Leaching method of nickel-cadmium waste battery positive-negative electrode mixed material
A technology of mixed materials and waste batteries, applied in the direction of improving process efficiency, etc., can solve the problems of industrial pure oxygen storage, transportation and use trouble, industrial pure oxygen is uneconomical for self-use, industrial pure oxygen is not large, etc., to achieve obvious economy Benefits and environmental benefits, lower pollution control costs, and the effect of increasing metal leaching rates
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Embodiment 1
[0014] Embodiment 1: 100g nickel-cadmium waste battery positive and negative electrode mixed material (containing nickel 30.5%, cobalt 1.6%, cadmium 28.1%) is added in the stainless steel reaction kettle that volume is 1L, adds the sulfuric acid 600ml of 1.5mol / L, at 40 Stir at ℃~50℃ (stirring speed 80r / min) into SO 2 After leaching for 2.5 hours, the leaching pressure was 0.05MPa. After the leaching was completed, liquid-solid separation was performed to obtain 580ml of leaching solution (excluding leaching slag washing water). The leaching rates of nickel, cobalt and cadmium are 99.0%, 98.7% and 99.3% respectively (calculated based on nickel, cobalt and cadmium entering the leaching solution and leaching slag washing solution).
Embodiment 2
[0015] Embodiment 2: 500g nickel-cadmium waste battery positive and negative electrode mixed material (containing nickel 30.5%, cobalt 1.6%, cadmium 28.1%) is added in the stainless steel reaction kettle that volume is 2L, adds the sulfuric acid 1700ml of 3.0mol / L, at 70 Stir at ℃~80℃ (stirring speed is 70r / min) for 1.0h leaching, leaching pressure is 0.15MPa, after leaching, liquid-solid separation is carried out to obtain 1600ml leaching solution (excluding leaching slag washing water), nickel, cobalt and cadmium The leaching rates are 99.7%, 99.2% and 99.4% (calculated based on nickel, cobalt and cadmium entering the leaching solution and leaching slag washing solution).
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