Journal of Chemical and Engineering Data, Vol.47, No.2, 316-321, 2002
Thermodynamics of octane-enhancing additives in gasolines: Vapor-liquid equilibrium of ternary mixtures containing di-isopropyl ether or cyclohexane and 1-hexene plus benzene at 313.15 K
Experimental isothermal P-x-y data for the ternary systems di-isopropyl ether (DIPE) + 1-hexene + benzene and 1-hexene + benzene + cyclohexane at 313.15 K are reported. Data reduction by Barker's method provides correlations for G(E), using the Wohl expansion; the Wilson, NRTL, and UNIQUAC models have also been applied successfully.