Dossier: Petroleum Industry Applications of Thermodynamics
Open Access
Issue
Oil & Gas Science and Technology - Rev. IFP
Volume 61, Number 3, May-June 2006
Dossier: Petroleum Industry Applications of Thermodynamics
Page(s) 303 - 317
DOI https://doi.org/10.2516/ogst:2006036a
Published online 01 January 2007
  • Abrams, D.S. Prausnitz, and J.M. (1975) Statistical thermodynamics of mixtures: a new expression for the Excess Gibbs free energy of partly or completely miscible systems, AICHE. J., 21, 116-128. [Google Scholar]
  • Austgen, D.M., Rochelle, T., Peng, X and Chen, CC. (1989) Model of Vapor-Liquid Equilibria for Aqueous Acid Gas - Alkanolamine Systems Using the Electrolyte-NRTL Equation, Ind. Eng. Chem. Res., 28, 1060-1073. [Google Scholar]
  • Benedict, M.,Webb, G.B. and Rubin, L.C. (1940) J. Chem. Phys., 8, 334. [CrossRef] [Google Scholar]
  • Boukouvalas, C.,Spiliotis, N.,Coutsikos, P.,Tzouvaras, N. and Tassios, D. (1994) Prediction of Liquid- vapour 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. [CrossRef] [Google Scholar]
  • Carlson, E. (1996) Don't Gamble with Physical Properties for simulation, Chem. Eng. Prog., 10, 35-46. [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 Eq., 105, 221-228. [Google Scholar]
  • Cavett, R.H. (1964) Physical Data for Distillation Calculation, Vapor-Liquid Equilibria, 27th Midyear meeting, API Division of Refining, San Fransisco, CA, May 15 1964. [Google Scholar]
  • Chapman, W.G.,Jackson, G. and Gubbins, K.E. (1988) Phase Equilibria of Associating Fluids : Chain Molecules with Multiple Bonding Sites, Mol. Phy, 65, 1057. [Google Scholar]
  • Chapman, W.G.,Gubbins K.E.,Jackson, G. and Radosz, M. (1990) New Reference equation of state for associating liquids, Ind. Eng. Chem. Res, 29, 1709-1721. [Google Scholar]
  • Chen, J.Fischer, K. and Gmehling, J. (2002) Modification of the PSRK mixing rules and results for vapour-liquid equilibria, enthalpy of mixing and activity coefficient at infinite dilution, Fluid Phase Equilibria, 200, 411-429. [CrossRef] [Google Scholar]
  • Coniglio, L.,Trassy, L. and Rauzy, E. (2000) Estimation of Thermophysical Properties of Heavy Hydrocarbons through a group contribution based equation of state, Ind. Eng. Chem. Res., 39, 5037-5048. [CrossRef] [Google Scholar]
  • Constantinou, L. and Gani R. (1994) New Group Contribution Method for estimating Properties of Pure Compounds, AIChE J. 40, 1697-1710. [Google Scholar]
  • de Hemptinne, J.C., Ungerer, P. (1995) Accuracy of the volumetric predictions of some important equations of state, including a modified version of the Lee & Kesler method, Fluid Phase Eq., 106, 81-109. [Google Scholar]
  • de Hemptinne, J.C., Barreau A., Ungerer, P., Behar, E. (1994) Evaluation of Equations of state at high pressure for light hydrocarbons, Proceedings of the 14th International Codata conference, 18-22 September. [Google Scholar]
  • DIPPR Thermophysical Properties Database, http://www.aiche. org/TechnicalSocieties/DIPPR/index.aspxEdmister, W.C. and Okamoto, K.K. (1959) Petr. Ref., 38, 8, 117-129. [Google Scholar]
  • Erlykina, M.E., Vatskova, V.G., Borisova, I.A., Umanskaya, N.I., Mikhailova, V.A. and Sokolov, N.I. (1984) Dampf-Fluessig Gleichgewicht im System Aceton – Wasser – Toluol bei Atmosphaerendruck, Deposited Doc. Oniitekhim, 1-12. [Google Scholar]
  • Flory (1944) Thermodynamics of Heterogeneous Polymers and their solutions, J. Chem. Phys, 12, 425-438. [Google Scholar]
