Dossier: International Conference - Thermodynamics 2007
Open Access
Issue
Oil & Gas Science and Technology - Rev. IFP
Volume 63, Number 3, May-June 2008
Dossier: International Conference - Thermodynamics 2007
Page(s) 305 - 319
DOI https://doi.org/10.2516/ogst:2008025
Published online 24 June 2008
  • Abrams D.S.,Prausnitz J.M. (1975) Statistical thermodynamics of liquid mixtures: a new expression for the excess Gibbs energy of partly or completely miscible systems, AIChE J. 21, 1, 116-128. [CrossRef]
  • Amer-Amezaga (1975) An. Quim. 71, 127.
  • Apelblat A.,Kohler F. (1976) J. Chem. Thermodyn. 8, 749. [CrossRef]
  • Clark G.N.I.,Haslam A.J.,Galindo A.,Jackson G. (2006) Developing optimal Wertheim-like models of water for use in Statistical Associating Fluid Theory (SAFT) and related approaches, Mol. Phys. 104, 3561-3581. [CrossRef]
  • Darwish N.A.,Abdulkarim M.A.,Ashour I.,Dwaidar A.M.,Athamneh F.S. (2002) Liquid-liquid equilibrium for the system water + acetic acid + 1-heptanol at 278.1, 293. 1, 303.1 and 313.1 K, Fluid Phase Equilibr. 200, 277-285. [CrossRef]
  • Derawi S.O.,Michelsen M.L.,Kontogeorgis G.M.,Stenby E.H. (2003a) Extension of the CPA equation of state to glycol-water cross-associating systems, Ind. Eng. Chem. Res. 42, 7, 1470-1477. [CrossRef]
  • Derawi S.O.,Michelsen M.L.,Kontogeorgis G.M.,Stenby E.H. (2003b) Application of the CPA equation of state to glycol/hydrocarbons liquid-liquid equilibria, Fluid Phase Equilibr. 209, 2, 163-184. [CrossRef]
  • Folas G.K.,Derawi S.O.,Michelsen M.L.,Stenby E.H.,Kontogeorgis G.M. (2005a) Recent applications of the Cubic- Plus-Association (CPA) equation of state to industrially important systems, Fluid Phase Equilibr. 228-229, 121-126. [CrossRef]
  • Folas G.K.,Gabrielsen J.,Michelsen M.L.,Stenby E.H.,Kontogeorgis G.M. (2005b) Application of the Cubic-Plus- Association (CPA) Equation of State to Cross-Associating Systems, Ind. Eng. Chem. Res. 44, 3823-3833. [CrossRef]
  • Folas G.K.,Kontogeorgis G.M.,Michelsen M.L.,Stenby E.H. (2006a) Application of the Cubic-Plus-Association equation of state to complex mixtures with aromatic hydrocarbons, Ind. Eng. Chem. Res. 45, 4, 1527-1538. [CrossRef]
  • Folas G.K.,Kontogeorgis G.M.,Michelsen M.L.,Stenby E.H. (2006b) Application of the Cubic-Plus-Association equation of state to mixtures with polar chemicals and high pressures, Ind. Eng. Chem. Res. 45, 4, 1516-1526. [CrossRef]
  • Fu Y.-H.,Sandler S.I. (1995) A simplified SAFT equation of state for associating compounds and mixtures, Ind. Eng. Chem. Res. 34, 1897-1909. [CrossRef]
  • Garcia-Lisbona N.M.,Galindo A.,Jackson G.,Burgess A.N. (1998) Predicting the high-pressure phase equilibria of binary aqueous solutions of 1-butanol, n-butoxyethanol and n- Decylpentaoxyethylene Ether (C10E10) using SAFR-HS approach, Mol. Phys. 93, 57. [CrossRef]
  • Gillespie P.C., Wilson G.M. (1982) Vapor-Liquid and Liquid- Liquid Equilibria: Water-Methane, Water-Carbon Dioxide, Water-Hydrogen Sulfide, Water-n-Pentane, Water-Methane-n- Pentane, GPA report 48, Wiltec Res. Co, Canada.
