Leaching method of anode material of lithium cobalt oxide waste battery
A technology for positive electrode materials and waste batteries, which is applied in the field of leaching of lithium cobalt oxide waste battery positive electrode materials, can solve the problems of large consumption of nitric acid, environmental pollution, large nitrogen oxides, etc., and achieve obvious economic and environmental benefits. Pollution control costs, the effect of avoiding the generation of pollutant nitrogen oxides
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Embodiment 1
[0023] Example 1: Add 100 g of lithium cobalt oxide waste battery cathode material (containing 53.6% cobalt, 5.3% lithium, 8.2% copper, and 3.4% aluminum) into a titanium-lined autoclave with a volume of 1 L, and add 900 ml of 3.5 mol / L sulfuric acid , add nitric acid 15g (as HNO 3 ) into 0.2MPa industrial pure oxygen, stirring at 50-60°C (stirring speed 80r / min) for leaching for 2.5 hours, and liquid-solid separation after leaching to obtain 850ml leaching solution (excluding leaching slag washing water) . The reaction tail gas is about 0.3L (converted into a volume with an absolute pressure of 0.1MPa), and the concentration of nitrogen oxides is 2.3mg / m 3 . The leaching rates of cobalt, lithium and copper are respectively 98.1%, 97.8% and 97.5% (calculated according to the cobalt, lithium and copper entering the leaching solution and leaching slag washing liquid).
Embodiment 2
[0024] Example 2: Add 400g of waste nickel metal hydride battery cathode material (containing 53.6% cobalt, 5.3% lithium, 8.2% copper, 3.4% aluminum) into a titanium-lined autoclave with a volume of 5L, and add 4.5L of 3.0mol / L sulfuric acid , add nitric acid 60g (as HNO 3 0.1MPa of industrial pure oxygen was introduced, and the reaction was stirred at 60-70°C for 3 hours. After the reaction, liquid-solid separation was carried out to obtain 4.3L of leaching solution (excluding leaching slag washing water), and the reaction tail gas was about 1L ( Converted into an absolute pressure of 0.1MPa), the concentration of nitrogen oxides is 2.5mg / m 3 . The leaching rates of cobalt, lithium and copper are 98.3%, 98.2% and 97.7% respectively (calculated based on the cobalt, lithium and copper entering the leaching solution and leaching slag washing solution).
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