IP Library › Granted Patent US 9,458,526
Granted Patent B2
US 9,458,526 · App. 14/765,307 · Granted Oct 4, 2016

Method for separating impurities from an acidic solution containing nickel and cobalt and/or scandium

Inventors: Masahiro Goto (Fukuoka, JP); Fukiko Kubota (Fukuoka, JP); Yuzo Baba (Fukuoka, JP); Yoshitomo Ozaki (Niihama, JP); Jiro Hayata (Niihama, JP); Tatsuya Higaki (Niihama, JP); Toshihiko Nagakura (Niihama, JP); Shinya Matsumoto (Niihama, JP)
Assignees: Kyushu University, National University Corporation; Sumitomo Metal Mining Co., Ltd.
C22B59/00C22B3/005C22B3/44C22B23/0453C22B23/0461Y02P10/234
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 9,458,526
App. No.
14/765,307
Granted
Oct 4, 2016
Kind
B2
Abstract

Provided is a method for efficiently separating nickel, cobalt and/or scandium, and impurities from an acidic solution containing impurities such as manganese, iron, zinc, and aluminum. A valuable-metal extracting agent of the present invention is expressed by general formula (1). In the formula, R 1 and R 2 each represent the same or different alkyl groups, R 3 represents a hydrogen atom or an alkyl group, and R 4 represents a hydrogen atom or a given group, other than an amino group, that bonds with an α carbon as an amino acid. In general formula (1), the inclusion of a glycine unit, a histidine unit, a lysine unit, an asparagine acid unit, or a normal methylglycine unit is preferred.

Claims (64)

1. A method of subjecting an acid solution containing at least one or more valuable components selected from nickel, cobalt, and scandium and one or more impurities selected from manganese, zinc, iron, aluminum, calcium, chromium, magnesium, copper, lead, sodium, lanthanum, neodymium, molybdenum, vanadium, tin, tungsten, samarium, rhenium, thallium, cerium, titanium, and lutetium to solvent extraction with a valuable metal extraction agent that comprises an amide derivative represented by the following general formula (I) to separate the valuable components and the impurities from the acid solution,

wherein, R 1 and R 2 each represent the same or different alkyl groups;

the alkyl group can be a straight chain or a branched chain;

R 3 represents a hydrogen atom or an alkyl group; and

R 4 represents a hydrogen atom or any group other than an amino group, which is bound to the α carbon as an amino acid.

2. The method according to claim 1 , wherein the amide derivative is any one or more of glycinamide derivatives, histidinamide derivatives, lysinamide derivatives, aspartamide derivatives, and N-methylglycine derivatives.

3. The method according to claim 1 , wherein

the acid solution contains nickel and zinc, and

the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 2.0 to 4.3.

4. The method according to claim 1 , wherein

the acid solution contains nickel and iron,

when the iron is trivalent iron, the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 1.0 to 3.2, and

when the iron is divalent iron, the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 2.0 to 4.5.

5. The method according to claim 1 , wherein

the acid solution contains cobalt and iron,

when the iron is trivalent iron, the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 1.0 to 4.0, and

when the iron is divalent iron, the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 2.0 to 4.5.

6. The method according to claim 1 , wherein

the acid solution contains nickel and aluminum, and

the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 2.0 to 4.5.

7. The method according to claim 1 , wherein

the acid solution contains nickel and/or cobalt and calcium, and

the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 2.0 to 4.0.

8. The method according to claim 1 , wherein

the acid solution contains cobalt and chromium, and

the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 2.8 to 3.5.

9. The method according to claim 1 , wherein

the acid solution contains nickel, cobalt, and/or scandium, and molybdenum, and

the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 0 to 2.

10. The method according to claim 1 , wherein

the acid solution contains scandium, and divalent iron and/or aluminum, and

the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 1.2 to 4.5.

11. The method according to claim 1 , wherein

the acid solution contains scandium and chromium, and

the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 1.2 to 3.5.

12. The method according to claim 2 , wherein

the acid solution contains nickel and zinc, and

the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 2.0 to 4.3.

13. The method according to claim 2 , wherein

the acid solution contains nickel and iron,

when the iron is trivalent iron, the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 1.0 to 3.2, and

when the iron is divalent iron, the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 2.0 to 4.5.

14. The method according to claim 2 , wherein

the acid solution contains cobalt and iron,

when the iron is trivalent iron, the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 1.0 to 4.0, and

when the iron is divalent iron, the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 2.0 to 4.5.

15. The method according to claim 2 , wherein

the acid solution contains nickel and aluminum, and

the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 2.0 to 4.5.

16. The method according to claim 2 , wherein

the acid solution contains nickel and/or cobalt and calcium, and

the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 2.0 to 4.0.

17. The method according to claim 2 , wherein

the acid solution contains cobalt and chromium, and

the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 2.8 to 3.5.

18. The method according to claim 2 , wherein

the acid solution contains nickel, cobalt, and/or scandium, and molybdenum, and

the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 0 to 2.

19. The method according to claim 2 , wherein

the acid solution contains scandium, and divalent iron and/or aluminum, and

the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 1.2 to 4.5.

20. The method according to claim 2 , wherein

the acid solution contains scandium and chromium, and

the acid solution is subjected to the solvent extraction with the pH of the acid solution adjusted to a range of 1.2 to 3.5.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 12, 2015
From: GOTO, MASAHIRO; KUBOTA, FUKIKO; BABA, YUZO; OZAKI, YOSHITOMO; HAYATA, JIRO; HIGAKI, TATSUYA; NAGAKURA, TOSHIHIKO; MATSUMOTO, SHINYA
To: KYUSHU UNIVERSITY, NATIONAL UNIVERSITY CORPORATION; SUMITOMO METAL MINING CO. LTD.
Reel/Frame 036306/0829 →
Priority Claims (2)
JP 2013-054944 · Mar 18, 2013 · national
JP 2013-098510 · May 8, 2013 · national
Continuity (1)
Related Publication 20160010177A1 · Jan 14, 2016