Recovery of lithium from Uyuni salar brine

被引:386
作者
An, Jeon Woong [2 ]
Kang, Dong Jun [2 ]
Khuyen Thi Tran [1 ]
Kim, Myong Jun [1 ]
Lim, Tuti [3 ]
Tam Tran [1 ]
机构
[1] Chonnam Natl Univ, Dept Energy & Resources Engn, Kwangju, South Korea
[2] Korea Resources Corp, Technol Res Inst, Seoul, South Korea
[3] Ngee Ann Polytech, Sch Life Sci & Chem Technol, Singapore, Singapore
关键词
Uyuni salar brine; High purity lithium carbonate; Removal of magnesium and sulphate; Calcium; Boron; MAGNESIUM-HYDROXIDE PRECIPITATION; KINETICS; LI2CO3; WASTE;
D O I
10.1016/j.hydromet.2012.02.008
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
A hydrometallurgical process was developed to recover lithium from a brine collected from Salar de Uyuni, Bolivia, which contains saturated levels of Na, Cl and sulphate, low Li (0.7-0.9 g/L Li) and high Mg (15-18 g/L Mg). Unlike other commercial salar brines currently being processed, the high levels of magnesium and sulphate in Uyuni brine would create difficulties during processing if conventional techniques were used. A two-stage precipitation was therefore first adopted in the process using lime to remove Mg and sulphate as Mg(OH)(2) and gypsum (CaSO4 center dot 2H(2)O). Boron (at 0.8 g/L in the raw brine), a valuable metal yet deleterious impurity in lithium products, could also be mostly recovered from the brine by adsorption at a pH lower than pH11.3 in this first stage. The residual Mg and Ca (including that added from lime) which were subsequently precipitated as Ca-Mg oxalate could be roasted to make dolime (CaO.MgO) for re-use in the first stage of precipitation. Evaporation of the treated brine up to 30 folds would produce 20 g/L Li liquors. The salt produced during evaporation was a mixture of NaCl and KCl, containing acceptable levels of sulphate, Mg, Ca, etc. The final precipitation of lithium at 80-90 degrees C produced a high purity (99.55%) and well crystalline lithium carbonate. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:64 / 70
页数:7
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