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, reduce pollution treatment costs, and increase the metal leaching rate
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Embodiment 1
[0011] Example 1: Add 100g of lithium cobalt oxide waste battery cathode material (containing 53.6% of cobalt, 5.3% of lithium, 8.2% of copper, and 3.4% of aluminum) into a stainless steel reactor with a volume of 2L, add 1150ml of 1.5mol / L sulfuric acid, Stir at 40℃~50℃ (stirring speed 80r / min) and pass SO 2 The leaching is 3.0h, and the leaching pressure is 0.05MPa. After the leaching is completed, liquid-solid separation is performed to obtain 1120ml leaching solution (without leaching residue washing water). The leaching rates of cobalt, lithium, copper and aluminum were 99.1%, 99.2%, 98.3% and 98.7% respectively (calculated based on the cobalt, lithium, copper and aluminum entering the leaching solution and the washing solution of the leaching residue).
Embodiment 2
[0012] Example 2: Add 500g of lithium cobalt oxide waste battery cathode material (containing 53.6% cobalt, 5.3% lithium, 8.2% copper, and 3.4% aluminum) into a stainless steel reactor with a volume of 5L, and add 3500ml of 3.0mol / L sulfuric acid, Stir at 70℃~80℃ (stirring speed 70r / min) and pass SO 2 After leaching for 1 hour, the leaching pressure is 0.15MPa. After leaching, liquid-solid separation is performed to obtain 3300ml leaching solution (without leaching residue washing water). The leaching rates of cobalt, lithium, copper, and aluminum are 99.6%, 99.8%, and 99.1%, respectively And 99.2% (calculated based on the cobalt, lithium, copper and aluminum entering the leaching solution and the washing solution of the leaching residue).
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