Method of recycling a component with rare earth element recovery
US-2024076760-A1 · Mar 7, 2024 · US
US2024352553A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024352553-A1 |
| Application number | US-202218569142-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jun 9, 2022 |
| Priority date | Jun 11, 2021 |
| Publication date | Oct 24, 2024 |
| Grant date | — |
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Methods are disclosed for leaching metal-containing materials, such as those contained in the cathode of spent lithium-ion batteries, using a leach solution of an amino acid and a reducing agent. The metal-containing material is treated with the leach solution to recover at least one metal. For example, when the metal-containing material is lithium cobalt (III) oxide (LiCoO2), leaching with the leach solution of the present invention enables the recovery of the lithium and/or cobalt metal.
Opening claim text (preview).
We claim: 1 . A method of leaching a metal-containing material (e.g., ore, concentrate, etc.), the method comprising: a) forming a leach solution by dissolving at least one amino acid and a reducing agent in water; b) forming a mixture of the leach solution of step (a) and a metal-containing material; c) leaching at least one metal from the metal-containing material by heating the mixture of step (b) in a temperature range from about 20° C. to about 100° C. or about 10° C. to about 95° C. 2 . The method of claim 1 , wherein the metal-containing material comprises LiCoO 2 . 3 . The method of claim 1 , wherein the at least one metal leached from the metal-containing material comprises lithium, cobalt, manganese or nickel (e.g, for battery recycling, using the present invention the metals leached may be manganese and/or nickel). 4 . The method of claim 1 , wherein the at least one amino acid is chosen from glycine, histidine and lysine. 5 . The method of claim 4 , wherein a concentration of the glycine in the leach solution is in a range from about 0.01M to about 2.0M, or from about 0.3 M to about 1.5 M, or even about 0.5 M. 6 . The method of claim 1 , wherein the reducing agent is sodium metabisulfite. 7 . The method of claim 6 , wherein a concentration of the sodium metabisulfite in the leach solution is in a range from about 0.1M to about 2.0 M, or from about 0.1 M to about 1.0 M, or even about 0.5 M. 8 . The method of claim 1 , further comprising adjusting the pH of the leach solution to a pH from about 1 to about 14, or from about 3 to about 7, or even from about 4.5 to 5.5. 9 . The method of claim 1 , wherein the metal-containing material is leached for a duration of about 10 minutes to about 180 minutes, or about 1 hour to about 96 hours. 10 . A method of recovering metal from a spent lithium-ion battery cathode, the method comprising: a) separating the cathode components comprising separating an aluminum foil in the cathode from a lithium containing material to recover one or more lithium compounds; b) forming a leach solution by dissolving glycine and sodium metabisulfite in water; c) forming a mixture of the leach solution of step (b) and said lithium containing material from step (a); d) leaching at least lithium and/or cobalt from the lithium containing material by heating the mixture of step (c) in a temperature range from about 20° C. to about 100° C. 11 . The method of claim 10 , wherein the separating in step (a) comprises physical separating using a method comprising crushing, milling, and/or air/gravity separation and collecting resulting or separated said lithium containing material (e.g. LiCoO 2 ). 12 . The method of claim 1 , wherein said metal-containing material is an ore or concentrate. 13 . The method of claim 1 , said temperature range is from about 10° C. to about 95° C. 14 . A method for leaching nickel and/or manganese from used batteries, the method comprising: a) separating a nickel and/or manganese containing material from the used battery; b) forming a leach solution by dissolving at least one amino acid and a reducing agent in water; c) forming a mixture of the leach solution of step (b) and the nickel and/or manganese containing material; d) leaching at least nickel and/or manganese from the nickel and/or manganese containing material by heating the mixture of step (c) in a temperature range from about 20° C. to about 100° C. or about 10° C. to about 95° C. wherein said at least one amino acid is chosen from glycine, histidine and lysine. 15 . The method of claim 14 , wherein said a reducing agent is sodium metabisulfite (SMB). 16 . The method of claim 14 , said temperature range is from about 10° C. to about 95° C. 17 . The method of claim 14 , wherein said lithium containing material comprises LiCoO 2 .
Reclaiming serviceable parts of waste accumulators · CPC title
Obtaining manganese · CPC title
Obtaining lithium · CPC title
by chemical methods · CPC title
Leaching processes · CPC title
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