Method for leaching positive pole material of waste lithium nickelate battery
A technology for lithium nickelate waste batteries and cathode materials, which is applied in the direction of improving process efficiency, can solve problems such as uneconomical self-use of industrial pure oxygen, complicated leaching equipment, and small amount of industrial pure oxygen, etc., and achieve obvious economic benefits and environmental protection. Benefit, reduce pollution control costs, improve the effect of metal leaching rate
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Embodiment 1
[0019] Example 1: Add 100g of lithium nickelate waste battery positive electrode material (containing 54.3% nickel, 5.5% lithium, 7.8% copper, 3.1% aluminum) and 30g of straw powder ≤ 1.5mm into a titanium-lined pressure reactor with a volume of 2L, Add 1300ml of a mixed acid solution with a sulfuric acid concentration of 1.5mol / L and a nitric acid concentration of 5g / L, stir at 60°C to 70°C (stirring speed 80r / min) for 4.0h, and perform liquid-solid separation after leaching to obtain 1250ml of leaching solution (without leaching slag washing water). The leaching rates of nickel, lithium, copper, and aluminum are 98.8%, 99.0%, 98.8%, and 98.9% respectively (calculated based on nickel, lithium, copper, and aluminum entering the leaching solution and leaching slag washing solution).
Embodiment 2
[0020] Example 2: 190 g of 500 g lithium nickelate waste battery cathode material (containing 54.3% nickel, 5.5% lithium, 7.8% copper, 3.1% aluminum) ≤ 1.5 mm straw powder 190 g is added to a titanium-lined pressure reactor with a volume of 5 L, and the 3200 ml of mixed acid solution with a sulfuric acid concentration of 3.5 mol / L and a nitric acid concentration of 10 g / L was stirred at 70°C to 80°C (stirring speed 70r / min) for 2.0 hours, and liquid-solid separation was performed after the leaching was completed to obtain 3000 ml of leached solution (without leaching slag washing water). The leaching rates of nickel, lithium, copper and aluminum are 99.0%, 99.3%, 99.0% and 98.4% respectively (calculated based on nickel, lithium, copper and aluminum entering the leaching solution and leaching slag washing solution).
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