María Cruz Burguet Bonancia-rekin lankidetzan egindako argitalpenak (18)

2011

  1. Separation of di-n-propyl ether and n-propyl alcohol by extractive distillation and pressure-swing distillation: Computer simulation and economic optimization

    Chemical Engineering and Processing: Process Intensification, Vol. 50, Núm. 11-12, pp. 1266-1274

2010

  1. Isobaric vapor-liquid equilibria for binary and ternary mixtures of ethanol and 2-propanol with 2-butanone and butyl propionate at 101.3 kPa

    Journal of Chemical and Engineering Data

  2. Liquid-liquid equilibria for the system 1-methyl propyl ethanoate (1) + acetic acid (2) + water (3) at (283.15 and 323.15) K

    Journal of Chemical and Engineering Data, Vol. 55, Núm. 1, pp. 523-525

  3. Phase equilibrium for the systems diisopropyl ether, isopropyl alcohol + 2,2,4-trimethylpentane and +n-heptane at 101.3 kPa

    Fluid Phase Equilibria, Vol. 289, Núm. 2, pp. 135-139

2009

  1. Isobaric vapor-liquid equilibria for binary and ternary mixtures of diisopropyl ether, 2-propyl alcohol, and n-Butyl propionate at 101.3 kPa

    Journal of Chemical and Engineering Data, Vol. 54, Núm. 11, pp. 2991-2995

  2. Isobaric vapour-liquid equilibria for the binary systems 4-methyl-2-pentanone + 1-butanol and + 2-butanol at 20 and 101.3 kPa

    Fluid Phase Equilibria, Vol. 277, Núm. 1, pp. 49-54

2008

  1. Erratum to "Effect of pressure and the capability of 2-methoxyethanol as a solvent in the behaviour of a diisopropyl ether-isopropyl alcohol azeotropic mixture" [Fluid Phase Equilib. 262 (2007) 271-279] (DOI:10.1016/j.fluid.2007.09.014)

    Fluid Phase Equilibria

  2. Isobaric (vapour + liquid + liquid) equilibrium data for (di-n-propyl ether + n-propyl alcohol + water) and (diisopropyl ether + isopropyl alcohol + water) systems at 100 kPa

    Journal of Chemical Thermodynamics, Vol. 40, Núm. 5, pp. 867-873

  3. Isobaric vapor-liquid equilibria for binary and ternary mixtures of diisopropyl ether, 2-propyl alcohol, and 3-methyl-1-butanol

    Journal of Chemical and Engineering Data, Vol. 53, Núm. 8, pp. 1897-1902

  4. Isobaric vapour-liquid equilibria for binary systems of 2-butanone with ethanol, 1-propanol, and 2-propanol at 20 and 101.3 kPa

    Fluid Phase Equilibria, Vol. 270, Núm. 1-2, pp. 62-68

  5. Study of liquid-liquid equilibrium of the systems isobutyl acetate + acetic acid + water and isobutyl alcohol + acetic acid + water at different temperatures

    Fluid Phase Equilibria, Vol. 271, Núm. 1-2, pp. 76-81

2007

  1. Effect of pressure and the capability of 2-methoxyethanol as a solvent in the behaviour of a diisopropyl ether-isopropyl alcohol azeotropic mixture

    Fluid Phase Equilibria, Vol. 262, Núm. 1-2, pp. 271-279

  2. Liquid-liquid equilibria of the systems dipropyl ether + n-propanol + water and dipropyl ether + n-propanol + ethylene glycol at different temperatures

    Fluid Phase Equilibria, Vol. 262, Núm. 1-2, pp. 76-81

  3. Phase equilibria involved in extractive distillation of dipropyl ether + 1-propyl alcohol using 2-ethoxyethanol as entrainer

    Fluid Phase Equilibria, Vol. 255, Núm. 1, pp. 62-69

  4. Phase equilibria involved in extractive distillation of dipropyl ether + 1-propyl alcohol using N,N-dimethylformamide as entrainer

    Journal of Chemical and Engineering Data, Vol. 52, Núm. 2, pp. 532-537

2006

  1. Isobaric apor-liquid equilibria for binary and ternary mixtures of dipropyl ether, 1-propyl alcohol, and butyl propionate

    Journal of Chemical and Engineering Data, Vol. 51, Núm. 6, pp. 2233-2238

  2. Isobaric vapor-liquid equilibria for the binary systems 1-propyl alcohol + dipropyl ether and 1-butyl alcohol + dibutyl ether at 20 and 101.3 kPa

    Fluid Phase Equilibria, Vol. 247, Núm. 1-2, pp. 47-53

  3. Vapor-liquid equilibria in the ternary system dipropyl ether + 1-propanol + 1-pentanol and the binary systems dipropyl ether + 1-pentanol, 1-propanol + 1-pentanol at 101.3 kPa

    Fluid Phase Equilibria, Vol. 247, Núm. 1-2, pp. 175-181