High-pressure fluid-phase equilibria: Experimental methods and systems investigated (1988–1993)

Fluid Phase Equilibria - Tập 106 Số 1-2 - Trang 213-282 - 1995
Ralf Dohrn1, Gerd Brunner1
1Thermische Verfahrenstechnik, TU Hamburg-Harburg, 21071 Hamburg, Germany

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Acevedo, 1992, Isothermal Vapor-Liquid Equilibria for the n-Pentane + Methyl Acetate + Dichloromethane System, Fluid Phase Eq., 74, 145, 10.1016/0378-3812(92)85059-H

Adams, 1988, New Apparatus for Measurement of Supercritical Fluid-Liquid Phase Equilibria, AIChE J., 34, 1387, 10.1002/aic.690340820

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Akgerman, 1993, Supercritical Extraction of Organic Components from Aqueous Slurries, 294

Al-Sahhaf, 1990, Vapor-Liquid Equilibria for the Ternary System N2 + CO2 + CH4 at 230 and 250 K, Fluid Phase Eq., 55, 159, 10.1016/0378-3812(90)85010-8

Al-Sahhaf, 1990, Bubble Point Measurements for the Ternary System Carbon Dioxide, Benzene and Naphthalene, Fluid Phase Eq., 55, 231, 10.1016/0378-3812(90)85015-3

Angelos, 1992, Measurement and Modeling of Phase Equilibria with Synthetic Multicomponent Mixtures, Fluid Phase Eq., 72, 189, 10.1016/0378-3812(92)85026-5

Arita, 1991, Vapour-Liquid Equilibrium of the Non-Azeotropic Refrigerant Mixture Formed by Chlorofluoromethane and 1,1,1,2-Tetrafluoroethane, Fluid Phase Eq., 63, 151, 10.1016/0378-3812(91)80027-S

Ashour, 1993, Equilibrium Solubility of Pure Mono-, Di-, and Trilaurin in Supercritical Carbon Dioxide — Experimental Measurements and Model Prediction, J. Supercritical Fluids, 6, 3, 10.1016/0896-8446(93)90003-G

Azevedo, 1988, Phase Equilibria of Systems Containing Limonene, Cineole and Supercritical Carbon Dioxide, 135

Azevedo, 1993, Phase Equilibria of Ethene + Limonene and Ethene + Cineole from 285 K to 308 K and Pressures to 8 MPa, Fluid Phase Eq., 83, 193, 10.1016/0378-3812(93)87022-S

Bamberger, 1988, Measurement and Model Prediction of Solubilities of Pure Fatty Acids, Pure Triglycerides, and Mixtures of Triglycerides in Supercritical Carbon Dioxide, J. Chem. Eng. Data, 33, 327, 10.1021/je00053a029

Barber, 1991, Solubility of Solid CCl4 in Supercritical CF4, J. Chem. Eng. Data, 36, 99, 10.1021/je00001a030

Barreiros, 1989, Excess Thermodynamic Properties of Argon + Methane: A Standard Simple Liquid System, Fluid Phase Eq., 49, 9, 10.1016/0378-3812(89)80002-0

Bartle, 1990, Measurement of Solubility in Supercritical Fluids Using Chromatographic Retention: the Solubility of Fluorene, Phenanthrene, and Pyrene in Carbon Dioxide, J. Chem. Eng. Data, 35, 355, 10.1021/je00061a037

Beard, 1993, Phase Equilibria at High Pressures for the EthaneHeptane and EthaneTriethylaluminum Systems, Fluid Phase Eq., 82, 93, 10.1016/0378-3812(93)87132-K

Becker, 1990, Liquid-Liquid Phase Equilibria in the Methanol + 2,2,4-Trimethylpentane and Methanol + Methylcyclopentane Systems at Pressures form 5 to 120 MPa, J. Chem. Eng. Data, 35, 449, 10.1021/je00062a023

Berg, 1990, Vapour-Liquid Equilibrium in the Sulfur Hexafluoride-n-Pentane System at High Pressure, Fluid Phase Eq., 54, 35, 10.1016/0378-3812(90)85068-L

