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This study introduces a mechanistic model for the recovery of lithium and cobalt from LiCoO$_2$ during acidic-reductive leaching, incorporating the effects of HCl and H$_2$O$_2$. The model accounts for various factors including particle size, film formation-dissolution dynamics, and passivation effects, and was validated against experimental data across multiple acid and H$_2$O$_2$ concentrations. Key findings indicate that while the model performs well at lower acid concentrations, it tends to over-predict recovery at higher acid levels in the presence of H$_2$O$_2$, suggesting areas for further refinement.
Recovery of lithium and cobalt from LiCoO$_2$ can be accurately modeled, revealing critical insights into the impact of acid and reducing agent concentrations on leaching efficiency.
We developed a new mechanistic model for lithium and cobalt recovery during acidic-reductive leaching from LiCoO$_2$. The system considers HCl as an acid and H$_2$O$_2$ as a reducing agent. The model tracks conversion of LCO, the particle radius, the acid, H$_2$O$_2$, formation-dissolution dynamics of Co$_3$O$_4$ film, the film thickness, recovery of lithium and cobalt, and moles of O$_2$. We introduced the film passivation effects for reduced recovery in the absence of H$_2$O$_2$. We validated the model against the experimental data of recovered Li and Co reported in literature at three acid concentrations (0.5 M, 1.5 M, and 2.5 M) and four H$_2$O$_2$ concentrations (0%, 0.2%, 0.4%, and 0.6% (v/v)). The model works reasonably well at 0.5 M and 1.5 M HCl for the 0% and 0.6% concentrations of H$_2$O$_2$. At 2.5 M HCl, the model over-predicts the data in the presence of H$_2$O$_2$, while it works well at 0% H$_2$O$_2$. We suggest pathways for further improvements in the model. The comprehensive mechanistic modelling framework for the leaching with a full list of the equations, the parameters, and the variables, reported for the first time, can be extended to other cathode chemistries and acid-reductive leaching systems.