Battery recycling
US-2023411724-A1 · Dec 21, 2023 · US
US2023090475A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2023090475-A1 |
| Application number | US-202217945451-A |
| Country | US |
| Kind code | A1 |
| Filing date | Sep 15, 2022 |
| Priority date | Sep 20, 2021 |
| Publication date | Mar 23, 2023 |
| Grant date | — |
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Methods for recovering a metal value from a metal-bearing material are provided. The method comprises agglomerating the metal-bearing material with an agglomeration solution comprising a raffinate, an oxidant, and citric acid or salts thereof to form an agglomerated metal-bearing material; leaching the agglomerated metal-bearing material with a leaching solution comprising the raffinate and the citric acid or salts thereof to produce a pregnant leaching solution and a leached material; re-oxidizing the leached material with a curing solution comprising the raffinate and the oxidant; and recovering the metal value from the pregnant leach solution to produce the raffinate.
Opening claim text (preview).
What is claimed is: 1 . A cyclic process comprising: leaching a metal-bearing material comprising a metal value with a leaching solution comprising a raffinate, sulfuric acid, an oxidant, and citric acid or salts thereof, to produce a leached material and a pregnant leach solution, the leached material comprising ferrous (Fe 2+ ) ions and ferric (Fe 3+ ) ions; curing the leached material with a curing solution comprising the raffinate and the oxidant to re-oxidize the ferrous (Fe 2+ ) ions to ferric (Fe 3+ ) ions and to produce a cured leached material; recycling the ferric (Fe 3+ ) ions to the leaching step; and recovering the metal value from the pregnant leach solution to produce the metal value and the raffinate; wherein the raffinate obtained after recovering the metal value is recycled to the leaching. 2 . The cyclic process of claim 1 , wherein the ferric (Fe 3+ ) ions are recycled to the leaching in the recycled raffinate. 3 . The cyclic process of claim 1 , wherein the curing solution further comprises the citric acid or salts thereof. 4 . The cyclic process of claim 1 , wherein the oxidant comprises hydrogen peroxide. 5 . The cyclic process of claim 1 , wherein the metal-bearing material comprises run-of-mine (ROM) material optionally augmented with the cured leach material obtained from the curing. 6 . The cyclic process of claim 5 , wherein the cured leach material comprises the ferric (Fe 3+ ) ions recycled to the leaching to augment the ROM material. 7 . The cyclic process of claim 1 , wherein the leaching and the subsequent curing are cyclically repeated prior to recovering the metal value from the pregnant leach solution. 8 . The cyclic process of claim 1 , wherein the leaching comprises a heap leach operation, wherein a first line directed to the heap is configured to provide the oxidant to the heap, and a second line directed to the heap is configured to provide the sulfuric acid and the citric acid or salts thereof to the heap. 9 . The cyclic process of claim 8 , wherein the oxidant comprises hydrogen peroxide. 10 . The cyclic process of claim 8 , wherein an output from a sugar fermentation process comprising citric acid or salts thereof is directed into the second line directed to the heap to provide the citric acid or salts thereof in the leaching. 11 . The cyclic process of claim 1 , further comprising a step of agglomerating the metal-bearing material with an agglomerating solution prior to leaching, the agglomerating solution comprising the raffinate, the oxidant, the sulfuric acid, and the citric acid or salts thereof. 12 . The cyclic process of claim 11 , wherein agglomeration comprises combining the metal-bearing material, the raffinate, the oxidant, and the citric acid or salts thereof in an agglomeration drum. 13 . The cyclic process of claim 1 , wherein the pregnant leach solution is repeatedly recycled back to the leaching step prior to recovering the metal value from the pregnant leach solution. 14 . The cyclic process of claim 1 , wherein the metal-bearing material comprises a primary or secondary copper sulfide, or mixtures thereof. 15 . The cyclic process of claim 1 , wherein recovering the metal value from the pregnant leach solution comprises a solvent extraction/electrowinning (SX/EW) process or a direct electrowinning (DEW) process. 16 . The cyclic process of claim 1 , wherein the leaching comprises a heap leach operation further comprising subsurface injection of the leaching solution into the heap. 17 . The cyclic process of claim 1 , wherein the metal-bearing material comprises a mixture of copper-bearing ROM ore and the leached material. 18 . The cyclic process of claim 1 , wherein leaching further comprises injection of air and/or oxygen into the leaching solution. 19 . The cyclic process of claim 1 , wherein the leaching comprises a heap leach operation further comprising subsurface injection of air and/or oxygen into the heap. 20 . The cyclic process of claim 19 , wherein subsurface injection of air and/or oxygen into the heap comprises subsurface injection of the leaching solution aerated with air and/or oxygen.
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