Bharath, 1989, Vapor-Liquid Equilibria for Binary Mixtures of Carbon Dioxide and Fatty Acid Ethyl Esters, Fluid Phase Eq., 50, 315, 10.1016/0378-3812(89)80298-5

Bharath, 1992, Phase Equilibrium Study for the Separation and Fractionation of Fatty Oil Components Using Supercritical Carbon Dioxide, Fluid Phase Eq., 81, 307, 10.1016/0378-3812(92)85159-6

Bharath, 1993, Phase Equilibria of Supercritical CO2− Fatty Oil Component Binary Systems, Fluid Phase Eq., 83, 183, 10.1016/0378-3812(93)87021-R

Bian, 1993, Simultaneous Determination of Vapor-Liquid Equilibrium and Molar Volumes for Coexisting Phases up to the Critical Temperature with a Static Method, Fluid Phase Eq., 90, 177, 10.1016/0378-3812(93)85012-B

Blanc, 1988, Vapor-Liquid Equilibria for the EthanePropane System at Low Temperature, J. Chem. Eng. Data, 33, 111, 10.1021/je00052a015

Bolaños, 1991, Production of Mesophase Pitch by Supercritical Fluid Extraction, 78

Bolz, 1991, A New Synthetic Method for High Pressure Phase Equilibria of Ternary Mixtures, 510

Briones, 1989, Liquid-Liquid Equilibria for Oleic AcidWater Mixtures at Elevated Temperatures and Pressures, Fluid Phase Eq., 53, 475, 10.1016/0378-3812(89)80113-X

Brown, 1988, Vapor-Liquid Equilibria in the Carbon DioxideEthane System, Fluid Phase Eq., 40, 169, 10.1016/0378-3812(88)80028-1

Brown, 1989, Vapor-Liquid Equilibria in the Nitrogen + Carbon Dioxide + Ethane System, Fluid Phase Eq., 51, 299, 10.1016/0378-3812(89)80372-3

Brown, 1989, Vapor-Liquid Equilibria for the Binary Systems of Nitrogen, Carbon Dioxide, and n-Butane at Temperatures from 220 to 344 K, Fluid Phase Eq., 53, 7, 10.1016/0378-3812(89)80067-6

Brunetti, 1989, Deacidification of Olive Oils by Supercritical Carbon Dioxide, JAOCS, 66, 209, 10.1007/BF02546062

Brunner, 1994

Brunner, 1991, Separation of Tocopherols from Deodorizer Condensates by Countercurrent Extraction with Carbon Dioxide, J. Supercritical Fluids, 4, 72, 10.1016/0896-8446(91)90034-4

Brunner, 1993, High Pressure Liquid-Liquid Equilibria in Ternary Systems Containing Water, Benzene, Toluene, n-Hexane and n-Hexadecane, Fluid Phase Eq., 82, 165, 10.1016/0378-3812(93)87140-V

Brunner, 1994, Phase Equilibria in Systems Containing Hydrogen, Carbon Dioxide, Water and Hydrocarbons, Fluid Phase Eq., 100, 253, 10.1016/0378-3812(94)80013-8

Bulley, 1992, Extraction/Fractionation of Egg Yolk Using Supercritical CO2 and Alcohol Entrainers, J. Supercritical Fluids, 5, 13, 10.1016/0896-8446(92)90035-I

Carroll, 1989, Phase Equilibrium in the System WaterHydrogen Sulphide: Experimental Determination of the LLV Locus, Can. J. Chem. Eng., 67, 468, 10.1002/cjce.5450670318

Carroll, 1992, Phase Equilibria in the System WaterMethyldiethanolaminePropane, AIChE J., 38, 511, 10.1002/aic.690380405

Chai Kao, 1993, Equation-of-State Analysis of Phase Behavior for WaterSurfactantSupercritical Fluid Mixtures, 74

Chang, 1992, The Solubility of Carbon Dioxide in Organic Solvents at Elevated Pressures, Fluid Phase Eq., 74, 235, 10.1016/0378-3812(92)85064-F

Chareton, 1990, Bubble Pressures and Saturated Liquid Molar Volumes of Binary and Ternary Refrigerant Mixtures, J. Chem. Eng. Data, 35, 162, 10.1021/je00060a019

