Infusion method of Ni-MH used battery anode and cathode mixed material
A nickel-metal hydride waste battery and mixed material technology, applied in the direction of improving process efficiency, can solve the problems of large consumption of nitric acid, polluting the environment, large nitrogen oxides, etc., achieve obvious economic and environmental benefits, and save pollution control Cost, the effect of avoiding the production of pollutant nitrogen oxides
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Embodiment 1
[0050] Example 1: Add 100 g of waste nickel-hydrogen battery positive and negative mixed materials (containing 57.5% nickel, 6.1% cobalt, and 13.2% rare earth) into a titanium-lined autoclave with a volume of 1 L, add 600 ml of 3.0 mol / L sulfuric acid, and add Nitric acid 9g (as HNO 3 0.2MPa industrial pure oxygen, stirring at 50-60°C (stirring speed 80r / min) for 2 hours, liquid-solid separation after leaching, to obtain 580ml leaching solution (excluding leaching slag washing water ). The reaction tail gas is about 1.2L (converted into a volume with an absolute pressure of 0.1MPa), and the concentration of nitrogen oxides is 2.6mg / m 3 . The leaching rates of nickel, cobalt and rare earth are 98.6%, 97.2% and 6.4% respectively (calculated according to nickel, cobalt and rare earth entering the leaching solution and leaching slag washing solution).
Embodiment 2
[0051] Example 2: 500g of waste nickel-hydrogen battery positive and negative mixed materials (containing 57.5% nickel, 6.1% cobalt, and 13.2% rare earth) were added into a titanium-lined autoclave with a volume of 5L, and 4.5L of 2.0mol / L sulfuric acid was added, Add 70g of nitric acid (as HNO 3 ) into 0.1MPa industrial pure oxygen, stirring at 60-70°C (stirring speed: 80r / min) for 3 hours, and liquid-solid separation after leaching, to obtain 4.8L leaching solution (not including leaching slag washing water), the reaction tail gas is about 1L (converted into a volume with an absolute pressure of 0.1MPa), and the concentration of nitrogen oxides is 3.3mg / m 3 . The leaching rates of nickel, cobalt and rare earths are 98.8%, 98.1% and 8.5% respectively (calculated according to nickel, cobalt and rare earths entering the leaching solution and leaching slag washing solution).
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