  • Fredenslund, Aa, Gmehling, J. and Rasmussen, P. (1977) Vapour-Liquid Equilibria using UNIFAC, Elsevier, Amsterdam. [Google Scholar]
  • Fredenslund, Aa,Jones, R.L. and Prausnitz, J.M. (1975) Group contribution estimation of Activity coefficients in nonideal liquid mixtures, AIChE. J., 27, 1089-1099. [Google Scholar]
  • Gasem, K.A.M., Gao, W., Pan, Z., Robinson Jr, R.L. (2001) A modified temperature dependence for the Peng–Robinson equation of state Fluid Phase Equilib. 181 113–125. [Google Scholar]
  • Gmehling, J., Li, J. and Fischer, K (1997) Further Development of the SRK model prediction of gas solubilities and vapor-liquid equilibria at low and high pressures. Fluid Phase Equilibria, 141, 113-127. [Google Scholar]
  • Grayson, H.G. and Streed, C.W. (1963) Vapor-Liquid Equilibria for high temperature, high pressure hydrogen-hydrocarbon systems, 6th World Congres for Petroleum. [Google Scholar]
  • Holderbaum, T. and Gmehling, J. (1991) PSRK: A group contribution equation of state based on UNIFAC Fluid Phase Equilibria 70, 251-265. [Google Scholar]
  • Huron, M.J. and Vidal, J. (1979) New mixing rules in simple equations of state for representing vapour-liquid equilibria of strongly non-ideal mixtures, Fluid Phase Eq., 3, 255-271. [Google Scholar]
  • Joback, K. and Reid, R.C. (1987) Estimation of Pure Component Properties from Group Contributions, Chem. Eng. Comm., 57, 233-243. [Google Scholar]
  • Jaubert, J.N. and Mutelet (2004) VLE predictions with the Peng–Robinson equation of state and temperature dependent kij calculated through a group contribution method Fluid Phase Equilibria 224, 285–304. [Google Scholar]
  • Jaubert, J.N., Vitu S., Mutelet, F. and Corriou, J.P. (2005) Extension of the PPR78 model (predictive 1978, Peng–Robinson EOS with temperature dependent kij calculated through a group contribution method) to systems containing aromatic compounds Fluid Phase Equilibria 237, 193–211. [Google Scholar]
  • Kamps (2005) Model for the Gibbs Excess Energy of Mixed-Solvent (Chemical-Reacting and Gas-Containing) Electrolyte Systems, Ind. Eng. Chem. Res.,44, 1, 201-225. [Google Scholar]
  • Kordas, A.,Magoulas K.,Stamakis S.,Tassios, D. (1995) Methanehydrocarbon interaction parameters correlation for the Peng-Robinson and the t-mPR equation of state, Fluid Phase Eq., 112, 33-44. [CrossRef] [Google Scholar]
  • Lee, B.I. and M.G. Kesler (1975) A generalized Thermodynamic Correlation Based on Three-Parameter Corresponding States, AIChE. J., 21, 3, 510. [Google Scholar]
  • Leibovici (1993) A consistent procedure for the estimation of properties associated to lumped systems, Fluid Phase Eq. 87, 189-197. [Google Scholar]
  • Leibovici, C.F., Barker, J.W. and Waché, D. (2000) Method for delumping the results of compositional reservoir simulation SPE J. 5, 227-235. [Google Scholar]
  • Levelt Sengers, J.M.H (1970) “Scaling predictions for thermodynamic anomalies near tha gas-liquid critical point” Ind. Eng. Chem. Fundam., 9, N° 3, 470-480. [Google Scholar]
  • Li, J, Polka, H.M. and Gmehling, J.A. (1994) A GE model for single and mixed solvent electrolyte systems: 1. Model and Results for strong electrolytes Fluid Phase Eq. 94, 89-114. [Google Scholar]
  • Liu, Y. and Watanasiri, S. (1999) Succesfully Simulate Electrolyte Systems, Chem. Eng. Prog., 10, 25-42. [Google Scholar]
  • Marrero, J. and Gani, R. (2001) Group Contribution Based Estimation of Pure Component Properties, Fluid Phase Eq., 183, 184-208. [Google Scholar]