Chen, 1993, Phase Behavior of LCST and UCST Solutions of Branchy Copolymers: Experiment and SAFT Modeling, Fluid Phase Eq., 83, 391, 10.1016/0378-3812(93)87043-Z

Chen, 1993, Mass Spectrometer Composition Probe for Batch Cell Studies of Supercritical Fluid Phase Equilibria, J. Chem. Eng. Data, 38, 211, 10.1021/je00010a006

Chen, 1989, Three-Phase Liquid-Liquid-Vapor Equilibria in the Nitrogen + Ethane + n-Butane System, J. Chem. Eng. Data, 34, 233, 10.1021/je00056a025

Chen, 1989, Three-Phase Liquid-Liquid-Vapor Equilibria in the Nitrogen + Methane + n-Heptane System, J. Chem. Eng. Data, 34, 312, 10.1021/je00057a016

Cheng, 1989, Vapor-Liquid Equilibrium in the System Carbon Dioxide + n-Pentane form 252 to 458 K at Pressures to 10 MPa, J. Chem. Eng. Data, 34, 319, 10.1021/je00057a018

Chou, 1990, High-Pressure Vapor-Liquid Equilibria for CO2n-Decane, CO2Tetralin and CO2/n-Decane/Tetralin at 71.1 and 104.4 °C, J. Chem. Eng. Data, 35, 26, 10.1021/je00059a008

Chou, 1989, Solubility of Ethylene in n-Eicosane, n-Octacoosane, and n-Hexatriacontane, J. Chem. Eng. Data, 34, 68, 10.1021/je00055a019

Christensen, 1992, Phase Equilibria for TetralinWater and 1-MethylnaphthaleneWater Mixtures at Elevated Temperatures and Pressures, Fluid Phase Eq., 71, 63, 10.1016/0378-3812(92)85005-S

Christou, 1991, Gas-Liquid Critical Temperatures of Mixtures of Propane, Butane, Pentane, Sulfur Hexafluoride, Dichlorodifluoromethane and Chlorotrifluoromethane with Less Volatile Compounds of a Range of Varying Polarities, Fluid Phase Eq., 67, 45, 10.1016/0378-3812(91)90046-A

Christou, 1991, Phase Behavior of 1-Alkanol + Alkane Mixtures: Gas-Liquid Critical Temperatures, Fluid Phase Eq., 67, 259, 10.1016/0378-3812(91)90060-K

Christou, 1991, Gas-Liquid Critical Temperatures of Binary Mixtures Containing a Low Molecular Weight Polydimethylsiloxane or Hexaethyldisiloxane, Fluid Phase Eq., 62, 153, 10.1016/0378-3812(91)87012-X

Chun, 1993, Vapor-Liquid Equilibria of Mixtures of Propane and Isomeric Hexanes, J. Chem. Eng. Data, 38, 494, 10.1021/je00012a003

Chung, 1992, Multiphase Behavior of Binary and Tenary Systems of Heavy Aromatic Hydrocarbons with Supercritical Carbon Dioxide, Fluid Phase Eq., 81, 321, 10.1016/0378-3812(92)85160-A

Chylinski, 1992, Phase Equilibrium Measurements in Gas-Condensates, Fluid Phase Eq., 76, 225, 10.1016/0378-3812(92)85090-U

Chylinski, 1993, VLE in Hydrocarbons of Greatly Differing Volatilities, Fluid Phase Eq., 82, 131, 10.1016/0378-3812(93)87136-O

Coats, 1991, Fluid Phase Equilibria for the Methyl ChlorideWater System, Fluid Phase Eq., 65, 327, 10.1016/0378-3812(91)87033-6

Connemann, 1990, Measurement and Representation of Ternary Vapour-Liquid-Liquid Equilibria, Fluid Phase Eq., 60, 99, 10.1016/0378-3812(90)85045-C

Coorens, 1988, Phase Equilibria in Binary Mixtures of Propane and Tripalmitin, Fluid Phase Eq., 40, 135, 10.1016/0378-3812(88)80026-8

Crovetto, 1992, Solubility of CO2 in Water and Density of Aqueous CO2 Near the Solvent Critical Temperature, Fluid Phase Eq., 74, 271, 10.1016/0378-3812(92)85067-I

