Lithium-ion batteries recycling process
A lithium-ion battery and ion battery technology, applied in battery recycling, secondary batteries, recycling technology, etc., can solve the problem of inability to process battery purification and value-added elements
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Embodiment I
[0100] All processes of the battery recycling method described in the following examples were carried out continuously at laboratory scale. They include mincing, grinding, sieving, electrolyte solvent extraction, leaching, precipitation (sulfide, hydroxide, and carbonation), solvent extraction, electrowinning, and crystallization. First, the battery is roughly shredded, and the electrolyte solvent is recovered by evaporation. The chopped solids are then finely ground, then sieved and magnetized to remove plastic and iron respectively and leached. Na 2 S was added to the leachate to obtain sulfide precipitation, and then the pH of the resulting leachate was increased to obtain hydroxide precipitation. The leachate is then contacted with an organic solvent. This organic solvent is then washed, stripped, and finally transferred to an electrowinning cell. The pH of the aqueous solution is raised again to obtain nickel hydroxide. Afterwards, the temperature is lowered to remov...
Embodiment II
[0114] The method of Example 1 was repeated, except that three other operations were added: sieving, magnetic iron removal and reuse of the final aqueous solution containing a small amount of lithium.
[0115] Sieving is used to separate the metal powder from unwanted residue (plastic and metal parts) before leaching the metal powder. Small parts of iron are then removed by magnetic force. These two added actions help reduce the amount of iron precipitation and hydroxide filtration time.
[0116] Recycling the final aqueous solution containing a small amount of lithium back to the leaching step not only complies with environmental standards and saves water, but also recovers the remaining lithium that has not been carbonated.
[0117] Table 2
[0118]
Embodiment III
[0120] In this embodiment, in order to further improve the efficiency of the leaching operation, the leaching operation is repeated.
[0121] The efficiency of the leaching operation can be improved by optimizing the leaching parameters. Use a reducing agent such as 10g / L aluminum (foil) or 4g / L manganese dioxide to replace some or all of the hydrogen peroxide. Add 1.6mL / g H 2 o 2 and 4g / L MnO 2 seems to be the most effective.
[0122]
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