A review of Barker's activity coefficient method and VLE data reduction

被引：11

作者：

Islam, Akand W. ^{[1
]}

Rahman, Md Hafizur ^{[2
]}

机构：

[1] Univ Alabama, Dept Chem & Biol Engn, Tuscaloosa, AL 35401 USA

[2] Univ British Columbia, Dept Chem & Biol Engn, Vancouver, BC V5Z 1M9, Canada

来源：

JOURNAL OF CHEMICAL THERMODYNAMICS | 2012年 / 44卷 / 01期

关键词：

Barker's method; Activity coefficient; Data reduction; Excess Gibbs free energy; VAPOR-LIQUID-EQUILIBRIUM; GIBBS FREE-ENERGIES; TOTAL PRESSURE MEASUREMENTS; EXCESS FREE-ENERGY; PLUS N-HEPTANE; AROMATICS EXTRACTION SYSTEMS; BINARY-MIXTURES; 323.15; K; THERMODYNAMIC PROPERTIES; T=298.15 K;

D O I：

10.1016/j.jct.2011.08.013

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

The method of Barker is a popular scheme for determination of activity coefficients from total pressure measurements. A comprehensive review of this method is presented in this study. While discussing this technique various aspects of (vapor + liquid) equilibrium (VLE) data reduction process including types of algorithms applied, roles of saturated vapor pressures and equilibrium vapor compositions data, and types of objective functions used are analyzed. Activity coefficient or liquid state models frequently used in VLE data reduction are shown and their comparisons are investigated. More so, advantages and limitations of Barker's method are demonstrated. (C) 2011 Elsevier Ltd. All rights reserved.

引用

页码：31 / 37

页数：7

共 161 条

[1] VAPOR-LIQUID-EQUILIBRIUM .4. REDUCTION OF P-X DATA FOR TERNARY-SYSTEMS [J].

ABBOTT, MM ;

FLOESS, JK ;

WALSH, GE ;

VANNESS, HC .

AICHE JOURNAL, 1975, 21 (01) :72-76

[2]

ABBOTT MM, 1975, AICHE J, V21, P62, DOI 10.1002/aic.690210107

[3] EXTENSION OF BARKERS METHOD FOR REDUCTION OF VLE DATA [J].

ABBOTT, MM ;

VANNESS, HC .

FLUID PHASE EQUILIBRIA, 1977, 1 (01) :3-11

[4] MEASUREMENT OF VAPOR-LIQUID-EQUILIBRIUM IN SYSTEMS WITH COMPONENTS OF VERY DIFFERENT VOLATILITY BY TOTAL PRESSURE STATIC METHOD [J].

AIM, K .

FLUID PHASE EQUILIBRIA, 1978, 2 (02) :119-142

[5] Isobaric vapour-liquid equilibria for binary mixtures of 1,2-dibromoethane with 1,2-dichloroethane, trichloromethane, and 1,1,2,2-tetrachloroethane at atmospheric pressure [J].

Al-Hayan, MNM ;

Al-Kandary, JAM .

FLUID PHASE EQUILIBRIA, 2006, 239 (02) :133-137

[6] Vapour-liquid equilibrium of octane-enhancing additives in gasolines 2.: Total pressure data and gE for binary and ternary mixtures containing tert-amylmethyl ether (TAME), tert-amyl alcohol (TAOH) and n-hexane [J].

Alonso, C ;

Montero, EA ;

Chamorro, CR ;

Segovia, JJ ;

Martín, MC ;

Villamañán, MA .

FLUID PHASE EQUILIBRIA, 2001, 182 (1-2) :241-255

[7] Vapor-Liquid Equilibrium of Aqueous Alkaline Nitrate and Nitrite Solutions for Absorption Refrigeration Cycles with High-Temperature Driving Heat [J].

Alvarez, Maria E. ;

Bourouis, Mahmoud ;

Esteve, Xavier .

JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2011, 56 (03) :491-496

[8] Isothermal vapour-liquid equilibria of binary systems of 1,2-dichloroethane with ethers [J].

Amireche-Ziar, Faouzia ;

Boukais-Belaribi, Ghenima ;

Jakob, Antje ;

Mokbel, Ilham ;

Belaribi, Farid Brahim .

FLUID PHASE EQUILIBRIA, 2008, 268 (1-2) :39-44

[9] EVALUATION OF PARAMETERS FOR NON-LINEAR THERMODYNAMIC MODELS [J].

ANDERSON, TF ;

ABRAMS, DS ;

GRENS, EA .

AICHE JOURNAL, 1978, 24 (01) :20-29

[10] VAPOR-PRESSURES OF (TETRACHLORO-METHANE + ALPHA,OMEGA-DICHLOROALKANE) [J].

AZPIAZU, Y ;

ROYO, F ;

LOSA, CG .

JOURNAL OF CHEMICAL THERMODYNAMICS, 1984, 16 (06) :561-565

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