Multistage-batch bipolar membrane electrodialysis for base production from high-salinity wastewater

被引:8
|
作者
Hussain, Arif [1 ]
Yan, Haiyang [1 ]
Ul Afsar, Noor [1 ]
Jiang, Chenxiao [1 ]
Wang, Yaoming [1 ]
Xu, Tongwen [1 ]
机构
[1] Univ Sci & Technol China, Sch Chem & Mat Sci, Dept Appl Chem, Anhui Prov Engn Lab Funct Membrane Sci & Technol, Hefei 230026, Peoples R China
基金
中国国家自然科学基金;
关键词
bipolar membrane electrodialysis; multistage-batch; base production; high-salinity wastewater; INNOVATIVE BENEFICIAL REUSE; ANION-EXCHANGE; NANOFILTRATION MEMBRANES; DESALINATION; TECHNOLOGIES; ACID; TRANSPORT; SELECTIVITY; RECOVERY; MODEL;
D O I
10.1007/s11705-021-2114-2
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Bipolar membrane electrodialysis (BMED) is considered a state-of-the-art technology for the conversion of salts into acids and bases. However, the low concentration of base generated from a traditional BMED process may limit the viability of this technology for a large-scale application. Herein, we report an especially designed multistage-batch (two/three-stage-batch) BMED process to increase the base concentration by adjusting different volume ratios in the acid (V-acid), base (V-base), and salt compartments (V-salt). The findings indicated that performance of the two-stage-batch with a volume ratio of V-acid: V-base:V-salt = 1:1:5 was superior in comparison to the three-stage-batch with a volume ratio of V-acid:V-base:V-salt = 1:1:2. Besides, the base concentration could be further increased by exchanging the acid produced in the acid compartment with fresh water in the second stage-batch process. With the two-stage-batch BMED, the maximum concentration of the base can be obtained up to 3.40 mol.L-1, which was higher than the most reported base production by BMED. The low energy consumption and high current efficiency further authenticate that the designed process is reliable, cost-effective, and more productive to convert saline water into valuable industrial commodities.
引用
收藏
页码:764 / 773
页数:10
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