Biobutanol obtained via an acetone–butanol–ethanol
(ABE) fermentation process is now considered a potential biofuel.
In recent times low density phosphonium cations were found to remove
butanol from aqueous solutions. In this regard, low density phosphonium-based
ionic liquids (ILs) trihexyl(tetradecyl)phosphonium dicyanamide [TDTHP][DCA]
and trihexyl(tetradecyl)phosphonium decanoate [TDTHP][DEC] have been
used for the separation of 1-butanol from aqueous solution. Ternary
liquid–liquid equilibrium data for IL(1)–1-butanol(2)–water(3)
are measured at T = 298.15 K and p = 1 atm. Butanol partition coefficients are obtained in the range
of 25–85 and 20–290 for [TDTHP][DCA] and [TDTHP][DEC],
respectively. 1H NMR spectra indicates the absence of IL
and water in the raffinate and extract phase, respectively. This experimentally
confirms that there will be negligible cross-contamination of water
and IL in either phase. The separation factor of butanol over water
approaches infinity for both systems. A wider spread of binodal curve
indicated a higher recovery of butanol at different feed concentrations.
The experimental data were compared with excess Gibb’s free
energy models, namely the nonrandom two liquid (NRTL) and the universal
quasichemical (UNIQUAC) models. NRTL and UNIQUAC gave root mean square
deviation (RMSD) values in the range of 0.12–0.14% and 0.48–0.55%,
respectively, for both ILs. Further the predictive ability of a statistical
mechanical framework was also performed using the well-known COSMO-RS
model. The COSMO-RS model gave RMSD values of 18.67% and 16.21% for
the systems containing the ILs respectively, [TDTHP][DCA] and [TDTHP][DEC].