Lithium recovery from brine using a λ-MnO2/activated carbon hybrid supercapacitor system

被引:181
作者
Kim, Seoni [1 ]
Lee, Jaehan [1 ]
Kang, Jin Soo [1 ,2 ]
Jo, Kyusik [1 ]
Kim, Seonghwan [1 ]
Sung, Yung-Eun [1 ,2 ]
Yoon, Jeyong [1 ]
机构
[1] Seoul Natl Univ, Sch Chem & Biol Engn, Seoul 151742, South Korea
[2] Inst for Basic Sci Korea, Ctr Nanoparticle Res, Seoul 151742, South Korea
关键词
Lithium recovery; lambda-MnO2; Activated carbon; Hybrid supercapacitor; ION BATTERY; HIGH-ENERGY; ADSORBENT; ADSORPTION; EXTRACTION; STABILITY; CHLORIDE; POWER;
D O I
10.1016/j.chemosphere.2015.01.024
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Lithium is one of the most important elements in various fields including energy storage, medicine manufacturing and the glass industry, and demands for lithium are constantly increasing these days. The lime soda evaporation process using brine lake water is the major extraction method for lithium, but this process is not only inefficient and time-consuming but also causes a few environmental problems. Electrochemical recovery processes of lithium ions have been proposed recently, but the better idea for the silver negative electrodes used in these systems is required to reduce its cost or increase long term stability. Here, we report an electrochemical lithium recovery method based on a lambda-MnO2/activated carbon hybrid supercapacitor system. In this system, lithium ions and counter anions are effectively captured at each electrode with low energy consumption in a salt solution containing various cationic species or simulated Salar de Atacama brine lake water in Chile. Furthermore, we designed this system as a flow process for practical applications. By experimental analyses, we confirmed that this system has high selectivity and long-term stability, with its performance being retained even after repetitive captures and releases of lithium ions. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:50 / 56
页数:7
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