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Cited article:

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Equilibrium Data for the Oxygen + Propane Binary System at Temperatures of (110.22, 120.13, 130.58, and 139.95) K

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Vapor–liquid equilibrium measurements and modeling of the n-butane+ethanol system from 323 to 423K

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Vapor–liquid equilibrium data for the nitrogen+n-octane system from (344.5 to 543.5)K and at pressures up to 50MPa

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Experimental techniques for the determination of thermophysical properties to enhance chemical processes

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Vapor–liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353K and pressures up to 4.16MPa

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Solubility of ethylbenzene and xylene in pure water and aqueous alkanolamine solutions

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(Vapor+liquid) equilibrium data for (carbon dioxide+1,1-difluoroethane) system at temperatures from (258 to 343)K and pressures up to about 8MPa

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Isothermal P, x, y data for the argon+carbon dioxide system at six temperatures from 233.32 to 299.21K and pressures up to 14MPa

C. Coquelet, A. Valtz, F. Dieu, et al.
Fluid Phase Equilibria 273 (1-2) 38 (2008)
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High-Pressure Vapor−Liquid Equilibria in the Nitrogen + n-Hexane System

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Phase Equilibrium Data for the Binary System Dinitrogen Monoxide + Propane

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Monatshefte für Chemie - Chemical Monthly 138 (7) 637 (2007)
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High-pressure (vapor+liquid) equilibria in the (nitrogen+n-heptane) system

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High-pressure vapor–liquid equilibria for CO2+alkanol systems and densities of n-dodecane and n-tridecane

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Fluid Phase Equilibria 259 (1) 23 (2007)
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Needs of thermodynamic properties measurements and modeling in the frame of new regulations on refrigerants

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New isothermal vapor–liquid equilibria for the CO2+n-nonane, and CO2+n-undecane systems

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Fluid Phase Equilibria 259 (1) 45 (2007)
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High-pressure vapor–liquid equilibria in the nitrogen–n-nonane system

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The Journal of Supercritical Fluids 42 (1) 36 (2007)
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Vapor–liquid equilibrium data for the hexafluoroethane+carbon dioxide system at temperatures from 253 to 297K and pressures up to 6.5MPa

Alain Valtz, Christophe Coquelet and Dominique Richon
Fluid Phase Equilibria 258 (2) 179 (2007)
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Measurement of VLE (TPx or TPxy data) for hydrogen sulfide+(dimethylsulfide or ethylmethylsulfide or carbon disulfide) and methane solubilities in (dimethylsulfide or ethylmethylsulfide or methylmercaptan or ethylmercaptan)

P. Guilbot, K. Fischer, A. Valtz, et al.
Fluid Phase Equilibria 260 (1) 49 (2007)
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High-pressure vapor–liquid equilibria in the nitrogen–n-pentane system

Guadalupe Silva-Oliver, Gaudencio Eliosa-Jiménez, Fernando García-Sánchez and Juan R. Avendaño-Gómez
Fluid Phase Equilibria 250 (1-2) 37 (2006)
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Experimental Vapor−Liquid Equilibria for the Carbon Dioxide + Octane and Carbon Dioxide + Decane Systems

R. Jiménez-Gallegos, L. A. Galicia-Luna and O. Elizalde-Solis
Journal of Chemical & Engineering Data 51 (5) 1624 (2006)
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Solubility data for benzene in aqueous solutions of methyldiethanolamine (MDEA) and of diglycolamine (DGA)

A. Valtz, C. Coquelet and D. Richon
Thermochimica Acta 443 (2) 245 (2006)
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Vapour–liquid equilibrium data for the hydrogen sulphide+n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa

Pascal Théveneau, Christophe Coquelet and Dominique Richon
Fluid Phase Equilibria 249 (1-2) 179 (2006)
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Diffusion During the Supercritical Drying of Silica Gels

Yasmine Masmoudi, Arnaud Rigacci, Pierre Ilbizian, Francois Cauneau and Patrick Achard
Drying Technology 24 (9) 1121 (2006)
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Experimental Determination and Correlation of Phase Equilibria for the Ethane + 1-Propanol and Propane + 1-Propanol Systems

Rodrigo Jiménez-Gallegos, Luis A. Galicia-Luna, Christian Bouchot, Luis E. Camacho-Camacho and Octavio Elizalde-Solis
Journal of Chemical & Engineering Data 51 (5) 1629 (2006)
https://doi.org/10.1021/je060112r

Measurement of physical properties of refrigerant mixtures. Determination of phase diagrams

