Publicacións nas que colabora con José Enrique Tojo Suárez (24)

2007

  1. Dynamic viscosities of binary mixtures of cycloalkanes with primary alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO interaction parameters

    Journal of Chemical Thermodynamics, Vol. 39, Núm. 2, pp. 322-334

2006

  1. Dynamic viscosities of a series of 1-alkyl-3-methylimidazolium chloride ionic liquids and their binary mixtures with water at several temperatures

    Journal of Chemical and Engineering Data, Vol. 51, Núm. 2, pp. 696-701

  2. Viscosities, densities, and speed of sound of the cycloalkanes with secondary alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO interaction parameters

    Journal of Chemical and Engineering Data, Vol. 51, Núm. 3, pp. 1076-1087

  3. Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K

    Journal of Chemical Thermodynamics, Vol. 38, Núm. 10, pp. 1172-1185

2005

  1. Dynamic viscosities of the binary systems cyclohexane and cyclopentane with acetone, butanone, or 2-pentanone at three temperatures T = (293.15, 298.15, and 303.15) K

    Journal of Chemical and Engineering Data, Vol. 50, Núm. 4, pp. 1462-1469

  2. Vapor-liquid equilibria for the quaternary reactive system ethyl acetate + ethanol + water + acetic acid and some of the constituent binary systems at 101.3 kPa

    Fluid Phase Equilibria, Vol. 235, Núm. 2, pp. 215-222

2004

  1. Dynamic viscosities of 2-butanol with alkanes (C8, C 10, and C12) at several temperatures

    Journal of Chemical Thermodynamics, Vol. 36, Núm. 4, pp. 267-275

  2. Dynamic viscosities of 2-pentanol with alkanes (octane, decane, and dodecane) at three temperatures T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters

    Journal of Chemical and Engineering Data, Vol. 49, Núm. 5, pp. 1225-1230

  3. Dynamic viscosities of diethyl carbonate with linear and secondary alcohols at several temperatures

    Journal of Chemical and Engineering Data, Vol. 49, Núm. 1, pp. 157-162

  4. Dynamic viscosities, densities, and speed of sound and derived properties of the binary systems acetic acid with water, methanol, ethanol, ethyl acetate and methyl acetate at T = (293.15, 298.15, and 303.15) K at atmospheric pressure

    Journal of Chemical and Engineering Data, Vol. 49, Núm. 6, pp. 1590-1596

  5. Viscosities of dimethyl carbonate with alcohols at several temperatures: UNIFAC-VISCO interaction parameters (-OCOO-/alcohol)

    Fluid Phase Equilibria, Vol. 216, Núm. 1, pp. 167-174

2003

  1. Isobaric phase equilibria of diethyl carbonate with five alcohols at 101.3 kPa

    Journal of Chemical and Engineering Data, Vol. 48, Núm. 1, pp. 86-91

  2. Procesos de separación

    La investigación del Grupo Especializado de Termodinámica de las Reales Sociedades Españolas de Física y de Química : año 2003 (Universidad de Extremadura), pp. 29-54

  3. Viscosities of dimethyl carbonate or diethyl carbonate with alkanes at four temperatures. New UNIFAC-VISCO parameters

    Journal of Chemical and Engineering Data, Vol. 48, Núm. 1, pp. 146-151

  4. Viscosities, densities and speeds of sound of the binary systems: 2-propanol with octane, or decane, or dodecane at T = (293.15, 298.15, and 303.15) K

    Journal of Chemical Thermodynamics, Vol. 35, Núm. 6, pp. 939-953

2002

  1. Automatic implementation of thermodynamic models for reliable parameter estimation using computer algebra

    Computers and Chemical Engineering, Vol. 26, Núm. 10, pp. 1473-1479

  2. Isobaric vapor-liquid equilibria of diethyl carbonate with four alkanes at 101.3 kPa

    Journal of Chemical and Engineering Data, Vol. 47, Núm. 5, pp. 1098-1102

  3. Phase equilibria of the binary systems 1-hexene with o-xylene, m-xylene, p-xylene, toluene, and ethylbenzene at 101.3 kPa

    Journal of Chemical and Engineering Data, Vol. 47, Núm. 4, pp. 867-871

  4. Vapour-liquid equilibria of dimethyl carbonate with linear alcohols and estimation of interaction parameters for the UNIFAC and ASOG method

    Fluid Phase Equilibria, Vol. 201, Núm. 1, pp. 187-201

1995

  1. Vapor-Liquid Equilibria for the Ternary System Acetone + Methanol + Chlorobenzene at 101.325 kPa

    Journal of Chemical and Engineering Data, Vol. 40, Núm. 6, pp. 1203-1205