Dossier: InMoTher 2012 - Industrial Use of Molecular Thermodynamics
Open Access
Issue
Oil Gas Sci. Technol. – Rev. IFP Energies nouvelles
Volume 68, Number 2, March-April 2013
Dossier: InMoTher 2012 - Industrial Use of Molecular Thermodynamics
Page(s) 217 - 233
DOI https://doi.org/10.2516/ogst/2012061
Published online 23 April 2013
  • Cai H.Y., Shaw J.M., Chung K.H. (2001) Hydrogen solubility measurements in heavy oil and bitumen cuts, Fuel 80, 1055-1063. [CrossRef]
  • Chao K.C., Seader J.D. (1961) A general correlation of vapor-liquid equilibria in hydrocarbon mixtures, AIChE J. 7, 4, 598-605. [CrossRef]
  • de Hemptinne J.C., Ledanois J.M., Mougin P., Barreau A. (2012) Select Thermodynamic Models for Process Simulation, Editions Technip, Paris.
  • Ferrando N., Ungerer P. (2007) Hydrogen/hydrocarbon phase equilibrium modeling with a cubic equation of state and a Monte Carlo method, Fluid Phase Equilib. 254, 1-2, 211-223. [CrossRef]
  • Florusse L.J., Peters C.J., Pàmies J.C., Vega L.F., Meijer H. (2003) Solubility of hydrogen in heavy n-alkanes: Experiments and SAFT modelling, AIChE J. 49, 12, 3260-3269. [CrossRef]
  • Grayson H.G., Streed C.W. (1963) Vapor-liquid equilibria for high temperature, high pressure hydrogen-hydrocarbon systems, 6th World Petroleum Congress, Frankfurt am Main, Germany, 19-26 June, pp. 169-181.
  • Hildebrand, J.H., (1916) Solubility. Journal of the American Society 38, 8, 1452-1473. [CrossRef]
  • Huang, H.H., Lin, H.M., Tsai, F.N., Chao, K.C. (1988) Solubility of Synthesis Gases in Heavy n-Paraffins and Fischer-Tropsch Wax, Ind. Eng. Chem. Res. 27, 1, 162-169. [CrossRef]
  • Le Thi, C., Tamouza, S., Passarello, J.P., Tobaly, P., de Hemptinne, J.C. (2006) Modeling Phase Equilibrium of H2 + n-Alkane and CO2 + n-Alkane Binary Mixtures Using a Group Contribution Statistical Association Fluid Theory Equation of State (GC-SAFT-EOS) with a kij Group Contribution Method, Ind. Eng. Chem. Res. 45, 20, 6803-6810. [CrossRef]
  • Lin H.M., Sebastian H.M., Chao K.C. (1980a) Gas-Liquid Equilibrium in Hydrogen + n-Hexadecane and Methane + n-Hexadecane at Elevated Temperatures and Pressure, J. Chem. Eng. Data 25, 3, 252-254. [CrossRef]
  • Lin, H.M., Sebastian, H.M., Chao, K.C. (1980b) Gas-Liquid Equilibria of Hydrogen + 1-Mehtyl Naphthalene at 457°C, Fluid Phase Equilib. 4, 321. [CrossRef]
  • Lin H.M., Sebastian H.M., Simnick J.J., Chao K.C. (1981) Solubiilties of Hydrogen and Methane in Coals Liquids, Ind. Eng. Chem. Process Des. Dev. 20, 2, 253-256. [CrossRef]
  • Malone P.V., Kobayashi R. (1990) Ligth Gas Solubility in Phenanthrene: The Hydrogen-Phenanthrene and Methane- Phenanthrene, Fluid Phase Equilib. 55, 193-205. [CrossRef]
  • Moysan J.M., Huron J.M., Paradowski H., Vidal J. (1983) Prediction of the solubility of hydrogen in hydrocarbon solvents through cubic equation of state, Chem. Eng. Sci. 38, 7, 1085-1092. [CrossRef]
  • Park J., Robinson R.L., Gasem K.A.M. (1995) Solubilities of Hydrogen in Heavy Normal Paraffins at Temperatures from 323.2 to 423.2 K and Pressure to 17.4 MPa, J. Chem. Eng. Data 40, 1, 241-244. [CrossRef]
  • Park J., Robinson R.L., Gasem K.A.M. (1996) Solubilities of Hydrogen in Aromatic Hydrocarbons from 323 to 433 K and Pressures to 21.7 MPa, J. Chem. Eng. Data 41, 1, 70-73. [CrossRef]
  • Riazi M.R. (2005) Charaterization and Properties of Petroleum Fractions, ASTM International, Conshohocken, PA, 1st Edition.
