Recovery of Li and Fe from spent lithium iron phosphate using organic acid leaching system
(1. Faculty of Metallurgical and Energy Engineering, Kunming University of Science and Technology, Kunming 650093, China;
2. National Engineering Laboratory of Vacuum Metallurgy, Kunming University of Science and Technology, Kunming 650093, China)
2. National Engineering Laboratory of Vacuum Metallurgy, Kunming University of Science and Technology, Kunming 650093, China)
Abstract: The valuable metals, lithium and iron, were recovered from spent LiFePO4 cathode powder by hydro- metallurgy, and the recycled products were used as raw materials for the preparation of lithium iron phosphate. By the optimization of the leaching process parameters, the leaching efficiency of Li reached 96.56% at pyruvic acid concentration of 3.0 mol/L, volume of H2O2 of 2 mL, solid-to-liquid ratio of 0.1 g/mL, reaction temperature of 80 °C, and reaction time of 20 min. The leached residue was characterized by XRD, XPS, and FE-SEM coupled with EDS, and the results showed that the leached residue was FePO4 with an Fe/P molar ratio of 0.974. After adjusting the pH of the leaching solution to 12.0 and stirring for 2 h at 80 °C, the recovery of Li from the leaching solution was enabled by in-situ precipitation in the form of Li3PO4 with a purity of 96.5 wt.%. The reaction kinetic data of Li leaching using the pyruvic acid/H2O2 solution were fit to the Avrami model with R2>0.95. The low activation energy of the Li leaching process indicated that diffusion step limited the reaction rate during the leaching process.
Key words: spent LiFePO4; pyruvic acid; leaching kinetics; Avrami model; lithium ion batteries