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Home All issues Volume 55 / No 6 (November-December 2000) Oil & Gas Science and Technology - Rev. IFP, 55 6 (2000) 617-637 References
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Oil & Gas Science and Technology - Rev. IFP
Volume 55, Number 6, November-December 2000
Page(s) 617 - 637
DOI https://doi.org/10.2516/ogst:2000047
Published online 01 December 2006
  • Abdoul, W., Rauzy, E. et Péneloux, A. (1991) Group- Contribution Equation of State for Correlating and Predicting Thermodynamic Properties of Weakly Polar and Non-Associating Mixtures; Binary and Multicomponent Systems. Fluid Phase Eq., 68, 47-102. [Google Scholar]
  • Anderko, A. (1992) Modeling Phase Equilibria using an Equation of State Incorporating Association. Fluid Phase Eq., 75, 89-103. [CrossRef] [Google Scholar]
  • Asano, K.,Nakahara, T. et Kobayashi, R. (1971) K-Values at Essentially Infinite Dilution for Carbon Dioxide and Hydrogen Sulfide in the Methane-n-octane System at Low Temperatures and Elevated Pressures. J. Chem. Eng. Data, 16, 1, 16-18. [CrossRef] [Google Scholar]
  • Balley, D.M., Chung, H.L., Holste, J.C., Hall, K.R., Eubank, P.T. et Marsh, K.M. (1987) Thermodynamic Properties of Pure Hydrogen Sulfide and Mixtures Containing Hydrogen Sulfide with Methane, Carbon Dioxide, Methylcyclohexane and Toluene. Rapport GPA, RR107. [Google Scholar]
  • Barreau, A.,Vidal, J. et Mogensen, G. (1993) Isobaric Heat Capacity Calculation of Light Hydrocarbons by Means of Equations of State. Revue de l’Institut français du pétrole, 48, 5, 515-525. [Google Scholar]
  • Benaouda, A., Fürst, W. et Watansiri, S. (1995) Représentation de la solubilité des gaz à haute pression à l’aide d’une équation d’état applicable aux solutions d’électrolytes. Récents progrès en génie des procédés.. [Google Scholar]
  • Brelvi, S.W. et O’Connell, J.P. (1972) Corresponding States Correlations for Liquid Compressibility and Partial Molar Volumes of Gases at Infinite Dilution in Liquids. AIChE J., 18, 6, 1239-1243. [CrossRef] [Google Scholar]
  • Carrier, H. (1996) Contribution à l’étude thermodynamique de solutions d’électrolytes sous haute pression, haute température. Thèse, université de Pau et des Pays de l’Adour. [Google Scholar]
  • Carroll, J.J. (1991) What is Henry’s Law? Chem. Eng. Progress, 87, 9, 48-52. [Google Scholar]
  • Carroll, J.J. (1992) Use Henry’s Law for Multicomponent Mixtures. Chem. Eng. Progress, 88, 8, 53-58. [Google Scholar]
  • Carroll, J.J. et Mather, A.E. (1995) A Generalized Correlation for the Peng-Robinson Interaction Coefficients for Paraffin-Hydrogen Sulfide Binary Systems. Fluid Phase Eq., 105, 221-228. [Google Scholar]
  • Chandler, K.,Pouillot, F.L.L. et Eckert, C. (1996) Phase Equilibria of Alkanes in Natural Gas Systems. Alcanes in Carbon Dioxide. J. Chem. Eng. Data, 41, 6-10. [CrossRef] [Google Scholar]
  • Chappelaer, P.S., Asano, K., Nakahara, T. et Kobayashi, R. (1969) Analysis and Recommendations for K-Values for Carbon Dioxide and Hydrogen Sulfide at Infinite Dilution in the Methane-n-octane System. Proc. of the 49th Annual Convention of the National Gas Processor’s Association. [Google Scholar]
