Leaching method of nickel-cadmium waste battery positive-negative electrode mixed material
A technology of mixed materials and positive and negative electrodes, which is applied in the field of leaching mixed positive and negative electrodes of nickel-cadmium waste batteries, can solve the problems of industrial pure oxygen storage, transportation and use, uneconomical industrial pure oxygen for personal use, and insufficient amount of industrial pure oxygen Major problems, achieving obvious economic and environmental benefits, reducing pollution treatment costs, and improving the metal leaching rate
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Embodiment 1
[0022] Example 1: 100g of waste nickel-cadmium battery positive and negative mixed materials (containing 30.5% nickel, 1.6% cobalt, and 28.1% cadmium) and ≤1.5mm coconut shell powder 19.5g were added to a titanium-lined pressure reactor with a volume of 1L. Add 590ml of a mixed acid solution with a sulfuric acid concentration of 1.5mol / L and a nitric acid concentration of 5g / L, stir at 50°C to 60°C (stirring speed 80r / min) for leaching for 4 hours, and perform liquid-solid separation after leaching to obtain 560ml of leaching solution (excluding leaching slag washing water). The leaching rates of nickel, cobalt and cadmium are 99.3%, 99.0% and 99.4% respectively (calculated based on nickel, cobalt and cadmium entering the leaching solution and leaching slag washing solution).
Embodiment 2
[0023] Example 2: 500g of waste nickel-cadmium battery positive and negative mixed materials (containing 30.5% nickel, 1.6% cobalt, 28.1% cadmium) ≤ 1.5mm coconut shell powder 120g was added to a titanium-lined pressure reactor with a volume of 5L, and sulfuric acid was added Concentration of 2.5mol / L, nitric acid concentration of 10g / L mixed acid solution 2200ml, stirred at 70 ℃ ~ 80 ℃ (stirring speed 70r / min) leaching 2h, liquid-solid separation after leaching, to obtain 2000ml leaching solution (excluding leaching slag washing water), the leaching rates of nickel, cobalt and cadmium are 99.6%, 99.4% and 99.3% respectively (calculated based on nickel, cobalt and cadmium entering the leaching solution and leaching slag washing solution).
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