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Accueil Tous les numéros Volume 72 / Numéro 1 (January–February 2017) Oil Gas Sci. Technol. – Rev. IFP Energies nouvelles, 72 1 (2017) 2 Références
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Numéro
Oil Gas Sci. Technol. – Rev. IFP Energies nouvelles
Volume 72, Numéro 1, January–February 2017
Numéro d'article 2
Nombre de pages 11
DOI https://doi.org/10.2516/ogst/2016023
Publié en ligne 26 janvier 2017
  • Cai H.Y., Shaw J.M., Chung K.H. (2001) Hydrogen solubility measurements in heavy oil and bitumen cuts, Fuel 80, 8, 1055–1063. [CrossRef] [Google Scholar]
  • Carreón-Calderón B., Uribe-Vargas V., Ramírez-Jaramillo E., Ramírez-de-Santiago M. (2012) Thermodynamic characterization of undefined petroleum fractions using group contribution methods, Ind. Eng. Chem. Res. 51, 43, 14188–14198. [CrossRef] [Google Scholar]
  • Carreón-Calderón B., Uribe-Vargas V., Ramírez-de-Santiago M., Ramírez-Jaramillo E. (2014) Thermodynamic characterization of heavy petroleum fluids using group contribution methods, Ind. Eng. Chem. Res. 53, 13, 5598–5607. [CrossRef] [Google Scholar]
  • Chávez L.M., Alonso F., Ancheyta J. (2014) Vapor-liquid equilibrium of hydrogen-hydrocarbon systems and its effects on hydroprocessing reactors, Fuel 138, 156–175. [CrossRef] [Google Scholar]
  • Chen J., Mulgundmath V., Wang N. (2011) Accounting for vapor-liquid equilibrium in the modeling and simulation of a commercial hydrotreating reactor, Ind. Eng. Chem. Res. 50, 1571–1579. [CrossRef] [Google Scholar]
  • Connolly J.F., Kandalic G.A. (1986) Gas solubilities, vapor-liquid equilibria, and partial molal volumes in some hydrogen-hydrocarbon systems, J. Chem. Eng. Data 31, 4, 396–406. [CrossRef] [Google Scholar]
  • Deiters U.K. (2013) Comments on the modeling of hydrogen and hydrogen-containing mixtures with cubic equations of state, Fluid Phase Equilib. 352, 93–96. [CrossRef] [Google Scholar]
  • Elbro H.S., Fredenslund A., Rasmussen P. (1991) Group contribution method for the prediction of liquid densities as a function of temperature for solvents, oligomers, and polymers, Ind. Eng. Chem. Res. 30, 12, 2576–2582. [CrossRef] [Google Scholar]
  • Firoozabadi A. (1988) Reservoir-Fluid Phase Behavior and Volumetric Prediction With Equations of State (includes associated papers 18400 and 18579), J. Petrol. Technol. 40, 397–406. [CrossRef] [Google Scholar]
  • 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 modeling, AIChE J. 49, 12, 3260–3269. [CrossRef] [Google Scholar]
  • Hook B.D. (1985) Effect of feed volatility on conversion in trickle bed reactors, Ind. Eng. Chem. Fundam. 24, 3, 398–401, Available at: http://www.scopus.com/inward/record.url?eid=2-s2.0-0022110777&partnerID=40&md5=a9e63ff4de18848d030986e035bd2866. [CrossRef] [Google Scholar]
  • Horstmann S., Jabłoniec A., Krafczyk J., Fischer K., Gmehling J. (2005) PSRK group contribution equation of state: comprehensive revision and extension IV, including critical constants and α-function parameters for 1000 components, Fluid Phase Equilib. 227, 2, 157–164. [CrossRef] [Google Scholar]
  • Ihmels E.C., Gmehling J. (2003) Extension and revision of the group contribution method GCVOL for the prediction of pure compound liquid densities, Ind. Eng. Chem. Res. 42, 2, 408–412. [CrossRef] [Google Scholar]