Cygnarowicz, 1990, Equilibrium Solubilities of β-Carotene in Supercritical Carbon Dioxide, Fluid Phase Eq., 59, 57, 10.1016/0378-3812(90)85146-2

Danesh, 1990, A Novel Sampling Method for Compositional Analysis of High Pressure Fluids, Fluid Phase Eq., 57, 161, 10.1016/0378-3812(90)80018-7

Daneshvar, 1990, High-Pressure Phase Equilibria of Poly (ethylene glycol)Carbon Dioxide Systems, J. Phys. Chem., 94, 2124, 10.1021/j100368a071

Daridon, 1993, Density and Phase Behavior of the Ternary System MethaneCarbon DioxideHexadecanebetween 293 and 423 K and up to 50 MPa. Study of the Effect of Adding Water, Ber. Bunsenges. Phys. Chem., 97, 246

Darwish, 1993, Solubility of Methane in Heavy Normal Paraffins at Temperatures from 323 to 423 K and Pressures to 10.7 MPa, J. Chem. Eng. Data, 38, 44, 10.1021/je00009a010

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De Leeuw, 1989, High Pressure Phase Equilibria of the Binary Systems N2 + Benzene, N2 + p-Xylene and N2 + Naphthalene, Fluid Phase Eq., 49, 75, 10.1016/0378-3812(89)80007-X

De Leeuw, 1992, The Experimental Determination and Modelling of VLE for Binary Subsystems of the Quaternary System N2+CH4+C4H10+C14H10 up to 1000 Bar and 440 K, Fluid Phase Eq., 73, 285, 10.1016/0378-3812(92)80015-2

De Loos, 1988, Vapour-Liquid Equilibria and Critical Phenomena in Methanol + n-Alkane Systems, Fluid Phase Eq., 42, 209, 10.1016/0378-3812(88)80060-8

Dholabhai, 1993, Equilibrium Conditions for Carbon Dioxide Hydrate Formation in Aqueous Electrolyte Solutions, J. Chem. Eng. Data, 38, 650, 10.1021/je00012a045

Di Giacomo, 1989, Solubility of Essential Oil Components in Compressed Supercritical Carbon Dioxide, Fluid Phase Eq., 52, 405, 10.1016/0378-3812(89)80346-2

Dimitrelis, 1989, Solubilities of n-Octadecane, Phenanthrene, and n-OctadecanePhenanthrene ixtures in Supercritical Propane at 390 and 420 K and Pressures to 60 bar, J. Chem. Eng. Data, 34, 286, 10.1021/je00057a010

Dohrn, 1994

Dohr, 1993, Experimental Measurements of Phase Equilibria for Ternary and Quaternary Systems of Glucose, Water, CO2 and Ethanol with a Novel Apparatus, Fluid Phase Eq., 83, 149, 10.1016/0378-3812(93)87017-U

D'Souza, 1988, High Pressure Phase Equilibria in the System Glucose + Fructose + Water + Ethanol + Carbon Dioxide, Fluid Phase Eq., 39, 211, 10.1016/0378-3812(88)85005-2

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Eliosa, 1990, Gas-Liquid Pressure-Temperature-Composition Critical Loci for n-Butanenitrile with C5 to C11 n-Alkanes, Fluid Phase Eq., 61, 99, 10.1016/0378-3812(90)90007-A

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Fangyue, 1992, The Influence of Nitrogen on Fluid Phase Equilibria in the System Ethane + n-Decylbenzene up to 100 MPa, Fluid Phase Eq., 71, 273, 10.1016/0378-3812(92)80003-R

Feng, 1992, Solubility of Hydrogen Sulfide in n-Eicosane at Elevated Pressure, J. Chem. Eng. Data, 37, 412, 10.1021/je00008a009

Feng, 1993, Solubility of H2S in n-Hexadecane at Elevated Pressure, Can. J. Chem. Eng., 71, 327, 10.1002/cjce.5450710221

Feng, 1988, An Apparatus for Determining High Pressure Fluid Phase Equilibria and Its Applications to Supercritical Carbon Dioxide Mixtures, 75

