Streamlined lithium-ion battery waste recycling

Patent metadata

Field	Value
Publication number	US-2023387490-A1
Application number	US-202318323631-A
Country	US
Kind code	A1
Filing date	May 25, 2023
Priority date	May 27, 2022
Publication date	Nov 30, 2023
Grant date	—

Abstract

A process for recovering and purifying nickel (Ni), manganese (Mn), cobalt (Co), and lithium (Li) from black mass obtained from recycling of lithium-ion batteries to produce high purity products. The process may include reductive acid leaching, impurity removal, precipitation of valuable metals such as Ni, Co, Mn, and Li. The process may also include recycling of Li compounds as hydroxide or carbonate as a source of alkaline reagent for impurity removal and/or precipitation of the valuable metals.

First claim

What is claimed is:

1 . A method of recovering lithium-ion battery materials from black mass, wherein the method comprises:
acid leaching the black mass in a first stage to produce acid-leached material; and subsequently, applying a reducing agent to the acid-leached material in a second stage.

2 . The method of claim 1 , wherein the reducing agent includes hydrogen peroxide (H 2 O 2 ).

3 . The method of claim 1 , wherein the black mass may include copper (Cu) and aluminum (Al) impurities, and wherein the copper and aluminum impurities can act as reducing agents in the first stage.

4 . The method of claim 1 , wherein the first stage is performed at a first temperature and the second stage is performed at a second temperature, and the second temperature is lower than the first temperature.

5 . The method of claim 1 , wherein valuable metals recovered by the method include one or more of nickel (Ni), manganese (Mn), cobalt (Co), and lithium (Li).

6 . A method of recovering valuable metals from black mass, wherein the method comprises:
performing upstream processes on the black mass; and using a Li basic solution as a reagent in one or more of the upstream processes.

7 . The method of claim 6 , wherein the upstream processes include one or more of impurity removal by chemical precipitation, impurity removal by ion exchange, and mixed or co-precipitation.

8 . The method of claim 6 , further comprising an impurity removal step, and wherein the use of the Li basic solution reduces loss of one or more of Ni, Mn, Co, and Li during the impurity removal step.

9 . The method of claim 6 , wherein the Li basic solution includes an impure solution of lithium hydroxide (LiOH).

10 . The method of claim 6 , wherein the Li basic solution includes an impure solution of lithium carbonate (Li 2 CO 3 ).

11 . A process for recovering and purifying valuable metals from black mass obtained from recycling of lithium-ion batteries, wherein the valuable metals include one or more of Ni, Mn, Co, and Li, and wherein the process comprises:
(a) leaching the black mass to form an acid leached slurry including an acidic pregnant leach solution (PLS) containing the valuable metals and impurities, and an insoluble material; (b) separating the acidic PLS and the insoluble material; (c) adjusting the pH of the acidic PLS for impurity removal to form a pH-adjusted slurry including an impurity precipitate containing the impurities and a pH-adjusted PLS containing the one or more of Ni, Mn, Co, and Li; (d) separating the pH-adjusted PLS and the impurity precipitate; (e) removing residual impurities from the pH-adjusted PLS by adsorption using an ion exchange resin to form a purified PLS containing the valuable metals, wherein the removing includes eluting the adsorbed impurities from the ion-exchange resin using an eluent and regenerating the ion-exchange resin; (f) adjusting the pH of the purified PLS containing the valuable metals using a Li basic solution to form the mixed precipitate slurry, wherein the concentrations of the valuable metals may be adjusted according to the ratio required for a product by adding corresponding sulfates; (g) separating the mixed precipitate containing the valuable metals and a solution containing Li; (h) processing the solution containing Li to produce a basic solution for use in at least one of steps (c), (e), and/or (f); and (i) recovering Li as high-purity Li 2 CO 3 or high-purity LiOH.

12 . The process of claim 11 wherein the black mass includes the valuable metals, graphite, and at least one of iron (Fe), Al, and Cu.

13 . The process of claim 11 wherein the leaching includes a two-stage leaching process including acid leaching with an acid at suitable conditions and reductive leaching with a reducing agent at suitable conditions.

14 . The process of claim 13 in which the acid includes sulfuric acid and the reducing agent includes hydrogen peroxide (H 2 O 2 ).

15 . The process of claim 11 in which the reagent for adjusting the pH includes the Li basic solution.

16 . The process of claim 11 in which the reagent for regenerating the ion exchange resin includes the Li basic solution.

17 . The process of claim 11 in which the reagent for mixed precipitation includes the Li basic solution.

18 . The process of claim 15 , wherein the Li basic solution includes an impure solution of LiOH.

19 . The process of claim 16 , wherein the Li basic solution includes an impure solution of LiOH.

20 . The process of claim 17 , wherein the Li basic solution includes an impure solution of LiOH.

Assignees

• Ii Vi Delaware Inc

Inventors

• Nazari Ghazaleh
• Abrenica Gomer

Classifications

• C22B7/005

  Separation by a physical processing technique only, e.g. by mechanical breaking · CPC title

• H01M10/54 Primary

  Reclaiming serviceable parts of waste accumulators · CPC title

• C22B47/00

  Obtaining manganese · CPC title

• C22B23/0446

  with an ammoniacal liquor or with a hydroxide of an alkali or alkaline-earth metal · CPC title

• C22B23/0461

  by chemical methods · CPC title