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Pure Component and Binary Vapor−Liquid Equilibrium + Modeling for Hexafluoropropylene and Hexafluoropropylene Oxide with Toluene and Hexafluoroethane
Shalendra C. Subramoney, Wayne M. Nelson, Alain Valtz, et al. Journal of Chemical & Engineering Data 55(1) 411 (2010) https://doi.org/10.1021/je900400v
Isothermal Vapor−Liquid Equilibrium Data for the Hexafluoropropylene (R1216) + Propylene System at Temperatures from (263.17 to 353.14) K
Christophe Coquelet, Alain Valtz, Paramespri Naidoo, Deresh Ramjugernath and Dominique Richon Journal of Chemical & Engineering Data 55(4) 1636 (2010) https://doi.org/10.1021/je900703f
Equipment using a “static-analytic” method for solubility measurements in potentially hazardous binary mixtures under cryogenic temperatures
Equilibrium Data for the Oxygen + Propane Binary System at Temperatures of (110.22, 120.13, 130.58, and 139.95) K
Deborah Houssin-Agbomson, Christophe Coquelet, Philippe Arpentinier, Fabrice Delcorso and Dominique Richon Journal of Chemical & Engineering Data 55(10) 4412 (2010) https://doi.org/10.1021/je100574y
Isothermal Vapor−Liquid Equilibrium Data of 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylformamide (DMF) Working Fluids for an Absorption Heat Transformer
Raouf Zehioua, Christophe Coquelet, Abdeslam-Hassen Meniai and Dominique Richon Journal of Chemical & Engineering Data 55(2) 985 (2010) https://doi.org/10.1021/je900440t
Liquid–liquid equilibrium of (water+1-propanol+1-pentanol) system at 298.15 and 323.15K
Vapor−Liquid Equilibrium Data for the Nitrogen + n-Decane System from (344 to 563) K and at Pressures up to 50 MPa
Fernando García-Sánchez, Gaudencio Eliosa-Jiménez, Guadalupe Silva-Oliver and Blanca E. García-Flores Journal of Chemical & Engineering Data 54(5) 1560 (2009) https://doi.org/10.1021/je800881t
Vapor–liquid equilibria of the (hexafluoroethane+1,1,1-trifluoroethane) binary system from 258 to 343K up to 3.89MPa
Hakim Madani, Alain Valtz, Christophe Coquelet, Abdeslam Hassen Meniai and Dominique Richon International Journal of Refrigeration 32(6) 1396 (2009) https://doi.org/10.1016/j.ijrefrig.2009.01.018
Vapor–liquid equilibrium measurements and modeling of the n-butane+ethanol system from 323 to 423K
Chien-Bin Soo, Elise El Ahmar, Christophe Coquelet, Deresh Ramjugernath and Dominique Richon Fluid Phase Equilibria 286(1) 79 (2009) https://doi.org/10.1016/j.fluid.2009.08.007
Isothermal Vapor−Liquid Equilibrium Data for the Hexafluoroethane (R116) + Propane System at Temperatures from (263 to 323) K
Deresh Ramjugernath, Alain Valtz, Christophe Coquelet and Dominique Richon Journal of Chemical & Engineering Data 54(4) 1292 (2009) https://doi.org/10.1021/je800849s
Thermodynamic behavior of the CO2+SO2 mixture: Experimental and Monte Carlo simulation studies
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
Hakim Madani, Alain Valtz, Christophe Coquelet, Abdeslam Hassen Meniai and Dominique Richon Fluid Phase Equilibria 268(1-2) 68 (2008) https://doi.org/10.1016/j.fluid.2008.04.002
Solubility of ethylbenzene and xylene in pure water and aqueous alkanolamine solutions
(Vapor+liquid) equilibrium data for (carbon dioxide+1,1-difluoroethane) system at temperatures from (258 to 343)K and pressures up to about 8MPa
Hakim Madani, Alain Valtz, Christophe Coquelet, Abdeslam Hassen Meniai and Dominique Richon The Journal of Chemical Thermodynamics 40(10) 1490 (2008) https://doi.org/10.1016/j.jct.2008.06.002
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
High-Pressure Vapor−Liquid Equilibria in the Nitrogen + n-Hexane System
Gaudencio Eliosa-Jiménez, Guadalupe Silva-Oliver, Fernando García-Sánchez and Antonio de Ita de la Torre Journal of Chemical & Engineering Data 52(2) 395 (2007) https://doi.org/10.1021/je060341d
Phase Equilibrium Data for the Binary System Dinitrogen Monoxide + Propane
High-pressure (vapor+liquid) equilibria in the (nitrogen+n-heptane) system
Fernando García-Sánchez, Gaudencio Eliosa-Jiménez, Guadalupe Silva-Oliver and Armando Godínez-Silva The Journal of Chemical Thermodynamics 39(6) 893 (2007) https://doi.org/10.1016/j.jct.2006.11.007
High-pressure vapor–liquid equilibria for CO2+alkanol systems and densities of n-dodecane and n-tridecane
New isothermal vapor–liquid equilibria for the CO2+n-nonane, and CO2+n-undecane systems
Luis E. Camacho-Camacho, Luis A. Galicia-Luna, Octavio Elizalde-Solis and Zenaido Martínez-Ramírez Fluid Phase Equilibria 259(1) 45 (2007) https://doi.org/10.1016/j.fluid.2007.04.022
High-pressure vapor–liquid equilibria in the nitrogen–n-nonane system
Guadalupe Silva-Oliver, Gaudencio Eliosa-Jiménez, Fernando García-Sánchez and Juan Ramón Avendaño-Gómez The Journal of Supercritical Fluids 42(1) 36 (2007) https://doi.org/10.1016/j.supflu.2007.01.006
Vapor–liquid equilibrium data for the hexafluoroethane+carbon dioxide system at temperatures from 253 to 297K and pressures up to 6.5MPa
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)
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) https://doi.org/10.1016/j.fluid.2006.09.018
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) https://doi.org/10.1021/je060111z
Solubility data for benzene in aqueous solutions of methyldiethanolamine (MDEA) and of diglycolamine (DGA)
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) https://doi.org/10.1080/07373930600778270
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
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
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
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) https://doi.org/10.1021/ie048780y
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) https://doi.org/10.1021/ie049843f
Vapour–liquid equilibria in the carbon dioxide–water system, measurement and modelling from 278.2 to 318.2K
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
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) https://doi.org/10.1021/ie049867m
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
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
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
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
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
Supercritical Fluids as Solvents and Reaction Media
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
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
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
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
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