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
US12451533B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12451533-B2 |
| Application number | US-202318334801-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 14, 2023 |
| Priority date | Jan 15, 2021 |
| Publication date | Oct 21, 2025 |
| Grant date | Oct 21, 2025 |
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A method for reducing waste by recovering transition metal of a lithium secondary battery of the present invention includes preparing a cathode active material from a cathode of the lithium secondary battery, producing a first leachate by treating the cathode active material with a first acidic solution containing a reducing agent in an amount smaller than an amount corresponding to a reaction equivalent of the cathode active material, and producing a second leachate by treating the remaining cathode active material, which excludes a fraction contained in the first leachate, with a second acidic solution containing a reducing agent. Accordingly, extraction rate of manganese and purity of cobalt may be improved.
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The invention claimed is: 1. A method for reducing waste by recovering a transition metal of a lithium secondary battery, comprising: preparing a cathode active material from a cathode of a lithium secondary battery, wherein the cathode active material comprises a lithium transition metal oxide containing nickel, cobalt and manganese as transition metals; producing a first leachate by treating the cathode active material with a first acidic solution containing a first reducing agent in an amount less than an amount corresponding to a reaction equivalent of the cathode active material, wherein a content (wt %) of nickel or cobalt in the first leachate is greater than a content (wt %) of manganese in the first leachate; and producing a second leachate by treating a remaining cathode active material, which excludes a fraction included in the first leachate, with a second acidic solution containing a second reducing agent, wherein a content (wt %) of manganese in the second leachate is greater than a content (wt %) of nickel or cobalt in the second leachate. 2. The method for reducing waste according to claim 1 , wherein an amount of the first reducing agent used in producing the first leachate is 0.2 to 0.4 times the amount of the first reducing agent corresponding to the reaction equivalent of the cathode active material, wherein the amount of the first reducing agent corresponding to the reaction equivalent of the cathode active material is an amount of the first reducing agent required to reduce all of the transition metals included in the cathode active material. 3. The method for reducing waste according to claim 2 , wherein the reaction equivalent of the cathode active material of the first reducing agent is 0.5 mol based on 1 mol of the lithium transition metal oxide. 4. The method for reducing waste according to claim 3 , wherein the first reducing agent or the second reducing agent is hydrogen peroxide. 5. The method for reducing waste according to claim 2 , wherein an amount of the second reducing agent used in producing the second leachate is 0.8 to 1.2 times the amount of the second reducing agent corresponding to the reaction equivalent of the remaining cathode active material, wherein the amount of the second reducing agent corresponding to the reaction equivalent of the remaining cathode active material is an amount of the first reducing agent required to reduce all of the transition metals included in the remaining cathode active material. 6. The method for reducing waste according to claim 1 , wherein contents of cobalt and nickel contained in the first leachate are 75% to 100% by weight of a total weight of the transition metals, and a content of manganese contained in the second leachate is 30% to 75% by weight of the total weight of the transition metals. 7. The method for reducing waste according to claim 6 , further comprising sequentially extracting cobalt and nickel from the first leachate. 8. The method for reducing waste according to claim 6 , further comprising sequentially extracting manganese, cobalt and nickel from the second leachate. 9. The method for reducing waste according to claim 1 , wherein a weight ratio of the remaining cathode active material based on a weight of the cathode active material is 25% to 50% by weight. 10. The method for reducing waste according to claim 1 , wherein the first acidic solution and the second acidic solution include sulfuric acid.
with acids or salt solutions (C22B47/0072 takes precedence) · CPC title
with acids or salt solutions except ammonium salts solutions · CPC title
by acid leaching · CPC title
Li-accumulators · CPC title
Leaching processes · CPC title
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