Fluid Phase Equilibria, Vol.193, No.1-2, 289-301, 2002
Vapor-liquid equilibrium of octane-enhancing additives in gasolines - 4. Total pressure data and G(E) for ternary mixtures containing isopropyl ether or benzene and n-heptane+1-hexene at 313.15 K
The experimental isothermal P-x data at T = 313.15K for the two ternary systems (isopropylether+n-heptane+ 1-hexene) and (1-hexene + n-heptane + benzene) are reported. Data reduction by Barker's method provides correlation for G(E). The Wohl expansion, also Wilson, NRTL and UNIQUAC models have been applied successfully to the ternary systems. The experimental data, in this work are not available in the literature.