Fluid Phase Equilibria, Vol.230, No.1-2, 131-142, 2005
Activity coefficient at infinite dilution, azeotropic data, excess enthalpies and solid-liquid-equilibria for binary systems of alkanes and aromatics with esters
Binary azeotropic data have been measured at different pressures for ethyl acetate + heptane, methyl acetate + heptane, isopropyl acetate + hexane and isopropyl acetate + heptane by means of a wire band column. Additionally activity coefficients at infinite dilution have been determined for ethyl acetate and isopropyl acetate in decane and dodecane in the temperature range between 303.15 and 333.15 K with the help of the dilutor technique. Furthermore excess enthalpies for the binary systems methyl acetate + hexane, methyl acetate + decane, ethyl acetate + hexane and ethyl acetate + decane at 363.15 and 413.15 K have been studied with the help of isothermal flow calorimetry. Finally solid-liquid equilibria for the systems ethyl myristate + benzene and ethyl myristate +p-xylene have been investigated by a visual technique. All these data have been used for the revision and extension of the group interaction parameters of the group contribution method modified UNIFAC (Dortmund) and the group contribution equation of state VTPR. The experimental data was compared with the results predicted using the group contribution method modified UNIFAC (Dortmund) and the group contribution equation of state VTPR. © 2004 Elsevier B.V. All rights reserved.
Keywords:VTPR;modified UNIFAC (Dortmund);activity coefficients at infinite dilution;azeotropic data;excess enthalpies;solid-liquid equilibria