Search Results - "Gros, H.P."

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  1. 1

    Isothermal Vapor-Liquid Equilibrium Data for the Binaries Isobutane-Ethanol, Isobutane-1-Propanol, and Propane-Ethanol by Zabaloy, Marcelo S, Gros, Hernan P, Bottini, Susana B, Brignole, Esteban A

    Published in Journal of chemical and engineering data (01-04-1994)
    “…The recovery of alcohols from aqueous solutions by supercritical extraction has received considerable attention during the last decade. Light hydrocarbons…”
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    Journal Article
  2. 2

    High-Pressure Vapor−Liquid Equilibria for Propane + 2-Butanol, Propylene + 2-Butanol, and Propane + 2-Butanol + 2-Propanol by Gros, Hernán P, Zabaloy, Marcelo S, Brignole, Esteban A

    Published in Journal of chemical and engineering data (12-03-1996)
    “…Vapor−liquid equilibria have been measured for propane + 2-butanol, propylene + 2-butanol, and propane + 2-butanol + 2-propanol in the temperature range of…”
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    Journal Article
  3. 3

    A group contribution equation of state for associating mixtures by Gros, H.P., Bottini, S., Brignole, E.A.

    Published in Fluid phase equilibria (15-03-1996)
    “…In the present work a group contribution-associating-equation of state (GCA-EOS) is developed for the modeling of phase equilibria found in the near critical…”
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    Journal Article Conference Proceeding
  4. 4

    High pressure phase equilibrium modeling of mixtures containing associating compounds and gases by Gros, H.P., Bottini, S.B., Brignole, E.A.

    Published in Fluid phase equilibria (01-12-1997)
    “…In the present work, the group contribution-associating-equation of state (GCA-EOS) is applied for modeling high pressure phase equilibrium of mixtures…”
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    Journal Article
  5. 5

    Near-critical separation of aqueous azeotropic mixtures: process synthesis and optimization by Gros, H.P., Díaz, S., Brignole, E.A.

    Published in The Journal of supercritical fluids (15-03-1998)
    “…The near critical extraction of alcohols from aqueous solutions is addressed, combining reliable thermodynamic models with robust simulation and optimization…”
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    Journal Article
  6. 6

    Phase equilibrium dominant parameter matrix of multicomponent distillation trains by Gros, H.P., Urlic, L.E., Brignole, E.A.

    Published in Computers & chemical engineering (1997)
    “…A systematic tuning procedure of thermodynamic models, for realistic simulation of multicomponent distillation trains, is presented. The procedure allows a…”
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    Journal Article
  7. 7

    Vapor−Liquid Equilibrium Data for Propylene + Ethanol, Propylene + MEK, and Propylene + MTBE by Rojas, Andrés S, Gros, Hernán P, Brignole, Esteban A

    Published in Journal of chemical and engineering data (10-11-1997)
    “…Vapor−liquid equilibria (VLE) for propylene + ethanol, propylene + methyl ethyl ketone (MEK), and propylene + methyl tert-butyl ether (MTBE) were measured in…”
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    Journal Article
  8. 8

    Computation of the attractive energy parameter of normal fluids in cubic equations of state by Sacomani, P.A, Gros, H.P, Brignole, E.A

    Published in Fluid phase equilibria (31-07-1996)
    “…A generalized method is developed for the calculation of the attractive energy parameter in cubic equations of state (EOS). The procedure employs the principle…”
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    Journal Article