| Vapour–liquid equilibria in the carbon dioxide–water system, measurement and modelling from 278.2 to 318.2 K A Valtz, A Chapoy, C Coquelet, P Paricaud, D Richon Fluid phase equilibria 226, 333-344, 2004 | 455 | 2004 |
| Measurements and predictive models of high-pressure H2 solubility in brine (H2O+ NaCl) for underground hydrogen storage application S Chabab, P Théveneau, C Coquelet, J Corvisier, P Paricaud International Journal of Hydrogen Energy 45 (56), 32206-32220, 2020 | 135 | 2020 |
| Solubility measurement and modeling of water in the gas phase of the methane/water binary system at temperatures from 283.08 to 318.12 K and pressures up to 34.5 MPa A Chapoy, C Coquelet, D Richon Fluid phase equilibria 214 (1), 101-117, 2003 | 122 | 2003 |
| Development of a new alpha function for the Peng–Robinson equation of state: comparative study of alpha function models for pure gases (natural gas components) and water-gas … C Coquelet, A Chapoy, D Richon International journal of thermophysics 25 (1), 133-158, 2004 | 119 | 2004 |
| Effect of impurities on thermophysical properties and phase behaviour of a CO2-rich system in CCS A Chapoy, M Nazeri, M Kapateh, R Burgass, C Coquelet, B Tohidi International Journal of Greenhouse Gas Control 19, 92-100, 2013 | 109 | 2013 |
| Developments and applications in solubility E Wilhelm, A van Hook, U Domanska-Zelazna, RPT Tomkins, D Richon, ... Royal Society of Chemistry, 2007 | 99 | 2007 |
| Experimental measurements and correlation of vapor–liquid equilibrium and critical data for the CO2+ R1234yf and CO2+ R1234ze (E) binary mixtures N Juntarachat, A Valtz, C Coquelet, R Privat, JN Jaubert International Journal of Refrigeration 47, 141-152, 2014 | 98 | 2014 |
| Investigation of a two stage Rankine cycle for electric power plants B Liu, P Rivière, C Coquelet, R Gicquel, F David Applied Energy 100, 285-294, 2012 | 95 | 2012 |
| Comparative study of vapour-liquid equilibrium and density modelling of mixtures related to carbon capture and storage with the SRK, PR, PC-SAFT and SAFT-VR Mie equations of … AG Perez, C Coquelet, P Paricaud, A Chapoy Fluid Phase Equilibria 440, 19-35, 2017 | 75 | 2017 |
| Corrigendum to “Revised solubility data and modeling of water in the gas phase of the methane/water binary system at temperatures from 283.08 to 318.12 K and pressures up to 34 … A Chapoy, C Coquelet, D Richon Fluid Phase Equilibria 230 (1-2), 210-214, 2005 | 73 | 2005 |
| 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, D Richon Fluid phase equilibria 202 (1), 29-47, 2002 | 72 | 2002 |
| Solubility of hydrogen in methanol at temperatures from 248.41 to 308.20 K C Descamps, C Coquelet, C Bouallou, D Richon Thermochimica acta 430 (1-2), 1-7, 2005 | 70 | 2005 |
| New solubility data of hydrocarbons in water and modeling concerning vapor− liquid− liquid binary systems S Mokraoui, C Coquelet, A Valtz, PE Hegel, D Richon Industrial & engineering chemistry research 46 (26), 9257-9262, 2007 | 68 | 2007 |
| Solubilities of carbon dioxide and oxygen in the ionic liquids methyl trioctyl ammonium bis (trifluoromethylsulfonyl) imide, 1-butyl-3-methyl imidazolium bis … I Bahadur, K Osman, C Coquelet, P Naidoo, D Ramjugernath The Journal of Physical Chemistry B 119 (4), 1503-1514, 2015 | 64 | 2015 |
| Isothermal P, x, y data for the argon+ carbon dioxide system at six temperatures from 233.32 to 299.21 K and pressures up to 14 MPa C Coquelet, A Valtz, F Dieu, D Richon, P Arpentinier, F Lockwood Fluid phase equilibria 273 (1-2), 38-43, 2008 | 63 | 2008 |
| Solubility of hydrocarbons in water: Experimental measurements and modeling using a group contribution with association equation of state (GCA-EoS) S Pereda, JA Awan, AH Mohammadi, A Valtz, C Coquelet, EA Brignole, ... Fluid Phase Equilibria 275 (1), 52-59, 2009 | 62 | 2009 |
| 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 C Coquelet, A Chareton, A Valtz, A Baba-Ahmed, D Richon Journal of Chemical & Engineering Data 48 (2), 317-323, 2003 | 59 | 2003 |
| Vapour–liquid equilibrium data for the hydrogen sulphide (H2S)+ carbon dioxide (CO2) system at temperatures from 258 to 313 K A Chapoy, C Coquelet, H Liu, A Valtz, B Tohidi Fluid Phase Equilibria 356, 223-228, 2013 | 58 | 2013 |
| 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, D Richon Fluid phase equilibria 207 (1-2), 53-67, 2003 | 58 | 2003 |
| Determination of critical properties of pure and multi-component mixtures using a “dynamic–synthetic” apparatus CB Soo, P Théveneau, C Coquelet, D Ramjugernath, D Richon The Journal of Supercritical Fluids 55 (2), 545-553, 2010 | 57 | 2010 |
Alain VALTZMines Paristech在 mines-paristech.fr 的电子邮件经过验证
