A MODIFIED UNIFAC GROUP-CONTRIBUTION MODEL FOR PREDICTION OF PHASE-EQUILIBRIA AND HEATS OF MIXING

被引：851
作者：
LARSEN, BL
RASMUSSEN, P
FREDENSLUND, A
机构：
[1] TECH UNIV DENMARK,INST KEMITEKNIK,DK-2800 LYNGBY,DENMARK
[2] DECHEMA,FRANKFURT,FED REP GER
来源：
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH | 1987年 / 26卷 / 11期
关键词：
D O I：
10.1021/ie00071a018
中图分类号：
TQ [化学工业];
学科分类号：
0817 ;
摘要：
引用
收藏
页码：2274 / 2286
页数：13
相关论文
共 33 条
[1]  
ABRAMS DS, 1975, AICHE J, V21, P16
[2]  
BELOUSOV WP, 1970, TEMPL SMECH ZH KHIM, P1
[3]  
CHRISTENSEN C, 1984, DECHEMA CHEM DATA 1, V3
[4]  
CHRISTENSEN C, 1984, DECHEMA CHEM DATA 2, V3
[5]   THERMODYNAMIC PROPERTIES OF BINARY MIXTURES FREE ENERGY AND ENTROPY OF HEXADECANE SOLUTION FORMATION IN HEXANE ISOMERS [J].
FERNANDEZGARCIA, JG ;
GUILLEMI.M ;
BOISSONN.CH .
HELVETICA CHIMICA ACTA, 1968, 51 (07) :1733-+
[6]  
Fletcher R., 2013, PRACTICAL METHODS OP
[7]   FROM UNIFAC TO SUPERFAC AND BACK [J].
FREDENSLUND, A ;
RASMUSSEN, P .
FLUID PHASE EQUILIBRIA, 1985, 24 (1-2) :115-150
[8]  
Fredenslund A., 1977, VAPOR LIQUID EQUILIB
[9]   VAPOR-LIQUID-EQUILIBRIA BY UNIFAC GROUP CONTRIBUTION - REVISION AND EXTENSION .2. [J].
GMEHLING, J ;
RASMUSSEN, P ;
FREDENSLUND, A .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1982, 21 (01) :118-127
[10]  
Gmehling J, 1977, DECHEMA CHEM DATA SE, VI
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