Leaching method of nickel cobalt lithium manganate waste battery positive-negative electrode mixed material
A technology of nickel-cobalt lithium manganese oxide 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 industrial pure oxygen storage, transportation and use, uneconomical industrial pure oxygen for personal 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 of nickel-cobalt lithium manganate 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 29g ≤ 1.5mm distiller's grains Put it into a titanium-lined pressure reactor with a volume of 2L, add 1650ml of a mixed acid solution with a sulfuric acid concentration of 1.5mol / L and a nitric acid concentration of 5g / L, and leaching at 50°C to 60°C (stirring speed 80r / min) for 4h , after the leaching is finished, liquid-solid separation is carried out to obtain 1600ml leaching solution (excluding leaching slag washing water). The leaching rates of nickel, cobalt, lithium, copper, aluminum and manganese are 99.2%, 98.8%, 99.1%, 98.3%, 98.2% 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 105g ≤ 1.5mm distiller's grains Put it 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 2 hours. After leaching, carry out liquid-solid separation to obtain 2800ml leaching solution (excluding leaching slag washing water). The leaching rates of nickel, cobalt, lithium, copper, aluminum and manganese are 99.6%, 99.2%, 99.4%, 99.3%, 98.7% 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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