VAPOR-LIQUID-EQUILIBRIA FOR THE TERNARY-SYSTEM NORMAL-HEPTANE-NORMAL-PROPANOL-1, CHLOROBUTANE AND ITS CONSTITUENT BINARIES AT 318.15-K AND 338.15-K

被引：15

作者：

ASHRAF, FA ^{[1
]}

VERA, JH ^{[1
]}

机构：

[1] MCGILL UNIV,DEPT CHEM ENGN,MONTREAL H3A 2A7,QUEBEC,CANADA

来源：

CANADIAN JOURNAL OF CHEMICAL ENGINEERING | 1981年 / 59卷 / 01期

关键词：

D O I：

10.1002/cjce.5450590111

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：89 / 95

页数：7

共 15 条

[1] STATISTICAL THERMODYNAMICS OF LIQUID-MIXTURES - NEW EXPRESSION FOR EXCESS GIBBS ENERGY OF PARTLY OR COMPLETELY MISCIBLE SYSTEMS [J].

ABRAMS, DS ;

PRAUSNITZ, JM .

AICHE JOURNAL, 1975, 21 (01) :116-128

[2] APPLICATION OF UNIQUAC EQUATION TO CALCULATION OF MULTICOMPONENT PHASE-EQUILIBRIA .1. VAPOR-LIQUID-EQUILIBRIA [J].

ANDERSON, TF ;

PRAUSNITZ, JM .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1978, 17 (04) :552-561

[3] A SIMPLIFIED GROUP METHOD ANALYSIS [J].

ASHRAF, FA ;

VERA, JH .

FLUID PHASE EQUILIBRIA, 1980, 4 (3-4) :211-228

[4]

ASHRAF FA, 1979, THESIS MCGILL U MONT

[5]

DREISBACH RR, 1955, ADV CHEM SER, V15

[6] VAPOR-LIQUID EQUILIBRIA FROM TOTAL PRESSURE MEASUREMENTS - NEW APPARATUS [J].

GIBBS, RE ;

VANNESS, HC .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1972, 11 (03) :410-&

[7]

POWELL MJD, 1964, COMPUTER J, V7, P304

[8] MEASUREMENT OF VAPOR-LIQUID-EQUILIBRIA USING A SEMI-CONTINUOUS TOTAL PRESSURE STATIC EQUILIBRIUM STILL [J].

RONC, M ;

RATCLIFF, GR .

CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1976, 54 (04) :326-332

[9]

ROSSINI, 1969, API44 THERM RES CTR

[10]

SAYEGH SG, 1980, THESIS MCGILL U MONT

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