Publikationen, an denen er mitarbeitet BEATRIZ PRUDENCIA ORGE ALVAREZ (11)

2016

  1. Activity coefficients at infinite dilution for different alcohols and ketones in [EMpy][ESO4]: Experimental data and modeling with PC-SAFT

    Fluid Phase Equilibria, Vol. 424, pp. 32-40

2001

  1. Temperature dependence of binary mixing properties for acetone, methanol, and linear aliphatic alkanes (C6-C8)

    Journal of Chemical and Engineering Data, Vol. 46, Núm. 3, pp. 728-734

  2. Thermodynamic properties of the mixture acetone + methanol + n-octane at 25°C

    Journal of Solution Chemistry, Vol. 30, Núm. 2, pp. 133-148

2000

  1. Mixing properties of benzene+2-methyl-2-butanol+1-pentanol at 298.15 K. Experimental results and comparison between ERAS model and cubic EOS estimations for excess molar volumes

    Fluid Phase Equilibria, Vol. 170, Núm. 1, pp. 151-163

  2. Thermodynamics of (anisole+benzene, or toluene, or n-hexane, or cyclohexane, or 1-butanol, or 1-pentanol) at T = 298.15 K

    Journal of Chemical Thermodynamics, Vol. 32, Núm. 5, pp. 617-629

1999

  1. Liquid-liquid equilibria, and thermodynamic properties of the system methyl acetate + methanol + water at 298.15 K

    Physics and Chemistry of Liquids, Vol. 37, Núm. 3, pp. 193-213

  2. Temperature dependence of the refractive index for the mixtures {CH3(CH2)xOH, x = 1, 2}+{(CH3)2CH(CH2)yOH, y = 0, 1, 2} and estimation by means of cubic equations of state

    Journal of Thermal Analysis and Calorimetry, Vol. 56, Núm. 1, pp. 381-394

  3. Thermodynamic properties of the mixture benzene + cyclohexane + 2- methyl-2-butanol at the temperature 298.15 K: Excess molar volumes prediction by application of cubic equations of state

    Fluid Phase Equilibria, Vol. 154, Núm. 1, pp. 123-138

  4. Volumetric properties prediction by cubic EOS for non-ideal mixtures: Application to the ternary system acetone+methanol+n-hexane

    Thermochimica Acta, Vol. 328, Núm. 1-2, pp. 265-275

1998

  1. Thermodynamic behaviour of mixtures containing methyl acetate, methanol, and 1-butanol at 298.15 K: application of the ERAS model

    Fluid Phase Equilibria, Vol. 147, Núm. 1-2, pp. 285-300

  2. Thermodynamic properties of the ternary mixture acetone + methanol + ethanol at 298.15 K

    Journal of Chemical and Engineering Data, Vol. 43, Núm. 5, pp. 776-780