A compendium of phase change enthalpies published in 2010 is updated to include the
period 1880–2015. Phase change enthalpies including fusion, vaporization, and …

The group contribution method UNIFAC has become very popular because of its large range
of applicability and its reliable predictions of vapor− liquid equilibria. With the help of new …

For the first time vapor–liquid equilibrium (VLE) data for ternary systems containing ionic
liquids are reported. The data were measured by means of a computer-operated static VLE …

Ethyl tert-butyl ether (ETBE) is widely used as an oxygenate additive to gasoline; however, a
drawback in the conventional ETBE manufacture is the energy intensive product recovery …

The application range of the predictive Soave–Redlich–Kwong (PSRK) group contribution
equation of state (EOS) for the prediction of vapor–liquid equilibria (VLE) and gas solubilities …

This work was undertaken for the evaluation and revision of group-additivity values
necessary for predicting standard enthalpies of formation and enthalpies of vaporization of …

An apparatus for the measurement of vapor pressures of pure solvents and solutions at
different temperatures is described. The apparatus is tested for the temperature range …

This study presents a new, improved parameterisation of the temperature dependence of
activity coefficients in the AIOMFAC (Aerosol Inorganic–Organic Mixtures Functional groups …

Isothermal vapor− liquid equilibrium (VLE) data are reported for the binary systems
methanol+ 2, 2 '-diethanolamine and water+ 2, 2 '-diethanolamine and for the ternary system …

Isothermal P− x data (VLE) and excess enthalpy (h E) data for the binary systems methyl
formate, ethyl formate, and butyl formate+ water and toluene+ 1, 2-ethanediol have been …