In the reported study, experimental liquid–liquid
equilibrium
(LLE) data for extracting isopropanol from cyclohexane utilizing 1,4-butanediol,
1,2-propanediol, dimethyl sulfoxide, and N,N-dimethylformamide as solvents were obtained at 303.2 K
and atmospheric pressure. The separation factors derived from experimentally
measured LLE data were computed to determine the extracting capability
of the different solvents, and Othmer–Tobias, Hand, and Bachman
equations were used to estimate the reliability and consistency of
the LLE data. In addition, the nonrandom two-liquid (NRTL) thermodynamic
model in Aspen Plus software was used to regress the LLE data, providing
optimized binary interaction parameters. The regression results agreed
well with the experimentally determined LLE values, indicating that
the NRTL method was suitable to correlate the LLE data for the four
ternary systems.