Method of recovering cobalt and nickel
US-2023307735-A1 · Sep 28, 2023 · US
US11008638B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11008638-B2 |
| Application number | US-201916713921-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 13, 2019 |
| Priority date | Jan 10, 2018 |
| Publication date | May 18, 2021 |
| Grant date | May 18, 2021 |
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A method for separating nickel and cobalt from a solution includes the steps of: obtaining a solution containing nickel and cobalt by acid leaching of a cathode material of a waste lithium-ion battery, adjusting the pH of the solution containing nickel and cobalt to 3.5 to 4.5, adding extractants for extraction to separate the nickel and the cobalt. The cobalt enters the organic phase, the nickel remains in the aqueous phase, and the extractants contain an acidic extractant and an alkaline extractant. The method for efficiently separating nickel and cobalt through extraction adopts a non-saponification extraction method without using NaOH as a saponifier, thereby avoiding the discharge of saponification wastewater. Under acidic conditions, the cobalt in an acidic leaching solution is effectively extracted and separated into the organic phase through synergistic action of the acidic extractant and the alkaline extractant, thereby realizing the separation of nickel from cobalt.
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What is claimed is: 1. A method for separating nickel and cobalt from a solution, comprising the steps of: obtaining a solution containing nickel and cobalt by acid leaching of a cathode material of a waste lithium-ion battery, wherein in the solution, a content of nickel is a range of from 0.7 mol/L to 1.2 mol/L, a content of cobalt is in a range of from 0.05 mol/L to 0.25 mol/L, and the solution further comprises chloride ions having a concentration in a range of from 2 mol/L to 3.5 mol/L; adjusting the pH of the solution containing nickel and cobalt to be in a range of from 3.5 to 4.5; adding extractants to the solution after the pH of the solution is adjusted so as to separate the nickel and the cobalt, wherein the cobalt enters an organic phase, and the nickel remains in an aqueous phase, wherein the extractants contain an acidic extractant and an alkaline extractant, and the acidic extractant is 2-ethylhexyl dihydrogen phosphate or 2-ethylhexylphosphonic acid mono-2-ethylhexyl ester, and the alkaline extractant is an organic amine with alkyl groups having C 8 , C 9 , C 10 , or a combination thereof, wherein in the extractants, the volume ratio of the acidic extractant to the alkaline extractant is in a range of (2-4):(6-8). 2. The method according to claim 1 , wherein a reagent for adjusting the pH of the solution is sodium hydroxide and/or hydrochloric acid. 3. The method according to claim 1 , wherein the extractants further comprise a diluent, the diluent is kerosene or sulfonated kerosene, and the volume ratio of the sum of the two extractants to the diluent is 1:(2-4). 4. The method according to claim 1 , wherein the volume ratio of the extractants to the solution is (3-5):1. 5. The method according to claim 1 , wherein after the extractants for extraction are added, the resultant is shaken and allowed to stand for 8 to 15 min, and the organic phase is separated from the aqueous phase. 6. The method according to claim 1 , wherein the acidic extractant is 2-ethylhexylphosphonic acid mono-2-ethylhexyl ester, and the alkaline extractant is tri-octyl decyl amine. 7. The method according to claim 2 , wherein the volume ratio of the extractants to the solution is (3-5):1. 8. The method according to claim 2 , wherein after the extractants for extraction are added, the resultant is shaken and allowed to stand for 8 to 15 min, and the organic phase is separated from the aqueous phase.
Amines · CPC title
in acidic type solutions · CPC title
using a mixture of phosphorus-based acid derivatives of different types · CPC title
Phosphonic acid, e.g. H2P(O)(OH)2 · CPC title
Phosphoric acid, e.g. (O)P(OH)3 · CPC title
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