HIGH-PRESSURE FLUID PHASE-EQUILIBRIA - EXPERIMENTAL METHODS AND SYSTEMS INVESTIGATED (1978-1987)

被引：118

作者：

FORNARI, RE ^{[1
]}

ALESSI, P ^{[1
]}

KIKIC, I ^{[1
]}

机构：

[1] UNIV TRIESTE,IST CHIM APPL & IND,I-34127 TRIESTE,ITALY

来源：

FLUID PHASE EQUILIBRIA | 1990年 / 57卷 / 1-2期

关键词：

D O I：

10.1016/0378-3812(90)80010-9

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

The phase behaviour of fluid mixtures at high pressure has received great attention over the past decade. This upsurge of interest has been occasioned by the importance that high pressure fluid phase equilibria has now assumed in some industrial areas. This work reviews and classifies recently developed experimental methods for investigating high pressure fluid phase equilibria. A review of the systems studied in the last 10 years is also given. © 1990.

引用

页码：1 / 33

页数：33

共 83 条

[1] LIQUID + VAPOR EQUILIBRIA IN THE N2+CO2+CH4 SYSTEM [J].

ALSAHHAF, TA ;

KIDNAY, AJ ;

SLOAN, ED .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1983, 22 (04) :372-380

[2] VAPOR-LIQUID-EQUILIBRIA FOR THE CARBON DIOXIDE-1-BUTENE SYSTEM AT 37.7-DEGREES-C AND 45.0-DEGREES-C [J].

BEHRENS, PK ;

SANDLER, SI .

JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1983, 28 (01) :52-56

[3] SUPERCRITICAL FLUID EXTRACTION [J].

BRIGNOLE, EA .

FLUID PHASE EQUILIBRIA, 1986, 29 :133-144

[4] TERNARY PHASE-EQUILIBRIA FOR ACETIC ACID-WATER MIXTURES WITH SUPERCRITICAL CARBON-DIOXIDE [J].

BRIONES, JA ;

MULLINS, JC ;

THIES, MC ;

KIM, BU .

FLUID PHASE EQUILIBRIA, 1987, 36 :235-246

[5] VAPOR LIQUID EQUILIBRIUM IN THE SYSTEM DIMETHYL ETHER METHANOL FROM 0 TO 180-DEGREES-C AND AT PRESSURES TO 6.7 MPA [J].

CHANG, E ;

CALADO, JCG ;

STREETT, WB .

JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1982, 27 (03) :293-298

[6] SOLUBILITIES OF CARBON-DIOXIDE IN METHANOL AND METHANOL-WATER AT HIGH-PRESSURES - EXPERIMENTAL-DATA AND MODELING [J].

CHANG, TE ;

ROUSSEAU, RW .

FLUID PHASE EQUILIBRIA, 1985, 23 (2-3) :243-258

[7] APPLICATION OF A GENERALIZED MULTIPROPERTY APPARATUS TO MEASURE PHASE-EQUILIBRIUM AND VAPOR-PHASE DENSITIES OF SUPERCRITICAL CARBON-DIOXIDE IN NORMAL-HEXADECANE SYSTEMS UP TO 26 MPA [J].

CHAROENSOMBUTAMON, T ;

MARTIN, RJ ;

KOBAYASHI, R .

FLUID PHASE EQUILIBRIA, 1986, 31 (01) :89-104

[8]

DEFERNANDEZ MEP, 1987, FLUID PHASE EQUILIBR, V36, P91

[9] HIGH-PRESSURE PHASE-EQUILIBRIA - EXPERIMENTAL METHODS [J].

DEITERS, UK ;

SCHNEIDER, GM .

FLUID PHASE EQUILIBRIA, 1986, 29 :145-160

[10] VAPOR LIQUID CRITICAL CURVE OF THE SYSTEM ETHANE + 2-METHYLPROPANE [J].

DELOOS, TW ;

VANDERKOOI, HJ ;

OTT, PL .

JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1986, 31 (02) :166-168

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