Processing hard rock lithium minerals or other materials to produce lithium materials and byproducts converted from a sodium sulfate intermediate product
US-2024425381-A1 · Dec 26, 2024 · US
US10490866B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10490866-B2 |
| Application number | US-201615768407-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 14, 2016 |
| Priority date | Oct 14, 2015 |
| Publication date | Nov 26, 2019 |
| Grant date | Nov 26, 2019 |
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A method for the acid dissolution of LiCoO 2 contained in the cathode of lithium ion batteries, using acetic or tartaric acid as leaching agent, the method being characterized in that it comprises a first stage and a second stage, wherein said first stage comprises the step of separating the cathode components, while said second stage comprises the step of dissolving the pure LiCoO 2 with at least one acid. The method allows achieving an economically viable complete recycling process with low environmental impact.
Opening claim text (preview).
The invention claimed is: 1. A method for acid dissolution of LiCoO 2 contained in a Li-ion battery cathode, the method comprising a first stage and a second stage, wherein the first stage comprises a step of separating the cathode components by one or more steps of removal of adhesives used to adhere the LiCoO 2 to an aluminum foil in the Li-ion battery, wherein such removal of adhesives is effected by means of one diluted acid selected from the group consisting of H 4 C 2 O 2 , H 6 C 4 O 6 , H 8 C 6 O 7 , and H 2 SO 4 , and thus obtaining an aluminum foil as a recycling material, an effluent containing a remainder of the acid used in the first stage, and LiCoO 2 without impurities, and wherein the second stage comprises the step of dissolving LiCoO 2 from the first stage with acetic acid or tartaric acid as a leaching agent and hydrogen peroxide as a reducing agent. 2. The method according to claim 1 , wherein the removal of adhesives by means of one diluted acid comprises several reuse stages of H 4 C 2 O 2 , H 6 C 4 O 6 , H 8 C 6 O 7 , or H 2 SO 4 . 3. The method according to claim 2 , wherein after removal of adhesives with H 2 SO 4 , the effluent generated therefrom is dried at low temperature and obtained residues are treated by a waste operator. 4. The method according to claim 1 , further comprising a step of recycling the effluent generated after one or more steps of removal of adhesives with one diluted acid selected from H 4 C 2 O 2 , H 6 C 4 O 6 , or H 8 C 6 O 7 into the second stage, for dissolution of LiCoO 2 . 5. The method according to claim 1 , wherein the second stage starts from a solid without impurities, which is dissolved with acetic or tartaric acids at a concentration lower than 15% v/v or lower than 5% w/v, using a reaction time of less than 60 minutes and a temperature of 75° C., achieving complete dissolution of LiCoO 2 . 6. The method according to claim 1 , further comprising a step of subjecting the LiCoO 2 dissolved in the second stage to a sol-gel synthesis method for re-synthesizing LiCoO 2 .
by acid leaching · CPC title
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