Liste non exhaustive des publications scientifiques faisant référence au ROLSITM™ :
Plaquette de présentation
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Exemples de clients et d'applications utilisant le ROLSITM
Contacts techniques :
Pascal Théveneau : +33 1 64 69 49 80
Christophe Coquelet : +33 1 64 69 49 62
S. Laugier, D. Richon
New apparatus to perform fast determinations of mixture vapor-liquid equilibria up to 10 MPa and 423 K.
Rev. Sci. Instrum., 57, 469 (1986)
D. Richon, S. Laugier, H. Renon
High pressure vapor-liquid equilibria for binary mixtures containing N2, CO2, H2S, and an aromatic hydrocarbon or propycyclohexane in the range 313-473 K.
J. Chem. Eng. data, 37, 264-268, (1992)
S. Laugier, D. Richon, H. Renon
Ethylene + olefine binary systems : Vapor-liquid equilibrium experimental data and modeling.
J. Chem. Eng. data, 39, 388-391, (1994)
S. Laugier, D. Richon
Vapor-liquid equilibria for hydrogen sulfide + hexane, + cyclohexane, + benzene, + pentadecane, and + (hexane + pentadecane).
J. Chem. Eng. Data, 40(1), 153-159, (1995)
Vapor-liquid equilibria for volatile-sulfur-containing systems. Propane-sulfur-containing systems and
ethane-sulfur-containing systems.
GPA Research Report (RR-135) , Tulsa, Oklahoma, Project 876, (1995)
S. Laugier, D. Richon
High pressure vapor-liquid equilibria for ethylene + 4-methyl-1-pentene and 1-butene + 1-hexene
J. Chem. Eng. Data, 41, 282-284, (1996)
S. Laugier, D. Richon
High Pressure Vapor-Liquid-Equilibria of Two Binary Systems : Carbon Dioxide + Cyclohexanol and Carbon dioxide + Cyclohexanone
J. Chem. Eng. Data, 42, 155-159, (1997)
A. Baba-Ahmed, D. Richon
Isothermal vapor-liquid equilibria for the partially miscible ethanenitrile +propane system at temperatures from 303.15 K to 373.15K and pressures to 4 MPa
The International Electronic Journal of Physico-Chemical Data. 3, 167-172, (1997)
S. Benmansour, D. Richon
Vapor-liquid equilibria and densities for difluoromethane (R-32) + pentafluoroethane (R-125) binary mixtures at temperatures between 253 K and 333 K and pressures up to 20 MPa (26375 data points).
The International Electronic Journal of Physico-Chemical Data., 5, 9-18, (1999).
S. Benmansour, D. Richon
Vapor-liquid equilibria and densities of the binary refrigerant mixture composed of difluoromethane (R-32) and 1,1,1,2-tetrafluoroethane (R-134a) at temperatures between 253 K and 333 K and pressures up to 20 MPa (19413 data points). Experimental data and correlations.
The International Electronic Journal of Physico-Chemical Data., 5, 55-64, (1999).
A. Baba-Ahmed, P. Guilbot, D. Richon
New equipment using a static-analytic method for the study of vapour-liquid equilibria at temperatures down to 77 K.
Fluid Phase Equilib. 166, 225-236, (1999).
A. Valtz, H. Legendre, P. Guilbot, D. Richon
L’échantillonneur-injecteur ROLSI (Rapid On-Line Sampler-Injector), un nouvel outil de micro-prélèvement pour l’analyse en ligne dans un large domaine de pressions et températures.
Spectra Analyse, 208 (mai-juin), 30-33, (1999).
L. A. Galicia-Luna, A. Ortega-Rodriguez, D. Richon
New Apparatus for the Fast Determination of High-Pressure Vapor-Liquid Equilibria of Mixtures and of Accurate Critical Pressures.
J. Chem. Eng. Data, 45, 265-271, (2000).
P. Guilbot, A. Valtz, H. Legendre, D. Richon
Rapid On-Line Sampler-Injector –A Reliable Tool for HT-HP Sampling and On-Line.
Analysis . Analusis, 28, 426-431, (2000).
C. Valencia – Duran, A. Valtz, L.A. Galicia-Luna, D. Richon
Isothermal Vapor-liquid equilibria of the Carbon dioxide (CO2) N,N-Dimethylformamide (DMF) system at temperatures from 293.15 to 338.05 K and Pressures up to 12 Mpa.
J. Chem. Eng. Data 46 (6) 1589-1592 (2001).
C. Duran-Valencia, G. Pointurier, A. Valtz, P. Guilbot and D. Richon
Vapor – Liquid Equilibrium (VLE) Data for the Carbon Dioxide (CO2) + 1,1,1,2-Tetrafluoroethane (R134a) System at Temperatures from 252.95 K to 292.95 K and Pressures up to 2 MPa.
