Method for preparing lithium carbonate and ternary precursor by recycling waste ternary lithium battery
A ternary lithium battery and ternary battery technology, applied in the field of solid waste recycling, can solve problems such as affecting the quality of nickel-cobalt-manganese precursors, reducing lithium recovery rate, etc., reducing the difficulty of acid leaching and high recovery rate of valuable metals , the effect of shortening the process
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Embodiment 1
[0024] Put the waste ternary lithium-ion battery into salt water for discharge, then disassemble, crush and sieve. Take 50g of the undersize powder, and roast it under the condition of 550°C for 2h without air. The roasted product and 200mL water were mechanically stirred and leached at 45°C, and CO was continuously introduced at a flow rate of 200mL / min. 2 . After the reaction, the lithium-containing water immersion liquid and water leaching residue were obtained by solid-liquid separation. After testing and calculation, the leaching rate of lithium reached 90.2%, and the leaching rates of nickel, cobalt, and manganese were 0.65%, 0.08%, and 0.12%, respectively. Lithium-containing water The immersion solution is evaporated and crystallized at 100° C. to obtain a lithium carbonate product with a purity of more than 99%. The water leaching residue is acid-leached with sulfuric acid whose total molar weight of nickel, cobalt and manganese is 1.4 times, acid leaching for 2 hour...
Embodiment 2
[0026] Put the waste ternary lithium-ion battery into salt water for discharge, then disassemble, crush and sieve. Take 50g of undersize powder, and roast it in air isolation at 600°C for 3h. The roasted product was leached with 250 mL of water under mechanical stirring at 40 °C, and CO was continuously introduced at a flow rate of 100 mL / min. 2 . After the reaction, the lithium-containing water immersion solution and water leaching residue were obtained by solid-liquid separation. After testing and calculation, the leaching rate of lithium reached 91.3%, and the leaching rates of nickel, cobalt, and manganese were 0.64%, 0.05%, and 0.16%, respectively. Lithium-containing water The immersion solution is evaporated and crystallized at 100° C. to obtain a lithium carbonate product with a purity of more than 99%. The water leaching residue is acid-leached with sulfuric acid whose total molar weight of nickel, cobalt and manganese is 1.2 times, acid leaching for 1 hour under the...
Embodiment 3
[0028] Put the waste ternary lithium-ion battery into salt water for discharge, then disassemble, crush and sieve. Take 50g of the undersize powder, and roast it under the condition of 650°C for 1h without air. The roasted product and 300mL water were mechanically stirred and leached at 25°C, and CO was continuously introduced at a flow rate of 150mL / min. 2. After the reaction, the lithium-containing water immersion solution and water leaching residue were obtained by solid-liquid separation. After testing and calculation, the leaching rate of lithium reached 90.4%, and the leaching rates of nickel, cobalt, and manganese were 0.69%, 0.09%, and 0.18%, respectively. Lithium-containing water The immersion solution is evaporated and crystallized at 100° C. to obtain a lithium carbonate product with a purity of more than 99%. The water leaching residue is acid-leached with sulfuric acid whose total molar weight of nickel, cobalt and manganese is 1.6 times, acid leaching for 3 hou...
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