Method for recovering and recycling electrolyte salts from lithium batteries
US-2022231350-A1 · Jul 21, 2022 · US
US12525662B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12525662-B2 |
| Application number | US-202218288725-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 22, 2022 |
| Priority date | Aug 15, 2022 |
| Publication date | Jan 13, 2026 |
| Grant date | Jan 13, 2026 |
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A method for recycling and treating an electrolytic solution of a lithium ion battery includes S1: cooling a fully discharged lithium ion battery below a freezing point of the electrolytic solution, and then disassembling and crushing the lithium ion battery to obtain a crushed solid containing the electrolytic solution, S2: under a protection of an inert gas, placing the crushed solid in a supercritical CO2 extraction instrument in which an entrainer is added; S3: conducting extraction; and S4: collection an extraction product with a cryogenic device, and adsorbing water in the extraction product using a 4 Å type lithiated molecular sieve, adsorbing HF in the extraction product using weak-base anion-exchange resin and adsorbing organic acid and alcohol in the extraction product using a 5 Å type lithiated molecular sieve.
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The invention claimed is: 1 . A method for recycling and treating an electrolytic solution of a lithium ion battery, comprising: S1: cooling a fully discharged lithium ion battery below a freezing point of the electrolytic solution, and then disassembling and crushing the lithium ion battery to obtain a crushed solid containing the electrolytic solution; S2: under a protection of an inert gas, placing the crushed solid in a supercritical CO 2 extraction instrument in which an entrainer is added; S3: conducting co-extraction with a supercritical CO 2 and the entrainer; and S4: collecting an extraction product which comprises water, hydrofluoric acid (HF), organic acid and alcohol with a cryogenic device, and adsorbing water in the extraction product using a 4 Å type lithiated molecular sieve, adsorbing HF in the extraction product using weak-base anion-exchange resin and adsorbing organic acid and alcohol in the extraction product using a 5 Å type lithiated molecular sieve; wherein the extraction comprises static extraction and dynamic extraction; the entrainer is a cyclic carbonate entrainer, and when the dynamic extraction starts, the addition flow rate of the cyclic carbonate entrainer is 8% of a flow rate of the supercritical CO 2 ; or the entrainer is a cyclic carbonate-N,N-dimethylformamide mixed entrainer, wherein the mass ratio of cyclic carbonate to N,N-dimethylformamide is 4:1, and when the dynamic extraction starts, the addition flow rate of the cyclic carbonate-N,N-dimethylformamide mixed entrainer is 8% of the flow rate of the supercritical CO 2 ; and the 4 Å type lithiated molecular sieve is made by lithiating a 4 Å type molecular sieve with a LiCl ethanol solution, wherein a concentration of the LiCl ethanol solution is 1.8-2.2 mol/L; and a number of lithiation treatments is 5-10 times; and/or, the 5 Å type lithiated molecular sieve is made by lithiating a 5 Å type molecular sieve with a LiCl ethanol solution, wherein a concentration of the LiCl ethanol solution is 1.8-2.2 mol/L; and a number of lithiation treatments is 5-10 times. 2 . The method for recycling and treating the electrolytic solution of the lithium ion battery according to claim 1 , wherein time for the static extraction is 18-22 min, and time for the dynamic extraction is 35-55 min. 3 . The method for recycling and treating the electrolytic solution of the lithium ion battery according to claim 1 , wherein for the extraction, a pressure is 21-35 MPa, and a temperature is 40-55° C.
Anion-exchange · CPC title
Size-selective separation, e.g. size-exclusion chromatography; Gel filtration; Permeation · CPC title
with a supercritical fluid · CPC title
Batteries · CPC title
involving an extraction step · CPC title
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