Revision and summary of the group contribution equation of state parameter table: Application to edible oil constituents

被引:29
作者
Fornari, Tiziana [1 ]
机构
[1] Univ Autonoma Madrid, Fac Ciencias, Seccion Dept Ciencias Alimentacion, E-28049 Madrid, Spain
关键词
group contribution; equation of state; thermodynamic modeling; Supercritical fluids;
D O I
10.1016/j.fluid.2007.09.007
中图分类号
O414.1 [热力学];
学科分类号
摘要
The Group Contribution Equation of State (GC-EoS) was developed by Skjold-Jorgensen in 1984 for predicting phase equilibria of non-polar and polar mixtures. Since the model development, theGC-EoS group parameter table has been revised and extended, and the predictive capability of the model has been widely spread. Furthermore, the model has been successfully applied in the phase equilibria modeling of separation processes, particularly those related with supercritical fluids, and has also been used as a predictive tool for process simulation and optimization. This work is a comprehensive review of the present status of the GC-EoS parameter table, including revisions and extensions carried out by different authors since the model development until present. For a better understanding, available parameters are reported and organized in adequate tables. Additionally, the parameters for the carboxylic acid (COOH) group, which allow the modeling of an important family of compounds, i.e. carboxylic acids, are included in the present work. The application of the model to represent phase equilibria in mixtures of carbon dioxide and the main constituents of edible oils and derived products, demonstrate the capability of the model to be used in supercritical fluid oil-process simulation and optimization. (c) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:187 / 209
页数:23
相关论文
共 46 条
[1]
Phase equilibria of allyl sulfide plus carbon dioxide binary mixtures - Experimental data and thermodynamic modeling [J].
Andreatta, A. E. ;
Bottini, S. B. ;
Florusse, L. J. ;
Peters, C. J. .
JOURNAL OF SUPERCRITICAL FLUIDS, 2006, 38 (03) :306-311
[2]
BAMBERGER A, 1994, FLUID PHASE EQUILIBR, V97, P167, DOI 10.1016/0378-3812(94)85014-3
[3]
VAPOR LIQUID EQUILIBRIA FOR BINARY-MIXTURES OF CARBON-DIOXIDE AND FATTY-ACID ETHYL-ESTERS [J].
BHARATH, R ;
INOMATA, H ;
ARAI, K ;
SHOJI, K ;
NOGUCHI, Y .
FLUID PHASE EQUILIBRIA, 1989, 50 (03) :315-327
[4]
PHASE-EQUILIBRIA OF SUPERCRITICAL CO2 - FATTY OIL COMPONENT BINARY-SYSTEMS [J].
BHARATH, R ;
YAMANE, S ;
INOMATA, H ;
ADSCHIRI, T ;
ARAI, K .
FLUID PHASE EQUILIBRIA, 1993, 83 :183-192
[5]
PHASE-EQUILIBRIUM STUDY FOR THE SEPARATION AND FRACTIONATION OF FATTY OIL COMPONENTS USING SUPERCRITICAL CARBON-DIOXIDE [J].
BHARATH, R ;
INOMATA, H ;
ADSCHIRI, T ;
ARAI, K .
FLUID PHASE EQUILIBRIA, 1992, 81 (1-2) :307-320
[6]
Phase behavior and modeling of supercritical carbon dioxide-organic acid mixtures [J].
Byun, HS ;
Kim, K ;
McHugh, MA .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (12) :4580-4587
[7]
Phase equilibrium for the extraction of squalene from shark liver oil using supercritical carbon dioxide [J].
Catchpole, OJ ;
vonKamp, JC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (09) :3762-3768
[8]
Solubility of fish oil components in supercritical CO2 and CO2 plus ethanol mixtures [J].
Catchpole, OJ ;
Grey, JB ;
Noermark, KA .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1998, 43 (06) :1091-1095
[9]
Vapor-liquid equilibria of carbon dioxide with linoleic acid, α-tocopherol and triolein at elevated pressures [J].
Chen, CC ;
Chang, CMJ ;
Yang, PW .
FLUID PHASE EQUILIBRIA, 2000, 175 (1-2) :107-115
[10]
High-pressure fluid phase equilibria - Experimental methods and systems investigated (1994-1999) [J].
Christov, M ;
Dohrn, R .
FLUID PHASE EQUILIBRIA, 2002, 202 (01) :153-218