1. Three-chamber electrochemical reactor for selective lithium extraction from brine.
- Author
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Feng Y, Park Y, Hao S, Fang Z, Terlier T, Zhang X, Qiu C, Zhang S, Chen F, Zhu P, Nguyen Q, Wang H, and Biswal SL
- Abstract
Efficient lithium recovery from geothermal brines is crucial for the battery industry. Current electrochemical separation methods struggle with the simultaneous presence of Na
+ , K+ , Mg2+ , and Ca2+ because these cations are similar to Li+ , making it challenging to separate effectively. We address these challenges with a three-chamber reactor featuring a polymer porous solid electrolyte in the middle layer. This design improves the transference number of Li+ (tLi + ) by 2.1 times compared to the two-chamber reactor and also reduces the chlorine evolution reaction, a common side reaction in electrochemical lithium extraction, to only 6.4% in Faradaic Efficiency. Employing a lithium-ion conductive glass ceramic (LICGC) membrane, the reactor achieved high tLi + of 97.5% in LiOH production from simulated brine, while the concentrations of Na+ K+ , Mg2+ , and Ca2+ are below the detection limit. Electrochemical experiments and surface analysis elucidated the cation transport mechanism, highlighting the impact of Na+ on Li+ migration at the LICGC interface., Competing Interests: Competing interests statement:Y.F., Z.F., H.W., and S.L.B. are inventors on a provisional United States patent application titled “Electrochemical Manufacturing of Lithium Hydroxide from Geothermal Brines in a Three-chamber Solid Electrolyte Reactor using a LICGC membrane” for the technology related to this work.- Published
- 2024
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