CALCULATION OF MULTIPHASE EQUILIBRIA BY A GROUP CONTRIBUTION EQUATION OF STATE

被引：7

作者：

SUEN, SY ^{[1
]}

CHEN, YP ^{[1
]}

WONG, DS ^{[1
]}

机构：

[1] NATL TSING HUA UNIV,DEPT CHEM ENGN,HSINCHU 300,TAIWAN

来源：

FLUID PHASE EQUILIBRIA | 1989年 / 52卷

关键词：

D O I：

10.1016/0378-3812(89)80313-9

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

引用

页码：75 / 82

页数：8

共 10 条

[1]

Gmehling J., 1986, VAPOR LIQUID EQUILIB, VI, P501

[2]

Gmehling J., 1977, VAPOR LIQUID EQUILIB

[3] A NEW GROUP-CONTRIBUTION EQUATION OF STATE FOR VAPOR-LIQUID-EQUILIBRIA [J].

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RASMUSSEN, P ;

FREDENSLUND, A .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1986, 25 (04) :636-645

[4] MEASUREMENT AND CORRELATION OF LIQUID-LIQUID EQUILIBRIA OF BINARY AND TERNARY-SYSTEMS CONTAINING METHANOL AND HYDROCARBONS [J].

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IWAI, Y ;

ARAI, Y ;

NAGATANI, M .

FLUID PHASE EQUILIBRIA, 1987, 36 :35-47

[5] NEW MIXING RULES IN SIMPLE EQUATIONS OF STATE FOR REPRESENTING VAPOR-LIQUID-EQUILIBRIA OF STRONGLY NON-IDEAL MIXTURES [J].

HURON, MJ ;

VIDAL, J .

FLUID PHASE EQUILIBRIA, 1979, 3 (04) :255-271

[6] A MODIFIED UNIFAC GROUP-CONTRIBUTION MODEL FOR PREDICTION OF PHASE-EQUILIBRIA AND HEATS OF MIXING [J].

LARSEN, BL ;

RASMUSSEN, P ;

FREDENSLUND, A .

INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1987, 26 (11) :2274-2286

[7] METHANE NORMAL-BUTANE WATER SYSTEM IN 2-PHASE AND 3-PHASE REGIONS [J].

MCKETTA, JJ ;

KATZ, DL .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1948, 40 (05) :853-863

[8] A NEW CUBIC EQUATION OF STATE FOR FLUIDS AND FLUID MIXTURES [J].

PATEL, NC ;

TEJA, AS .

CHEMICAL ENGINEERING SCIENCE, 1982, 37 (03) :463-473

[9] A CUBIC EQUATION OF STATE FOR PREDICTING VAPOR LIQUID EQUILIBRIA OF HYDROCARBON MIXTURES USING A GROUP CONTRIBUTION MIXING RULE [J].

SHENG, YJ ;

CHEN, YP ;

WONG, DSH .

FLUID PHASE EQUILIBRIA, 1989, 46 (2-3) :197-210

[10]

Sorensen JM, 1979, LIQUID LIQUID EQUILI

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