Gallium extraction agent and gallium extraction method
US-9803262-B2 · Oct 31, 2017 · US
US10036082B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10036082-B2 |
| Application number | US-201515544079-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 28, 2015 |
| Priority date | Jan 20, 2015 |
| Publication date | Jul 31, 2018 |
| Grant date | Jul 31, 2018 |
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Provided are: an extractant which is capable of quickly and highly efficiently extracting zirconium from an acidic solution that is obtained by acid leaching a material containing zirconium and scandium such as an SOFC electrode material; and a method for extracting zirconium, which uses this extractant. A zirconium extractant according to the present invention is composed of an amide derivative represented by general formula (I). In the formula, R1 and R2 respectively represent the same or different alkyl groups, each of which may be linear or branched; R3 represents a hydrogen atom or an alkyl group; and R4 represents a hydrogen atom or an arbitrary group other than an amino group, said arbitrary group being bonded, as an amino acid, to the α carbon.
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The invention claimed is: 1. A method for extracting zirconium, wherein a first acidic solution containing zirconium or containing zirconium and scandium is subjected to solvent extraction with a zirconium extraction agent consisting of amide derivatives represented by the following general formulas to extract the zirconium from the first acidic solution: wherein R 1 and R 2 each represent the same or different alkyl group, the alkyl group may be a straight chain or a branched chain and R 3 represents a hydrogen atom or an alkyl group. 2. The method for extracting zirconium according to claim 1 , wherein the first acidic solution further contains one or more selected from the group consisting of scandium, titanium, lanthanum and yttrium, and the first acidic solution is subjected to the first solvent extraction with the pH of the acidic solution adjusted to 0.8 or lower. 3. The method for extracting zirconium according to claim 1 , wherein after solvent extraction with the zirconium extraction agent, a second acidic solution having a pH of 0 or higher and 0.5 or lower is mixed with the extraction agent which has extracted the zirconium from the first acidic solution to carry out back extraction, and the extraction agent and the second acidic solution are then separated to separate zirconium and at least one or more components selected from the group consisting of scandium, titanium, lanthanum and yttrium. 4. The method for extracting zirconium according to claim 3 , wherein after the back extraction, a third acidic solution with a pH of 0.8 or higher and 1.5 or lower is brought into contact with the extraction agent to separate zirconium or zirconium and scandium, and one or more components selected from the group consisting of titanium, lanthanum and yttrium, and a fourth acidic solution adjusted to a pH of 0.2 or lower is then mixed with the extraction agent to separate zirconium and scandium. 5. The method for extracting zirconium according to claim 1 , wherein the first acidic solution is obtained by acid dissolution of an electrode material for solid oxide fuel cells. 6. The method for extracting zirconium according to claim 1 , wherein the alkyl group in R 1 and R 2 is a branched chain, and the number of carbons in the alkyl group in R 1 and R 2 is 5 to 11.
Obtaining zirconium or hafnium {(treatment or purification of solutions by liquid-liquid extraction, by ion exchange or by adsorption C22B3/00, C01G25/003, C01G27/003)} · CPC title
Applications, solvents used · CPC title
having the nitrogen atoms of the carboxamide groups bound to hydrogen atoms or to acyclic carbon atoms · CPC title
Carboxylic acids · CPC title
by liquid-liquid extraction using organic compounds · CPC title
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