Method for leaching positive-negative pole material mixture of waste lithium nickel cobalt manganese oxide battery
A technology of nickel-cobalt lithium manganate and mixed materials is applied in the field of leaching of positive and negative electrode mixed materials of nickel-cobalt lithium manganate waste batteries, which can solve the problems of storage, transportation and use of industrial pure oxygen, uneconomical self-use of industrial pure oxygen, It can achieve obvious economic and environmental benefits, reduce pollution control costs, and improve metal leaching rate.
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Embodiment 1
[0025] Example 1: 100g of nickel-cobalt lithium manganese oxide waste battery positive and negative mixed materials (containing 14.5% nickel, 20.3% cobalt, 17.5% lithium, 2.2% aluminum, 2.5% copper, 12.9% manganese) and ≤1.5mm Elephant grass Add 29g of powder into a titanium-lined pressure reactor with a volume of 2L, add 1650ml of a mixed acid solution with a concentration of sulfuric acid of 1.5mol / L and a concentration of nitric acid of 5g / L, and stir in a closed manner at 50°C to 60°C (stirring speed 80r / min) After leaching for 4 hours, liquid-solid separation was performed after leaching to obtain 1600ml of leaching solution (excluding leaching slag washing water). The leaching rates of nickel, cobalt, lithium, copper, aluminum and manganese are 99.2%, 99.1%, 99.3%, 98.9%, 98.7% and 99.1% respectively (according to the nickel, cobalt and lithium in the leaching solution and leaching slag washing solution , copper, aluminum and manganese calculations).
Embodiment 2
[0026] Example 2: 300g of nickel-cobalt lithium manganate waste battery positive and negative mixed materials (containing 14.5% nickel, 20.3% cobalt, 17.5% lithium, 2.2% aluminum, 2.5% copper, 12.9% manganese) and ≤1.5mm elephant grass Add 105g of powder into a titanium-lined pressure reactor with a volume of 5L, add 3000ml of a mixed acid solution with a concentration of sulfuric acid of 3mol / L and a concentration of nitric acid of 10g / L, and stir at 70°C to 80°C (stirring speed 70r / min) for leaching 2h, liquid-solid separation is carried out after leaching, and 2800ml leaching solution is obtained (excluding leaching slag washing water). The leaching rates of nickel, cobalt, lithium, copper, aluminum and manganese are 99.5%, 99.4%, 99.6%, 99.1%, 98.5% and 99.3% respectively (according to the nickel, cobalt and lithium in the leaching solution and leaching slag washing solution , copper, aluminum and manganese calculations).
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