  • Riazi M.R., Al-Sahhaf T.A. (1996) Physical Properties of Heavy Petroleum Fractions and Crude Oils, Fluid Phase Equilib. 117, 271-224. [NASA ADS] [CrossRef] [PubMed]
  • Riazi M.R., Vera J.H. (2005) Method to Calculate the Solubilities of Light Gases in Petroleum and Coal Liquid Fractions on the Basis of Their P/N/A Composition, Ind. Eng. Chem. Res. 44, 1, 186-192. [CrossRef]
  • Riazi M.R., Roomi Y.A. (2007) A method to predict solubility of hydrogen in hydrocarbons and their mixtures, Chem. Eng. Sci. 62, 6649-6658. [CrossRef]
  • Robinson R.L., Chao K.C. (1971) A Correlation of Vaporization Equilibrium Ratios for Gas Processing Systems, Ind. Eng. Chem. Process Des. Dev. 10, 2, 221-229. [CrossRef]
  • Scatchard G. (1931) Equilibria in Non-Electrolyte Solutions in Relation to the Vapor Pressure and Densities of the Components, Chemical Reviews 8, 2, 321-333. [CrossRef]
  • Scatchard G., Hildebrand J.H. (1934) Non-Electrolyte Solutions, Journal of the American Society 54, 4, 995-996. [CrossRef]
  • Sebastian H.M., Simnick J.J., Lin H.M., Chao K.C. (1980) Gas- Liquid Equilibrium in the Hydrogen + n-Decane System at Elevated Temperatures and Pressures, J. Chem. Eng. Data 25, 1, 68-70. [CrossRef]
  • Shaw J.M. (1987) A Correlation for Hydrogen Solubility in Alicyclic and Aromatic Solvents, Can. J. Chem. Eng. 65, 293-298. [CrossRef]
  • Smith J.M., Van Ness H.C., Abott M.M. (1996) Introduction to Chemical Engineering Thermodynamics, McGraw-Hill, New York, 5th Edition.
  • Srinivas G., Field R., Watanasiri S., Herzog H. (2012) Correlation to predict solubility of hydrogen and carbon monoxide in heavy paraffins, Fluid Phase Equilib. 320, 11-25. [CrossRef]
  • Tran T.K.S., NguyenHuynh D., Ferrando N., Passarello J.P., de Hemptinne J.C., Tobaly P. (2009) Modeling VLE of H2 + Hydrocarbon Mixtures Using a Group Contribution SAFT with kij Correlation Method Based on London’s Theory, Energy Fuels 23, 2658-2665. [CrossRef]
  • Twu C.H., Coon J.E., Harvey A.H., Cunningham J.R. (1996) An Approach for the Application of a Cubic Equation of State to Hydrogen-Hydrocarbon Systems, Ind. Eng. Chem. Res. 35, 3, 905-910. [CrossRef]
  • Walas M.W. (1985) Phase Equilibria in Chemical Engineering, Butterworth-Heinemann, Massachusetts.
  • Yao, J., Sebastian, H.M., Lin, H.M., Chao, K.C. (1977-1978) Gas- Liquid Equilibria in Mixtures of Hydrogen and 1-Methyl Naphthalene, Fluid Phase Equilib. 1, 4, 293-304. [CrossRef]
  • Zernov V.S., Kogan V.B., Egudina O.G., Kobyakov V.M., Babayants T.V., Kalichava L.I. (1990) Phase Equilibria and Volume Ratios in the Systems Heptane and Ethylene, J. Appl. Chem. USSR 63, 7, 1469-1472.

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.