  • Grenner A.,Schmelzer J., von Solms N.,Kontogeorgis G.M. (2006) Comparison of Two Association Models (Elliott-Suresh- Donohue and Simplified PC-SAFT) for Complex Phase Equilibria of Hydrocarbon-Water and Amine-Containing Mixtures, Ind. Eng. Chem. Res. 45, 8170. [CrossRef]
  • Gross J.,Sadowski G. (2002) Application of the Perturbed-Chain SAFT Equation of State to Associating Systems, Ind. Eng. Chem. Res. 41, 5510-5515. [CrossRef]
  • Hessel D.,Geiseler G. (1965) Pressure dependence of the heteroazeotropic system butanol-H2O, Z. Phys. Chem. (Leipzig) 229, 199.
  • Hong, Kobayashi (1988) Fluid Phase Equilibr. 41, 269.
  • Huang S.H.,Radosz M. (1990) Equation of state for small, large, polydisperse and associating molecules, Ind. Eng. Chem. Res. 29, 2284-2294. [CrossRef]
  • Jou F.-Y.,Mather A.E. (2003) Liquid-Liquid Equilibria for Binary Mixtures of Water + Benzene, Water + Toluene, and Water + p-Xylene from 273 K to 458 K, J. Chem. Eng. Data 48, 750-752. [CrossRef]
  • Kaarsholm M.,Derawi S.O.,Michelsen M.L.,Kontogeorgis G.M. (2005) Extension of the Cubic-Plus-Association (CPA) Equation of State to Amines, Ind. Eng. Chem. Res. 44, 12, 4406-4413. [CrossRef]
  • Kamlet M.J.,Abboud J.M.,Abraham M.H.,Taft R.W. (1983) Linear solvation energy relationships. 23. A comprehensive collection of the solvatochromic parameters, π, α,β and some methods for simplifying the generalized solvatochromic equation, J. Org. Chem. 48, 2877-2887. [CrossRef]
  • Kharin S. et al. (1969) Khim. Khim. Tekhnol. 12, 424.
  • Kleiner M., Sadowski G. (2007) Modeling of polar systems using PCP-SAFT: an approach to account for induced-association interactions. Submitted for publication.
  • Kontogeorgis G.M.,Voutsas E.,Yakoumis I.,Tassios D.P. (1996) An equation of state for associating fluids, Ind. Eng. Chem. Res. 35, 4310-4318. [CrossRef]
  • Kontogeorgis G.M.,Yakoumis I.V.,Meijer H.,Hendriks E.M.,Moorwood T. (1999) Multicomponent phase equilibrium calculations for water-methanol-alkane mixtures, Fluid Phase Equilibr. 158-160, 201-209. [CrossRef]
  • Kontogeorgis G.M.,Michelsen M.L.,Folas G.,Derawi S.O., von Solms N.,Stenby E.H. (2006a) Ten years with the CPA (Cubic- Plus-Association) equation of state Part I (Pure Compounds and Self-Associating Systems), Ind. Eng. Chem. Res. 45, 14, 4855-4868. [CrossRef]
  • Kontogeorgis G.M.,Michelsen M.L.,Folas G.,Derawi S., von Solms N.,Stenby E.H. (2006b) Ten years with the CPA (Cubic- Plus-Association) equation of state Part II (Cross-Associating and Multicomponent systems), Ind. Eng. Chem. Res. 45, 14, 4869-4878. [CrossRef]
  • Kontogeorgis G.M., Folas G., von Solms N., Michelsen M.L., Stenby E.H. (2007) Modelling of Associating Mixtures for applications in the oil & gas and chemical industries, Fluid Phase Equilibr. 261, 205-211.
