COMPUTATIONAL METHODS FOR HIGH-PRESSURE PHASE-EQUILIBRIA AND OTHER FLUID-PHASE PROPERTIES USING A PARTITION-FUNCTION .2. MIXTURES

被引：43

作者：

ANDERSON, TF ^{[1
]}

PRAUSNITZ, JM ^{[1
]}

机构：

[1] UNIV CALIF BERKELEY,DEPT CHEM ENGN,BERKELEY,CA 94720

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT | 1980年 / 19卷 / 01期

关键词：

D O I：

10.1021/i260073a002

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：9 / 14

页数：6

共 10 条

[1] LOW-TEMPERATURE PHASE EQUILIBRIA - CARBON DIOXIDE-PROPANE SYSTEM [J].

AKERS, WW ;

KELLEY, RE ;

LIPSCOMB, TG .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1954, 46 (12) :2535-2536

[2]

COWARD I, 1978, T I CHEM ENG-LOND, V56, P19

[3] PERTURBED HARD CHAIN THEORY FOR FLUID MIXTURES - THERMODYNAMIC PROPERTIES FOR MIXTURES IN NATURAL-GAS AND PETROLEUM TECHNOLOGY [J].

DONOHUE, MD ;

PRAUSNITZ, JM .

AICHE JOURNAL, 1978, 24 (05) :849-860

[4]

GRENS EA, 1978, COMMUNICATION

[5]

King C.J., 1971, SEPARATION PROCESSES

[6] CALCULATION OF HIGH-PRESSURE VAPOR-LIQUID-EQUILIBRIA FROM A CORRESPONDING-STATES CORRELATION WITH EMPHASIS ON ASYMMETRIC MIXTURES [J].

PLOCKER, U ;

KNAPP, H ;

PRAUSNITZ, J .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1978, 17 (03) :324-332

[7]

Rachford H.H., 1952, T AM I MIN MET ENG, V4, P19

[8]

RACHFORD HH, 1952, J PET TECHNOL, P3

[9]

ROBINSON DB, 1975, RR15 GAP RES REP

[10]

WICHTERLE I, 1972, J CHEM ENG DATA, V17, P4, DOI 10.1021/je60052a019

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