Method for recycling valuable metal from waste lithium-ion power battery
A power battery and valuable metal technology, applied in battery recycling, waste collector recycling, recycling technology and other directions, can solve the problems of insignificant economic benefits, low recycling efficiency, complex process flow, etc., and achieve steps to reduce battery classification , considerable economic benefits, the effect of simple recycling process
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Embodiment 1
[0028] A method for recovering valuable metals in waste lithium-ion power batteries, such as figure 1 shown, including the following steps:
[0029] (1) Disassemble and shell the waste lithium-ion power battery after discharge to obtain the battery core;
[0030] (2) Disassemble and separate the positive electrode sheet from the battery core;
[0031] (3) The positive electrode sheet is calcined at 400°C for 4h in a nitrogen atmosphere, and the binder PVDF and separator in the battery core are pyrolyzed;
[0032] (4) The battery core obtained in step (3) is crushed and passed through an 80-mesh sieve, and the under-sieve is taken to obtain a mixed powder of LFP and NCM;
[0033] (5) Add 4mol / L sulfuric acid and 2ml hydrogen peroxide per gram to the mixed powder in sequence, the reaction temperature is 90°C, and the mass-volume ratio of the added mixed powder to sulfuric acid is 1 / 10 (kg / L) , filter to remove carbon residue to obtain leachate;
[0034] (6) Adjust the leachi...
Embodiment 2
[0041] (1) Disassemble and shell the waste lithium-ion power battery after discharge to obtain the battery core;
[0042] (2) Disassemble and separate the positive electrode sheet from the battery core;
[0043] (3) The positive electrode sheet is calcined at 500°C for 3 hours in a nitrogen atmosphere, and the binder PVDF and separator in the battery core are pyrolyzed;
[0044] (4) The battery core obtained in step (3) is crushed and passed through an 80-mesh sieve, and the under-sieve is taken to obtain a mixed powder of LFP and NCM;
[0045] (5) Add 3mol / L sulfuric acid and 4ml hydrogen peroxide per gram to the mixed powder in turn, the reaction temperature is 80°C, and the mass-volume ratio of the added mixed powder to sulfuric acid is 1 / 8 (kg / L) , filter to remove carbon residue to obtain leachate;
[0046] (6) Adjust the leaching solution with ammonia water to pH=2 to precipitate ferric phosphate, and filter to obtain the filtrate;
[0047] (7) Adjust the leaching sol...
Embodiment 3
[0053] (1) Disassemble and shell the waste lithium-ion power battery after discharge to obtain the battery core;
[0054] (2) Disassemble and separate the positive electrode sheet from the battery core;
[0055] (3) The positive electrode sheet is calcined at 600°C for 2 hours in a nitrogen atmosphere, and the binder PVDF and separator in the battery core are pyrolyzed;
[0056] (4) The battery core obtained in step (3) is crushed and passed through an 80-mesh sieve, and the under-sieve is taken to obtain a mixed powder of LFP and NCM;
[0057] (5) Add 2.5mol / L of sulfuric acid and 3ml of hydrogen peroxide per gram of material in turn to the mixed powder, the reaction temperature is 60°C, and the mass-volume ratio of the added mixed powder to sulfuric acid is 1 / 6 (kg / L ), filter to remove carbon residue to obtain leachate;
[0058] (6) Adjust the leaching solution with ammonia water to pH=2.5 to precipitate ferric phosphate, and filter to obtain the filtrate;
[0059] (7) A...
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