Recycling method of waste lithium iron phosphate battery
A lithium iron phosphate battery and recovery method technology, applied in chemical instruments and methods, iron oxides, phosphorus compounds, etc., can solve the problems of inability to thoroughly remove impurities and purification of leachate, loss of lithium, and low purity of recovered products, and achieve both environmental protection and Economic benefits, lower requirements for production equipment, and the effect of easy control of the reaction end point
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Embodiment 1
[0041] A method for recycling waste lithium iron phosphate batteries, comprising:
[0042] (1) Soak the waste lithium iron phosphate battery in 5% NaCl solution until the end-of-discharge voltage is 1V, disassemble the battery cell, and then carry out mechanical crushing, roasting, and screening to obtain electrodes with a particle size of less than 0.1mm The active material powder is filtered and dried to obtain the material to be treated after alkali washing; among them, during the alkali washing process, the lye used is NaOH, the pH of the lye is 10, the alkali wash time is controlled at 15min, and the temperature is controlled at 25 ℃;
[0043] (2) the material that step (1) obtains adopts dilute sulfuric acid+H 2 o 2 Leach out, filter and obtain lithium-rich leach solution (i.e. lithium enrichment solution) and filter residue (i.e. iron-rich phosphorus slag); specific parameters are as follows: 0.2mol / L H 2 SO 4 , the dosage is solid-liquid ratio 50g / L, H 2 o 2 The ...
Embodiment 2
[0052] A method for recycling waste lithium iron phosphate batteries, comprising:
[0053] (1) Soak the waste lithium iron phosphate battery in 5% NaCl solution until the end-of-discharge voltage is 1V, disassemble the battery cell, and then carry out mechanical crushing, roasting, and screening to obtain electrodes with a particle size of less than 0.1mm The active material powder is filtered and dried to obtain the material to be treated after alkali washing; among them, in the alkali washing process, the lye used is KOH, the pH of the lye is 12, the alkali wash time is controlled at 55min, and the temperature is controlled at 45 ℃;
[0054] (2) the material that step (1) is obtained adopts citric acid+FeCl 3 Leaching, filtering to obtain lithium-rich leaching solution (i.e. lithium enrichment solution) and filter residue (i.e. iron-rich phosphorus slag); specific parameters are as follows: 0.5mol / L citric acid, the dosage is 200g / L solid-to-liquid ratio, FeCl 3 The dosage...
Embodiment 3
[0063] A method for recycling waste lithium iron phosphate batteries, comprising:
[0064] (1) Soak the waste lithium iron phosphate battery in 5% NaCl solution until the end-of-discharge voltage is 1V, disassemble the battery cell, and then carry out mechanical crushing, roasting, and screening to obtain electrodes with a particle size of less than 0.1mm The active material powder is filtered and dried to obtain the material to be treated after alkali washing; wherein, in the alkali washing process, the alkali used is NH 4 OH, the pH of the lye is 14, the alkaline washing time is controlled at 60 minutes, and the temperature is controlled at 35°C;
[0065] (2) The material obtained in step (1) is leached with acetic acid+NaClO (solid oxidizer), filtered to obtain a lithium-rich leach solution (i.e. lithium enrichment solution) and filter residue (i.e. iron-rich phosphorus slag); specific parameters are as follows: 0.3mol / L acetic acid, the dosage is solid-liquid ratio 100g / ...
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