Fink, 1990, Modeling the Vapor-Liquid Equilibria of 1,1,1-Trichloroethane + Carbon Dioxide and Toluene + Carbon Dioxide at 308, 323, and 353 K, Ind. Eng. Chem. Res., 29, 295, 10.1021/ie00098a022

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Fornari, 1990, High Pressure Fluid Phase Equilibria: Experimental Methods and Systems Investigated (1978–1987), Fluid Phase Eq., 57, 1, 10.1016/0378-3812(90)80010-9

Foster, 1991, Solubility of Oleic Acid in Supercritical Carbon Dioxide, J. Supercritical Fluids, 4, 127, 10.1016/0896-8446(91)90041-4

Foster, 1993, Polar and Nonpolar Cosolvent Effects on the Solubility of Cholesterol in Supercritrical Fluids, Ind. Eng. Chem. Res., 32, 2849, 10.1021/ie00023a056

Fransson, 1992, Vapor-Liquid Equilibrium in Binary Systems of n-Pentane + Chlorodifluoroethane, J. Chem. Eng. Data, 37, 521, 10.1021/je00008a034

Garcia-Sanchez, 1991, Critical Loci for Binary Chloroalkane-n-Alkane Mixtures. III. 1,1-Dichloroethane with C3C9 n-Alkanes, Fluid Phase Eq., 62, 87, 10.1016/0378-3812(91)87007-V

Gasem, 1989, Equilibrium Phase Compositions, Phase Densities, and Interfacial Tensions for CO2 + n-Tetradecane, J. Chem. Eng. Data, 34, 191, 10.1021/je00056a013

Ghonasgi, 1991, Measurement and Modeling of Supercritical Carbon Dioxide Extraction of Phenol from Water, J. Supercritical Fluids, 4, 53, 10.1016/0896-8446(91)90031-Z

Glówka, 1992, Volumetric Properties of Ammonia + Argon, + Helium, + Methane, and + Nitrogen Mixtures between 298 and 423 K by the Burnett-Isochoric Method, Fluid Phase Eq., 78, 285, 10.1016/0378-3812(92)87042-L

Göppert, 1988, Vapor-Liquid Equilibria in Aqueous Solutions of Ammonia and Carbon Dioxide at Temperatures between 333 and 393 K and Pressures up to 7 MPa, Fluid Phase Eq., 41, 153, 10.1016/0378-3812(88)80042-6

Góral, 1992, Vapour-Liquid Equilibria. The Ternary System AcetoneHexaneCyclohexane at 313.15 K, Fluid Phase Eq., 81, 261, 10.1016/0378-3812(92)85156-3

Graaf, 1992, Gas-Liquid Solubilities of the Methanol Synthesis Components in Various Solvents, J. Chem. Eng. Data, 37, 146, 10.1021/je00006a004

Gracia, 1992, Vapour Pressures of (Butan-1-ol + Hexane) at Temperatures between 283.10 K and 323.12 K, J. Chem. Thermodynamics, 24, 463, 10.1016/S0021-9614(05)80118-1

Gregg, 1993, Phase Behavior of Binary EthylenePropylene Copolymer Solutions in Sub- and Supercritical Ethylene and Propylene, Fluid Phase Eq., 83, 375, 10.1016/0378-3812(93)87041-X

Gregg, 1993, Vapor-Liquid Equilibria for Carbon Dioxide and 1-Methylnaphthalene: Experiment and Correlation, Fluid Phase Eq., 86, 211, 10.1016/0378-3812(93)87177-3

Gregg, 1993, Phase Equilibria of Binary and Ternary n-Alkane Solutions in Supercritical Ethylene, 1-Butene, and Ethylene + 1-Butene: Transition from Type A through LCST to U-LCST Behavior Predicted and Confirmed Experimentally, Ind. Eng. Chem. Res., 32, 1442, 10.1021/ie00019a019

Gregorowicz, 1993, Liquid-Liquid-Vapour Phase Equilibria in the System Ethane + Propane + Eicosane: Retrograde Behavior of the Heavy Liquid Phase, Fluid Phase Eq., 84, 225, 10.1016/0378-3812(93)85125-6

