Open Access
Numéro
Oil & Gas Science and Technology - Rev. IFP
Volume 55, Numéro 1, January-February 2000
Page(s) 87 - 121
DOI https://doi.org/10.2516/ogst:2000005
Publié en ligne 1 novembre 2006
  • Botton, R. (1970) Gas Solid Contacting in Fluidized Beds. AIChE Symp. Series, 66, 101, 8-18. [Google Scholar]
  • Botton, R. (1980) Réacteurs à lit fluidisé gaz/solide à haut taux de conversion, miniaturisation de l’échelle pilote. Contrat DGRST (France) Annexes du rapport, n° 77, 7-1614 (82 pages). [Google Scholar]
  • Botton, R.,Bergougnou, M.A. et Vergnes, F. (1995) High Performance Catalytic Fluidized Bed Reactors. Direct Scale-Up from Laboratory Data (Conversion and Selectivity). Fundamentals about Phenomenological and Bubble Models. Proc. of 8th Intern. Conf. on Fluid. Engineering Foundation, Tours, Preprints, 1, 585-592. [Google Scholar]
  • Botton, R., Laguerie, C. et Vergnes, F. (1985) Lits fluidisés catalytiques à haut taux de conversion - Simulation au laboratoire. Journées européennes de fluidisation de Toulouse, 18-20 sept., 424-432. [Google Scholar]
  • Botton, R. et Vergnes, F. (1981) Catalytic Fluidized Reactor Scale-Up. An Approach from Chemical and Specifically Physical Laboratory Data Without the Need of a Pilot Plant Stage. Chem. Ing. Techn., 11, 481 et VDI Bericht, 409, 567-587. [Google Scholar]
  • Botton, R., Vergnes, F. et Bergougnou, M.A. (1983) Validation by Means of Industrial Data of Kunii-Levenspiel Models which Can be Used in the Scale-Up to Commercial Size of Fluidised Bed Reactors. Proc. of 4th Inter. Conf. on Fluid. Engineering Foundation, Kashikojima, 851-858. [Google Scholar]
  • Chiba, T. et Kobayashi, N. (1970) Chem. Eng. Sci., 25, 1375. [CrossRef] [Google Scholar]
  • Colburn, A.P. (1930) Relation between Mass Transfer and Fluid Friction. Industrial and Engineering Chemistry, 22, 9, 967-970. [Google Scholar]
  • Davidson, J.F. et Harrison, D. (1963) Fluidised Particles, Cambridge University Press. [Google Scholar]
  • Davidson, J.F. et Harrison, D. (1971) Fluidization, Academic Press. Davies, L. et Richardson, J.F. (1966) Trans. Instr. Chem. Eng., 44, T293. [Google Scholar]
  • Davies, R.M. et Taylor, G. (1950) The Mechanics of Large Bubbles Rising through Extended Liquids in Tubes. Proc. Roy. Soc., A 200, 375. [Google Scholar]
  • De Vries, R.J., Van Swaaij, W.P.M.,Mantoni, C. et Heijkoop, A. (1972) Design Criteria and Performance of the Commercial Reactor for the Shell Chlorine Process. Proc. of the 5th European Symp. on Chem. Reaction Engineering, Amsterdam, B9, 59-69. [MathSciNet] [Google Scholar]
  • Drinkenburg, A.A.H. et Rietema, K. (1972) Gas Transfer from Bubbles in a Fluidized Bed to the Dense Phase-1 Theory. Chem. Eng. Sci., 27, 1765-1774. [Google Scholar]
  • Geldart, D. (1973) Powder Technology, 7, 285-292. [Google Scholar]
  • Gilliland, E.R. et Mason, E.A. (1949) Gas and Solid Mixing in Fluidized Beds. Ind. Eng. Chem., 41, 6, 1191-1196. [Google Scholar]
  • Guedes de Carvalho, J.R.F. et Harrison, D. (1975) Mass Transfer from a Slug to a Fluidized Bed. Proc. of First Intern. Conf. on Fluid. Engineering Foundation, 245. [Google Scholar]
  • Higbie, R. (1935) Trans. Am. Instr. Chem. Eng., 31, 365. [Google Scholar]
  • Jackson, R. (1963) Trans. Instr. Chem. Eng., 41, 22. [Google Scholar]
