Leaching method of lithium cobaltate waste battery positive electrode material
A technology for positive electrode materials and waste batteries, which is applied in the leaching field of positive electrode materials for lithium cobalt oxide waste batteries, and can solve problems such as troublesome storage, transportation and use of industrial pure oxygen, uneconomical use of industrial pure oxygen for personal use, and small amount of industrial pure oxygen. , to achieve obvious economic and environmental benefits, lower pollution control costs, and increase the metal leaching rate
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Embodiment 1
[0015] Example 1: Add 100g of lithium cobaltate lithium waste battery cathode material (containing 53.6% cobalt, 5.3% lithium, 8.2% copper, 3.4% aluminum) into a stainless steel reactor with a volume of 2L, add 1200ml of 1.5mol / L sulfuric acid, Add 1300ml of 1.5mol / L sulfuric acid, add Na 2 SO 3 51g (300ml solution), leaching at 40°C-50°C under airtight stirring (stirring speed 80r / min) for 2.5h, after leaching, liquid-solid separation was carried out to obtain 1450ml leaching solution (excluding leaching slag washing water). The leaching rates of cobalt, lithium, copper, and aluminum are 98.5%, 98.6%, 98.0%, and 98.1% respectively (calculated based on cobalt, lithium, copper, and aluminum entering the leaching solution and leaching slag washing solution).
Embodiment 2
[0016] Example 2: Add 500g of lithium cobalt oxide waste battery positive electrode material (containing 53.6% cobalt, 5.3% lithium, 8.2% copper, 3.4% aluminum) into a stainless steel reactor with a volume of 5L, and add it into a stainless steel reactor with a volume of 5L , add 3200 ml of 3.5mol / L sulfuric acid, add Na 2 SO 3 280g (1600ml solution), leaching at 70℃~80℃ with airtight stirring (stirring speed 70r / min) for 1.0h, after leaching, liquid-solid separation was carried out to obtain 4600ml leaching solution (excluding leaching slag washing water), cobalt, lithium The leaching rates of , copper and aluminum are 99.8%, 99.6%, 99.0% and 99.4% respectively (calculated based on cobalt, lithium, copper and aluminum entering the leaching solution and leaching slag washing solution).
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