4.5 Article

Thermodynamic modeling of dealcoholization of beverages using supercritical CO2: Application to wine samples

Journal

JOURNAL OF SUPERCRITICAL FLUIDS
Volume 52, Issue 2, Pages 183-188

Publisher

ELSEVIER SCIENCE BV
DOI: 10.1016/j.supflu.2009.12.011

Keywords

Supercritical CO2 extraction; Alcoholic beverages; Phase equilibria

Funding

  1. Comunidad Autonoma de Madrid [S-505/AGR-0153]
  2. Ministerio de Ciencia e Innovacion [AGL2007-64198/ALI]
  3. Spain and Miguel Torres S.A [CEN-20072003]
  4. Universidad Autonoma de Madrid, Spain

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The supercritical removal of ethanol from alcoholic beverages (brandy, wine, and cider) was studied using the GC-EoS model to represent the phase equilibria behavior of the CO2 + beverage mixture. Each alcoholic drink was represented as the ethanol + water mixture with the corresponding ethanol concentration (35 wt% for brandy, 9-12 wt% for different wines and 6 wt% for cider). The thermodynamic modeling was based on an accurate representation of the CO2 + ethanol and CO2 + water binary mixtures, and the CO2 + ethanol + water ternary mixture. The GC-EoS model was employed to simulate the countercurrent supercritical CO2 dealcoholization of the referred beverages; the results obtained compared good with experimental data from the literature. Thus, the model was used to estimate process conditions to achieve an ethanol content reduction from ca. 10 wt% to values lower than 1 wt%. The model results were tested by carrying out several extraction assays using wine, in a 3 m height packed column at 308 K, pressures in the range of 9-18 MPa and solvent to wine ratio between 9 and 30 kg/kg. (C) 2010 Elsevier B.V. All rights reserved.

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