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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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

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

Fluid Phase Equilibria, Vol. 193, Iss. 1, 2002-01 ,pp. : 289-301

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Vapor-liquid equilibrium of octane-enhancing additives in gasolines - 5. Total pressure data and G E for binary and ternary mixtures containing 1,1-dimethylpropyl methyl ether (TAME), 1-propanol and n-hexane at 313.15 K

By Alonso C.   Montero E.A.   Chamorro C.R.   Segovia J.J.   Martin M.C.   Villamanan M.A.  

Fluid Phase Equilibria, Vol. 212, Iss. 1, 2003-09 ,pp. : 81-95

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Vapour-liquid equilibrium of octane-enhancing additives in gasolines - 2. Total pressure data and g E for binary and ternary mixtures containing tert-amylmethyl ether (TAME), tert-amyl alcohol (TAOH) and n-hexane

By Alonso C.   Montero E.A.   Chamorro C.R.   Segovia J.J.   Martn M.C.   Villamanan M.A.  

Fluid Phase Equilibria, Vol. 182, Iss. 1, 2001-06 ,pp. : 241-255

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Isothermal v.l.e. and excess molar Gibbs energy of binary and ternary mixtures containing diisopropyl ether,n -heptane and isopropanol at T= 313.15 K

By Chamorro   Segovia   Martin M.C.   Villamanan M.A.  

Journal of Chemical Thermodynamics, Vol. 34, Iss. 1, 2002-01 ,pp. : 13-28

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