- Apostolou, D.,Kalospiros, N. and Tassios, D. (1995) Prediction of Gas Solubilities using the LCVM Equation of State-Excess Gibbs Free-Energy Model. Ind. Eng. Chem. Res., 34, 948-957. [CrossRef] [Google Scholar]
- Avlonitis, G.,Mourikas, G.,Stamataki, S. and Tassios, D. (1994) A Generalized Correlation for the Interaction Coefficients of N2-Hydrocarbon Binary Mixtures. Fluid Phase Equilibria, 101, 53-68. [CrossRef] [Google Scholar]
- Boukouvalas, C.,Spiliotis, N.,Coutsikos, P.,Tzouvaras, N. and Tassios, D. (1994) Prediction of Vapor-Liquid Equilibrium with the LCVM Model: A Linear Combination of the Vidal and Michelsen Mixing Rules Coupled with the Original UNIFAC and the t-mPR Equation of State. Fluid Phase Equilibria, 92, 75-106. [Google Scholar]
- Carroll, J.J. and Mather, A.E. (1995) A Generalized Correlation for the Peng-Robinson Interaction Coefficients for Paraffin- Hydrogen Sulfide Binary Systems. Fluid Phase Equilibria, 105, 221-228. [Google Scholar]
- Clarke, E.C. and Glew, D.N. (1970) Deuterium and Hydrogen Sulfides: Vapor Pressures, Molar Volumes, and Thermodynamic Properties. Can. J. of Chemistry, 48, 764-775. [CrossRef] [Google Scholar]
- Coats, K.H. and Smart, G.T. (1986) Application of a Regression- Based EoS, PVT Program to Laboratory Data. SPE Reservoir Engineering, 5, 277-299. [CrossRef] [Google Scholar]
- Czerwienski, G.J., Tomasula, P and Tassios, D. (1988) Vapor- Liquid Equilibria with the VdN-711 Equation of State. Fluid Phase Equilibria, 42, 63-83. [CrossRef] [Google Scholar]
- Daubert, T.E. and Danner, R.P. (1985) Data Compilation Tables of Properties of Pure Compounds. AIChE, New York. [Google Scholar]
- Daubert, T.E. and Danner, R.P. (1989) Data Compilation Tables of Properties of Pure Compounds. AIChE, New York. [Google Scholar]
- Eakijn, B.E. and de Vaney, W.E. (1974) Vapor-Liquid Equilibria in Hydrogen-Hydrogen Sulfide—C9 Hydrocarbon Systems. AIChE Symp. Ser, 70, 80-90. [Google Scholar]
- Feng, G.X. and 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. and Mather, A.E. (1993a) Solubility of H2S in n-dodecane. Fluid Phase Equilibria, 87, 341-346. [Google Scholar]
- Feng, G.X. and Mather, A.E. (1993b) Solubility of H2S in n-hexadecane at Elevated Pressure. Can. J. Chem. Eng., 71, 327-328. [CrossRef] [Google Scholar]
- Feng, G.X.,Mather, A.E. and Carroll, J.J. (1995) The Solubility of Hydrogen Sulfide in Mixtures of n-hexadecane and n-eicosane. Can. J. Chem. Eng., 73, 154-155. [CrossRef] [Google Scholar]
- Huang, S.S.S. and Robinson, D.B. (1984) Vapor-Liquid Equilibrium in Selected Aromatic Binary Systems, m-xylene- Hydrogen Sulfide and Mesitylene-Hydrogen Sulfide. Fluid Phase Equilibria, 17, 373-382. [CrossRef] [Google Scholar]
- Huang, S.S.S. and Robinson, D.B. (1985) Equilibrium Phase Properties of the Ethylcyclohexane-Hydrogen Sulfide and npropylcyclohexane- Hydrogen Sulfide Binary Systems. J. Chem. Eng. Data, 30, 154-157. [CrossRef] [Google Scholar]
- Jhaveri, B.S. and Youngren, G.K. (1984) Three Parameters Modification of the Peng-Robinson Equation of State to Improve Volume Predictions. SPE, Paper 1311. [Google Scholar]
- Kesler, M.G. and Lee, B.I. (1976) Improved Prediction of Enthalpy of Fractions. Hydrocarbon Processing, 55, 3, 153-158. [Google Scholar]
- Knapp, H., Döring, R., Oellrich, L., Plöcker, V. and Prausnitz, J.M. (1982) Vapor-Liquid Equilibria for Mixtures of Low Boiling Substances. DECHEMA Chemistry Data Series, VI. [Google Scholar]
- Kohn, J.P. and Kurata, F. (1958) Heterogeneous Phase Equilibria of the Methane-Hydrogen Sulfide System. AIChE J., 4, 211-217. [CrossRef] [Google Scholar]
- Kordas, A.,Magoulas, K.,Stamataki, S. and Tassios, D.P. (1995) Methane-Hydrocarbons Interaction Parameters Correlation for the Peng-Robinson and the Translated Peng-Robinson Equations of State. Fluid Phase Equilibria, 112, 33-44. [Google Scholar]
- Kordas, A.,Tsoutsouras, K.,Stamataki, S. and Tassios, D.P. (1994) A Generalized Correlation for the Interaction Coefficients of CO2-Hydrocarbon Binary Mixtures. Fluid Phase Equilibria, 93, 141-166. [CrossRef] [Google Scholar]
- Laugier, S. and Richon, D. (1995) Vapor-Liquid Equilibria for Hydrogen Sulfide + Hexane, + Cyclohexane, + Benzene, + Pentadecane, and + (Hexane and Pentadecane). J. Chem. Eng. Data, 40, 153-159. [CrossRef] [Google Scholar]
