Present status of group-contribution methods for the synthesis and design of chemical processes

被引:46
作者
Gmehling, J [1 ]
机构
[1] Univ Oldenburg, D-26111 Oldenburg, Germany
关键词
phase equilibria; group-contribution methods; equations of state;
D O I
10.1016/S0378-3812(97)00242-2
中图分类号
O414.1 [热力学];
学科分类号
摘要
The reliable knowledge of the phase equilibrium behavior and the excess properties of the system to be separated is a prerequisite for the synthesis, design and optimization of separation processes. Two different approaches (g(E)-models, equations of state) can be used to predict the behavior of multicomponent systems using binary data alone. When experimental data are missing, group-contribution methods can be successfully applied to predict the phase equilibrium behavior or to supplement the existing data base. While at the beginning the main objective of group-contribution methods was the prediction of vapor-liquid equilibria (VLE) of subcritical compounds in a limited temperature range, an improved model allows not only to predict VLE, bur also solid-liquid equilibria (SLE), liquid-liquid equilibria (LLE), gamma(x) and h(E) in the whole composition and a large temperature range. By using group-contribution methods in g(E)-mixing rules of equations of state the advantages of the phi-phi-approach can be exploited and the range of applicability of the group-contribution concept can be extended to supercritical compounds and for the prediction of other important properties (densities, enthalpies, etc.). In this paper, the present status and typical results of the different group-contribution models will be shown and an outlook on future developments will be given. (C) 1998 Elsevier Science B.V.
引用
收藏
页码:37 / 47
页数:11
相关论文
共 26 条
[1]   PREDICTION OF VAPOR-LIQUID-EQUILIBRIUM WITH THE LCVM MODEL - A LINEAR COMBINATION OF THE VIDAL AND MICHELSEN MIXING RULES COUPLED WITH THE ORIGINAL UNIFAC AND THE T-MPR EQUATION OF STATE [J].
BOUKOUVALAS, C ;
SPILIOTIS, N ;
COUTSIKOS, P ;
TZOUVARAS, N ;
TASSIOS, D .
FLUID PHASE EQUILIBRIA, 1994, 92 :75-106
[2]   HIGH-PRESSURE VAPOR-LIQUID-EQUILIBRIUM WITH A UNIFAC-BASED EQUATION OF STATE [J].
DAHL, S ;
MICHELSEN, ML .
AICHE JOURNAL, 1990, 36 (12) :1829-1836
[3]  
Eckermann R, 1977, DECHEMA Chemistry Data Series
[4]   Further development, status and results of the PSRK method for the prediction of vapor-liquid equilibria and gas solubilities [J].
Fischer, K ;
Gmehling, J .
FLUID PHASE EQUILIBRIA, 1996, 121 (1-2) :185-206
[5]   PHASE-EQUILIBRIUM MODELS IN THE SYNTHESIS AND DESIGN OF SEPARATION PROCESSES [J].
GMEHLING, J .
CHEMIE INGENIEUR TECHNIK, 1994, 66 (06) :792-808
[6]   EXCESS-ENTHALPIES FOR 1,1,1-TRICHLOROETHANE WITH ALKANES, KETONES, AND ESTERS [J].
GMEHLING, J .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1993, 38 (01) :143-146
[7]   Further development of the PSRK model for the prediction of gas solubilities and vapor-liquid-equilibria at low and high pressures II [J].
Gmehling, J ;
Li, JD ;
Fischer, K .
FLUID PHASE EQUILIBRIA, 1997, 141 (1-2) :113-127
[8]   A MODIFIED UNIFAC MODEL .2. PRESENT PARAMETER MATRIX AND RESULTS FOR DIFFERENT THERMODYNAMIC PROPERTIES [J].
GMEHLING, J ;
LI, JD ;
SCHILLER, M .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1993, 32 (01) :178-193
[9]  
GMEHLING J, 1984, DECHEMA CHEM DATA SE
[10]  
Gmehling J., 1986, DECHEMA CHEM DATA SE