  • Koschel D.,Coxam J.Y.,Majer V. (2007) Enthalpy and solubility data of H2S in water at conditions of interest for geological sequestration, Ind. Eng. Chem. Res. 46, 4, 1421. [CrossRef]
  • Kziazckzac A., Moorthi K. (1985) Prediction of thermodynamic properties of alkylphenol + hydrocarbon binary systems on the basis of pure liquid properties, Fluid Phase Equilibr. 153-164.
  • Leet W.A,Lin H.,Chao K. (1987) Mutual Solubilities in Six Binary Mixtures of Water + a Heavy Hydrocarbon or a Derivative, J. Chem. Eng. Data 32, 37-40. [CrossRef]
  • Leu et al. (1992) Fluid Phase Equilibr. 72, 163.
  • Li X.-S.,Englezos P. (2004) Vapor-liquid equilibrium of systems containing alcohols, water, carbon dioxide and hydrocarbons using SAFT, Fluid Phase Equilibr. 224, 111-118. [CrossRef]
  • Li X.-S.,Englezos P. (2003) Vapor-liquid equilibrium of systems containing alcohols using the Statistical Associating Fluid Theory, Ind. Eng. Chem. Res. 42, 4953-4961. [CrossRef]
  • Li X.-S.,Wu H.-J.,Englezos P. (2006) Prediction of gas hydrate formation conditions in the presence of methanol, glycerol, ethylene glycols and triethylene glycol with the Statistical Associating Fluid Theory Equation of State, Ind. Eng. Chem. Res. 45, 2131-2137. [CrossRef]
  • Lohmann J.,Joh R.,Gmehling J. (1997) Solid-Liquid Equilibria of Viscous Binary Mixtures with Alcohols, J. Chem. Eng. Data 42, 1170. [CrossRef]
  • Niederbroecker H.,Schmelzer J. (1997) Isothermal vapor-liquid equilibria in binary mixtures containing normal alkanes (nonane, undecane, or dodecane) and cresols (2-methylphenol or 3- methylphenol) at 373 to 453 K, Int. Electron. J. Phys.-Chem. Data 3, 197-204.
  • Ohgaki, Katayama (1976) J. Chem. Eng. Data 21, 53.
  • Oliveira M.B.,Freire M.G.,Marrucho I.M.,Kontogeorgis G.M.,Queimada A.J.,Coutinho J.A.P. (2007) Modeling the liquid-liquid equilibria for water-fluorocarbons with the Cubic-Plus- Association equation of state, Ind. Eng. Chem. Res. 46, 4, 1415-1420. [CrossRef]
  • Paricaud P.,Galindo A.,Jackson G. (2002) Review. Recent advances in the use of the SAFT approach in describing electrolytes, interfaces, liquid crystals and polymers, Fluid Phase Equlibr. 194-197, 87-96. [CrossRef]
  • Perakis C.,Voutsas E.,Magoulas K.,Tassios D. (2006) Thermodynamic modeling of the vapor-liquid equilibrium of water/ethanol/CO2 system, Fluid Phase Equilibr. 243, 1-2, 142-150. [CrossRef]
  • Perakis C.A.,Voutsas E.C.,Magoulas K.G.,Tassios D.P. (2007) Thermodynamic modeling of water plus acetic acid + CO2 system: The importance of association sites of water and of the nonassociation contribution for the CPA and SAFT-type models, Ind. Eng. Chem. Res. 46, 3, 932-938. [CrossRef]
  • Pfohl O.,Pagel A.,Brunner G. (1999) Phase equilibria in systems containing o-cresol, p-cresol, carbon dioxide and ethanol at 323.15-473.15 K and 10-35 MPa, Fluid Phase Equilibr. 157, 53-79. [CrossRef]
  • Pfohl O.,Avramova P.,Brunner G. (1997) Two- and three-phase equilibria in systems containing benzene derivatives, carbon dioxide and water at 373.15 K and 10-30 MPa, Fluid Phase Equilibr. 141, 179-206. [CrossRef]
  • Renon H.,Prausnitz J.M. (1968) Local compositions in thermodynamic excess functions for liquid mixtures, AIChE J. 14, 1, 135-144. [CrossRef]
  • Ruffine L.,Mougin P.,Barreau A. (2006) How to represent hydrogen sulfide within the CPA equation of state, Ind. Eng. Chem. Res. 45, 7688-7700. [CrossRef]
  • Schmelzer J.,Niederbroecker H.,Partzsch S.,Voeckler R.,Meinhardt R. (1996) Isothermal vapor-liquid equilibria in binary mixtures containing hydrocarbons (nonane, decane, dodecane, butylbenzene, or 2-methylnaphthalene) and phenol or cresols (2-methylphenol or 3- methylphenol) at 373 to 453 K, Int. Electron. J. Phys.-Chem. Data 2, 153-162.
