Prediction of alcohol-hydrocarbon phase behavior within a SAFT equation of state is a well-
studied topic in the recent literature. Most of these studies focus on the phase behavior of …

The Riedel vapor pressure correlation is a useful model that has been employed for
decades. The shape of the temperature dependent correlation is a strong function of the …

The availability of vapor pressure data is essential to validate thermodynamic models and
enhance the thermodynamic correlations. Despite its importance, there is limited vapor …

Experimental isothermal P–x data at T= 313.15 K for the binary systems 1, 1-dimethylethyl
methyl ether (MTBE)+ n-hexane and methanol+ n-hexane, and the ternary system MTBE+ …

(Vapour+ liquid) equilibria (VLE) data of (1-butanol+ benzene, or toluene, or o-, or m-, or p-
xylene) measured by the static method at T=(308.15±0.01) K over the entire composition …

(Vapour+ liquid) equilibria data of (di-isopropyl ether+ 1-butanol+ benzene),(di-isopropyl
ether+ 1-butanol) and (1-butanol+ benzene) have been measured at T= 313.15 K using an …

In this work, we extend the Group Contribution with Association Equation of State (GCA-
EOS) to model the phase behavior of mixtures comprising ethers and alcohols. The model …

New experimental isothermal P, x, y data for the ternary systems dibutyl ether+
cyclohexane+ heptane and dibutyl ether+ cyclohexane+ 1-hexene and for the binary …

New accurate vapour liquid equilibrium data for the ternary mixture formed by dibutyl ether
(DBE), toluene and heptane at 313.15 K have been measured. A static method using an …

Experimental isothermal P− x− y data for the ternary system 1, 1-dimethylethyl methyl ether
(MTBE)+ 1-propanol+ hexane and for the binary system 1, 1-dimethylethyl methyl ether …