Since the condensation temperatures of Cyclohexane and Benzene are close, the distillation process is useless for extraction, and it must be done with the help of a solvent. Sulfolane is widely used as a solvent for extracting aromatic hydrocarbons. The experimental (Liquid-Liquid) equilibrium (LLE) data will measure the ternary system of [Sulfolane + Benzene + Cyclohexane] and the pseudo-ternary systems (PTS) of [(Sulfolane + 2-propanol) + Benzene + Cyclohexane] at a temperature of 303.15 K under atmospheric pressure. Experimental distribution coefficients and selectivity factors were presented to evaluate the efficiency of the solvent for the extraction of benzene from cyclohexane. Solvents included pure sulfolane and a mixture of sulfolane with 5, 10, and 20% mass fractions of 2-propanol. The results indicated that adding 10% and 20% propanol to sulfolane leads to an increase of 70% and 169% in selectivity and a decrease of 14.3% and 2.9% in distribution coefficient respectively. It was found that using the cheaper solvent of Sulfurane + 2-Propanol can have the same efficiency in extracting cyclohexane from benzene compared to the expensive solvent of Sulfurane. The LLE data of the studied system are used to achieve binary interaction parameters in universal quasichemical)UNIQUAC(and non-random two-liquid)NRTL(thermodynamic models. They minimize the root mean square deviations (RMSD) between the experimental data and the computed results. The UNIQUAC model fits better with the liquid-liquid equilibrium data set for the systems considered. The low values of RMSD indicate that the ternary and pseudo-ternary systems could be well-fitted by the NRTL and UNIQUAC models. RMSDs achieved measuring computed and experimental two-phase compositions are 0.0481 for the UNIQUAC and 0.0512 for the NRTL models.
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