Cobalt and nickel extraction separation method capable of reducing coextraction
A separation method and extraction technology, which is applied in the field of cobalt and nickel separation and recovery, can solve the problems of reduced cobalt and nickel separation efficiency, reduced nickel co-extraction, and reduced co-extraction, so as to reduce co-extraction phenomenon, improve extraction and separation efficiency, and reduce co-extraction rate effect
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Embodiment 1
[0056] The separation method steps of the present embodiment are as follows:
[0057] (1) Extraction of cobalt in sulfuric acid leaching solution
[0058] The concentrations of cobalt and nickel in the sulfuric acid leaching solution of the positive electrode material of lithium-ion batteries are 17.10g / L and 4.53g / L respectively. First, adjust the pH to 4.0-4.5 with sodium hydroxide, filter to remove trace impurities, and then adjust with glacial acetic acid and sodium hydroxide. The pH of the leaching solution was adjusted to 5.2 (n(Co):n(acetic acid)=1:34.5), and the leaching solution was diluted 5 times at the same time. Use 0.4mol / L P507 with a saponification rate of 70% for extraction, the ratio O / A is 1:1, 25°C, 150 rpm, shaking extraction for 15min, the cobalt and nickel in the raffinate (water phase) The contents of 0.10g / L and 0.82g / L respectively, the equilibrium pH=5.45, △pH=0.25, and the primary extraction efficiencies of cobalt and nickel are 97.0% and 9.49% res...
Embodiment 2
[0065] The separation method steps of the present embodiment are as follows:
[0066] (1) Extraction of cobalt in sulfuric acid leaching solution
[0067] The concentrations of cobalt and nickel in the sulfuric acid leaching solution of the cathode material of lithium ion batteries are 16.40g / L and 4.85g / L respectively, and the pH of the leaching solution is adjusted to 5.4 with glacial acetic acid and sodium hydroxide (n(Co):n(acetic acid)=1:38 ), while the leachate was diluted 5 times, extracted with 0.4mol / L P507 with a saponification rate of 62%, compared to O / A of 1:1, 25°C, rotating speed 150 rpm, shaking extraction for 15min, raffinate The contents of cobalt and nickel in the (water phase) are 0.12g / L and 0.89g / L respectively, the equilibrium pH=5.58, △pH=0.18, and the primary extraction efficiencies of cobalt and nickel are 96.34% and 8.25% respectively.
[0068] Under the same extraction conditions as above, the above raffinate was extracted for the second time with ...
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