Here, Ni, Co, and Li ions in the leachate obtained from
commercial
LiCoO2/LiNiO2 cathode materials by hydrothermal
leaching with citric acid were precipitated and separated in order
using a series of precipitants, dimethylglyoxime (DMG), (NH4)2C2O4, and Na3PO4, respectively. The parameters including the pH value, precipitant
amount, and reaction temperature were optimized during the metal separation
step. Finally, the recovery rates of Ni, Co, and Li were 97.2, 96.1,
and 94.1%, respectively, with the purities of Ni, Co, and Li in the
corresponding precipitate being 96.3, 96.2, and 99.9%, respectively.
The method of hydrothermal leaching was compared with the method of
traditional leaching in terms of the leaching mechanism and the metal
separation performance of the obtained leachates. Compared with the
traditional leaching with a reductant (e.g., H2O2), hydrothermal leaching is performed at higher temperatures and
requires pressure-resistant reactors, but it can reduce the consumption
of chemicals such as reductants, promote the reaction rate, and improve
industrial applicability. Even though the leaching mechanisms were
different, the leachates obtained by hydrothermal and traditional
leaching showed comparable performance in the metal separation step,
indicating hydrothermal leaching is qualified to produce leachates
for lithium-ion battery (LIB) recycling. With the success of isolating
metal components from the leachate obtained by hydrothermal leaching,
an upgraded hydrometallurgical method, composed of hydrothermal leaching
and precipitation separation steps, was officially launched for LIB
recycling and is subject to further development.