  • Chen, C.C. et Evans, L.B. (1986) A Local Composition Model for the Excess Gibbs Energy of Aqueous Electrolyte Systems. AIChE J., 32, 444-454. [CrossRef] [Google Scholar]
  • Davison, R., Mayder, A., Hladiuk, D. et Jarrell, J.L. (1996) Zama Acid Gas Disposal/Miscible Flood Implementation and Results. 47th Annual Technical Meeting of The Petroleum Society, Calgary, Alberta, Canada. [Google Scholar]
  • Debye, P. et Hückel, E. (1923a) Zur Theorie der Elektrolyte I : Gefrierpunktserniedrigung und verwandte Erscheinungen. Phys. Z., 24, 9, 185-207. [Google Scholar]
  • Debye, P. et Hückel, E. (1923b) Zur Theorie der Elektrolyte II : das Grensgesetz für die elektrische Leitf㧩gkeit. Phys. Z., 24, 15, 305-325. [Google Scholar]
  • D襯ntaines, A.D. (1997) Étude bibliographique sur les mélanges H2S-CO2 et CH4-H2S-CO2. Note technique ADD/ADD, 71. [Google Scholar]
  • De Hemptinne, J.C. (1994) Comparaison de différents modèles de calcul pour la solubilité des gaz (CH4, CO2, et H2S) dans l’eau en présence de sels. Rapport IFP, réf 41439. [Google Scholar]
  • De Hemptinne, J.C. (1997) Étude de modèles permettant de décrire la saturation en eau d’un gaz. Rapport ARTEP, réf IFP 43594. [Google Scholar]
  • De Hemptinne, J.C. et Ungerer, P. (1995) Accuracy of the Volumetric Predictions of some Important Equations of State, Including a Modified Version of the Lee et Kesler Method. Fluid Phase Eq., 106, 81-109. [Google Scholar]
  • De Hemptinne, J.C., Brunella, I., Moracchini, G. et Zhou, H. (1996) Influence of Water on the Estimate of Gas in Place. Annual Technical Conference and Exhibition, octobre 1996, Rapport ARTEP, SPE 36669. [Google Scholar]
  • De Hemptinne, J.C., Duchet-Suchaux, P., Zhou, H., Rauzy, E., Ye, S. et Dordain, L. (2000a) Propriétés des systèmes eau hydrocarbures : rapport de synthèse. Rapport IFP-ARTEP, réf. 52982. [Google Scholar]
  • De Hemptinne, J.C., Dhima, A. et Shakir, S. (2000b) The Henry Constant for 20 Hydrocarbons, CO2 and H2S in Water as a Function of Pressure and Temperature. J. Chem. Eng. Data (submitted). [Google Scholar]
  • Dhima, A., de Hemptinne, J.C. et Moracchini, G. (1998) Solubility of Light Hydrocarbons and their Mixtures in Pure Water under High Pressure. Fluid Phase Eq., 145, 129-150. [CrossRef] [Google Scholar]
  • Dhima, A., de Hemptinne, J.C. et Jose, J. (1999) Solubility of Hydrocarbons in Water under High Pressure. Ind. Eng. Chem. Res., 38, 3144-3161. [CrossRef] [Google Scholar]
  • DIPPR (1985) Data Compilation of Pure Compound Properties Version 8.0. NIST Standard Reference Database 11, AIChE. [Google Scholar]
  • Duarte-Garza, H., Hwang, C.A., Kidd, M.W., Lau, W.W.R., M�r, D., Eubank, P.T., Holste, J.C. et Hall, K.R. (1995) Thermodynamic Properties of CO2 + C2H6 Mixtures. Rapport GPA, RR139. [Google Scholar]
  • Eakin, B.E. et De Vaney, W.E. (1974) Vapor-Liquid Equilibria in Hydrogen-Hydrogen Sulfide-C9 Hydrocarbon Systems. AIChE Symposium Series, 70, 140, 80-90. [Google Scholar]
