Lithium recovery process of waste lithium ion batteries
A lithium-ion battery and waste technology, applied in the field of lithium recovery technology, can solve the problems of difficult purification, long process, waste, etc., and achieve the effect of efficient recovery, simple process and high recovery rate
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Embodiment 1
[0018] A kind of lithium reclaiming process of waste and old lithium ion battery, carries out according to the following steps,
[0019] (a) Crushing and sorting waste lithium-ion batteries to obtain positive and negative electrode active material powders and separators; crushing includes two steps of coarse crushing and fine crushing; after testing, the nickel in the positive and negative electrode active material powders obtained by sorting The mass content is 16%, the mass content of cobalt is 10%, the mass content of manganese is 15%, and the mass content of lithium is 7%, and the separator component obtained by sorting is polyethylene;
[0020] (b) Place the positive and negative active material powder and separator obtained by sorting in step (a) into a roasting furnace with a temperature of 600° C. for 3 h, wherein the added mass of the separator is 11% of the added mass of the positive and negative active material powder %;
[0021] (c) leaching the roasted product ob...
Embodiment 2
[0024] A kind of lithium recovery process of waste lithium ion battery, its step is basically the same as the step of the lithium recovery process of waste lithium ion battery in embodiment 1, and its difference is:
[0025] 1. In step (a), after testing, in step (a), the mass content of nickel in the positive and negative electrode active material powder obtained by sorting is 19%, the mass content of cobalt is 8%, and the mass content of manganese is 18%, The mass content of lithium is 5%, and the separator components obtained by sorting are polyethylene and polypropylene;
[0026] 2. In step (b), the temperature of the roasting furnace is controlled at 650° C., the mass of the separator is 20% of the mass of the positive and negative active material powders, and the roasting time is controlled at 5 hours;
[0027] 3. In step (c), the solid-to-liquid ratio of the roasted product to the oxalic acid solution is 15g:1L, the molar concentration of oxalic acid is 1.5mol / l, the le...
Embodiment 3
[0030] A kind of lithium recovery process of waste lithium ion battery, its step is basically the same as the step of the lithium recovery process of waste lithium ion battery in embodiment 1, and its difference is:
[0031] 1. In step (a), after testing, in step (a), the mass content of nickel in the positive and negative electrode active material powder obtained by sorting is 17%, the mass content of cobalt is 7%, the mass content of manganese is 15.5%, The mass content of lithium is 6%, and the separator components obtained by sorting are polyethylene and polypropylene;
[0032] 2. In step (b), the temperature of the roasting furnace is controlled at 625° C., the mass of the separator is 18% of the mass of the positive and negative active material powders, and the roasting time is controlled at 4 hours;
[0033] 3. In step (c), the solid-to-liquid ratio of the roasted product to the oxalic acid solution is 45g:1L, the molar concentration of oxalic acid is 2mol / l, the leachi...
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