In
this work, new experimental vapor-pressure data of 14 esters
were obtained using the transpiration method. Besides dimethyl fumarate,
dimethyl maleate, diethyl maleate, benzyl ethanoate, benzyl propanoate,
and benzyl butanoate, eight representatives of the homologous series
of ethyl alkanoates were investigated. The pure-component vapor pressures
and liquid densities were modeled by means of Perturbed-Chain Statistical
Associating Fluid Theory (PC-SAFT) and SAFT-γ Mie. Satisfying
modeling results could be achieved with both equations of state. Furthermore,
the molar excess enthalpies of 12 binary mixtures benzyl ethanoate
+ n-alkane were modeled. Only one binary interaction
parameter was fitted for PC-SAFT to quantitatively predict the molar
excess enthalpies of all binary mixtures under study, while SAFT-γ
Mie predicts these properties in qualitative agreement with the experimental
data. Finally, the liquid–liquid equilibria of three binary
mixtures ester (benzyl ethanoate, dimethyl maleate, and diethyl maleate)
+ water were investigated. These systems show a very low and almost
temperature-independent solubility of the ester in the aqueous phase,
whereas the moderate solubility of water in the organic phase is temperature-dependent.
Promisingly, both PC-SAFT and SAFT-γ Mie predicted broad and
unsymmetrical miscibility gaps for these mixtures, which is in qualitative
agreement with the experimental data.