Separation of heavy rare-earth elements by non-aqueous solvent extraction: Flowsheet development and mixer-settler tests

被引:31
|
作者
Dewulf, Brecht [1 ]
Riano, Sofia [1 ]
Binnemans, Koen [1 ]
机构
[1] Katholieke Univ Leuven, Dept Chem, Celestijnenlaan 200F,POB 2404, B-3001 Leuven, Belgium
基金
欧盟地平线“2020”;
关键词
Counter-current liquid-liquid extraction; Lanthanides; Process development; Solvometallurgy; ETHYLENE-GLYCOL; PERVAPORATION SEPARATION; IONIC LIQUID; ACID; MIXTURES; SPECIATION; MEMBRANES; RECOVERY; MEDIA; RESIN;
D O I
10.1016/j.seppur.2022.120882
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The separation of rare-earth elements (REEs) is considered one of the most challenging processes in solvent extraction. In recent years, non-aqueous solvent extraction, a unit operation within solvometallurgy, has stepped into the limelight as one of the promising techniques for efficient REEs separation. In this paper, a rare-earth hydroxide concentrate, originating from mining waste and containing mainly heavy rare-earth elements (HREEs), was redissolved in ethylene glycol + 10 vol% water, 0.43 mol L-1 HCl and 0.8 mol L-1 NaCl. Based on batch experiments, a conceptual flowsheet was proposed for the separation of the HREEs into 2 groups: a thulium group (Tm, Yb and Lu) and a dysprosium group (Dy, Ho, Er and Y). Continuous solvent extraction tests in lab-scale mixer-settlers were performed to confirm the technical feasibility of the developed system, as well as to identify and resolve possible bottleneck points. Eventually, using only 16 stages of lab-scale mixer-settlers, the purity of the thulium group and dysprosium group elements, originally 34% and 54%, respectively, reached 99.8% and 98.7%, respectively. Further optimization remains necessary for the separation and purification into highly pure single REEs.
引用
收藏
页数:9
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