  • Selleck F.T.,Carmichael L.T.,Sage B.H. (1952) Phase behaviour in the Hydrogen Sulfide-Water System, Ind. Eng. Chem. 44, 9, 2219-2226. [CrossRef]
  • Sidgwick V.,Spurrell W.J.,Davies T.E. (1915) The solubility of the nitrophenols and other isomeric di-substitution products of benzene, J. Chem. Soc. 107, 1202-1213. [CrossRef]
  • Simnick J.J.,Sebastian H.M.,Lin H.-M.,Chao K.-C. (1979) Fluid Phase Equilibr. 3, 145. [CrossRef]
  • Suresh J.,Beckman E.J. (1994) Prediction of liquid-liquid equilibria in ternary systems from binary data, Fluid Phase Equilibr. 99, 219-240. [CrossRef]
  • Suresh S.J.,Elliott J.R. (1992) Multiphase equilibrium analysis via a generalized equation of state for associating mixtures, Ind. Eng. Chem. Res. 31, 2783-2794. [CrossRef]
  • Sørensen J.M., Arlt W. (1980) Liquid – liquid equilibrium data collection, (Binary Systems), DECHEMA Chemistry Data Series, Frankfurt, 1980, Vol. 5, Part. 1.
  • Varhanickova D., Shiu W., Mackay D. (1996) Aqueous Solubilities of Alkylphenols and Methoxyphenols at 25 C, J. Chem. Eng. Data 40, 448-451. [CrossRef]
  • Von Solms N.,Michelsen M.L.,Kontogeorgis G.M. (2004) Applying association theories to polar fluids, Ind. Eng. Chem. Res. 43, 7, 1803-1806. [CrossRef]
  • Voutsas E.C.,Yakoumis I.V.,Tassios D.P. (1999) Prediction of phase equilibria in water/alcohol/alkane systems, Fluid Phase Equilibr. 158, 151-163. [CrossRef]
  • Voutsas E.,Perakis C.,Pappa G.,Tassios D.P. (2007) An evaluation of the performance of the Cubic-Plus-Association equation of state in mixtures of non-polar, polar and associating compounds: towards a single model for non-polymeric systems, Fluid Phase Equilibr. 261, 343-350. [CrossRef]
  • Walsh J.M.,Ikonomou G.D.,Donohue M.D. (1987) Fluid Phase Equilibr. 33, 295. [CrossRef]
  • Wolbach J.P.,Sandler S.I. (1997) Using molecular orbital calculations to describe the phase behaviour of hydrogen-bonding fluids, Ind. Eng. Chem. Res. 36, 4041-4051. [CrossRef]
  • Wolbach J.P., Sandler S.I. (1998) Using molecular orbital calculations to describe the phase behaviour of cross-associating mixtures Ind. Eng. Chem. Res. 37, 2917-2928.
  • Yoon et al. (1993) J. Chem. Eng. Data 38, 53.

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