Wet process for recovering valuable metals from lithium battery

Patent metadata

Field	Value
Publication number	US-12559379-B2
Application number	US-202318212177-A
Country	US
Kind code	B2
Filing date	Jun 20, 2023
Priority date	Aug 17, 2021
Publication date	Feb 24, 2026
Grant date	Feb 24, 2026

Abstract

The present disclosure discloses a wet process for recovering valuable metals from a lithium battery. In the method, a waste lithium battery powder is subjected to selective leaching under the condition that a hydrogen sulfide gas is introduced through pressurization, such that Mn 2+ , Li + , and Al 3+ metal ions enter a first-stage leaching liquor and nickel, cobalt, copper, and iron exist in a first-stage leaching residue in the form of a sulfide; then a pH of the first-stage leaching liquor is adjusted to remove aluminum and manganese, which achieves extremely thorough metal separation and leads to relatively pure products; a first-stage leaching residue is subjected to leaching in an acid liquor under a negative pressure, such that the sulfides of nickel, cobalt, iron, and copper are dissolved in a second-stage leaching liquor, and a hydrogen sulfide gas produced can be recycled in the first-stage leaching procedure through pressurization.

First claim

The invention claimed is:

1 . A wet process for recovering valuable metals from a lithium battery, comprising the following steps:
subjecting a waste lithium battery powder to first-stage leaching in a first acid liquor introduced with a hydrogen sulfide gas, and conducting solid-liquid separation to obtain a first-stage leaching residue and a first-stage leaching liquor; wherein a solid-to-liquid ratio of the waste lithium battery powder to the first acid liquor is 100 to 250 g/L; and the first-stage leaching is conducted at a temperature of 20-90° C., a pH of 3.0-3.5, and a pressure of 0-6 MPa; adjusting the pH of the first-stage leaching liquor with an alkali liquor to sequentially remove aluminum and manganese to obtain a lithium-containing filtrate; wherein a process of the sequentially removing aluminum and manganese is: adjusting the pH with the alkali liquor to 5.0-5.5 first, and conducting solid-liquid separation to obtain a filtrate containing manganese and lithium, and an aluminum residue; and further adjusting the pH of the filtrate with the alkali liquor to 10.5-11.0, and conducting solid-liquid separation to obtain a lithium-containing filtrate and a manganese residue; adding sodium carbonate to the lithium-containing filtrate, then conducting a solid-liquid separation to obtain lithium carbonate and a salt-containing wastewater; adding a second acid liquor to the first-stage leaching residue for second-stage leaching, and conducting a solid-liquid separation to obtain a second-stage leaching liquor containing nickel and cobalt ions; adding iron powder to the second-stage leaching liquor, conducting a solid-liquid separation to remove a copper residue; adding an oxidant to a resulting copper-removing second-stage leaching liquor, adjusting the pH to 3.5-4.0, and conducting a solid-liquid separation to remove an iron residue to obtain a solution of nickel salt and cobalt salt.

2 . The method according to claim 1 , wherein a solid-to-liquid ratio of the first-stage leaching residue to the second acid liquor is 200 to 500 g/L; the second acid liquor has a concentration of 0.1-6.0 mol/L; and the second-stage leaching is conducted at a temperature of 30-180° C. and a pressure of −0.2˜−0.01 MPa.

3 . The method according to claim 1 , wherein hydrogen sulfide produced in the second-stage leaching is subjected to recycle use in the first-stage leaching.

4 . The method according to claim 3 , wherein a molar ratio of the iron powder to the copper ions in the second-stage leaching liquor is (1.0-1.1):1.

5 . The method according to claim 3 , wherein the oxidant is one or more selected from the group consisting of oxygen, hydrogen peroxide, and persulfuric acid.

6 . The method according to claim 3 , wherein after the oxidant is added, the pH is adjusted using one or more selected from the group consisting of a hydroxide, a carbonate, and an oxide of nickel or cobalt to remove iron.

Assignees

• Guangdong Brunp Recycling Technology Co Ltd
• Hunan Brunp Recycling Tech Co Ltd
• Hunan Brunp Ev Recycling Co Ltd

Inventors

• Xie Yinghao
• Yu Haijun
• Li Aixia
• Zhang Xuemei
• Li Changdong

Classifications

• H01M10/54

  Reclaiming serviceable parts of waste accumulators · CPC title

• C22B47/00

  Obtaining manganese · CPC title

• C22B26/12 Primary

  Obtaining lithium · CPC title

• C22B23/043

  Sulfurated acids or salts thereof · CPC title

• C22B21/0023

  from waste materials · CPC title