EXTENSION OF UNIFAC TO HIGH-PRESSURE VLE USING VIDAL MIXING RULES

被引:17
作者
GUPTE, PA [1 ]
DAUBERT, TE [1 ]
机构
[1] PENN STATE UNIV,DEPT CHEM ENGN,UNIVERSITY PK,PA 16802
关键词
The Design Institute for Physical Property Data of the American Institute of Chemical Engineers provided financial support of the work. The authors acknowledge Prof. Jean Vidal; Prof; Aa; Fredenslund; Dr. Jorgen Mollerup; and Dr. Steen Skjold-Jorgensen for helpful discussions;
D O I
10.1016/0378-3812(86)85075-0
中图分类号
O414.1 [热力学];
学科分类号
摘要
引用
收藏
页码:155 / 170
页数:16
相关论文
共 24 条
[1]  
BUTCHER KL, 1968, J APPL CHEM, V18, P100
[2]  
DANNER RP, 1986, DATA PREDICTION MANU, pCH6
[3]  
ELLIS SRM, 1961, CHEM AGE INDIA, V12, P377
[4]   FROM UNIFAC TO SUPERFAC AND BACK [J].
FREDENSLUND, A ;
RASMUSSEN, P .
FLUID PHASE EQUILIBRIA, 1985, 24 (1-2) :115-150
[5]   GROUP-CONTRIBUTION ESTIMATION OF ACTIVITY-COEFFICIENTS IN NONIDEAL LIQUID-MIXTURES [J].
FREDENSLUND, A ;
JONES, RL ;
PRAUSNITZ, JM .
AICHE JOURNAL, 1975, 21 (06) :1086-1099
[6]   MODIFIED SOAVE EQUATION OF STATE FOR PHASE-EQUILIBRIUM CALCULATIONS .1. HYDROCARBON SYSTEMS [J].
GRABOSKI, MS ;
DAUBERT, TE .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1978, 17 (04) :443-448
[7]  
GRISWOLD J, 1952, CHEM ENG PROG S SER, V48, P18
[8]  
GUGGENHEIM EA, 1952, MIXTURES, pCH10
[9]  
GUPTE PA, 1986, IND ENG CHEM PROCESS, V25
[10]   GENERALIZED METHOD FOR PREDICTING 2ND VIRIAL-COEFFICIENTS [J].
HAYDEN, JG ;
OCONNELL, JP .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1975, 14 (03) :209-216