  • Economou, I.G. et Donohue, M.D. (1992) Equation of State with Multiple Associating Sites for Water and Water-Hydrocarbon Mixtures. Ind. Eng. Chem. Res., 31, 2388-2394. [CrossRef] [Google Scholar]
  • Economou, I.G. et Tsonopoulos, C. (1997) Associating Models and Mixing Rules in Equations of State for Water-Hydrocarbon Mixtures. Chem. Eng. Sci., 52, 4, 511-525. [CrossRef] [Google Scholar]
  • Feng, G.X. et Mather, A.E. (1992) Solubility of Hydrogen Sulfide in n-eicosane at Elevated Pressure. J. Chem. Eng. Data, 37, 412-413. [CrossRef] [Google Scholar]
  • Feng, G.X. et Mather, A.E. (1993) Solubility of H2S in ndodecane. Fluid Phase Eq., 87, 341-146. [CrossRef] [Google Scholar]
  • Fenghour, A.,Wakeham, W.A. et Watson, J.T.R. (1996) Densities of (Water + Carbon Dioxide) in the Temperature Range 415 K to 700 K and Pressures up to 35 MPa. J. Chem. Thermodynamics, 28, 433-446. [CrossRef] [Google Scholar]
  • Fogg, P.G.T. et Gerrard, W. (1991) Solubility of Gases in Liquids, J. Wiley & Sons, Chichester. [Google Scholar]
  • F�W. et Renon, H. (1993) Representation of Excess Properties of Electrolyte Solutions using a New Equation of State. AIChE J., 39, 2, 335-343. [CrossRef] [Google Scholar]
  • Gallagher, J.S.Crovetto, R. et Levelt-Sengers, J.M.H. (1993) The Thermodynamic Behavior of the CO2-H2O System from 400 K to 1000 K, up to 100 MPa and 30% Mole Fraction of CO2. J. Phys. Chem. Ref. Data, 22, 2, 431-449. [CrossRef] [Google Scholar]
  • Gammon, B.E. et Marsh, K.N. (1995) Thermodynamic Properties of CO2 + H2S Mixtures. Rapport GPA, RR141. [Google Scholar]
  • Gillespie, C. et Wilson, G.M. (1982) Vapor-Liquid and Liquid- Liquid Equilibria: Water-Methane; Water-Carbon Dioxide; Water-Hydrogen Sulfide; Water-n-pentane; Water-Methanen- pentane. Rapport GPA, RR48, Provo, UT. [Google Scholar]
  • GPA (1994) Engineering Data Book, 10e 袮, Gas Processors Suppliers Association, 2. [Google Scholar]
  • Guggenheim, E.A. (1935) The Specific Thermodynamic Properties of Aqueous Solutions of Strong Electrolytes. Phil. Mag., 19, 588. [CrossRef] [Google Scholar]
  • Harvey, A.H. (1996) Semiempirical Correlation for Henry’s Constants over Large Temperature Ranges. AICHE J., 42, 1491-1494. [Google Scholar]
  • Harvey, A.H. et Levelt-Sengers, J.M.H. (1990) Correlation of Aqueous Henry’s Constants from 0°C to the Critical Point. AIChE J., 36, 4, 539-546. [CrossRef] [Google Scholar]
  • Hensel, W.E. et Massoth, F.E. (1964) Phase Equilibria for the Ternary System: CH4-CO2-H2S at Low Temperatures. J. Chem. Eng. Data, 9, 3. [CrossRef] [Google Scholar]
  • Hwang, C.A., Duarte-Gaza, H., Eubank, P.T., Holste, J.C. et Hall, K.R. (1995) Thermodynamic Properties of CO2 + CH4 Mixtures. Rapport GPA, RR138. [Google Scholar]
  • Ikonomou, G.D. et Donohue, M.D. (1986) Thermodynamics of Hydrogen-Bonded Molecules: The Associated Perturbed Anisotropic Chain Theory. AIChE J., 32, 10, 1716-1725. [CrossRef] [Google Scholar]
  • Ikonomou, G.D. et Donohue, M.D. (1987) COMPACT: A Simple Equation of State for Associated Molecules. Fluid Phase Eq., 33, 61-90. [CrossRef] [Google Scholar]
