INFINITE DILUTION ACTIVITY-COEFFICIENTS PREDICTED BY UNIFAC GROUP CONTRIBUTION

被引：92

作者：

BASTOS, JC ^{[1
]}

SOARES, ME ^{[1
]}

MEDINA, AG ^{[1
]}

机构：

[1] UNIV PORTO,FAC ENGN,CTR ENGN QUIM,RUA DOS BRAGAS,P-4099 PORTO,PORTUGAL

来源：

关键词：

D O I：

10.1021/ie00079a030

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：1269 / 1277

页数：9

共 14 条

[1] UNIFAC AND INFINITE DILUTION ACTIVITY-COEFFICIENTS
ALESSI, P
FREDENSLUND, A
RASMUSSEN, P
[J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1982, 60 (02) : 300 - 304
[2] BASTOS J, 1984, CHISA 84 PRAHA
[3] SELECTION OF SOLVENTS FOR EXTRACTIVE DISTILLATION - A DATA-BANK FOR ACTIVITY-COEFFICIENTS AT INFINITE DILUTION
BASTOS, JC
SOARES, ME
MEDINA, AG
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1985, 24 (02): : 420 - 426
[4] Fredenslund A, 1977, VAPOUR LIQUID EQUILI
[5] VAPOR-LIQUID-EQUILIBRIA BY UNIFAC GROUP CONTRIBUTION - REVISION AND EXTENSION .2.
GMEHLING, J
RASMUSSEN, P
FREDENSLUND, A
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1982, 21 (01): : 118 - 127
[6] Gmehling J., 1979, DECHEMA CHEM DATA SE
[7] ON THE COMBINATORIAL PART OF THE UNIFAC AND UNIQUAC MODELS
KIKIC, I
ALESSI, P
RASMUSSEN, P
FREDENSLUND, A
[J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1980, 58 (02) : 253 - 258
[8] Kojima K, 1979, PREDICTION VAPOR LIQ
[9] VAPOR LIQUID EQUILIBRIA BY UNIFAC GROUP CONTRIBUTION - REVISION AND EXTENSION .3.
MACEDO, EA
WEIDLICH, U
GMEHLING, J
RASMUSSEN, P
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1983, 22 (04): : 676 - 678
[10] UNIFAC PARAMETER TABLE FOR PREDICTION OF LIQUID-LIQUID EQUILIBRIA
MAGNUSSEN, T
RASMUSSEN, P
FREDENSLUND, A
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1981, 20 (02): : 331 - 339