  • Kunii, D. et Levenspiel, O. (1968) Bubbling Bed Model. Ind. Eng. Fund., 7, 6, 441-451. [Google Scholar]
  • Kunii, D. et Levenspiel, O. (1969) Fluidization Engineering, Wiley. [Google Scholar]
  • Kunii, D. et Levenspiel, O. (1993) Fluidization Engineering, Butterworth-Heinmann. [Google Scholar]
  • Matheson, G.L.,Herbst, W.A. et Holt, P.H. (1949) Caracteristics of Fluid and Solid Systems. Ind. Eng. Chem., 41, 6, 1089-1100. [Google Scholar]
  • Matsen, J.M. (1970) Expansion of Fluidized Beds in Slug Flow. AIChE, Symp. Series, 66, 101, 47-51. [Google Scholar]
  • Matsen, J.M. (1973) Evidence of Maximum Bubble Size in a Fluidized Bed. AIChE, Symp. Series, 69, 126, 30-33. [Google Scholar]
  • May, W.G. (1959) Fluidized Bed Reactors Studies. Chem. Eng. Prog., 55, 12, 49-55. [Google Scholar]
  • Miyauchi, T., Furusaki, S, Morooka, S. et Ikeda, Y. (1981) Transport Phenomena and Reaction in Fluidized Catalytic Beds. Advances in Chemical Engineering, 11, Academic Press, New York. [Google Scholar]
  • Murray, J.D. (1965) J. Fluid. Mech., 21, 465 et 2257. [CrossRef] [MathSciNet] [Google Scholar]
  • Nicklin, D.J. (1962) Two-Phase Bubble Flow. Chem. Eng. Sci., 17, 693. [Google Scholar]
  • Partridge, B.A. et Rowe, P.N. (1966) Trans. Instr. Chem. Eng., 44, 335. [Google Scholar]
  • Rietema, K. et Hoebink, J., (1975) Mass Transfer from Single Rising Bubbles to the Dense Phase in Three Dimensional Fluidized Bed. Fluidization Technologie, D.L. Keairns (éd.), Mc Graw Hill, 1, 279. [Google Scholar]
  • Rowe, P.N. (1964) Chem. Eng. Prog., 60, 75. [CrossRef] [Google Scholar]
  • Rowe, P.N. (1965) Trans. Instn. Chem. Engrs., 43, T157 [Google Scholar]
  • Rowe, P.N. (1976) Prediction of Bubble Size in a Gas Fluidised Bed. Chem. Eng. Sci., 31, 285-288. [Google Scholar]
  • Rowe, P.N.,Evans, T.J. et Middleton, J.C. (1971) Chem. Eng. Sci., 26, 11, 1943. [CrossRef] [Google Scholar]
  • Rowe, P.N. et Partridge, B.A. (1962) Proceeding of the Symposium on the Interaction between Fluids and Particules. Inst. Chem. Eng., 135, In Rotenburg, P.A. (Edit.). [Google Scholar]
  • Schugerl, K. (1971) Chap. 6 in Fluidization. Academic Press, Londres, 261-292. [Google Scholar]
  • Stewart, et Davidson, J.F. (1967) Slug Flow in Fluidised Beds. Powder Technology, 1, 61-80. [CrossRef] [Google Scholar]
  • Toei, R. et Matsuno, R. (1969) Int. Chem. Eng., 9, 358. [Google Scholar]
  • Van Deemter, J.J. (1961) Mixing and Contacting in Gas-Solid Fluidized Beds. Chem. Eng. Sci., 13, 143-154. [Google Scholar]
  • Walker, B.V. (1975) Trans. Instr. Chem. Eng., 53, 255. [Google Scholar]
  • Werther, J. (1974) Bubbles in Gas-Fluidized Beds. Trans. Instr. Chem. Eng., 52, 149-168. [Google Scholar]
  • Werther, J. (1980) Modeling and Scale-up of Industrial Fluidized Bed Reactors. Chem. Eng. Sci., 35, 372-379. [Google Scholar]
  • Yerushalmi, J.,Turner, D.H. et Squires, A.M. (1976) The Fast Fluidized Bed. Ind. Eng. Process Des. Dev., 15,1, 147-152. [Google Scholar]

Les statistiques affichées correspondent au cumul d'une part des vues des résumés de l'article et d'autre part des vues et téléchargements de l'article plein-texte (PDF, Full-HTML, ePub... selon les formats disponibles) sur la platefome Vision4Press.

Les statistiques sont disponibles avec un délai de 48 à 96 heures et sont mises à jour quotidiennement en semaine.

Le chargement des statistiques peut être long.