A kind of comprehensive recycling method of waste lithium ion battery
A technology for lithium-ion batteries and waste lithium batteries, which is applied in battery recycling, waste collector recycling, recycling technology, etc., can solve the problem of not being able to achieve high-efficiency and prioritizing lithium extraction.
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Embodiment 1
[0035] Get ternary waste lithium battery powder 50g, add 4mol / L sulfuric acid, add 10g additive potassium permanganate (KMnO 4 ), under the condition of 20 ℃, after stirring and reacting for 2h, filter to obtain the mixed solution and leaching slag containing nickel sulfate, cobalt sulfate, manganese sulfate and lithium sulfate in the filtrate, and the leaching effect is as follows: figure 1 , 2 and 3. Adjust the pH of the filtrate to ≈5.5, remove impurities, and obtain a high-concentration lithium-containing solution. The lithium-containing solution is subjected to a lithium precipitation process using sodium carbonate to obtain a pure lithium carbonate product.
[0036]The leaching residue is reduced and leached with sulfuric acid and hydrogen peroxide, the sulfuric acid is 1.1 times the theoretical amount, and the hydrogen peroxide is 1.4 times the theoretical amount. Under the condition of 60 ° C, a high-concentration mixed solution containing nickel sulfate, cobalt sulfa...
Embodiment 2
[0040] Take 50g of ternary waste lithium battery cell powder, add 4mol / L sulfuric acid, add 30g of additive KMnO 4 , under the condition of 50 ℃, after stirring and reacting for 4 hours, filter to obtain a solution containing nickel-cobalt-lithium and leaching residue, the leaching effect is shown in figure 1 , 2 And 3, adjust the filtrate pH ≈ 5-5.5, remove impurities, obtain a high-concentration lithium-containing solution, and then use sodium carbonate to perform a lithium-precipitation process on the lithium-containing solution to obtain a lithium carbonate product.
[0041] The leaching residue is reduced and leached with sulfuric acid and hydrogen peroxide. The sulfuric acid is 1.05 times the theoretical amount, and the hydrogen peroxide is 1.3 times the theoretical amount. At 60°C, a high-concentration lithium-containing solution is obtained, wherein nickel: 61.75g / L, cobalt: 23.75g / L, manganese: 35.15g / L. Adjust the pH of the lithium-containing solution to ≈4.5, and...
Embodiment 3
[0045] Take 50g of ternary waste lithium battery cell powder, add 4mol / L sulfuric acid, add additive KMnO 4 40g, under the condition of 80 ℃, after stirring and reacting for 12h, filter to obtain a solution containing nickel lithium manganese (leaching effect see figure 1 , 2 , 3), adjust the filtrate pH ≈ 5-5.5, remove impurities, obtain a high-concentration lithium-containing solution, and then perform a lithium precipitation process to obtain a lithium carbonate product
[0046] The leaching residue is reduced and leached with sulfuric acid and hydrogen peroxide. The sulfuric acid is 0.95 times the theoretical amount, and the hydrogen peroxide is 1.1 times the theoretical amount. Under the condition of 60 ° C, a high-concentration nickel-cobalt-manganese-containing solution is obtained, nickel: 55.25g / L, cobalt: 21.25g / L, manganese: 31.45g / L, adjust the pH of the solution to ≈4.5, and use 25% P204 to extract and remove impurities after nickel soap. The extraction stage is...
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