Rare earth and zinc extraction and separation method in stripping raffinate of europium by reduction extraction
An anti-raffinate and separation method technology, applied in rare earth metal compounds, chemical instruments and methods, liquid solution solvent extraction, etc., can solve the problems of easy formation of colloids, cumbersome operation procedures, difficult filtration, etc., to improve the separation capacity. , The effect of improving the extraction rate of rare earth ions and reducing the extraction rate of Zn2+
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Embodiment 1
[0014] The back raffinate for reducing and extracting europium is a mixed solution of rare earth chloride and zinc chloride. 4 After Cl is used as the feed liquid, NH in the feed liquid 4 Cl concentration is 3mol / L, rare earth chloride concentration is 0.7mol / L, ZnCl 2 The concentration is 0.4942mol / L, the acidity is 0.15mol / L, the rare earth chloride contains Sm 2 o 3 63.44%, Eu 2 o 3 11.06%, Gd 2 o 3 is 25.5%, and the organic phase consists of 1.5mol / LP 507 - Composition of kerosene, saponification degree is 0.54mol / L, with addition of NH 4 ClGdCl 3 The solution is used as a wash solution, and the NH in the wash solution 4 Cl concentration is 3mol / L, GdCl 3 The concentration is 0.15mol / L, the acidity is 0.15mol / L, the number of extraction stages is 15 stages in the extraction section, and 15 stages in the washing section. The raffinate and the organic phase loaded with rare earth, the raffinate containing zinc is used as the raw material for the preparation of zin...
Embodiment 2
[0016] The back raffinate for reducing and extracting europium is a mixed solution of rare earth chloride and zinc chloride. 4 After Cl is used as the feed liquid, NH in the feed liquid 4 Cl concentration is 3mol / L, rare earth chloride concentration is 0.6071mol / L, ZnCl 2 The concentration is 0.2698mol / L, the acidity is 0.15mol / L, the rare earth chloride contains Sm 2 o 3 63.44%, Eu 2 o 3 11.06%, Gd 2 o 3 is 25.5%, and the organic phase consists of 1.5mol / LP 507 - Composition of kerosene, saponification degree is 0.54mol / L, with addition of NH 4 ClGdCl 3 The solution is used as a wash solution, and the NH in the wash solution 4 Cl concentration is 3mol / L, GdCl 3 The concentration is 0.15mol / L, the acidity is 0.15mol / L, the number of extraction stages is 15 stages in the extraction section, and 15 stages in the washing section. The raffinate and the organic phase loaded with rare earth, the raffinate containing zinc is used as the raw material for the preparation of ...
Embodiment 3
[0018] The back raffinate for reducing and extracting europium is a mixed solution of rare earth chloride and zinc chloride. 4 After Cl is used as the feed liquid, NH in the feed liquid 4 Cl concentration is 3mol / L, rare earth chloride concentration is 0.5228mol / L, ZnCl 2 The concentration is 0.2108mol / L, the acidity is 0.15mol / L, the rare earth chloride contains Sm2 o 3 63.44%, Eu 2 o 3 11.06%, Gd 2 o 3 is 25.5%, and the organic phase consists of 1.5mol / LP 507 - Composition of kerosene, saponification degree is 0.54mol / L, with addition of NH 4 ClGdCl 3 The solution is used as a wash solution, and the NH in the wash solution 4 Cl concentration is 3mol / L, GdCl 3 The concentration is 0.15mol / L, the acidity is 0.15mol / L, the number of extraction stages is 15 stages in the extraction section, and 15 stages in the washing section. The raffinate and the organic phase loaded with rare earths, the raffinate containing zinc is used as the raw material for the preparation of z...
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