Leaching method of nickel-cadmium waste battery positive electrode material
A technology for positive electrode materials and waste batteries, which is applied in the field of leaching of nickel-cadmium waste battery positive electrode materials, can solve the problems of industrial pure oxygen storage, transportation and use troubles, industrial pure oxygen is uneconomical for personal use, and the amount of industrial pure oxygen is not large, etc. Achieve obvious economic and environmental benefits, reduce pollution treatment costs, and increase metal leaching rate
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Embodiment 1
[0020] Example 1: Add 100 g of the positive electrode material (containing 55.2% nickel, 3.8% cobalt) and 35.5 g reed powder ≤ 1.5 mm into a titanium-lined pressure reactor with a volume of 2 L through roasting pretreatment, and add sulfuric acid concentration 800ml of mixed acid solution with a concentration of 1.5mol / L and a concentration of nitric acid of 5g / L was stirred at 50°C to 60°C (stirring speed 80r / min) for 4 hours, and liquid-solid separation was performed after the leaching was completed to obtain 770ml of leaching solution (without leaching slag washing water). The leaching rates of nickel and cobalt are 99.1% and 99.0% respectively (calculated based on nickel and cobalt entering the leaching solution and leaching slag washing solution).
Embodiment 2
[0021] Example 2: Add 220 g of reed powder ≤ 1.5 mm into a titanium-lined pressure reactor with a volume of 5 L, and add sulfuric acid at a concentration of 3.0 mol / L, nitric acid concentration of 10g / L mixed acid solution 2500 ml, stirred at 70 ℃ ~ 80 ℃ (stirring speed 70r / min) leaching for 2 hours, after leaching, liquid-solid separation was carried out to obtain 2300 ml leaching solution (without leaching slag washing water). The leaching rates of nickel and cobalt are 99.4% and 99.1% respectively (calculated based on nickel and cobalt entering the leaching solution and leaching slag washing solution).
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