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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.
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