Isobaric
vapor–liquid equilibria (VLE) of binary mixtures
of the ionic liquid (IL) 1-hexyl-3-methylimidazolium trifluoromethanesulfonate
(C6mimTfO) and the n-alkyl alcohols methanol,
ethanol, propan-1-ol, and butan-1-ol at three pressures are reported.
Measurements were carried out at pressures of p =
1000, 700, and 500 mbar, which allowed to cover compositions in the
range of 0.24–0.35 ≤ x (n-alkyl alcohol) ≤ 1.0 and temperatures in the range of 321.8
K ≤ T ≤ 423.6 K. The experimental data
are described applying two theoretical models: (1) the nonrandom two-liquid
(NRTL) model as an example of a descriptive model for calculating
the excess free Gibbs energy G
E and (2)
the perturbed-chain statistical associating fluid theory (PC-SAFT)
equation of state (EoS) as an example of a model based on statistical
thermodynamics. Both approaches allow a description of the phase equilibria
with good accuracy (AARDVLE,NRTL ≤ 0.3% and AARDVLE,PC‑SAFT ≤ 1.1%) and redraw its details, partially
quantitative, when applied as a fitting algorithm (NRTL) or when applying
the PC-SAFT theory. The present work is a continuation of an ongoing
study, which aims at developing the structure–property relationships
of ILs. With the present results, a first systematic view on the impact
of the alkyl side chain length of the C
x
mim+ (x = 2, 4, 6) cation on the boiling
behavior of binary IL (C
x
mimTfO)/n-alkyl alcohol mixtures is provided by scaling the boiling
temperatures of the mixtures with that of the pure alcohol master
plot results. Our data reveal that increasing the alkyl chain length
of the C
x
mim+ cation causes
an enhancement of the attractive forces between the IL and the n-alkyl alcohol moieties, resulting in an increase in the
relative boiling temperature of the binary mixture.