Leaching method for anode and cathode mixed materials of waste LiCoxNiyMnzO2 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 large nitrogen oxides, pollute the environment, large consumption of nitric acid, etc. Nitric acid consumption, obvious economic and environmental benefits, and the effect of saving pollution control costs
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Embodiment 1
[0048] Example 1: Add 100g of nickel-cobalt lithium manganate waste battery positive and negative electrode mixed material (containing 14.5% nickel, 20.3% cobalt, 17.5% lithium, 2.2% aluminum, 2.5% copper, 12.9% manganese) into a stainless steel with a volume of 2L In the autoclave, add 1800ml of 3.0mol / L nitric acid, pass through industrial pure oxygen of 0.2MPa, stir at 40-50°C (stirring speed 80r / min) for leaching for 2.5 hours, and carry out liquid-solid separation after leaching to obtain 1700ml Leaching solution (excluding leaching slag washing water). The reaction tail gas is about 600ml (converted into a volume with an absolute pressure of 0.1MPa), and the concentration of nitrogen oxides is 6.3mg / m 3 . The leaching rates of nickel, cobalt and lithium are 99.2%, 99.4% and 99.6% respectively (calculated according to the nickel, cobalt and lithium entering the leaching solution and leaching slag washing solution).
Embodiment 2
[0049] Example 2: Add 500g 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) into a stainless steel with a volume of 10L In the autoclave, add 6.8L of 4.0mol / L nitric acid, pass through industrial pure oxygen of 0.1MPa, stir at 50-60°C (stirring speed 80r / min) for leaching for 2 hours, carry out liquid-solid separation after leaching, and obtain 6.5L of leaching solution (excluding leaching slag washing water), about 6.4L of reaction tail gas (converted into a volume with an absolute pressure of 0.1MPa), and a nitrogen oxide concentration of 8.1mg / m 3 . The leaching rates of nickel, cobalt and lithium are respectively 99.1%, 99.3% and 99.4% (calculated according to the nickel, cobalt and lithium entering the leaching solution and the leaching slag washing solution).
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