Gregorowicz, 1993, Three-Phase Equilibria in the Binary System Ethylene + Eicosane and the Ternary System Propane + Ethylene + Eicosane, J. Chem. Eng. Data, 38, 417, 10.1021/je00011a023

Gregorowicz, 1993, Liquid-Liquid-Vapour Phase Equilibria in the System Methane + Ethane + Eicosane: Retrograde Behaviour of the Heavy Liquid Phase, Fluid Phase Eq., 85, 225, 10.1016/0378-3812(93)80016-G

Gu, 1993, Experimental and Modeling Studies on the Phase Behavior of High H2S-Content Natural Gas Mixtures, Fluid Phase Eq., 82, 173, 10.1016/0378-3812(93)87141-M

Gupta, 1991, Supercritical Carbon Dioxide Extraction of a Phenolic Mixture from an Aqueous Waste Stream, J. Supercritical Fluids, 4, 181, 10.1016/0896-8446(91)90006-R

Gurdial, 1993, Phase Behavior of Supercritical Fluid-Entrainer Systems, 34

Hammam, 1992, Solubilities of Pure Lipids in Supercritical Carbon Dioxide, J. Supercritical Fluids, 5, 101, 10.1016/0896-8446(92)90026-G

Hammam, 1993, Phase Behavior of Some Pure Lipids in Supercritical Carbon Dioxide, J. Supercritical Fluids, 6, 223, 10.1016/0896-8446(93)90030-2

Han, 1992, An Apparatus for Phase Equilibrium Studies of Carbon Dioxide + Heavy Hydrocarbon Systems, Can. J. Chem. Eng., 70, 1164, 10.1002/cjce.5450700617

Hansen, 1993, Solubility Measurement by Direct Injection of Supercritical-Fluid Solutions into a HPLC System, J. Supercritical Fluids, 6, 229, 10.1016/0896-8446(93)90031-R

Hasch, 1991, Phase Behavior of the EthyleneMethyl Acrylate System, Fluid Phase Eq., 64, 251, 10.1016/0378-3812(91)90017-2

Hasch, 1993, The Effect of Copolymer Architecture on Solution Behavior, Fluid Phase Eq., 83, 341, 10.1016/0378-3812(93)87037-2

Hayduk, 1991, A High Pressure Solubility Apparatus for Gases of High Solubility, Can. J. Chem. Eng., 69, 1193, 10.1002/cjce.5450690520

Heilig, 1990, Phase Equilibria of Multicomponent Fluid Systems to High Pressures and Temperatures, Ber. Bunsenges. Phys. Chem., 94, 25, 10.1002/bbpc.19900940107

Hicks, 1978, A Bibliography of Thermodynamic Quantities for Binary Fluid Mixtures, Chemical Thermodynamics, 2

Hirohama, 1993, Measurement and Correlation of Phase Equilibria for the Carbon DioxideEthanolWater System, J. Chem. Eng. Japan, 26, 408, 10.1252/jcej.26.408

Hirohama, 1993, Phase Equilibria for the Carbon DioxideEthanolWater System with Trace Amounts of Organic Compounds, J. Chem. Eng. Japan, 26, 247, 10.1252/jcej.26.247

Hissong, 1993, Critical Properties and Vapor-Liquid Equilibria of the Binary System Propane + Neopentane, J. Chem. Eng. Data, 38, 486, 10.1021/je00012a002

Hochgeschurtz, 1993, Production of Mesophase Pitch by Supercritical Fluid Extraction, 347

Holder, 1992, Solubility of Ethylene in Benzene at Pressures to 9 MPa and Temperatures from 353 to 433 K, J. Chem. Eng. Data, 37, 100, 10.1021/je00005a026

Hollar, 1990, Solubility of Naphthalene in Mixtures of Carbon Dioxide and Ethane, J. Chem. Eng. Data, 35, 271, 10.1021/je00061a013

Holldorff, 1988, Binary Vapor-Liquid-Liquid Equilibrium of Dimethyl EtherWater and Mutual Solubilities of Methyl Chloride and Water: Experimental Results and Data Reduction, Fluid Phase Eq., 44, 195, 10.1016/0378-3812(88)80111-0