  • Kato, K.,Nagahama, K. et Hirata, M. (1981) Generalized Interaction Parameters for the Peng-Robinson Equation of State: Carbon Dioxide-n-paraffin Binary Systems. Fluid Phase Eq., 7, 219-231. [CrossRef] [Google Scholar]
  • Kikic, I.,Fermeglia, M. et Rasmussen, P. (1991) UNIFAC Prediction of Vapor-Liquid Equilibria in Mixed Solvent-Salt Systems. Chem. Eng. Sci., 46, 11, 2775-2780. [CrossRef] [Google Scholar]
  • King, M.B. et Al-Najjar, H. (1977) The Solubilities of Carbon Dioxide, Hydrogen Sulphide and Propane in some Normal Alkane Solvents—I: Experimental Determinations in the Range 15-70°C and Comparison with Ideal Solution Values. Chem. Eng. Sci., 33, 1241-1246. [CrossRef] [Google Scholar]
  • Kiran, E.,Pöhler, H. et Xiong, Y. (1996) Volumetric Properties of Pentane + Carbon Dioxide at High Pressures. J. Chem. Eng. Data, 41, 158-165. [CrossRef] [Google Scholar]
  • Kohn, A. et Kurata, F. (1959) Volumetric Behavior of the Methane-Hydrogen Sulfide System at Low Temperatures and High Pressures. J. Chem. Eng. Data, 4, 1, 33-36. [CrossRef] [Google Scholar]
  • Leder, F. et Irani, C.A. (1975) Upper Critical Solution Temperatures in Carbon Dioxide-Hydrocarbon Systems. J. Chem. Eng. Data, 20, 3, 323-327 [CrossRef] [Google Scholar]
  • Lee, J.I. et Mather, A.E. (1977) Solubility of Hydrogen Sulfide in Water. Ber. Bunsen-Gesellschaft, 81, 10, 1020-1023. [Google Scholar]
  • Leu, A.D. et Robinson, D.B. (1989) Equilibrium Phase Properties of the n-butane-Hydrogen Sulfide and Isobutane-Hydrogen Sulfide Binary Systems. J. Chem. Eng. Data, 34, 315-319. [CrossRef] [Google Scholar]
  • Li, J., Van der Beken, I.,Ye, S.,Carrier, H. et Xans, P. (1997) Prediction of the Solubility and Gas-Liquid Equilibria for Gas- Water and Light Hydrocarbon-Water Systems at High Temperatures and Pressures with a Group Contribution Equation of State. Fluid Phase Eq., 131, 107-118. [CrossRef] [Google Scholar]
  • Li, Q.,Gu, M.,Chen, W.,Zhou, X. et Guo, T. (1994) Détermination expérimentale et modélisation pour des modèles prédictifs du comportement de phases de gaz naturels riches en H2S. J. Chem. Eng. of Chinese Universities, 8, 3, 209-215 (trad. fran栩se). [Google Scholar]
  • Li, Y.K. et Nghiem, L.X. (1986) Phase Equilibria of Oil, Gas and Water/Brine Mixtures from a Cubic Equation of State and Henry’s Law. Can. J. Chem. Eng., 64, 486-496. [CrossRef] [Google Scholar]
  • Liphard, K.G. et Schneider, G.M. (1975) Phase Equilibria and Critical Phenomena in Fluid Mixtures of Carbon Dioxide + 2,6,10,15,19,23 Hexamethyl Tetracosane. J. Chem. Thermodynamics, 7, 805-814. [CrossRef] [Google Scholar]
  • Lown, D.A., Thirsk, H.R. et Wynne-Jones, L. (1968) Effect of Pressure on Ionization Equilibria in Water at 25°C. J. Sol. Chem., 2073-2080. [Google Scholar]
  • Lyckman, E.W.,Eckert, C.A. et Prausnitz, J.M. (1965) Generalized Reference Fugacities for Phase Equilibrium Thermodynamics. Chem. Eng. Sci., 20, 685-691. [CrossRef] [Google Scholar]
  • Macedo, E.,Skovborg, P. et Rasmussen, P. (1990) Calculation of Phase Equilibria for Solutions of Strong Electrolytes in Solvent- Water Mixtures. Chem. Eng. Sci., 45, 875-882. [CrossRef] [Google Scholar]
