1 |
Vapor-liquid equilibrium of octane-enhancing additives in gasolines -6. Total pressure data and G(E) for binary and ternary mixtures containing 1, 1-dimethlethyl methyl ether (MTBE), methanol and n-hexane at 313.15 K Alonso C, Montero EA, Chamorro CR, Segovia JJ, Martin MC, Villamanan MA Fluid Phase Equilibria, 217(2), 157, 2004 |
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Characterization and modelling of a gasoline containing 1,1-dimethylethyl methyl ether (MTBE), diisopropyl ether (DIPE) or 1,1-dimethylpropyl methyl ether (TAME) as fuel oxygenate based on new isothermal binary vapour-liquid data Chamorro CR, Martin MC, Villamanan MA, Segovia JJ Fluid Phase Equilibria, 220(1), 105, 2004 |
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Vapor-liquid equilibrium of octane-enhancing additives in gasolines - 5. Total pressure data and GE for binary and ternary mixtures containing 1,1-dimethylpropyl methyl ether (TAME), 1-propanol and n-hexane at 313.15 K Alonso C, Montero EA, Chamorro UR, Segovia JJ, Martin MC, Villamanan MA Fluid Phase Equilibria, 212(1-2), 81, 2003 |
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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 Chamorro CR, Segovia JJ, Martin MC, Villamanan MA Fluid Phase Equilibria, 193(1-2), 289, 2002 |
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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 Chamorro CR, Segovia JJ, Martin MC, Villamanan MA Fluid Phase Equilibria, 182(1-2), 229, 2001 |
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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 plus cyclohexane at 313.15 K Chamorro CR, Segovia J, Martin MC, Villamanan MA Fluid Phase Equilibria, 191(1-2), 71, 2001 |
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Experimental investigation of the vapor-liquid equilibrium at 313.15 K of the ternary system tert-amylmethyl ether (TAME) plus n-heptane plus methanol Chamorro CR, Segovia JJ, Martin MC, Villamanan MA Fluid Phase Equilibria, 165(2), 197, 1999 |