Holldorff, 1988, Vapor Pressures of n-Butane, Dimethyl Ether, Methyl Chloride, Methanol and the Vapor-Liquid Equilibrium of Dimethyl EtherMethanol: Experimental Apparatus, Results and Data Reduction, Fluid Phase Eq., 40, 113, 10.1016/0378-3812(88)80024-4

Holldorff, 1988, Vapor-Liquid Equilibria of the Binary Mixtures Methyl ChlorideMethanol and Dimethyl EtherMethyl Chloride and of the Ternary Mixture Dimethyl EtherMethyl ChlorideMethanol, Fluid Phase Eq., 43, 29, 10.1016/0378-3812(88)80069-4

Hong, 1988, Vapor-Liquid Equilibrium Studies for the Carbon DioxideMethanol System, Fluid Phase Eq., 41, 269, 10.1016/0378-3812(88)80011-6

Hong, 1991, Solid-Liquid-Vapor Phase Equilibria of the Mixture Carbon Dioxide + n-Hexane + n-Hexatriacontane, J. Supercritical Fluids, 4, 227, 10.1016/0896-8446(91)90015-X

Hong, 1992, Multiphase Equilibria of the Mixture Carbon Dioxide + Toluene + Naphthalene, Fluid Phase Eq., 74, 133, 10.1016/0378-3812(92)85058-G

Hong, 1993, Phase Equilibria of the Mixtures Methane + n-Hexane + n-Hexatriacontane, Methane + Toluene + Naphthalene, and Methane + n-Hexane + Naphthalene, Fluid Phase Eq., 87, 255, 10.1016/0378-3812(93)85030-P

Hooper, 1988, High-Temperature Mutual Solubilities for some Binary and Ternary Aqueous Mixtures Containing Aromatic and Chlorinated Hydrocarbons, J. Chem. Eng. Data, 33, 502, 10.1021/je00054a032

Horizoe, 1993, Phase Equilibrium Study for the Separation of EthanolWater Solution Using Subcritical and Supercritical Hydrocarbon Solvent Extraction, Fluid Phase Eq., 84, 297, 10.1016/0378-3812(93)85129-A

Hovey, 1990, Vapor-Liquid Phase Equilibria of Potassium ChlorideWater Mixtures: Equation-of-State Representation for KClH2O and NaClH2O, J. Phys. Chem., 94, 1175, 10.1021/j100366a032

Hölscher, 1989, Fluid Phase Equilibria of Binary and Ternary Mixtures of CO2 with Hexadecane, 1-Dodecanol, 1-Hexadecanol and 2-Ethoxy-Ethanol at 333.2 and 393.2 K and at Pressures up to 33 MPa, Fluid Phase Eq., 49, 103, 10.1016/0378-3812(89)80008-1

Huang, 1990, Phase Behavior of Reservoir Fluids II: Supercritical Carbon Dioxide and Bitumen Fractions, Fluid Phase Eq., 60, 81, 10.1016/0378-3812(90)85044-B

Huang, 1988, Solubility of Carbon Dioxide, Methane, and Ethane in n-Octacosane, J. Chem. Eng. Data, 33, 143, 10.1021/je00052a025

Huang, 1988, Solubility of Carbon Dioxide, Methane, and Ethane in n-Eicosane, J. Chem. Eng. Data, 33, 145, 10.1021/je00052a026

Huang, 1988, Solubility of Synthesis Gases in Heavy n-Paraffins and Fischer-Tropsch Wax, Ind. Eng. Chem. Res., 27, 162, 10.1021/ie00073a030

Hutchenson, 1990, Vapor-Liquid Equilibrium for PhenanthreneToluene Mixtures at Elevated Temperatures and Pressures, Fluid Phase Eq., 60, 309, 10.1016/0378-3812(90)85060-N

Hutchenson, 1991, Fractionation of Petroleum Pitch with Supercritical Toluene, J. Supercritical Fluids, 4, 7, 10.1016/0896-8446(91)90025-2

Ikawa, 1993, Separation Process of Ethanol from Aqueous Solutions Using Supercritical Carbon Dioxide, Fluid Phase Eq., 83, 167, 10.1016/0378-3812(93)87019-W

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