Leaching method of nickel cobalt lithium manganate waste battery positive-negative electrode mixed material
A technology of nickel-cobalt-lithium-manganese-manganate and mixed materials, which is applied in the field of leaching the positive and negative electrode mixed materials of nickel-cobalt-lithium-manganese-oxide waste batteries, can solve the problems of storage, transportation and use of industrial pure oxygen, and uneconomical use of industrial pure oxygen for self-use. The industrial pure oxygen amount is not large, etc., to achieve obvious economic and environmental benefits, reduce pollution treatment costs, and improve the effect of metal leaching rate
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Embodiment 1
[0025]Example 1: 100g nickel-cobalt lithium manganese oxide waste battery positive and negative mixed material (containing 14.5% nickel, 20.3% cobalt, 17.5% lithium, 2.2% aluminum, 2.5% copper, 12.9% manganese) and ≤ 1.5mm grass powder Add 29g 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 at 50°C to 60°C (stirring speed 80r / min) for leaching After 4 hours, liquid-solid separation was carried out after leaching to obtain 1600ml leaching solution (excluding leaching slag washing water). The leaching rates of nickel, cobalt, lithium, copper, aluminum and manganese are 99.2%, 98.9%, 99.2%, 99.0%, 98.8% and 99.0% 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 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 grass powder Add 105g into a titanium-lined pressure reactor with a volume of 5L, add 3000ml of a mixed acid solution with a sulfuric acid concentration of 3mol / L and a nitric acid concentration of 10g / L, and leaching at 70°C to 80°C (stirring speed 70r / min) for 2h , after the leaching is finished, liquid-solid separation is carried out to obtain 2800ml leaching solution (excluding leaching slag washing water). The leaching rates of nickel, cobalt, lithium, copper, aluminum and manganese are 99.5%, 99.2%, 99.5%, 99.3%, 98.6% 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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