  • Mock, B.,Evans, L.B. et Chen, C.C. (1986) Thermodynamic Representation of Phase Equilibria of Mixed Solvent Electrolyte Systems. AIChE J., 32, 1655-1664. [CrossRef] [Google Scholar]
  • Morin, E. et Montel, F. (1996) Accurate Predictions for the Production of Vaporized Water. SPE Annual Technical Conference and Exhibition, SPE 30719. [Google Scholar]
  • Mundis, C.J., Yarborough, L. et Robinson, R.L. Jr (1977) Vaporization Equilibrium Ratios for CO2 and H2S in Paraffinic, Naphtenic and Aromatic Solvents. Ind. Eng. Chem. Process Des. Dev., 16, 2, 254-259. [Google Scholar]
  • Ng, H.J.,Robinson, D.B. et Leu, A.D. (1985) Critical Phenomena in a Mixture of Methane, Carbon Dioxide and Hydrogen Sulfide. Fluid Phase Eq., 19, 273. [CrossRef] [Google Scholar]
  • Ng, H.J. et Robinson, D.B. (1986) The Influence of Water and Carbon Dioxide on the Phase Behavior and Properties of a Condensate Fluid. 61st Annual Technical Conference and Exhibition, Nouvelle-Orléans, LA, octobre, SPE 15401. [Google Scholar]
  • Nicolaisen, H.,Rasmussen, P. et Sorensen, J.M. (1993) Correlation and Prediction of Mineral Solubilities in the Reciprocal Salt System (Na+, K+)(Cl–, SO4 – –)-H2O at 0-100°C. Chem. Eng. Sci., 48, 18, 3149-3158. [CrossRef] [Google Scholar]
  • Nighswander, J.A.,Kalogerakis, N. et Mehrotra, A.K. (1989) Solubilities of Carbon Dioxide in Water and 1 wt% NaCl Solution at Pressures up to 10 MPa and Temperatures from 80°C to 200°C. J. Chem. Eng. Data, 34, 355-360. [CrossRef] [Google Scholar]
  • Nishiumi, H.,Tsutomu, A. et Takeuchi, K. (1988) Generalization of the Binary Interaction Parameter of the Peng-Robinson Equation of State by Component Family. Fluid Phase Eq., 42, 43-62. [CrossRef] [Google Scholar]
  • O’Connell, J. et Prausnitz, J.M. (1964) Thermodynamics of Gas Solubility in Mixed Solvents. I&EC Fundamentals, 3, 4, 347-351. [CrossRef] [MathSciNet] [Google Scholar]
  • Ohgaki, K. et Katayama, T. (1977) Isothermal Vapor-Liquid Equilibrium Data for the Ethane-Carbon Dioxide System at High Pressures. Fluid Phase Eq., 1, 27-32. [CrossRef] [Google Scholar]
  • Olds, R.H.,Reamer, H.H.,Sage, B.H. et Lacey, W.N. (1949) Phase Equilibria in Hydrocarbon Systems: The n-butane-Carbon Dioxide System. Ind. Eng. Chem., 41, 3, 475-482. [CrossRef] [Google Scholar]
  • Owen, B.B. et Brinkley, S.R. (1941) Chem. Rev., 29, 461. [Google Scholar]
  • Paux, F. et Zhou, H. (1997) Field Case: Match of a 600 Bars Depletion and 40 Years of History in a Fractured Carbonate Sour Gas Field. SPE Annual Technical Conference and Exhibition, SPE 38909. [Google Scholar]
  • Pitzer, K.S. (1980) Electrolytes. From Dilute Solutions to Fused Salts. J. Am. Chem. Soc., 102, 9, 2902-2906. [CrossRef] [Google Scholar]
  • Platzer, B. et Maurer, G. (1989) A Generalized Equation of State for Pure Polar and Nonpolar Fluids. Fluid Phase Eq., 51, 223-236. [CrossRef] [Google Scholar]
  • Poetmann, F.H. et Katz, D.L. (1945) Phase Behavior of Binary Carbon Dioxide-Paraffin Systems. Ind. Eng. Chem., 37, 9, 847-853. [CrossRef] [Google Scholar]
