Vapor-liquid equilibrium of octane-enhancing additives in gasolines - 1. Total pressure data and g E for binary and ternary mixtures containing di-isopropyl ether (DIPE), n-heptane and benzene at 313.15 K

By Chamorro C.R.   Segovia J.J.   Martn M.C.   Villamanan M.A.  

Fluid Phase Equilibria, Vol. 182, Iss. 1, 2001-06 ,pp. : 229-239

Elsevier

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Excess thermodynamic properties of binary and ternary mixtures containing methyl 1,1-dimethylethyl ether (MTBE),n-heptane, and methanol atT = 313.15 K

By Segovia J.J.   Martín M.C.   Chamorro C.R.   Villamañán M.A.  

Journal of Chemical Thermodynamics, Vol. 31, Iss. 9, 1999-09 ,pp. : 1231-1246

Academic Press

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Vapor-liquid equilibrium of octane-enhancing additives in gasolines - 3. Total pressure data and g E for ternary mixtures containing di-isopropyl ether or benzene and n-heptane + cyclohexane at 313.15 K

By Chamorro C.R.   Segovia J.J.   Martn M.C.   Villamanan M.A.  

Fluid Phase Equilibria, Vol. 191, Iss. 1, 2001-11 ,pp. : 71-82

Elsevier

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Excess enthalpies of the ternary mixtures: diisopropyl ether+n-octane+(n-heptane or n-dodecane) at 298.15 K

By Wang Z.   Horikawa Y.   Benson G.C.   Lu B.C.-Y.  

Fluid Phase Equilibria, Vol. 181, Iss. 1, 2001-05 ,pp. : 215-224

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Excess enthalpies of the ternary mixtures: tetrahydrofuran + (diisopropyl ether or 2-methyltetrahydrofuran) + n-heptane at 298.15 K

By Wang Z.   Kodama D.   Benson G.C.   Lu B.C.-Y.  

Fluid Phase Equilibria, Vol. 216, Iss. 2, 2004-02 ,pp. : 293-299

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