Method and apparatus for recycling lithium iron phosphate batteries
US-10741890-B2 · Aug 11, 2020 · US
US2024183005A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024183005-A1 |
| Application number | US-202218553250-A |
| Country | US |
| Kind code | A1 |
| Filing date | Mar 28, 2022 |
| Priority date | Mar 30, 2021 |
| Publication date | Jun 6, 2024 |
| Grant date | — |
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A method for dissolving a positive electrode material of a battery including a step during which the positive electrode material, comprising lithium and optionally cobalt and/or nickel, is submerged in an acid solution having a pH between 0 and 4, the acid solution containing either manganese ions or hydrogen peroxide, by means of which the lithium and optionally the cobalt and/or nickel is dissolved, and the manganese ions are selectively precipitated in the form of manganese oxyhydroxide.
Opening claim text (preview).
What is claimed is: 1 . A method for dissolving a positive electrode material of a battery comprising a step during which the positive electrode material, including lithium, manganese and possibly cobalt and/or nickel, is immersed in an acid solution at a pH comprised between 0 and 4, wherein the acid solution contains hydrogen peroxide, whereby, on the one hand, the lithium and possibly the cobalt and/or the nickel are put into solution and, on the other hand, the manganese is dissolved, which selectively precipitates in the form of a manganese oxyhydroxide. 2 . The method according to claim 1 , wherein the manganese of the positive electrode material is entirely recovered in the form of manganese oxohydroxide. 3 . The method according to claim 1 , wherein the duration of the leaching step is between 1 h and 24 h. 4 . The method according to claim 1 , wherein the volume concentration of hydrogen peroxide is between 1% and 12%, and preferably between 1% and 6%. 5 . The method according to claim 4 , wherein the volume concentration of hydrogen peroxide is between 1% and 4%. 6 . The method according to claim 5 , wherein the volume concentration of hydrogen peroxide is between 2% and 3%. 7 . The method according to claim 1 , wherein the pH is between 1 and 2.5. 8 . The method according claim 1 , wherein the solid/liquid ratio is between 5% and 40%, and advantageously between 5% and 20%. 9 . The method according to claim 1 , wherein the ratio between the volume concentration of hydrogen peroxide and the solid/liquid ratio is between 0.1 and 0.4 and preferably between 0.2 and 0.3. 10 . The method according to claim 1 , wherein the positive electrode is an NMC electrode. 11 . The method according to claim 1 , wherein the temperature of the solution is between 70° C. and 100° C., preferably between 80° C. and 95° C. 12 . The method according to claim 1 , wherein the positive electrode material is in a particulate form. 13 . The method according to claim 1 , wherein the solid/liquid ratio is between 5% and 40% and the volume concentration of hydrogen peroxide is between 1% and 12%. 14 . The method according to claim 13 , wherein the solid/liquid ratio is comprised between 5% and 20% and the volume concentration of hydrogen peroxide is between 1% and 6%. 15 . The method according to claim 1 , wherein the solid/liquid ratio is between 5% and 10%, the pH is comprised between 1 and 2.5 and the volume concentration of hydrogen peroxide is between 1% and 3%.
Obtaining manganese · CPC title
Oxides · CPC title
Sulfuric acid {, other sulfurated acids or salts thereof} · CPC title
by physical processes, e.g. by filtration, by magnetic means {, or by thermal decomposition} (treatment or purification of solutions by liquid-liquid extraction C22B3/26) · CPC title
by chemical processes (treatment or purification of solutions by liquid-liquid extraction C22B3/26, by ion-exchange extraction C22B3/42) · CPC title
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