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

被引:16
|
作者
Ruiz-Rodriguez, Alejandro [1 ]
Fornari, Tiziana [2 ]
Judith Hernandez, Elvis [2 ]
Javier Senorans, F. [2 ]
Reglero, Guillermo [2 ]
机构
[1] CSIC, Inst Fermentac Ind, E-28006 Madrid, Spain
[2] Univ Autonoma Madrid, Secc Dept Ciencias Alimentac, E-28049 Madrid, Spain
来源
JOURNAL OF SUPERCRITICAL FLUIDS | 2010年 / 52卷 / 02期
关键词
Supercritical CO2 extraction; Alcoholic beverages; Phase equilibria; GROUP-CONTRIBUTION EQUATION; VAPOR-LIQUID-EQUILIBRIUM; CARBON-DIOXIDE-ETHANOL; ELEVATED PRESSURES; PHASE-EQUILIBRIUM; FLUID EXTRACTION; WATER; SYSTEMS; MIXTURES; ACETONE;
D O I
10.1016/j.supflu.2009.12.011
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
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.
引用
收藏
页码:183 / 188
页数:6
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