Open Access
Oil Gas Sci. Technol. – Rev. IFP Energies nouvelles
Volume 72, Number 1, January–February 2017
Article Number 2
Number of page(s) 11
Published online 26 January 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: [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. [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]

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.