C. Coquelet, F. Rivollet, C. Jarne, A. Valtz and D. Richon
Energy Conversion and Management 47 (20) 3672 (2006)
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Vapour–liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a)+dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3MPa

Alain Valtz, Leila Gicquel, Christophe Coquelet and Dominique Richon
Fluid Phase Equilibria 230 (1-2) 184 (2005)
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High pressure vapor–liquid equilibria for the systems thiophene+nonane+CO2, and thiophene+decane+CO2

Octavio Elizalde-Solis and Luis A. Galicia-Luna
Fluid Phase Equilibria 236 (1-2) 178 (2005)
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Experimental Measurement and Phase Behavior Modeling of Hydrogen Sulfide−Water Binary System

Antonin Chapoy, Amir H. Mohammadi, Bahman Tohidi, Alain Valtz and Dominique Richon
Industrial & Engineering Chemistry Research 44 (19) 7567 (2005)
https://doi.org/10.1021/ie050201h

Vapor–liquid equilibrium data for the difluoromethane (R32)–dimethyl ether (RE170) system at temperatures from 283.03 to 363.21K and pressures up to 5.5MPa

Christophe Coquelet, Alain Valtz and Dominique Richon
Fluid Phase Equilibria 232 (1-2) 44 (2005)
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Solubility of hydrogen in methanol at temperatures from 248.41 to 308.20K

C. Descamps, C. Coquelet, C. Bouallou and D. Richon
Thermochimica Acta 430 (1-2) 1 (2005)
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Solubility of Thiophene + Pentane and Thiophene + Octane Binary Mixtures in Supercritical Carbon Dioxide at Temperatures from 333 to 383 K

Octavio Elizalde-Solis and Luis A. Galicia-Luna
Industrial & Engineering Chemistry Research 44 (15) 5757 (2005)
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Experimental Measurement and Thermodynamic Modeling of Water Content in Methane and Ethane Systems

Amir H. Mohammadi, Antonin Chapoy, Dominique Richon and Bahman Tohidi
Industrial & Engineering Chemistry Research 43 (22) 7148 (2004)
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Vapour–liquid equilibria in the carbon dioxide–water system, measurement and modelling from 278.2 to 318.2K

Alain Valtz, Antonin Chapoy, Christophe Coquelet, Patrice Paricaud and Dominique Richon
Fluid Phase Equilibria 226 333 (2004)
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Vapor–liquid equilibrium data for the carbon dioxide (CO2) + difluoromethane (R32) system at temperatures from 283.12 to 343.25 K and pressures up to 7.46 MPa

F Rivollet, A Chapoy, C Coquelet and D Richon
Fluid Phase Equilibria 218 (1) 95 (2004)
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A Semiempirical Approach for Estimating the Water Content of Natural Gases

Amir H. Mohammadi, Antonin Chapoy, Bahman Tohidi and Dominique Richon
Industrial & Engineering Chemistry Research 43 (22) 7137 (2004)
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Vapor–liquid equilibrium data for the sulfur dioxide (SO2) + 1,1,1,2,3,3,3-heptafluoropropane (R227ea) system at temperatures from 288.07 to 403.19 K and pressures up to 5.38 MPa

A Valtz, C Coquelet and D Richon
Fluid Phase Equilibria 220 (1) 75 (2004)
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Vapor−Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Propane + Dimethyl Ether and Propene + Dimethyl Ether at Temperatures from (298 to 323) K

Sven Horstmann, Gerhard Birke and Kai Fischer
Journal of Chemical & Engineering Data 49 (1) 38 (2004)
https://doi.org/10.1021/je0301242

Experimental determination of carbon dioxide solubility data in aqueous alkanolamine solutions

Réda Sidi-Boumedine, Sven Horstmann, Kai Fischer, et al.
Fluid Phase Equilibria 218 (1) 85 (2004)
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Vapour–liquid equilibrium measurements and correlation of the difluoromethane (R32) + propane (R290) + 1,1,1,2,3,3,3-heptafluoropropane (R227ea) ternary mixture at temperatures from 269.85 to 328.35K

C Coquelet, A Chareton and D Richon
Fluid Phase Equilibria 218 (2) 209 (2004)
https://doi.org/10.1016/j.fluid.2003.12.009

Gas solubility measurement and modeling for methane–water and methane–ethane–n-butane–water systems at low temperature conditions

Antonin Chapoy, Amir H. Mohammadi, Dominique Richon and Bahman Tohidi
Fluid Phase Equilibria 220 (1) 113 (2004)
https://doi.org/10.1016/j.fluid.2004.02.010

