Nickel extraction method

Patent metadata

Field	Value
Publication number	US-9725786-B2
Application number	US-201314650364-A
Country	US
Kind code	B2
Filing date	Sep 6, 2013
Priority date	Dec 12, 2012
Publication date	Aug 8, 2017
Grant date	Aug 8, 2017

Abstract

In the present invention, nickel is selectively extracted from an acidic solution that contains a high concentration of manganese. This valuable metal extraction agent is represented by the general formula. In the formula, R 1 and R 2 are alkyl groups that may be the same or different, R 3 is a hydrogen atom or an alkyl group, and R 4 is a hydrogen atom or any group, other than an amino group, bonded to an α carbon atom of an amino acid. The general formula preferably has a glycine unit, a histidine unit, a lysine unit, an aspartic acid unit or a n-methylglycine unit. When extracting nickel by using this extraction agent, it is preferable to adjust the pH of the acidic solution to 2.3 to 5.5 inclusive.

First claim

The invention claimed is:

1. A nickel extraction method, wherein an acid solution containing manganese and nickel is subjected to solvent extraction with an extraction agent comprising an amide derivative represented by the formula:

to extract the nickel from the acid solution;
wherein, R 1 and R 2 are the same or different and each represent a straight or branched alkyl group; and
R 3 represents a hydrogen atom or an alkyl group.

2. The nickel extraction method according to claim 1 , wherein the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 2.3 to 5.5.

3. The nickel extraction method according to claim 1 , wherein the acid solution further contains cobalt and the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of from 2.6 to 3.5.

4. The nickel extraction method according to claim 1 , wherein the acid solution further contains cobalt and the method comprises:
the first separation step in which solvent extraction is carried out with the pH of the acid solution adjusted to 3.5 to 5.0 to separate an organic phase containing nickel and cobalt and an aqueous phase containing manganese, and
the second separation step in which the organic phase after the first separation step is mixed with a starting solution for back extraction adjusted to a pH of 2.6 to 3.5 to separate an organic phase containing nickel and an aqueous phase containing cobalt.

Assignees

• Univ Kyushu Nat Univ Corp
• Sumitomo Metal Mining Co

Inventors

• Goto Masahiro
• Kubota Fukiko
• Baba Yuzo

Classifications

• Y02P10/234

  Cross-Sectional Technologies · mapped topic

• C22B3/44

  by chemical processes (treatment or purification of solutions by liquid-liquid extraction C22B3/26, by ion-exchange extraction C22B3/42) · CPC title

• Y02W30/84

  Recycling of batteries or fuel cells · CPC title

• H01M10/54 Primary

  Reclaiming serviceable parts of waste accumulators · CPC title

• C22B23/0461

  by chemical methods · CPC title