Method for leaching anode and cathode mixed material of waste lithium nickel manganese cobalt battery
A technology of nickel-cobalt-lithium-manganese-manganate and mixed materials, which is applied in the field of leaching of positive and negative electrode mixed materials of nickel-cobalt-lithium-manganese-oxide waste batteries, can solve the problems of large nitrogen oxides, large consumption of nitric acid, and environmental pollution, and achieve obvious Economic and environmental benefits, saving pollution control costs, and avoiding the effects of pollutant nitrogen oxides
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Embodiment 1
[0049] Example 1: Add 100 g of nickel-cobalt lithium manganate waste battery positive and negative electrode mixed materials (containing 14.5% nickel, 20.3% cobalt, 17.5% lithium, 2.2% aluminum, 2.5% copper, and 12.9% manganese) into a liner with a volume of 2L In the titanium autoclave, add 1400ml of sulfuric acid of 3.0mol / L, add nitric acid 20g (as HNO 3 0.2 MPa of industrial pure oxygen, stirring at 50-60°C (stirring speed 80r / min) for 3 hours, liquid-solid separation after leaching, to obtain 1300ml leaching solution (excluding leaching slag washing water ). The reaction tail gas is about 1.8L (converted into a volume with an absolute pressure of 0.1MPa), and the concentration of nitrogen oxides is 2.6mg / m 3 . The leaching rates of nickel, cobalt and lithium are 98.1%, 98.4% and 99.3% (calculated according to the nickel, cobalt and lithium entering the leaching solution and leaching slag washing solution).
Embodiment 2
[0050] Example 2: Add 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) into a liner with a volume of 5L In the titanium autoclave, add 4.8L of sulfuric acid of 2.5mol / L, add nitric acid 80g (as HNO 3 ) into 0.1MPa industrial pure oxygen, stirring at 60-70°C (stirring speed: 80r / min) for 2.5 hours, and liquid-solid separation after leaching to obtain 4.7L leaching solution (excluding leaching slag washing water), the reaction tail gas is about 0.4L (converted into a volume of 0.1MPa absolute pressure), and the concentration of nitrogen oxides is 3.1mg / m 3 . The leaching rates of nickel, cobalt and lithium are 98.2%, 98.7% and 99.5% respectively (calculated according to nickel, cobalt and lithium entering the leaching solution and leaching slag washing solution).
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