Publications by the researcher in collaboration with José Juan Segovia Puras (12)

2012

  1. 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

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

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

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