Leaching method of lithium iron phosphate waste battery positive electrode material
A technology of lithium iron phosphate and positive electrode materials, which is applied in the field of leaching of lithium iron phosphate waste battery positive electrode materials, which can solve the problems of industrial pure oxygen storage, transportation and use, uneconomical industrial pure oxygen for personal use, and small amount of industrial pure oxygen, etc. problems, achieving obvious economic and environmental benefits, reducing pollution control costs, and low cost
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Embodiment 1
[0013] Example 1: Add 100 g of lithium iron phosphate waste battery positive electrode material (containing 4.3% lithium, 5.2% aluminum, and 34.8% iron) into a stainless steel reactor with a volume of 1 L, add 820 ml of 1.5 mol / L sulfuric acid, and heat Stirring at 50°C (stirring speed 80r / min) into SO 2 After leaching for 3.0 hours, the leaching pressure was 0.05MPa. After the leaching was completed, liquid-solid separation was performed to obtain 780ml of leaching solution (excluding leaching slag washing water). The leaching rates of lithium, aluminum and iron are 99.7%, 0.01% and 99.5% respectively (calculated based on lithium, aluminum and iron entering the leaching solution and leaching slag washing solution).
Embodiment 2
[0014] Example 2: Add 300g of lithium iron phosphate waste battery positive electrode material (containing 4.3% lithium, 5.2% aluminum, and 34.8% iron) into a stainless steel reactor with a volume of 2L, add 1500ml of 3.0mol / L sulfuric acid, and heat it at 70°C- Stir at 80°C (stirring speed 70r / min) for 1 hour of leaching, and the leaching pressure is 0.15MPa. After leaching, liquid-solid separation is carried out to obtain 1300ml of leaching solution (excluding leaching slag washing water). The leaching rates of lithium, aluminum and iron are 99.8%, 0.01% and 99.7% respectively (calculated based on lithium, aluminum and iron entering the leaching solution and leaching slag washing solution).
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