Method for selectively leaching lithium from anode material of failed lithium iron phosphate battery
A lithium iron phosphate battery and positive electrode material technology, applied in the field of selective leaching of lithium, can solve the problems of large impurities and low recovery efficiency of iron phosphate, and achieve the effects of higher acid consumption, better separation effect and less acid consumption
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Embodiment 1
[0017] Example 1: A method using H 3 PO 4 -H 2 o 2 Systematic method for treating invalid lithium iron phosphate battery cathode material
[0018] The anode material of the spent lithium iron phosphate battery, after removing aluminum, is mixed with a phosphoric acid solution with a mass fraction of 10% at a liquid-solid mass ratio of 5:1 and continuously stirred. Slowly add hydrogen peroxide solution with a mass fraction of 50% at 25°C, the mass ratio of the added hydrogen peroxide to the positive electrode material is 0.5:1, react with Na 3 PO 4 The pH of the solution was adjusted to 4.5. Filtration, the filter residue is ferric phosphate, the filtrate is the deferron leaching solution, and the leaching rate of lithium is 95.23%.
Embodiment 2
[0019] Example 2: A method using H 3 PO 4 -H 2 o 2 Systematic method for treating invalid lithium iron phosphate battery cathode material
[0020] The anode material of the spent lithium iron phosphate battery, after removing aluminum, was mixed with the phosphoric acid solution with a mass fraction of 85% according to the liquid-solid mass ratio of 0.5:1, and the slurry was continuously stirred. Slowly add hydrogen peroxide solution with a mass fraction of 10% at 90°C, the mass ratio of the added hydrogen peroxide to the positive electrode material is 3:1, react with K after 6 hours 3 PO 4 The pH of the solution was adjusted to 3.0. Filtration, the filter residue is ferric phosphate, the filtrate is the deferron leaching solution, and the leaching rate of lithium is 99.21%.
Embodiment 3
[0021] Example 3: A method using H 3 PO 4 -H 2 o 2 Systematic method for treating invalid lithium iron phosphate battery cathode material
[0022] The anode material of the spent lithium iron phosphate battery, after removing aluminum, is mixed with a phosphoric acid solution with a mass fraction of 50% at a liquid-solid mass ratio of 0.5:1 and continuously stirred. Slowly add a hydrogen peroxide solution with a mass fraction of 35% at 60°C, the mass ratio of the added hydrogen peroxide to the positive electrode material is 1.5:1, and react with Na 3 PO 4 with K 3 PO 4 The mixed solution was adjusted to pH 4.0. Filtration, the filter residue is ferric phosphate, the filtrate is the deferron leaching solution, and the lithium leaching rate is 99.83%.
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