REPRESENTATION OF THE VAPOR-LIQUID-EQUILIBRIUM OF THE TERNARY-SYSTEM CARBON-DIOXIDE PROPANE METHANOL AND ITS BINARIES WITH A CUBIC EQUATION OF STATE - A NEW MIXING RULE

被引：35
作者：
SCHWARTZENTRUBER, J
GALIVELSOLASTIOUK, F
RENON, H
机构：
来源：
FLUID PHASE EQUILIBRIA | 1987年 / 38卷 / 03期
关键词：
D O I：
10.1016/0378-3812(87)85002-1
中图分类号：
O414.1 [热力学];
学科分类号：
摘要：
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页码：217 / 226
页数：10
相关论文
共 13 条
[1]   A NEW MIXING RULE MODIFIED CONVENTIONAL MIXING RULE [J].
ADACHI, Y ;
SUGIE, H .
FLUID PHASE EQUILIBRIA, 1986, 28 (02) :103-118
[2]   ESTIMATION OF PARAMETERS IN NONLINEAR, IMPLICIT MODELS [J].
BRITT, HI ;
LUECKE, RH .
TECHNOMETRICS, 1973, 15 (02) :233-247
[3]   VAPOR-LIQUID-EQUILIBRIUM DATA FOR THE PROPANE METHANOL AND PROPANE METHANOL CARBON-DIOXIDE SYSTEM [J].
GALIVELSOLASTIOUK, F ;
LAUGIER, S ;
RICHON, D .
FLUID PHASE EQUILIBRIA, 1986, 28 (01) :73-85
[4]  
HURON MJ, 1979, FLUID PHASE EQUILIBR, V3, P225
[5]   A VERSATILE PHASE-EQUILIBRIUM EQUATION OF STATE [J].
MATHIAS, PM .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1983, 22 (03) :385-391
[6]  
OHGAKI K, 1976, J CHEM ENG DATA, V21, P1428
[7]  
PANAGIOTOPOULOS AZ, 1986, ACS SYM SER, V300, P571
[8]   PHASE EQUILIBRIA IN HYDROCARBON SYSTEMS - VOLUMETRIC AND PHASE BEHAVIOR OF THE PROPANE-CARBON DIOXIDE SYSTEM [J].
REAMER, HH ;
SAGE, BH ;
LACEY, WN .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1951, 43 (11) :2515-2520
[9]  
Reid R.C., 1977, PROPERTIES GASES LIQ, V3rd
[10]   LOCAL COMPOSITIONS IN THERMODYNAMIC EXCESS FUNCTIONS FOR LIQUID MIXTURES [J].
RENON, H ;
PRAUSNITZ, JM .
AICHE JOURNAL, 1968, 14 (01) :135-+
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