- Leu, A.D and 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]
- Leu, A. and Robinson, D.B. (1992) High Pressure Vapor-Liquid Equilibrium Phase Properties of the Isopentane-Hydrogen Sulfide and Neopentane-Hydrogen Sulfide Binary Systems. J. Chem. Eng. Data, 37, 14-17. [CrossRef] [Google Scholar]
- Magoulas, K. and Tassios, D. (1990) Thermophysical Properties of n-alkanes from C1 to C20 and their Prediction for Higher Ones. Fluid Phase Equilibria, 56, 119-140. [CrossRef] [Google Scholar]
- Moysan, J.M.,Paradowski, H. and Vidal, J. (1986) Prediction of Phase Behaviour of Gas-Containing Systems with Cubic Equations of State. Chem. Eng. Science, 41, 2069-2074. [Google Scholar]
- Ng, H.J.,Karla, H.,Robinson, D.B. and Kubota, H. (1980) Equilibrium Phase Properties of the Toluene-Hydrogen Sulfide and n-heptane-Hydrogen Sulfide Binary Systems. J. Chem. Eng. Data, 25, 51-55. [CrossRef] [Google Scholar]
- Nishiumi, H.,Arai, T. and Takeuchi, K. (1988) Generalization of the Binary Interaction Parameter of the Peng-Robinson Equation of State by Component Family. Fluid Phase Equilibria, 42, 43-62. [Google Scholar]
- North Aegean Petroleum Corporation (1991) Personal communication.Peng, D.Y. and Robinson, D.B. (1976) A New Two-Constant Equation of State. Ind. Eng. Chem. Fundam., 15, 59-64. [CrossRef] [Google Scholar]
- Reamer, H.H.,Sage, B.H. and Lacey, W.N. (1951) Phase Equilibria in Hydrocarbon Systems. Ind. Eng. Chem., 43, 976-980. [CrossRef] [Google Scholar]
- Richon, D.,Laugier, S. and Renon, H. (1992) High Pressure Vapor-Liquid Equilibrium Data for Binary Mixtures Containing N2, CO2, H2S and an Aromatic Hydrocarbon or Propylcyclohexane in the Range 313-473 K. J. Chem. Eng. Data, 37, 264-268. [CrossRef] [Google Scholar]
- Robinson, D.B. and Bailey, J.A. (1957) The Carbon Dioxide- Hydrogen Sulfide-Methane System. Part I. Phase Behaviour at 100oF. Can. J. Chem. Eng., 35, 151-158. [Google Scholar]
- Robinson, D.B.,Lorenzo, A.P. and Macrygeorgos, C.A. (1959) The Carbon Dioxide-Hydrogen Sulfide-Methane System. Part II. Phase Behaviour at 40oF and 160oF. Can. J. Chem Eng., 37, 212-217. [Google Scholar]
- Spiliotis, N.,Boukouvalas, C.,Tzouvaras, N. and Tassios, D. (1994a) Application of the LCVM Model to Multicomponent Systems: Extension of the UNIFAC Interaction Parameter Table and Prediction of the Phase Behavior of Synthetic Gas Condensate and Oil Systems. Fluid Phase Equilibria, 101, 187-210 [CrossRef] [Google Scholar]
- Spiliotis, N.,Magoulas, K. and Tassios, D. (1994b) Prediction of the Solubility of Aromatic Hydrocarbons in Supercritical CO2 with EoS/GE Models. Fluid Phase Equilibria, 102, 121-141. [CrossRef] [Google Scholar]
- Swain, E.J. (1993) US Refiners Face Declining Crude Quality, Insufficient Price Spread. Oil & Gas J., 91, 9, 62-65. [Google Scholar]
- Twu, C.H. (1984) An Internally Consistent Correlation for Predicting the Critical Properties and Molecular Weights of Petroleum and Coal-Tar Liquids. Fluid Phase Equilibria, 16, 137-150. [Google Scholar]
- Valderrama, J.O., Obaid-Ur-Rehrman, S. and Cisternas, L.A. (1987) Application of a New Cubic Equation of State to Hydrogen Sulfide Mixtures. Chem. Eng. Science, 42, 2935-2940. [CrossRef] [Google Scholar]
- Voutsas, E.C.,Boukouvalas, C.J.,Kalospiros, N.S. and Tassios, D.P. (1996) The Performance of EoS/GE Models in the Prediction of Vapor-Liquid Equilibria in Asymmetric Systems. Fluid Phase Equilibria, 116, 480-487. [CrossRef] [Google Scholar]
- Whitson, C.H. (1980) Characterizing Hydrocarbon Plus Fractions. European Offshore Petroleum Conference and Exhibition, London, Oct. 21-24, SPE, Paper 2233. [Google Scholar]
- Yakoumis, I.V.,Vlachos, K.,Kontogeorgis, G.M.,Coutsikos, P.,Kalospiros, N.S.,Kolisis, F.N. and Tassios, D.P. (1996) Application of the LCVM Model to Systems Containing Organic Compounds and Supercritical Carbon Dioxide. J. Supercrit. Fluids, 9, 88-98. [CrossRef] [Google Scholar]
Open Access
Numéro |
Oil & Gas Science and Technology - Rev. IFP
Volume 55, Numéro 5, September-October 2000
|
|
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Page(s) | 511 - 522 | |
DOI | https://doi.org/10.2516/ogst:2000038 | |
Publié en ligne | 1 octobre 2006 |
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