Method for recovering valuable metals by reduction smelting of positive electrode materials of waste lithium iron phosphate batteries
A technology for lithium iron phosphate batteries and cathode materials, which is applied in the direction of improving process efficiency, can solve the problems of large acid consumption, high recovery cost, long process flow, etc., and achieves simple operation process, high recovery cost and long process flow. Effect
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Embodiment 1
[0028] A method for reducing, smelting, and recovering valuable metals from a waste lithium iron phosphate battery cathode material, comprising the following steps:
[0029] Accurately weigh 50g of waste lithium iron phosphate battery cathode material, 100g of waste lead paste (the mass content of lead sulfate is 60%, the same below), and the amount of reducing agent (coke) is 6% of the total mass of the above two, and mix them well. Then put it into a corundum crucible, and then put the crucible into an electric furnace for reduction and smelting. During the process, argon gas was introduced as a protective gas, and the reduction temperature was controlled to be 550 ° C and the reduction time was 120 minutes. After the reduction is completed, the reduction product is taken out, and the slag and the metal are separated, weighed and analyzed. Lithium is recovered from the reduced slag by carbonized water leaching, and the remaining slag phase is collected to recover iron.
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Embodiment 2
[0032] A method for reducing, smelting, and recovering valuable metals from a waste lithium iron phosphate battery cathode material, comprising the following steps:
[0033]Accurately weigh 50g of waste lithium iron phosphate battery material, 120g of waste lead paste, and the amount of reducing agent (coke) is 8% of the total mass of the above two, fully mixed and put into a corundum crucible, and then put the crucible into an electric furnace The reduction smelting was carried out, argon gas was introduced into the process as a protective gas, the reduction temperature was controlled to be 650 °C, and the reduction time was 150 min. After the reduction is completed, the reduction product is taken out, and the slag and the metal are separated, weighed and analyzed. The reduced slag is leached by carbonization to recover lithium, and the remaining slag phase is collected to recover iron.
[0034] In this embodiment, after leaching lithium with water, the yield of lithium is 9...
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Abstract
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