Miguel Ángel Villamañán Olfos-rekin lankidetzan egindako argitalpenak (16)

2012

  1. Ether+alcohol+hydrocarbon mixtures in fuels and bio-fuels: Excess enthalpies of binary mixtures containing dibutyl ether (DBE) or 1-butanol and 1-hexene or methylcyclohexane or toluene or cyclohexane or 2,2,4-trimethylpentane at 298.15K and 313.15K

    Fluid Phase Equilibria, Vol. 315, pp. 1-8

2011

  1. Reply to "comment on 'excess enthalpies of binary and ternary mixtures containing dibutyl ether, cyclohexane, and 1-butanol at 298.15 K'"

    Journal of Chemical and Engineering Data

2010

  1. Excess enthalpies of binary and ternary mixtures containing dibutyl ether (DBE), 1-butanol, and heptane at T = 298.15 K and 313.15 K

    Journal of Chemical Thermodynamics, Vol. 42, Núm. 1, pp. 28-37

  2. Excess enthalpies of oxygenated compounds + hydrocarbon mixtures: Binary and ternary mixtures containing dibutyl ether (DBE), 1-butanol and 2,2,4-trimethylpentane at 298.15 K

    Fluid Phase Equilibria, Vol. 290, Núm. 1-2, pp. 15-20

2009

  1. Erratum: Excess enthalpies of binary and ternary mixtures containing dibutyl ether, cyclohexane and 1-butanol at 298.15 K (Journal of Chemical and Engineering Data (2009) 54 (1672-1679)

    Journal of Chemical and Engineering Data

  2. Excess enthalpies of binary and ternary mixtures containing dibutyl ether, cyclohexane, and 1-butanol at 298.15 K

    Journal of Chemical and Engineering Data, Vol. 54, Núm. 6, pp. 1672-1679

  3. Excess enthalpies of ether + alcohol + hydrocarbon mixtures: Binary and ternary mixtures containing dibutyl ether (DBE), 1-butanol and benzene at 298.15 K and 313.15 K

    Fluid Phase Equilibria, Vol. 284, Núm. 2, pp. 106-113

2006

  1. Vapour-liquid equilibrium of octane enhancing additives in gasolines 7: Total pressure data and gE for the ternary mixture tert-amyl methyl ether (TAME), methanol and hexane at 313.15 K

    Fluid Phase Equilibria, Vol. 245, Núm. 1, pp. 52-56

2004

  1. Excess enthalpies of binary and ternary mixtures containing tert-amyl methyl ether (TAME), tert-amyl alcohol (TAOH) and hexane at 298.15 and 313.15 K

    Fluid Phase Equilibria

  2. Vapor-liquid equilibrium of octane-enhancing additives in gasolines: 6. Total pressure data and GE for binary and ternary mixtures containing 1,1-dimethylethyl methyl ether (MTBE), methanol and n-hexane at 313.15 K

    Fluid Phase Equilibria

2003

  1. 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

    Fluid Phase Equilibria, Vol. 212, Núm. 1-2, pp. 81-95

2001

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

    Fluid Phase Equilibria

1999

  1. Phase equilibrium properties of binary and ternary systems containing tert-amylmethyl ether (TAME) as oxygenate additive and gasoline substitution hydrocarbons at 313.15 K

    Fluid Phase Equilibria

1998

  1. Excess thermodynamic functions for ternary systems containing fuel oxygenates and substitution hydrocarbons. 2. Total-pressure data and G(E) for methyl tert-butyl ether/n-heptane/1-hexene at 313.15 K

    Fluid Phase Equilibria, Vol. 152, Núm. 2, pp. 265-276

1997

  1. Isothermal vapor-liquid equilibria of binary mixtures containing methyl tert-butyl ether (MTBE) and/or substitution hydrocarbons

    Fluid Phase Equilibria, Vol. 133, Núm. 1-2, pp. 155-162

1995

  1. Vapor-liquid equilibria of binary mixtures containing methyl tert-butyl ether (MTBE) and/or substitution hydrocarbons at 298.15 K and 313.15 K

    Fluid Phase Equilibria, Vol. 110, Núm. 1-2, pp. 219-230