Gas Solubility Measurement and Modeling for the Nitrogen + Water System from 274.18 K to 363.02 K

Antonin Chapoy, Amir H. Mohammadi, Bahman Tohidi and Dominique Richon
Journal of Chemical & Engineering Data 49 (4) 1110 (2004)
https://doi.org/10.1021/je049869d

Measurements and Thermodynamic Modeling of Vapor−Liquid Equilibria in Ethane−Water Systems from 274.26 to 343.08 K

Amir H. Mohammadi, Antonin Chapoy, Bahman Tohidi and Dominique Richon
Industrial & Engineering Chemistry Research 43 (17) 5418 (2004)
https://doi.org/10.1021/ie049747e

Solubility measurement and modeling for the system propane–water from 277.62 to 368.16K

Antonin Chapoy, Salim Mokraoui, Alain Valtz, et al.
Fluid Phase Equilibria 226 213 (2004)
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Vapor−Liquid−Liquid Equilibria, Azeotropic, and Excess Enthalpy Data for the Binary System n-Undecane + Propionamide and Pure-Component Vapor Pressure and Density Data for Propionamide

Sven Horstmann, Kai Fischer and Jürgen Gmehling
Journal of Chemical & Engineering Data 49 (6) 1494 (2004)
https://doi.org/10.1021/je034255e

Solubility measurement and modeling of water in the gas phase of the methane/water binary system at temperatures from 283.08 to 318.12K and pressures up to 34.5MPa

A. Chapoy, C. Coquelet and D. Richon
Fluid Phase Equilibria 214 (1) 101 (2003)
https://doi.org/10.1016/S0378-3812(03)00322-4

Vapor–liquid equilibrium data for the CO2 + 1,1,1,2,3,3,3,-heptafluoropropane (R227ea) system at temperatures from 276.01 to 367.30 K and pressures up to 7.4 MPa

A. Valtz, C. Coquelet, A. Baba-Ahmed and D. Richon
Fluid Phase Equilibria 207 (1-2) 53 (2003)
https://doi.org/10.1016/S0378-3812(02)00326-6

Vapour–liquid equilibrium data for the difluoromethane+1,1,1,2,3,3,3-heptafluoropropane system at temperatures from 283.20 to 343.38 K and pressures up to 4.5 MPa

C Coquelet, D Nguyen Hong, A Chareton, A Baba-Ahmed and D Richon
International Journal of Refrigeration 26 (5) 559 (2003)
https://doi.org/10.1016/S0140-7007(02)00164-0

Vapor–liquid equilibria and critical points of the CO2 + 1-hexanol and CO2 + 1-heptanol systems

O. Elizalde-Solis, L.A. Galicia-Luna, S.I. Sandler and J.G. Sampayo-Hernández
Fluid Phase Equilibria 210 (2) 215 (2003)
https://doi.org/10.1016/S0378-3812(03)00170-5

Vapor−Liquid Equilibrium Data for the Azeotropic Difluoromethane + Propane System at Temperatures from 294.83 to 343.26 K and Pressures up to 5.4 MPa

Christophe Coquelet, Albert Chareton, Alain Valtz, Abdelatif Baba-Ahmed and Dominique Richon
Journal of Chemical & Engineering Data 48 (2) 317 (2003)
https://doi.org/10.1021/je020115d

Vapor–liquid equilibrium data for the propane+1,1,1,2,3,3,3-heptafluoropropane (R227ea) system at temperatures from 293.16 to 353.18 K and pressures up to 3.4 MPa

A Valtz, C Coquelet, A Baba-Ahmed and D Richon
Fluid Phase Equilibria 202 (1) 29 (2002)
https://doi.org/10.1016/S0378-3812(02)00056-0

Solubility measurements for carbon dioxide and nitrous oxide in liquid oxygen at temperatures down to 90 K

V De Stefani, A Baba-Ahmed, A Valtz, D Meneses and D Richon
Fluid Phase Equilibria 200 (1) 19 (2002)
https://doi.org/10.1016/S0378-3812(01)00821-4

Isothermal Vapor−Liquid Equilibria of the Carbon Dioxide (CO2)−N,N-Dimethylformamide (DMF) System at Temperatures from 293.95 K to 338.05 K and Pressures up to 12 MPa

C. Duran-Valencia, A. Valtz, L. A. Galicia-Luna and D. Richon
Journal of Chemical & Engineering Data 46 (6) 1589 (2001)
https://doi.org/10.1021/je010055w