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Author:Richon, D.

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46 matching references were found.

Valtz, A.; Coquelet, C.; Baba-Ahmed, A.; Richon, D., 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, Fluid Phase Equilibria, 2002, 202, 1, 29-47, https://doi.org/10.1016/S0378-3812(02)00056-0 . [all data]

Noll, O.; Valtz, A.; Richon, D.; Getachew-Sawaya, T.; Mokbel, I.; Jose, J., Vapor pressures and liquid densities of N-methylethanolamine, diethanolamine, and N-methyldiethanolamine, ELDATA: Int. Electron. J. Phys. Chem. Data, 1998, 4, 3, 105. [all data]

Bouchot, C.; Richon, D., Gas, liquid, and saturated vapor-liquid densities and vapor pressures of difluoromethane (R-32) and octafluoropropane (R-218) at temperatures from 253 K to 333 K and pressure up to 14.5 MPa, Int. Electron. J. Phys.-Chem. Data, 1997, 3, 1-16. [all data]

Richon, D., New experimental developments for phase equilibrium measurements, Fluid Phase Equilib., 1996, 116, 421-8. [all data]

Laugier, S.; Richon, D., High-Pressure Vapor-Liquid Equilibria for Ethylene + 4-Methyl-1-pentene and 1-Butene + 1-Hexene, J. Chem. Eng. Data, 1996, 41, 282-4. [all data]

Laugier, S.; Richon, D., Vapor-Liquid Equilibria for Hydrogen Sulfide + Hexane, + Cyclohexane, + Benzene, + Pentadecane, and + (Hexane + Pentadecane), J. Chem. Eng. Data, 1995, 40, 153-9. [all data]

Luna-Galicia, L.A.; Richon, D.; Renon, H., J. Chem. Eng. Data, 1994, 39, 424-431. [all data]

Laugier, S.; Richon, D.; Renon, H., Bubble curves and saturated liquid molar volumes for chlorofluorohydrocarbon-hydrocarbon mixtures. Experimental data and modeling, J. Chem. Eng. Data, 1994, 39, 166-71. [all data]

Laugier, S.; Richon, D.; Renon, H., Ethylene + Olefin Binary Systems: Vapor-Liquid Equilibrium Experimental Data and Modeling, J. Chem. Eng. Data, 1994, 39, 388-91. [all data]

Laugier, S.; Richon, D.; Renon, H., Chlorofluorohydrocarbon-alcohol mixtures: bubble pressures and saturated liquid molar volumes (experimental data and modeling), Chem. Eng. Sci., 1994, 49, 2135-44. [all data]

Galicia-Luna, L.A.; Richon, D.; Renon, H., New Loading Technique for a Vibrating Tube Densimeter and Measdurements of Liquid Densities up to 39.5 MPa for Binary and Ternary Mixtures of the Carbon Dioxide-Methanol-Propane Systems, J. Chem. Eng. Data, 1994, 39, 424-31. [all data]

Bouchot, C.; Richon, D., Simultaneous measurements of phase equilibrium and volumetric properties by vibrating tube densimetry: Apparatus and results involving HFC, Sci. Tech. Froid, 1994, No. 2, 517-24. [all data]

Richon, D.; Laugier, S.; Renon, H., High-pressure vapor-liquid equilibrium data for binary mixtures containing molecular nitrogen, carbon dioxide, hydrogen sulfide and an aromatic hydrocarbon or propylcyclohexane in the range 313-473 K, J. Chem. Eng. Data, 1992, 37, 264-8. [all data]

Richon, D.; Laugier, S.; Renon, H., High-Pressure Vapor-Liquid Equilibria for Binary Mixtures Containing A Light Paraffin and an Aromatic COmpound or a Napthene in the Range 313-473K K, J. Chem. Eng. Data, 1991, 36, 104. [all data]

Laugier, S.; Richon, D.; Renon, H., Simultaneous determination of vapor-liquid equilibria and volumetri properties of ternary systems with a new experimental apparatus, Fluid Phase Equilib., 1990, 54, 19. [all data]

Chareton, A.; Valtz, A.; Laugier, S.; Richon, D.; Renon, H., Bubble Pressures and Saturated Liquid Molar Volumes of Binary and Ternary Refrigerant Mixtures, J. Chem. Eng. Data, 1990, 35, 162. [all data]

Renon, H.; Laugier, S.; Schwartzentruber, J.; Richon, D., New determinations of high pressure vapor-liquid equilibria in binary systems containing n-propylbenzene with nitrogen or carbon dioxide consistent with the Prausnitz-Keeler test, Fluid Phase Equilib., 1989, 51, 285. [all data]

Valtz, A.; Laugier, S.; Richon, D., Bubble Pressures and Saturated Liquid Molar Volumes of Trifluoro- and Modelization, J. Chem. Eng. Data, 1987, 32, 397. [all data]

Garcia-Sanchez, F.; Laugier, S.; Richon, D., Vapor-liquid equilibrium data for the methane-dimethylether and methane-diethylether systems between 282 and 344 K, J. Chem. Eng. Data, 1987, 32, 211. [all data]

Brignole, E.A.; Chareton, A.; Laugier, S.; Richon, D., Vapor-liquid equilibrium data for the methane-methylal binary mixtur between 273 and 432 K up to the critical region, J. Chem. Eng. Data, 1987, 32, 215. [all data]

Sorrentino, F.; Voilley, A.; Richon, D., AIChE J., 1986, 32, 1988. [all data]

Laugier, S.; Richon, D.; Renon, H., Representation of hydrogen-hydrocarbon vapor-liquid equilibria and saturated densities at high pressures and temperatures, Chem. Eng. Sci., 1986, 41, 2407. [all data]

