详细信息
Further investigation into lithium recovery from salt lake brines with different feed characteristics by electrodialysis ( SCI-EXPANDED收录 EI收录)
文献类型:期刊文献
英文题名:Further investigation into lithium recovery from salt lake brines with different feed characteristics by electrodialysis
作者:Nie, Xiao-Yao[1];Sun, Shu-Ying[1];Song, Xingfu[1];Yu, Jian-Guo[1]
机构:[1]East China Univ Sci & Technol, Natl Engn Res Ctr Integrated Utilizat Salt Lake R, Shanghai 200237, Peoples R China
年份:2017
卷号:530
起止页码:185
外文期刊名:JOURNAL OF MEMBRANE SCIENCE
收录:;EI(收录号:20170903396804);WOS:【SCI-EXPANDED(收录号:WOS:000397699100020)】;
基金:The research was supported by Natural Science Foundation of China (U1407120) and the National 863 Program (2012AA061601).
语种:英文
外文关键词:Electrodialysis; Brine; Lithium recovery; High salinity system
摘要:Although lithium resources are abundant in the salt lakes located in West China, the majority of these resources have a high Mg/Li ratio, which is problematic because traditional precipitation methods are unsuitable for lithium recovery from this type of brine. In our previous work, constant-current electrodialysis (ED) was applied to comprehensively investigate the effects of operating conditions on the Li+/Mg2+ separation, however, the experimental study considering the feed characteristic diversity and the theoretical analysis of the ionic transfer process considering the feed composition complexity were remained to be perfected. This work focused on resolving the remained questions therein. Initially, we determined the ion-exchange isotherm of the CSO membrane. The selective affinity towards divalent cation was validated, which laid the foundation for the development of the electric double layer (EDL). Then, we investigated the effects of applied voltage on the separation performance and optimized the power mode. The constant-voltage was verified to be a superior power mode compared to the constant-current applied in our previous work. Thereafter, the feed solutions characterized by different Mg/Li ratios, Na/Li ratios, and sulfate concentrations were treated by constant voltage ED, wherein the partitioning principle was further explained via a thermodynamic analysis of the aqueous species distribution of ions. The results showed that in a high-salinity aqueous system, mass transfer was significantly affected by the complexity of the ions' existing forms, which notably determined the steric hindrance and charge effect. As a specific transfer phenomenon, we found that sulfate ions provided large benefit to lithium recovery in the salt lake brine system. A natural brine experiment also showed that lithium recovery can be effectively achieved by ED. These observations indicated that ED has a wide adaptability for lithium recovery from brines with different feed characteristics.
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