José Juan Segovia Puras-rekin lankidetzan egindako argitalpenak (21)

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

  2. Vapour-liquid equilibria and excess enthalpies of the binary mixtures 1-pentanol with 2,2,4-trimethylpentane or n-heptane

    Fluid Phase Equilibria, Vol. 338, pp. 95-99

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

  2. Phase equilibrium properties of the ternary mixture dibutyl ether+toluene+heptane at 313.15K

    Fluid Phase Equilibria, Vol. 317, pp. 84-88

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

2008

  1. Phase equilibrium properties of binary and ternary mixtures containing dibutyl ether, cyclohexane, and heptane or 1-hexene at T = 313.15 K

    Journal of Chemical and Engineering Data, Vol. 53, Núm. 7, pp. 1486-1491

2006

  1. Experimental investigation of the vapour-liquid equilibrium of binary and ternary mixtures containing dibutyl ether (DBE), cyclohexane and toluene at 313.15 K

    Fluid Phase Equilibria, Vol. 245, Núm. 1, pp. 57-62

  2. 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

  3. 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