Fluid Phase Equilibria, Vol.267, No.2, 119-126, 2008
Vapour-liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid-liquid equilibria for binary alcohol-ketone systems
Isothermal vapour-liquid equilibria (VLE), solid-liquid equilibria and excess enthalpies have been measured for the systems cyclohexanone+cyclohexanol and 2-octanone+1-hexanol. Additionally in this paper binary azeotropic data at different pressures for 1-pentanol+2-hepta none and 1-hexanol+2-octanone have been determined with the help of a wire band column. Furthermore activity coefficients at infinite dilution for methanol, ethanol, 1-butanol and 1-propanol in 2-octanone at different temperatures have been measured with the help of the dilutor technique. These data together with literature data for alcohol-ketone systems were used to fit temperature-dependent group interaction parameters for the group contribution method modified UNIFAC (Dortmund) and the group contribution equation of state VTPR. (C) 2008 Elsevier B.V. All rights reserved.
Keywords:vapour-liquid equilibria;solid-liquid equilibria;excess enthalpies;activity coefficients at infinite dilution;modified UNIFAC