J. Chem. Eng. Data, 47, 59-61 (2002).
V. De Stefani, A. Baba-Ahmed, A. Valtz, D. Meneses, D. Richon
Solubility Measurements for Carbon Dioxide and Nitrous Oxide in Liquid Oxygen at Temperatures down to 90 K.
Fluid Phase Equilib. 200, 19-30, (2002)
C. Duran-Valencia, L.A. Galicia-Luna, D. Richon
Phase equilibrium data for the binary system N,N-dimethylformamide + ethylene and + ethane at several temperatures up to 18 MPa.
Fluid Phase. Equilib. 203, 295-307, (2002).
A. Valtz, C. Coquelet, A. Baba-Ahmed, D. Richon
Vapor-liquid equilibrium data for the propane + 1,1,1,2,3,3,3-heptafluoropropane (R227ea) system at temperatures from 293.16 K to 353.18 K and pressures up to 3.4 MPa.
Fluid Phase Equilib. 202, 29-47, (2002).
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.
Fluid Phase Equilib. 207, 53-67, (2003).
C. Coquelet, A. Chareton, A. Valtz, A. Baba-Ahmed and D. Richon
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.
J. Chem. Eng. Data, 48, 317-323, (2003).
C. Coquelet, D. Nguyen Hong, A. Chareton, A. Baba-Ahmed and D. Richon
Vapor-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.
International Journal of Refrigeration, 26, 559-565, (2003).
V. De Stefani, A. Baba-Ahmed, D. Richon
Experimental determination of carbon dioxide and nitrous oxide co-solubility in liquid oxygen.
Fluid Phase Equilib. 207, 131-142, (2003).
A. Valtz, M. Hegarty, D. Richon
Experimental determination of the solubility of aromatic compounds in aqueous solutions of various amines.
Fluid Phase Equilib. 210, 257-276, (2003).
A. Valtz , C. Coquelet and D. Richon
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. Representation of the critical point and azeotrope temperature dependence.
Fluid Phase Equilib. 220, 77-83 (2004).
C. Coquelet, A. Chareton, D. Richon
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 328.35 K.
Fluid Phase Equilib. 218, 209-214 (2004).
F. Rivollet, A. Chapoy, C. Coquelet, D. Richon
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 .
Fluid Phase Equilib. 218, 95-101, (2004).
A. Valtz, C. Coquelet, D. Richon.
Vapor-Liquid Equilibrium Data for the Sulfur Dioxide (SO2) + Difluoromethane (R32) System at Temperatures from 288.07 to 403.16 K and at Pressures up to 7.31 MPa.
Int. J. Thermophys. 25, 1695-1711, (2004).
A. Chapoy, S. Mokraoui, A. Valtz, D. Richon , A. H. Mohammadi, B. Tohidi.
Solubility Measuremend and Modeling for the System Propane-Water from 277.62 to 368.16K
Fluid Phase Equilib. 226, 213,220, (2004)
A. H. Mohammadi, A. Chapoy, B. Tohidi, D. Richon.
Measurements and thermodynamic modelling of Vapor – Liquid Equilibria in Ethane –Water Systems from 274.26 to 343.08 K.
Ind. Eng. Chem. Research, 43, 5418-5424, (2004).
A. Valtz, A. Chapoy, C. Coquelet, P. Paricaud, D. Richon.
Vapour - Liquid Equilibria in the Carbon Dioxide – Water System, Measurement and Modelling from 278.2 to 318.2 K.
Fluid Phase Equilib.226, 333-344, (2004).
A. H. Mohammadi, A. Chapoy, D. Richon, B. Tohidi.
Experimental Measurement and Thermodynamic Modeling of Water Content in Methane and Ethane Systems
Ind. Eng. Chem. Res. 43, 7137-7147, (2004).
C. DESCAMPS, C. COQUELET, C. BOUALLOU, D. RICHON.
Solubility of hydrogen in methanol at temperatures from 248.41 to 308.20 K
Thermochimica Acta, 430/1-2, 1-7, (2005).
A. VALTZ, C. COQUELET, D. RICHON.
Volumetric properties of the monoethanolamine-methanol mixtures at atmospheric pressure from 283.15 to 353.15 K
Thermochimica Acta., 428, 185-191. (2005).
A. VALTZ, L. GICQUEL, C. COQUELET, D. RICHON.
Vapour – liquide equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15 K and pressures up to about 3 MPa..
Fluid Phase Equilib., 230, 184-191, (2005).
C. COQUELET, A. VALTZ, D. RICHON.
Vapor -liquid equilibrium data for the difluoromethane (R32)-dimethyl ether (RE170) system at temperatures from 283.03 to 363.21 K and pressures up to 5.5 MPa.
Fuid Phase Equilib., 232, 9-44-49, (2005).