Method and system for recycling metal of lithium secondary battery
US-2025215522-A1 · Jul 3, 2025 · US
US2022349025A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2022349025-A1 |
| Application number | US-202117243032-A |
| Country | US |
| Kind code | A1 |
| Filing date | Apr 28, 2021 |
| Priority date | Apr 28, 2021 |
| Publication date | Nov 3, 2022 |
| Grant date | — |
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Methods for recovering a metal from a metal-containing material are provided. In embodiments, such a method comprises exposing a metal-containing material to a leaching solution comprising a solvent and a binoxalate, a tetraoxalate, or a combination thereof, under conditions to provide a leachate comprising a soluble metal oxalate; inducing precipitation of a metal-containing precipitate comprising the metal of the soluble metal oxalate from the leachate; and recovering the metal-containing precipitate.
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What is claimed is: 1 . A method for recovering a metal from a metal-containing material, the method comprising: (a) exposing a metal-containing material to a leaching solution comprising a solvent and a binoxalate, a tetraoxalate, or a combination thereof, under conditions to provide a leachate comprising a soluble metal oxalate; (b) inducing precipitation of a metal-containing precipitate comprising the metal of the soluble metal oxalate from the leachate; and (c) recovering the metal-containing precipitate. 2 . The method of claim 1 , wherein the metal-containing material is not ilmenite and is not a lithium-ion battery electrode material. 3 . The method of claim 1 , wherein the metal-containing material is bauxite. 4 . The method of claim 1 , wherein the binoxalate has formula AHC 2 O 4 and the tetraoxalate has formula AHC 2 O 4 .H 2 C 2 O 4 , wherein A is an ammonium cation, NR 4 , wherein each R is independently selected from a group consisting of hydrogen and an alkyl group; or A is an alkali metal cation. 5 . The method of claim 4 , wherein at least one R is not hydrogen. 6 . The method of claim 4 , wherein the binoxalate is not NH 4 HC 2 O 4 . 7 . The method of claim 1 , wherein the binoxalate has formula AHC 2 O 4 and the tetraoxalate has formula AHC 2 O 4 .H 2 C 2 O 4 , wherein A is an alkali metal cation. 8 . The method of claim 7 , wherein the binoxalate is KHC 2 O 4 , NaHC 2 O 4 , or a combination thereof and the tetraoxalate is KHC 2 O 4 .H 2 C 2 O 4 . 9 . The method of claim 1 , wherein at least two metals of the metal-containing material to be recovered are each present in the leachate as respective soluble metal oxalates. 10 . The method of claim 1 , further comprising: (d) inducing precipitation of a second metal-containing precipitate from the leachate comprising a second soluble metal oxalate, the second metal-containing precipitate comprising the metal of the second soluble metal oxalate; and (e) recovering the second metal-containing precipitate. 11 . The method of claim 10 , wherein the metal-containing precipitate precipitates out of the leachate at a first pH value and step (d) comprises adjusting the pH of the leachate to a second pH value to induce precipitation of the second metal-containing precipitate. 12 . The method of claim 1 , further comprising recovering the binoxalate, the tetraoxalate, or the combination thereof, from the leachate. 13 . The method of claim 12 , wherein the binoxalate, the tetraoxalate, or the combination thereof, is recovered by adjusting the leachate's pH to induce precipitation of the binoxalate, the tetraoxalate, or the combination thereof 14 . A method for recovering a metal from bauxite, the method comprising: (a) exposing bauxite to a leaching solution comprising a solvent and a binoxalate, a tetraoxalate, or a combination thereof, under conditions to provide a leachate comprising a Fe soluble metal oxalate and an Al soluble metal oxalate; (b) inducing precipitation of a Fe-containing precipitate from the leachate by adjusting the leachate's pH to a first value; (c) recovering the Fe-containing precipitate; (d) inducing precipitation of an Al-containing precipitate from the leachate by adjusting the leachate's pH to a second value; and (e) recovering the Al-containing precipitate. 15 . The method of claim 14 , further comprising recovering the binoxalate, the tetraoxalate, or the combination thereof from the leachate. 16 . The method of claim 14 , wherein the binoxalate has formula AHC 2 O 4 , wherein A is an ammonium cation, NR 4 , wherein each R is independently selected from a group consisting of hydrogen and an alkyl group; or A is an alkali metal cation. 17 . The method of claim 14 , wherein the binoxalate has formula AHC 2 O 4 and the tetraoxalate has formula AHC 2 O 4 .H 2 C 2 O 4 , wherein A is an alkali metal cation. 18 . The method of claim 17 , wherein the binoxalate is KHC 2 O 4 , NaHC 2 O 4 , or a combination thereof and the tetraoxalate is KHC 2 O 4 .H 2 C 2 O 4 . 19 . The method of claim 17 , wherein the binoxalate is KHC 2 O 4 and the tetraoxalate is KHC 2 O 4 .H 2 C 2 O 4 20 . The method of claim 14 , wherein the Al-containing precipitate is processed to form aluminum oxide and the aluminum oxide is used as a feedstock for the production of aluminum metal.
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by wet processes (C22B21/02, C22B21/04 and C22B21/06 take precedence) · CPC title
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