Laugier, S.; Richon, D., New apparatus to perform fast determinations of mixture vapor-liquid equilibria up to 10 MPa and 423 K, Rev. Sci. Instrum., 1986, 57, 469. [all data]

Galivel-Solastiouk, F.; Laugier, S.; Richon, D., Vapor-liquid equilibrium data for the propane-methanol and propane-methanol-carbon dioxide system, Fluid Phase Equilib., 1986, 28, 73. [all data]

Richon, D.; Sorrentino, F.; Voilley, A., Ind. Eng. Chem. Process Des. Dev., 1985, 24, 1160. [all data]

Guillevic, J.L.; Richon, D.; Renon, H., Vapor-liquid equilibrium data for the binary system water-ammonia at 403.1, 453.1, and 503.1 K up to 7.0 MPa, J. Chem. Eng. Data, 1985, 30, 332. [all data]

Dzialoszynski, L.; Richon, D.; Renon, H., Generalized semi-empirical non cubic equation of state for the representation of properties of pure substances, Chem. Eng. Commun., 1985, 39, 23. [all data]

Richon, D.; Laugier, S.; Gravier, J.F., , 1984. [all data]

Lebert, A.; Richon, D., J. Agric. Food CHem., 1984, 32, 1156. [all data]

Fontalba, F.; Richon, D.; Renon, H., Simultaneous determination of vapor-liquid equilibria and saturated densities up to 45 MPa and 433 K, Rev. Sci. Instrum., 1984, 55, 944-51. [all data]

Rousseaux, P.; Richon, D.; Renon, H., A Static Method for Determination of Vapor-Liquid Equilibriums and Sat. Liq. Molar Volumes at High Pressures and Temperatures Using a New Variable-Volume Cell, Fluid Phase Equilib., 1983, 11, 153-68. [all data]

Rousseaux, P.; Richon, D.; Renon, H., Volumetric Properties of n-Dodecane up to 423.1 K and 30.58 MPa, Fluid Phase Equilib., 1983, 11, 169-77. [all data]

Legret, D.; Desteve, J.; Richon, D.; Renon, H., Vapor-liquid equilibrium constants at infinite dilution deter- mined by a gas stripping method. ethane, propane, n-butane, n- pentane in the methane + n-decane system., AIChE J., 1983, 29, 137-144. [all data]

Guillevic, J.L.; Richon, D.; Renon, H., Vapor-Liquid Equilibrium Measurements up to 558 K and 7 MPa: A New Apparatus, Ind. Eng. Chem. Fundam., 1983, 22, 495. [all data]

Houzelle, C.; Legret, D.; Richon, D.; Renon, H., Vapor-liquid equilibria of corrosive components using a dynamic method: a new flow apparatus., Fluid Phase Equilib., 1983, 11, 179-85. [all data]

Meskel-Lesavre, M.; Richon, D.; Renon, H., Bubble Pressures and Saturated Liquid Molar Volumes of Trichloro fluoromethane-Chlorodifluoromethane Mixtures. Representation of Refrigerant-Mixtures Vapor-Liquid Equilibrium Data by a Modified F, Fluid Phase Equilib., 1982, 8, 37. [all data]

Meskel-Lesavre, M.; Richon, D.; Renon, H., Bubble Pressures and Liquid Molar Volumes of the System Chlorotrifluoromethan-1,1,2-trichlorotrifluoroethane, J. Chem. Eng. Data, 1982, 27, 160. [all data]

Legret, D.; Richon, D.; Renon, H., Vapor-liquid equilibria of methane + benzene, methane + methylbenzene ( toluene), methane + 1,3-dimethylbenzene (m-xylene), and methane + 1,3,5- trimethylbenzene (mesitylene) at 313.2 k up to the cri, J. Chem. Eng. Data, 1982, 27, 165-169. [all data]

Meskel-Lesavre, M.; Richon, D.; Renon, H., New variable volume cell for determining vapor-liquid equilibria and saturated liquid molar volumes by the static method., Ind. Eng. Chem. Fundam., 1981, 20, 284-9. [all data]

Legret, D.; Richon, D.; Renon, H., Vapor-liquid equilibria up to 100 mpa: a new apparatus, AIChE J., 1981, 27, 203-207. [all data]

Richon, D.; Antoine, P.; Renon, H., Infinite dilution activity coefficients of linear and branched alkanes from c(1) to c(9) in n-hexadecane by inert gas stripping, Ind. Eng. Chem. Process Des. Dev., 1980, 19, 144. [all data]

Richon, D.; Renon, H., Infinite Dilution Henry's Law Constants of Light Hydrocarbons in n-Hexadecane, n-Octadecane, and 2,2,4,4,6,8,8-Heptamethylnone by Inert Gas Stripping, J. Chem. Eng. Data, 1980, 25, 59-60. [all data]

Laugier, S.; Richon, D.; Renon, H., Vapor-Liquid Equilibria of Hydrogen-2,2,4-Trimethylpentane and Hydrogen- Toluene Systems at High Pressures and Temperature, J. Chem. Eng. Data, 1980, 25, 274. [all data]

Legret, D.; Richon, D.; Renon, H., Static still for measuring vapor-liquid equilibria up to 50 bar., Ind. Eng. Chem. Fundam., 1980, 19, 122-126. [all data]

Figuiere, P.; Hom, J.F.; Laugier, S.; Renon, H.; Richon, D.; Szwarc, H., Vapor-liquid equilibria up to 40,000 kpa and 400 c: a new static method, AIChE J., 1980, 26, 872. [all data]

Richon, D.; Viallard, A., Water systems + ester: I calorimetric studies of water systems + alkyl acetate, Can. J. Chem., 1976, 54, 2584. [all data]