Rosa Muñoz Guillen-rekin lankidetzan egindako argitalpenak (8)

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. Phase equilibrium for the esterification reaction of acetic acid + butan-1-ol at 101.3 kPa

    Journal of Chemical and Engineering Data, Vol. 53, Núm. 1, pp. 108-115

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. 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

  3. 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