Beyond basic UNIFAC

被引:14
作者
Abildskov, J
Gani, R [1 ]
Rasmussen, P
O'Connell, JP
机构
[1] Tech Univ Denmark, Dept Chem Engn, DK-2800 Lyngby, Denmark
[2] Univ Virginia, Dept Chem Engn, Charlottesville, VA 22901 USA
关键词
excess Gibbs energies; activity coefficients; group contribution; second-order;
D O I
10.1016/S0378-3812(99)00091-6
中图分类号
O414.1 [热力学];
学科分类号
摘要
A new approach is proposed to extend UNIFAC to more complex substances. While first-order solution-of-groups methods such as UNIFAC can successfully represent measured phase equilibria for structurally simple systems such as mixtures of n-alkanes and linear alkanols with good accuracy, they are not as good for branched chain and polyfunctional substances such as secondary or tertiary alcohols and diols with branched or cyclic alkanes. Our method models departure from first-order behavior by adding second-order contributions to first-order correlations. The second-order contributions are derived from perturbations with respect to structural and energetic parameters. The basis of the extension and its ability to correlate and predict effects due to structural differences in VLE, SLE, and activity coefficients at infinite dilution (gamma(infinity)) for binary and multicomponent systems is described. Addition of a few second-order group parameters to the UNIFAC tables has improved the results for essentially all cases where the molecular structure justifies including such effects. (C) 1999 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:349 / 356
页数:8
相关论文
共 16 条
[1]   VAPOR-LIQUID-EQUILIBRIUM OF THE SYSTEMS 1-PROPANOL-2,2,4-TRIMETHYLPENTANE AND 2-PROPANOL-NORMAL-HEXANE [J].
BERRO, C ;
NEAU, E ;
ROGALSKI, M .
FLUID PHASE EQUILIBRIA, 1981, 7 (01) :41-54
[2]   ESTIMATION OF THE ACENTRIC FACTOR AND THE LIQUID MOLAR VOLUME AT 298-K USING A NEW GROUP-CONTRIBUTION METHOD [J].
CONSTANTINOU, L ;
GANI, R ;
OCONNELL, JP .
FLUID PHASE EQUILIBRIA, 1995, 103 (01) :11-22
[3]   NEW GROUP-CONTRIBUTION METHOD FOR ESTIMATING PROPERTIES OF PURE COMPOUNDS [J].
CONSTANTINOU, L ;
GANI, R .
AICHE JOURNAL, 1994, 40 (10) :1697-1710
[4]   RECENT PROGRESS IN THE COMPUTATION OF EQUILIBRIUM RATIOS [J].
FREDENSLUND, A ;
RASMUSSEN, P ;
MICHELSEN, ML .
CHEMICAL ENGINEERING COMMUNICATIONS, 1980, 4 (4-5) :485-500
[5]  
Fredenslund A., 1977, VAPOR LIQUID EQUILIB
[6]  
GMEHLING J, 1978, DECHEMA CHEM DATA 2B, V1
[7]  
GUGGENHEIM E, 1952, MIXTURS
[8]   SPACE PREDICTOR FOR INFINITE DILUTION ACTIVITY-COEFFICIENTS [J].
HAIT, MJ ;
LIOTTA, CL ;
ECKERT, CA ;
BERGMANN, DL ;
KARACHEWSKI, AM ;
DALLAS, AJ ;
EIKENS, DI ;
LI, JJJ ;
CARR, PW ;
POE, RB ;
RUTAN, SC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1993, 32 (11) :2905-2914
[9]   VAPOR-LIQUID-EQUILIBRIA BY UNIFAC GROUP CONTRIBUTION .5. REVISION AND EXTENSION [J].
HANSEN, HK ;
RASMUSSEN, P ;
FREDENSLUND, A ;
SCHILLER, M ;
GMEHLING, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (10) :2352-2355
[10]   ON COMPOSITION DEPENDENT INTERACTION COEFFICIENTS [J].
MICHELSEN, ML ;
KISTENMACHER, H .
FLUID PHASE EQUILIBRIA, 1990, 58 (1-2) :229-230