Method for leaching positive pole material of waste lithium nickelate battery
A lithium nickel oxide waste battery and positive electrode material technology, applied in the direction of improving process efficiency, etc., can solve the problems of uneconomical industrial pure oxygen for personal use, troublesome storage, transportation and use of industrial pure oxygen, and small amount of industrial pure oxygen. Achieve obvious economic and environmental benefits, lower pollution control costs, and increase metal leaching rates
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Embodiment 1
[0015] Embodiment 1: 100g lithium nickelate waste battery positive electrode material (containing nickel 54.3%, lithium 5.5%, copper 7.8%, aluminum 3.1%) is added in the stainless steel reaction kettle that volume is 2L, adds the sulfuric acid 1300ml of 1.5mol / L, join (NH 4 ) 2 SO 3 59g (300ml solution), stirring at 40°C-50°C (stirring speed 80r / min) for 2.5 hours, liquid-solid separation after leaching, to obtain 1550ml leaching solution (excluding leaching slag washing water). The leaching rates of nickel, lithium, copper, and aluminum are 99.0%, 99.2%, 98.5%, and 98.2% respectively (calculated based on nickel, lithium, copper, and aluminum entering the leaching solution and leaching slag washing solution).
Embodiment 2
[0016] Embodiment 2: 500g lithium nickelate waste battery cathode material (containing nickel 54.3%, lithium 5.5%, copper 7.8%, aluminum 3.1%) is added in the stainless steel reaction kettle that volume is 5L, adds the sulfuric acid 3200ml of 3.5mol / L , join (NH 4 ) 2 SO 3 310g (1600ml solution), stirring at 70℃~80℃ (stirring speed 70r / min) for 1.0 hour, liquid-solid separation after leaching, to obtain 4600ml leaching solution (excluding leaching slag washing water). The leaching rates of nickel, lithium, copper and aluminum are 99.6%, 99.7%, 99.2% and 99.0% respectively (calculated based on nickel, lithium, copper and aluminum entering the leaching solution and leaching slag washing solution).
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