  • Pollack, N.R., Enick, R.M., Holder, G.D. et Mangone, J. (1986) The Effect of an Aqueous Phase on the CO2/Tetradecane and CO2/Maljamar Oil Systems: Experimental and Modelling Results. 61st Annual Technical Conference and Exhibition, Nouvelle-Orléans, LA, octobre, SPE 15400. [Google Scholar]
  • Prausnitz, J.M., Lichtenthaler, R.N. et de Azevedo, E.G. (1986) Molecular Thermodynamics of Fluid Phase Equilibria, 2e éd., Prentice Hall, NJ. [Google Scholar]
  • Prutton, C.F. et Savage, R.L. (1945) The Solubility of Carbon Dioxide in Calcium Chloride-Water Solutions at 75, 100, 120° and High Pressure. Am. Chem. Soc. J., 67, 1550-1554. [Google Scholar]
  • Rafal, M., Berthold, J.W., Scrivner, N.C. et Grise, S.L. (1994) Models for Electrolyte Solutions, Models for Thermodynamic and Phase Equilibria Calculations, Sandler, S.I. (éd.), Marcel Dekker, Inc., NY, 601-670. [Google Scholar]
  • Reamer, H.H. et Sage, B.H. (1965) Partial Volumetric Behavior in Hydrocarbon Systems: n-decane and Carbon Dioxide in the Liquid Phase of the n-decane-Carbon Dioxide System. J. Chem. Eng. Data, 10, 1, 49. [CrossRef] [Google Scholar]
  • Reamer, H.H.,Olds, R.H.,Sage, B.H. et Lacey, W.N. (1945) Phase Equilibria of Hydrocarbon Systems: Volumetric Behavior of Ethane-Carbon Dioxide System. Ind. Eng. Chem., 37, 7, 688. [CrossRef] [Google Scholar]
  • Reamer, H.H.,Sage, B.H. et Lacey, W.N. (1951) Phase Equilibria of Hydrocarbon Systems: Volumetric Behavior of Propane-Carbon Dioxide System. Ind. Eng. Chem., 43, 11, 2515-2520. [CrossRef] [Google Scholar]
  • Reamer, H.H.,Selleck, F.T.,Sage, B.H. et Lacey, W.N. (1953) Volumetric and Phase Behavior of Decane-Hydrogen Sulfide System. Ind. Eng. Chem., 45, 8, 1810-1812. [CrossRef] [Google Scholar]
  • Robinson, D.B. et Bailey, J.A. (1957) The Hydrocarbon- Hydrogen Sulfide-Methane System Part I: Phase Behavior at 100°F. Can. J. Chem. Eng., 35, 151. [Google Scholar]
  • Robinson, D.B.,Lorenzo, A. et Macryogeorgos, C.A. (1959) The Hydrocarbon-Hydrogen Sulfide-Methane System Part II: Phase Behavior at 40 and 160°F. Can. J. Chem. Eng., 37, 212. [CrossRef] [Google Scholar]
  • Robinson, D.B., Huang, S.S., Leu, A.D. et Ng, H.J. (1982) The Phase Behavior of Two Mixtures of Methane, Carbon Dioxide, Hydrogen Sulfide and Water. Rapport GPA, RR57. [Google Scholar]
  • Sadus, R.J. (1992) High Pressure Phase Behaviour of Multicomponent Fluid Mixtures, Elsevier Science Publishers, Amsterdam. [Google Scholar]
  • Sander, B.,Fredenslund, A. et Rasmussen, P. (1986) Calculation of Vapour-Liquid Equilibria in Mixed Solvent/Salt Systems using an Extended UNIQUAC Equation. Chem. Eng. Sci., 41, 1171-1183. [CrossRef] [Google Scholar]
  • Schneider, G.M.,Alwani, Z.,Heim, W.,Horvath, E. et Franck, E.U. (1967) Phasengleichgewichten und Kritische Erscheinungen in Binaren Ischsystemen bis 1500 bar. Chemie Ing. Techn., 39, 11, 649-656. [CrossRef] [Google Scholar]
  • Selleck, F.T.,Carmichael, L.T. et Sage, B.H. (1952) Phase Behavior in the Hydrogen Sulfide-Water System. Ind. Eng. Chem., 44, 9, 2219-2226. [CrossRef] [Google Scholar]
  • Son, K.Y. et Kobayashi, R. (1989) Water Content of a CO2-5.31 Mol Percent Methane Mixture. Rapport GPA, RR120. [Google Scholar]
