This work focuses on the extension of group parameters of the UNIFAC model to systems
with ionic liquids. The new group parameters for ionic liquids were obtained by means of …

The UNIFAC model has recently become very popular for ionic liquids (ILs) because of its
applicability for prediction of thermodynamic properties. This work is a continuation of our …

Considering that the predictive UNIFAC model is highly valuable for the solvent selection,
process design and optimization of separation tasks, a large extension of this model to ionic …

Vapor–liquid equilibria at 363.15 K, and excess enthalpies in the temperature range 363.15–
413.15 K of binary systems containing the ionic liquids 1-butyl-1-methylpyrrolidinium bis …

Ternary liquid–liquid equilibria (LLE) data in systems involving ionic liquids has been
investigated by several years, mainly due to the innovative role of ionic liquids as extraction …

The modified UNIFAC (Dortmund) parameter matrix for ionic liquids has been extended.
Two new main groups for the anions alkylsulfate [RSO 4]− and hexafluorophosphate [PF 6] …

The new group binary interaction parameters of UNIFAC model (anm and amn) between
CO2 and 22 ionic liquid (IL) groups were obtained by means of correlating the solubility data …

In recent years, due to their advantages on good stability, non-volatility, tunable viscosity
and tailor-made properties, ionic liquids (ILs) have been regarded as novel potential …

Prediction of thermodynamic behavior is essential for the early design stage of separation
processes including solvent selection, process optimization, and its performance evaluation …

The united chemical thermodynamic model, that is, COSMO‐UNIFAC model was first
extended to the systems containing ionic liquids (ILs). This model for ILs combines the …