  • Mathias, P.M. and Copeman, T.W. (1983) Extension of the peng-Robinson equation of state to complex mixtures: evaluation of the various forms of the local composition concept, Fluid Phase Eq., 13, 91-108. [CrossRef] [Google Scholar]
  • McCain (1990) The Properties of Petroleum Fluids, PennWell Publishing Co, Tulsa, OK. [Google Scholar]
  • Michelsen, M.L. (1990) A modified Huron-Vidal mixing rule for cubic equations of state, Fluid Phase Eq., 60, 213-219. [Google Scholar]
  • Montel, F. and Gouel, P. (1984) A new Lumping Scheme of Analytical Data for Compositional Studies, SPE 13119. [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. Sci., 41, 8, 2069-2074. [CrossRef] [Google Scholar]
  • Moysan, J.M., Paradowski, H. and Vidal, J. (1985) Correlation defines phase equilibria for H2, CH4 and N2 mixes, Hydrocarbon Processing, 73. [Google Scholar]
  • Neau, E.,Jaubert, J.N. and Rogalski, M. (1993) Characterization of Heavy Oils, Ind. Eng. Chem. Res., 32, 1196-1203. [CrossRef] [Google Scholar]
  • Newley, T.M.J. and Merrill, R.C. Jr. (1991) Pseudo-component Selection for Compositional Simulation, SPE Reservoir Engineering, 490-496. [Google Scholar]
  • Nicolaisen, H.,Rasmussen, P. and 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]
  • Pedersen, K.S., Fredenslund, Aa and Thomassen, P. (1989) Properties of Oils and Natural Gases, Gulf Publishing Co., Houston, Tx. [Google Scholar]
  • Péneloux, A., E. Rauzy and R. Frèze (1982) A consistent correction for Redlich-Kwong-Soave volumes, Fluid Phase Eq., 8, p7-23. [Google Scholar]
  • Peng, D.Y. and D.B. Robinson (1976) A new two-constant equation of state, Ind. Eng. Chem. Fundam., 15, 59-64. [Google Scholar]
  • Pitzer, K.S. (1995) Thermodynamics, Mc Graw Hill, NY, 3rd edition. [Google Scholar]
  • Pitzer, K.S. (1973) Thermodynamics of electrolytes I: Theoretical basis and general equations, J. Phys. Chem., 77, 2, 268-277. [CrossRef] [Google Scholar]
  • Poling, B.E., Prausnitz, J.M. and O'Conell, J.P. (2001) The properties of Gases and Liquids, Mc Graw Hill, 5th Edition. [Google Scholar]
  • Prausnitz, J.M., Lichtenthaler, R.N. and Gomes de Azevedo, E. (1999) Molecular Thermodynamics of Fluid Phase Equilibria, Prentice Hall Int., 3rd edition. [Google Scholar]
  • Rackett, H.G. (1970) Equation of state for saturated liquids, J.Chem.Eng.Data, 15, 4, 514-517. [Google Scholar]
  • Renon, H. and Prausnitz, J.M. (1968) Local Composition in thermodynamic Excess Functions for Liquid Mixtures, AIChE. J., 14, 135-144. [Google Scholar]
  • Riazi, M.R., Al-Sahhaf, T.A. and Al-Shammari, M.A. (1998) A Generalized Method for Estimation of Critical Constants, Fluid Phase Eq., Proceedings of the Eighth International Conference on Properties and Phase Equilibria for Product and Process design. [Google Scholar]
  • Riazi, M.R. (2005) Characterization and Properties of Petroleum Fractions, ASTM, January. [Google Scholar]
  • Ruffier-Meray V., Barreau, A. and Béhar, E. (1990) Optimal reduction of the analytical data necessary for the thermodynamic characterization of natural gases, SPE 20769, Annual Technical meeting, New Orleans. [Google Scholar]
  • Savelli, Labadie, Garcia, Meckler, Murray, Durandeau, Gobinot, Behar and Raynal (1981) Recommandantions pour l'établissement d'un rapport d'étude PVT, Revue de l'IFP, vol 36, n° 3, 293-307. [Google Scholar]
  • Scatchard, G. (1931) Chem. Rev. 8, 321. [CrossRef] [Google Scholar]
  • Setzmann, U. and Wagner, W. (1991) J. Phys. Chem. Ref. Data, 20, 1061. [CrossRef] [Google Scholar]
