Publicaciones en las que colabora con ROSA MARIA VILLAMAÑAN OLFOS (21)

2020

  1. P-x isothermal equilibrium data for two ternary systems containing long-chain bioalcohols: (1-butanol or 2-butanol + cyclohexane + methylbenzene) at 313.15 K

    Journal of Chemical Thermodynamics, Vol. 141

2017

  1. Characterization of second generation biofuels: Vapor-liquid equilibra (VLE) and excess enthalpies of bio-alcohol + hydrocarbon mixtures

    30th International Conference on Efficiency, Cost, Optimization, Simulation and Environmental Impact of Energy Systems, ECOS 2017

2015

  1. Isothermal vapor-liquid equilibrium and molar excess Gibbs energies of two ternary systems containing either 1-butanol or 2-butanol+1-hexene+methylbenzene at 313.15 K

    Fluid Phase Equilibria, Vol. 386, pp. 1-6

2014

  1. Phase equilibrium properties of binary and ternary mixtures containing 2-butanol, 2,2,4-trimethylpentane and 1-hexene at 313.15 K

    Fluid Phase Equilibria, Vol. 369, pp. 33-38

2013

  1. Vapour-liquid equilibria of binary and ternary mixtures containing 1-butanol, 2,2,4-trimethylpentane and 1-hexene at T = 313.15 K

    Journal of Chemical Thermodynamics, Vol. 63, pp. 164-168

2012

  1. Excess enthalpies of second generation biofuels

    Proceedings of the 25th International Conference on Efficiency, Cost, Optimization and Simulation of Energy Conversion Systems and Processes, ECOS 2012

  2. Vapor-liquid equilibria of binary mixtures containing 1-butanol and hydrocarbons at 313.15 K

    Journal of Chemical and Engineering Data, Vol. 57, Núm. 1, pp. 114-119

2011

  1. Thermodynamic properties of biofuels: Heat capacities of binary mixtures containing ethanol and hydrocarbons up to 20 MPa and the pure compounds using a new flow calorimeter

    Journal of Chemical Thermodynamics, Vol. 43, Núm. 12, pp. 1893-1896

2010

  1. Improvement and automation of a single sinker densimeter for the determination of (p, ρ, T) properties of mixtures of gases related with biogas

    Proceedings of the 23rd International Conference on Efficiency, Cost, Optimization, Simulation, and Environmental Impact of Energy Systems, ECOS 2010

  2. Thermodynamic characterization of bio-fuels: Excess functions for binary mixtures containing ETBE and hydrocarbons

    Energy, Vol. 35, Núm. 2, pp. 759-763

  3. Thermodynamic properties of binary and ternary mixtures containing di-isopropyl ether, 2-propanol, and benzene at T = 313.15 K

    Journal of Chemical and Engineering Data, Vol. 55, Núm. 8, pp. 2741-2745

2009

  1. Thermodynamic properties of biofuels: Heat capacities of binary mixtures containing ethanol and hydrocarbons up to 20 MPa using a new flow calorimeter

    ECOS 2009 - 22nd International Conference on Efficiency, Cost, Optimization, Simulation and Environmental Impact of Energy Systems

  2. Thermodynamics of fuels with a bio-synthetic component (IV): (Vapor + liquid) equilibrium data for the ternary mixture (ethyl 1,1-dimethylethyl ether + 1-hexene + toluene) at T = 313.15 K

    Journal of Chemical Thermodynamics, Vol. 41, Núm. 2, pp. 189-192

2008

  1. Thermodynamic characterization of bio-fuels: Excess functions for binary mixtures containing ETBE and hydrocarbons

    ECOS 2008 - Proceedings of the 21st International Conference on Efficiency, Cost, Optimization, Simulation and Environmental Impact of Energy Systems

  2. Thermodynamics of fuels with a biosynthetic component (III): Vapor-liquid equilibrium data for the ternary mixture ethyl 1,1-dimethylethyl ether, n-heptane and 1-hexene at T = 313.15 K

    Fluid Phase Equilibria, Vol. 265, Núm. 1-2, pp. 12-16

  3. Thermodynamics of fuels with a biosynthetic component. II. vapor-liquid equilibrium data for binary and ternary mixtures containing ethyl 1,1-dimethylethyl ether, 1-hexene, and cyclohexane at T = 313.15 K

    Journal of Chemical and Engineering Data, Vol. 53, Núm. 1, pp. 247-251

2006

  1. Co-combustion of meat and bone meal and biomass on a fluidized bed combustion chamber: An energy and exergy study

    ECOS 2006 - Proceedings of the 19th International Conference on Efficiency, Cost, Optimization, Simulation and Environmental Impact of Energy Systems

  2. Phase equilibrium properties of binary and ternary systems containing di-isopropyl ether + 1-butanol + benzene at 313.15 K

    Journal of Chemical Thermodynamics, Vol. 38, Núm. 5, pp. 547-553

  3. Thermodynamics of fuels with a biosynthetic component: Vapor-liquid equilibrium data for binary and ternary mixtures containing ethyl 1,1-dimethylethyl ether, n-heptane, and toluene at T = 313.15 K

    Journal of Chemical and Engineering Data, Vol. 51, Núm. 6, pp. 2091-2095

  4. Total pressure and excess Gibbs energy for the ternary mixture di-isopropyl ether + 1-propanol + benzene and its corresponding binary systems at 313.15 K

    Fluid Phase Equilibria, Vol. 239, Núm. 2, pp. 183-187