Publicaciones en las que colabora con JOSE JUAN SEGOVIA PURAS (19)

2017

  1. High Pressure Volumetric Properties of the Binary Mixtures Di-isopropyl Ether + 2,2,4-Trimethylpentane

    Journal of Chemical and Engineering Data, Vol. 62, Núm. 10, pp. 3610-3619

  2. High pressure liquid densities and excess volumes of the (di-isopropyl ether + 1-hexanol) system

    Journal of Chemical Thermodynamics, Vol. 113, pp. 213-218

  3. PVT properties of the binary system di-isopropyl ether + iso-octane for the development of new biofuels

    30th International Conference on Efficiency, Cost, Optimization, Simulation and Environmental Impact of Energy Systems, ECOS 2017

2013

  1. Excess enthalpies of ternary mixtures of oxygenated additives + hydrocarbon mixtures in fuels and bio-fuels: Dibutyl ether (DBE) and 1-butanol and 1-hexene or cyclohexane or 2,2,4 trimethylpentane at 298.15 K and 313.15 K

    Journal of Chemical Thermodynamics, Vol. 56, pp. 6-11

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. Phase equilibrium properties of binary and ternary mixtures containing 1,1-dimethylethyl methyl ether, 1-propanol, and hexane at T = 313.15 K

    Journal of Chemical and Engineering Data, Vol. 51, Núm. 6, pp. 2121-2125

  2. 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