Method for separating nickel and cobalt from a solution

Patent metadata

Field	Value
Publication number	US-2020115773-A1
Application number	US-201916713921-A
Country	US
Kind code	A1
Filing date	Dec 13, 2019
Priority date	Jan 10, 2018
Publication date	Apr 16, 2020
Grant date	—

Abstract

A method for separating nickel and cobalt from a solution includes the steps of: obtaining a solution containing nickel and cobalt by acid leaching of a cathode material of a waste lithium-ion battery, adjusting the pH of the solution containing nickel and cobalt to 3.5 to 4.5, adding extractants for extraction to separate the nickel and the cobalt. The cobalt enters the organic phase, the nickel remains in the aqueous phase, and the extractants contain an acidic extractant and an alkaline extractant. The method for efficiently separating nickel and cobalt through extraction adopts a non-saponification extraction method without using NaOH as a saponifier, thereby avoiding the discharge of saponification wastewater. Under acidic conditions, the cobalt in an acidic leaching solution is effectively extracted and separated into the organic phase through synergistic action of the acidic extractant and the alkaline extractant, thereby realizing the separation of nickel from cobalt.

First claim

What is claimed is:

1 . A method for separating nickel and cobalt from a solution, comprising the steps of:
obtaining a solution containing nickel and cobalt by acid leaching of a cathode material of a waste lithium-ion battery, adjusting the pH of the solution containing nickel and cobalt to 3.5 to 4.5, adding extractants for extraction to separate the nickel and the cobalt, wherein the cobalt enters a organic phase, and the nickel remains in am aqueous phase, wherein in the solution, the content of nickel is 0.7 to 1.2 mol/L, the content of cobalt is 0.05 to 0.25 mol/L, the extractants contain an acidic extractant and an alkaline extractant, and the acidic extractant is 2-ethylhexyl dihydrogen phosphate or 2-ethylhexylphosphonic acid mono-2-ethylhexyl ester, and the alkaline extractant is an organic amine with alkyl groups having C 8 , C 9 , C 10 , or a combination therefore, or a mixture thereof.

2 . The method according to claim 1 , wherein the solution containing nickel and cobalt further contains chloride ions, and the concentration of the chloride ions is 2 to 3.5 mol/L.

3 . The method according to claim 1 , wherein the reagent for adjusting the pH of the solution is sodium hydroxide and/or hydrochloric acid.

4 . The method according to claim 1 , wherein in the extractants, the volume ratio of the acidic extractant to the alkaline extractant is (1-9):(9-1).

5 . The method according to claim 4 , wherein in the extractants, the volume ratio of the acidic extractant to the alkaline extractant is (2-4):(6-8).

6 . The method according to claim 4 , wherein the extractants further comprise a diluent, the diluent is kerosene or sulfonated kerosene, and the volume ratio of the sum of the two extractants to the diluent is 1:(2-4).

7 . The method according to claim 1 , wherein the volume ratio of the extractants to the solution is (3-5):1.

8 . The method according to claim 1 , wherein after the extractants for extraction are added, the resultant is shaken and allowed to stand for 8 to 15 min, and the organic phase is separated from the aqueous phase.

9 . The method according to claim 1 , wherein the acidic extractant is 2-ethylhexylphosphonic acid mono-2-ethylhexyl ester, and the alkaline extractant is tri-octyl decyl amine.

10 . The method according to claim 2 , wherein in the extractants, the volume ratio of the acidic extractant to the alkaline extractant is (1-9):(9-1).

11 . The method according to claim 3 , wherein in the extractants, the volume ratio of the acidic extractant to the alkaline extractant is (1-9):(9-1).

12 . The method according to claim 2 , wherein the volume ratio of the extractants to the solution is (3-5):1.

13 . The method according to claim 3 , wherein the volume ratio of the extractants to the solution is (3-5):1.

14 . The method according to claim 2 , wherein after the extractants for extraction are added, the resultant is shaken and allowed to stand for 8 to 15 min, and the organic phase is separated from the aqueous phase.

15 . The method according to claim 3 , wherein after the extractants for extraction are added, the resultant is shaken and allowed to stand for 8 to 15 min, and the organic phase is separated from the aqueous phase.

Assignees

• Univ Beijing Technology

Inventors

• Xi Xiaoli
• Zhang Zhengzheng
• Ma Liwen
• Nie Zuoren

Classifications

• C22B7/007 Primary

  by acid leaching · CPC title

• C22B23/0484 Primary

  in acidic type solutions · CPC title

• C22B3/408

  using a mixture of phosphorus-based acid derivatives of different types · CPC title

• C22B3/282

  Aliphatic amines · CPC title

• C22B3/3846

  Phosphoric acid, e.g. (O)P(OH)3 · CPC title