A New Two-Constant Equation of State

被引：10160

作者：

PENG, D ^{[1
]}

ROBINSON, DB ^{[1
]}

机构：

[1] UNIV ALBERTA, DEPT CHEM ENGN, EDMONTON, ALBERTA, CANADA

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS | 1976年 / 15卷 / 01期

关键词：

D O I：

10.1021/i160057a011

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：59 / 64

页数：6

共 27 条

[11] MULTIPROPERTY ANALYSIS OF PVT, ENTHALPY AND PHASE EQUILIBRIUM DATA [J].

LIN, CJ ;

STARLING, KE ;

KWOK, YC .

CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1972, 50 (05) :644-&

[12]

Mage D, 1963, Chem Eng Prog Symp Ser., V59, P61

[13] PHASE EQUILIBRIA IN HYDROCARBON SYSTEMS - THE NORMAL-BUTANE-CARBON DIOXIDE SYSTEM [J].

OLDS, RH ;

REAMER, HH ;

SAGE, BH ;

LACEY, WN .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1949, 41 (03) :475-482

[14]

PENG D, 1975, 9TH WORLD PETR C T T

[15] Phase equilibria in hydrocarbon systems - Methane-decane system [J].

Reamer, HH ;

Olds, RH ;

Sage, BH ;

Lacey, WN .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1942, 34 :1526-1531

[16]

REAMER HH, 1957, J CHEM ENG DATA, V2, P9

[17] ON THE THERMODYNAMICS OF SOLUTIONS .5. AN EQUATION OF STATE - FUGACITIES OF GASEOUS SOLUTIONS [J].

REDLICH, O ;

KWONG, JNS .

CHEMICAL REVIEWS, 1949, 44 (01) :233-244

[18]

REDLICH O, 1963, CHEM ENG PROGR S SER, V59, P95

[19]

Rossini F.D., 1953, SELECTED VALUES PHYS

[20] EQUILIBRIUM CONSTANTS FROM A MODIFIED REDLICH-KWONG EQUATION OF STATE [J].

SOAVE, G .

CHEMICAL ENGINEERING SCIENCE, 1972, 27 (06) :1197-&

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