EDUARDO ATANASIO MONTERO GARCIA-rekin lankidetzan egindako argitalpenak (8)

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