  • Suleimenov, O.M. et Krupp, R.E. (1994) Solubility of Hydrogen Sulfide in Pure Water and in NaCl Solutions, from 20 to 320°C and at Saturation Pressures. Geochim. et Cosmochim. Acta, 58, 11, 2433-2444. [Google Scholar]
  • Takenouchi, S. et Kennedy, G.C. (1964) The Binary System H2O-CO2 at High Temperatures and Pressures. Am. J. Sci., 262, 1055-1074. [CrossRef] [Google Scholar]
  • Takenouchi, S. et Kennedy, G.C. (1965) The Solubility of Carbon Dioxide in NaCl Solutions at High Temperatures and Pressures. Am. J. Sci., 263, 445-454. [Google Scholar]
  • Tiffin, D.L.,Devera, A.L.,Luks, K.D. et Kohn, J.P. (1978) J. Chem. Eng. Data, 23, 45. [CrossRef] [Google Scholar]
  • Valderrama, J.O., Obaid-Ur-Rehman, S. et Cisternas, L.A. (1988) Generalized Interaction Parameters in Cubic Equations of State for CO2-n-alkane Mixtures. Fluid Phase Eq., 40, 217-233. [CrossRef] [Google Scholar]
  • Van der Beken, I. (1998) Thèse, université de Pau et des Pays de l’Adour. [Google Scholar]
  • Weisenberger, S. et Schumpe, A. (1996) Estimation of Gas Solubilities in Salt Solutions at Temperatures from 273 K to 363 K. AIChE J., 42, 1 [CrossRef] [Google Scholar]
  • Wichert, E. et Royan, T. (1996) Sulfur Disposal by Acid Gas Injection. Gas Technology Conference, Canada, SPE 35585. [Google Scholar]
  • Wichterle, I., Linek, J., Wagner, Z. et Kehiaian, H. (1993) Vapor- Liquid Equilibrium Bibliographic Database, Eldata SARL. [Google Scholar]
  • Wichterle, I., Linek, J., Wagner, Z. et Kehiaian, H. (1995) Vapor- Liquid Equilibrium Bibliographic Database, Supplement to 1993, Eldata SARL. [Google Scholar]
  • Wiebe, R. et Gaddy, V.L. (1940) The Solubility of Carbon Dioxide in Water at Various Temperatures from 12 to 40° and at Pressures to 500 Atmospheres. Critical phenomena. J. Am. Chem. Soc., 62, 815-817. [CrossRef] [Google Scholar]
  • Wilson, G.M. et Peterson, J.M. (1975) Enthalpy and Phase Boundary Measurements on Carbon Dioxide and Mixtures of Carbon Dioxide with Methane, Ethane and Hydrogen Sulfide. Rapport GPA, RR12, GPA, Tulsa, OK. [Google Scholar]
  • Worden, R.H.,Smalley, C. et Oxtoby, N.H. (1995) Gas Souring by Thermochemical Sulfate Reduction at 140°C. AAPG Bulletin, 79, 6, 854-863. [Google Scholar]
  • Yau, J.S. et Tsai, F.N. (1992) Correlation of Solubilities of Carbon Dioxide in Aromatic Compounds. Fluid Phase Eq., 73, 1-25. [CrossRef] [Google Scholar]
  • Ye, S. (1990) Mesure et exploitation de la vitesse d’ultrasons dans des liquides en pression ; Application à des fluides complexes d’origine pétrolière. Thèse, université de Pau et des Pays de l’Adour. [Google Scholar]
  • Ye, S.,Xans, P. et Lagourette, B. (1994) Modification of the Pitzer Model to Calculate the Mean Activity Coefficients of Electrolytes in a Water-Alcohol Mixed Solution. J. Sol. Chem., 23, 12, 1301-1315. [CrossRef] [Google Scholar]
  • Zemaitis, J.F., Clark, D.M., Rafal, M. et Scrivner, N.C. (1986) Handbook of Aqueous Electrolyte Thermodynamics, DIPPR (sponsored by AIChE). [Google Scholar]

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