“…Therefore, applying thermodynamic modeling becomes an efficient approach for designing task-specific DESs for liquid–liquid extraction applications. Various thermodynamic models, such as UNIFAC, , perturbed-chain statistical associating fluid theory (PC-SAFT), − and conductor-like screening model for real solvents (COSMO-RS), , can be employed to predict LLE in systems containing DESs. Nonetheless, UNIFAC is unsuitable for predicting the activity coefficients of salts due to the lack of group parameters.…”