]
Zhao, Zhang [1 ]
Hussain, Arif [1 ]
He, Yubin [1 ]
Ge, Liang [1 ,2 ]
Xu, Tongwen [1 ]
机构
[1] Univ Sci & Technol China, iCHEM Collaborat Innovat Ctr Chem Energy Mat, Sch Chem & Mat Sci, Dept Appl Chem,CAS Key Lab Soft Matter Chem, Hefei 230026, Peoples R China
[2] Univ Sci & Technol China, Appl Engn Technol Res Ctr Funct Membranes, Inst Adv Technol, Hefei 230088, Peoples R China
基金
中国国家自然科学基金;
关键词
Zwitterion membranes; Electrodialysis; Cation separation; Lithium extraction; Permselectivity; Crosslinking; ANION-EXCHANGE MEMBRANE; ELECTROCHEMICAL CHARACTERIZATION; CROWN-ETHER; FREE-ENERGY; LITHIUM; ION; POLYELECTROLYTE; PERFORMANCE; RECOVERY; PERMSELECTIVITY;
D O I
10.1016/j.seppur.2020.117619
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Lithium extraction from saline water by electrodialysis is an energy-efficient process. Herein, we examined a synergetic impact of amino isophthalic acid (AIPA) and the fixed quaternized groups to produce stable, cost-effective, and efficient zwitterion membranes (ZIMs) via a sol-gel process. We developed different membranes such as QAIPA-10, QAIPA-15, and QAIPA-20 by varying the amount of AIPA from 10 to 20 wt% in the base membrane. It was found that when the amount of AIPA increases, the Li+ flux also improved from 1.66 x 10(-10) mol cm(-2) s(-1) to 33.46 x 10(-10) mol cm(-2) s(-1), respectively. By comparing the membranes based on the various amounts of AIPA, the membrane with 20 wt% (QAIPA-20) had a higher Li+ flux and reasonable permselectivity due to the high WU, CEC as compared with the QAIPA-10, QAIPA-15 and base membranes. To further explore the performance of the QAIPA-20, we also studied various cation systems such as Na+/Mg2+, K+/Mg2+, and H+/Fe2+, respectively. The obtained results proved that AIPA strongly dictates the cation transport channels, hydrophilicity, and repulsive centers of the ZIMs. We may conclude that QAIPA-20 is effective for lithium extraction, water desalination, and acid recovery.
引用
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页数:8
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