Abstract

With the rapid growth in demand and capacity of lithium-ion batteries (LIBs), a large number of spent LIBs with the dual attributes of hazardous waste and high value-added resources have also experienced a spurt in retirement. In this paper, a process of hydrogen reduction - water-leaching to recover Li – H2SO4 cycle-leaching to recover Ni/Co/Mn to regenerate ternary cathode (NCM) precursor was used to treat mixed spent NCM, and its recovery mechanism was investigated. Under the optimal conditions, Li was completely converted into readily-soluble LiOH by hydrogen reduction and then recovered by water-leaching and CO2 precipitation to regenerate high-purity Li2CO3. While Ni/Co/Mn was reduced to low-valent and could basically be completely leached by H2SO4 and the H2SO4-leaching solution could be cycled to leach Ni/Co/Mn after supplementing with some H2SO4. When the cycle time reached 5, the concentrations of Ni/Co/Mn reached 144.79 g/L, 100.01 g/L, 113.39 g/L, respectively. Finally, a few solids that could not be completely dissolved due to the cycle were leached out by H2SO4 and mixed with the cycle-leaching solution to regenerate the NCM precursor with high-purity and excellent performance for direct commercial application by coprecipitation.

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