  • Soave, G. (1972) Equilibrium constants for a modified Redlich-Kwong equation of state,Chem. Eng. Sci, 27, 1197-1203. [Google Scholar]
  • Soave, G. (1995) A noncubic Equation of State for the Treatment ofHydrocarbon Fluids at Reservoir Conditions, Ind. Eng. Chem. Res., 34, 3981-3994. [CrossRef] [Google Scholar]
  • Soave, G. (1999) An effective modification of the Benedict Webb Rubin equation of state, Fluid Phase Eq., 164, 157-172. [CrossRef] [Google Scholar]
  • Soreide, I. (1989) mproved phase behaviour Prediction of Petroleum Reservoir Fluids from a cubic equation of state, PhD from the Norwegian Institute of Technology (NTH), Trondheim, Norway. [Google Scholar]
  • Soreide, I. and Whitson, C.H. (1992) Peng-Robinson predictions for hydrocarbons, CO2, N2, and H2S with pure water and NaCl brine, Fluid Phase Eq., 77, 217-240. [Google Scholar]
  • Twu, C.H. (1984) An internally consistent correlation for predicting the critical properties and molecular weights of petroleum and coaltar liquids, Fluid Phase Eq., 16, 137-150. [Google Scholar]
  • Twu, C.H.,Coon, J.E. and Cunningham, J.R. (1995) A new generalized alfa function for a cubic equation of state. Part I. Peng-Robinson equation, Fluid Phase Eq., 105, 49-59. [Google Scholar]
  • Ungerer, P. (1997) Prédiction des propriétés volumétriques des hydrocarures par une translation de volume améliorée Revue de l'Institut Français du Pétrole, 56 n° 6, 609-623. [Google Scholar]
  • Ungerer, P., Tavitian, B. and Boutin, A. (2005) Applicatioins of Molecular Simulation in the Oil and Gas Industry, Editions TECHNIP. [Google Scholar]
  • Valderrama, J.O., Obaid-Ur-Rehman, S. and Cisternas, L.A. (1988) Generalized interaction parameters in cubic equations of state for CO2-nalkane mixtures, Fluid Phase Eq., 40, 217-233. [CrossRef] [Google Scholar]
  • Van der Waals (1873) The equation of state for gases and liquids, Nobel Lectures in Physics, 1, 254-265, Elsevier, Amsterdam. [Google Scholar]
  • Vidal, J. (2003) Thermodynamics: Applications in Chemical Engineering and the Petroleum Industry, Editions Technip. [Google Scholar]
  • Werner, A., Behar, F., de Hemptinne, J.C. and Behar, E. (1996) Thermodynamic Properties of Petroleum Fluids during Expulsion and Migration from Source Rocks, Org. Geochem., 24, n° 10/11, 1079-1095. [Google Scholar]
  • Winn, F.W. (1952) Chem. Eng. Prog. Symposium, 42, 2. [Google Scholar]
  • Wong, D.S.H., H. Orbey and Sandler, S.I. (1992) Equation of state mixing rule for nonideal mixtures using available activity coefficient model parameters and that allows extrapolation over large ranges of temperatures and pressures, Ind. Eng. Chem. Res., 31, 2033-2039. [CrossRef] [Google Scholar]
  • Yan, W.,Topphoff, M.,Rose, C. and Gmehling, J. (1999) Prediction of vapor-liquid equilibria in mixed solvent electrolyte systems using the group contribution concept Fluid Phase Eq., 162, 97-113. [Google Scholar]
  • Younglove, B.A. and Ely, J.F. (1987) Thermophysical properties of fluids ii Methane, Ethane, Propane, Isobutane and Normal Butane, J. Phys. Chem. Ref. Data, 16, 4, 577. [NASA ADS] [CrossRef] [Google Scholar]

Current usage metrics show cumulative count of Article Views (full-text article views including HTML views, PDF and ePub downloads, according to the available data) and Abstracts Views on Vision4Press platform.

Data correspond to usage on the plateform after 2015. The current usage metrics is available 48-96 hours after online publication and is updated daily on week days.

Initial download of the metrics may take a while.