A NEW CUBIC EQUATION OF STATE FOR FLUIDS AND FLUID MIXTURES

被引：829

作者：

PATEL, NC

TEJA, AS

机构：

[1] LOUGHBOROUGH UNIV TECHNOL,DEPT CHEM ENGN,LOUGHBOROUGH LE11 3TU,LEICESTERSHIRE,ENGLAND

[2] GEORGIA INST TECHNOL,SCH CHEM ENGN,ATLANTA,GA 30332

来源：

关键词：

D O I：

10.1016/0009-2509(82)80099-7

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：463 / 473

页数：11

共 17 条

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[3] ADLER SB, 1977, ACS S SERIES, V60, P150
[4] NEW MODIFICATION OF REDLICH-KWONG EQUATION OF STATE BASED ON ANALYSIS OF A LARGE SET OF PURE COMPONENT DATA
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ASSELINE.L
RENON, H
[J]. CHEMICAL ENGINEERING SCIENCE, 1973, 28 (03) : 839 - 846
[5] VAPOR-LIQUID EQUILIBRIA AT HIGH PRESSURES . VAPOR-PHASE FUGACITY COEFFICIENTS IN NONPOLAR AND QUANTUM-GAS MIXTURES
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[J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1967, 6 (04): : 492 - +
[6] MODIFIED REDLICH-KWONG-SOAVE EQUATION OF STATE CAPABLE OF REPRESENTING LIQUID-STATE
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[J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1976, 15 (04): : 254 - 257
[7] MODIFIED SOAVE EQUATION OF STATE FOR PHASE-EQUILIBRIUM CALCULATIONS .1. HYDROCARBON SYSTEMS
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[J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1978, 17 (04): : 443 - 448
[8] 3-PARAMETER CUBIC EQUATION OF STATE FOR NORMAL SUBSTANCES
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KNAPP, H
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1980, 19 (03): : 291 - 294
[9] HEYEN G, 1980, 2ND P INT C PHAS EQ, V1
[10] NOTE ON USE OF ZC AS A 3RD PARAMETER WITH CORRESPONDING STATES PRINCIPLE
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