VAPOR-LIQUID-EQUILIBRIUM IN THE CARBON-DIOXIDE - P-CYMENE SYSTEM AT HIGH-PRESSURE

被引：9

作者：

WAGNER, Z

PAVLICEK, J

机构：

[1] E. Hála Laboratory of Thermodynamics, Institute of Chemical Process Fundamentals

来源：

FLUID PHASE EQUILIBRIA | 1993年 / 90卷 / 01期

关键词：

EXPERIMENTS; DATA; VLE HIGH PRESSURE; CARBON DIOXIDE; HYDROCARBONS;

D O I：

10.1016/0378-3812(93)85008-A

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

Vapour-liquid equilibrium data in the carbon dioxide - p-cymene system were measured isothermally at 313.15 K and 323.15 K at pressures ranging from 4 MPa to 10 MPa. The experimental data were fitted to the Soave-Redlich-Kwong equation of state adopting a maximum likelihood procedure.

引用

页码：135 / 141

页数：7

共 9 条

[1]

AMBROSE D, 1978, VAPOUR LIQUID CRITIC

[2]

DREISBACH RR, 1955, ADV CHEM SER, V15

[3] MODIFIED SOAVE EQUATION OF STATE FOR PHASE-EQUILIBRIUM CALCULATIONS .1. HYDROCARBON SYSTEMS [J].

GRABOSKI, MS ;

DAUBERT, TE .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1978, 17 (04) :443-448

[4] VANDERWAALS MIXING RULES FOR CUBIC EQUATIONS OF STATE - APPLICATIONS FOR SUPERCRITICAL FLUID EXTRACTION MODELING [J].

KWAK, TY ;

MANSOORI, GA .

CHEMICAL ENGINEERING SCIENCE, 1986, 41 (05) :1303-1309

[5] VAPOR-LIQUID-EQUILIBRIA IN THE ETHANE-NORMAL-BUTANE SYSTEM AT HIGH-PRESSURES [J].

LHOTAK, V ;

WICHTERLE, I .

FLUID PHASE EQUILIBRIA, 1981, 6 (3-4) :229-235

[6]

PAVLICEK J, 1993, UNPUB FLUID PHASE EQ

[7] ITERATIVE ESTIMATION OF MODEL PARAMETERS WHEN MEASUREMENTS OF ALL VARIABLES ARE SUBJECT TO ERROR [J].

ROD, V ;

HANCIL, V .

COMPUTERS & CHEMICAL ENGINEERING, 1980, 4 (01) :33-38

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

SOAVE, G .

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

[9] HIGH-PRESSURE VAPOR-LIQUID-EQUILIBRIUM IN SYSTEMS CONTAINING CARBON-DIOXIDE, 1-HEXENE, AND N-HEXANE [J].

WAGNER, Z ;

WICHTERLE, I .

FLUID PHASE EQUILIBRIA, 1987, 33 (1-2) :109-123

← 1 →