  • Jaubert J.N., Privat R., Mutelet F. (2010) Predicting the phase equilibria of synthetic petroleum fluids with the PPR78 approach, AIChE J. 56, 12, 3225–3235. [CrossRef] [Google Scholar]
  • Ji S., Wang Z., Guo A., Zhou Y., Chen K. (2013) Determination of hydrogen solubility in heavy fractions of crude oils by a modified direct method, J. Chem. Eng. Data 58, 12, 3453–3457. [CrossRef] [Google Scholar]
  • Joback K.G., Reid R.C. (1987) Estimation of pure-component properties from group-contributions, Chem. Eng. Commun. 57, 1-6, 233–243. [CrossRef] [Google Scholar]
  • Lal D., Otto F.D., Mather A.E. (1999) Solubility of hydrogen in Athabasca bitumen, Fuel 78, 12, 1437–1441. [CrossRef] [Google Scholar]
  • Lee B.I., Kesler M.G. (1975) A Generalized Thermodynamic Correlation Based on Three-Parameter Corresponding, AIChE J. 21, 3, 510–527. [CrossRef] [Google Scholar]
  • Lin H.M., Kim H., Guo T., Chao K.C. (1985) Equilibrium vaporization of a coal liquid from a Kentucky No. 9 coal, Ind. Eng. Chem. Process Des. Dev. 24, 1049–1055. [CrossRef] [Google Scholar]
  • Marrero J., Gani R. (2001) Group-contribution based estimation of pure component properties, Fluid Phase Equilib. 183-184, 183–208. [CrossRef] [Google Scholar]
  • Michelsen M.L. (1990) A modified Huron-Vidal mixing rule for cubic equations of state, Fluid Phase Equilib. 60, 1-2, 213–219. [CrossRef] [Google Scholar]
  • Nichols W.B., Reamer H.H., Sage B.H. (1957) Volumetric and phase behavior in the hydrogen-n-hexane system, AIChE J. 3, 2, 262–267. [CrossRef] [Google Scholar]
  • 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] [Google Scholar]
  • Pedersen K.S., Milter J., Sørensen H. (2004) Cubic equations of state applied to HT/HP and highly aromatic fluids, SPE J. 9, 186–192. [CrossRef] [Google Scholar]
  • Pellegrini L.A., Gamba S., Calemma V., Bonomi S. (2008) Modelling of hydrocracking with vapour - liquid equilibrium, Chem. Eng. Sci. 63, 4285–4291. [CrossRef] [Google Scholar]
  • Peng D.-Y., Robinson D.B. (1976) A new two-constant equation of state, Ind. Eng. Chem. Fundam. 15, 1, 59–64. [CrossRef] [Google Scholar]
  • Privat R., Jaubert J.N. (2013) Classification of global fluid-phase equilibrium behaviors in binary systems, Chem. Eng. Res. Des. 91, 10, 1807–1839. [CrossRef] [Google Scholar]
  • Qian J.W., Jaubert J.N., Privat R. (2013) Phase equilibria in hydrogen-containing binary systems modeled with the Peng-Robinson equation of state and temperature-dependent binary interaction parameters calculated through a group-contribution method, J. Supercrit. Fluids 75, 58–71. [CrossRef] [Google Scholar]
  • Saajanlehto M., Uusi-Kyyny P., Alopaeus V. (2014) Hydrogen solubility in heavy oil systems: experiments and modeling, Fuel 137, 393–404. [CrossRef] [Google Scholar]
  • Uribe-Vargas V., Carreón-Calderón B., Ramírez-Jaramillo E., Ramírez-de-Santiago M. (2016) Thermodynamic characterization of undefined petroleum fractions of gas condensate using group contribution, Oil Gas Sci. Technol. - Rev. IFP 71, 1, 5. [CrossRef] [EDP Sciences] [Google Scholar]
  • Xu X., Jaubert J.-N., Privat R., Duchet-Suchaux P., Braña-Mulero F. (2015) Predicting binary-interaction parameters of cubic equations of state for petroleum fluids containing pseudo-components, Ind. Eng. Chem. Res. 54, 10, 2816–2824. [CrossRef] [Google Scholar]
  • Young C.L. (1981) Hydrogen and Deuterium (Solubility Data Series), Pergamon Press, Australia, pp. 314–321. [Google Scholar]

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