Dossier: Chemical Reactors, from Mock-up to Industriel Reactor: Diagnostic Methods - Rencontres Scientifiques IFP, Solaize, Dec. 1999
Open Access
Numéro
Oil & Gas Science and Technology - Rev. IFP
Volume 55, Numéro 2, March-April 2000
Dossier: Chemical Reactors, from Mock-up to Industriel Reactor: Diagnostic Methods - Rencontres Scientifiques IFP, Solaize, Dec. 1999
Page(s) 187 - 207
DOI https://doi.org/10.2516/ogst:2000012
Publié en ligne 1 octobre 2006
  • Avidan, A.,Edwards, M. and Owen, H. (1990) Innovative Improvements Highlight FCC’s Past and Future. Oil & Gas J., 88, 2, 33-58. [Google Scholar]
  • Reichle, A.D. (1992) Fluid Catalytic Cracking Hits 50 Year Mark on the Run. Oil & Gas J., special issue, May 18, 41-45. [Google Scholar]
  • Murphy, J.R. (1992) Evolutionary Design Changes Mark FCC Process. Oil & Gas J., special issue, May 18, 49-58. [Google Scholar]
  • Avidan, A. (1992) FCC is Far From Being a Mature Technology. Oil & Gas J., special issue, May 18, 59-66. [Google Scholar]
  • Murcia, A.M. (1992) Numerous Changes Mark FCC Technology Advance. Oil & Gas J., special issue, May 18, 68-71. [Google Scholar]
  • Jahnig, C.E., Martin, H.Z. and Campbell, D.L. (1984) The Development of Fluid Catalytic Cracking. Chemtech, Feb., 106-112. [Google Scholar]
  • Dean, R.R., Mauleon, J.L. and Letzsch, W.S. (1982) New Resid Cracker. Oil & Gas J., special issue, part 1, 80, 40, 75-80; part 2, 80, 41, 168-176. [Google Scholar]
  • Marcilly, C.R. and Bonifay, R.R. (1996) Catalytic Cracking of Resid Feedstocks. Arab. J. Sci. Eng., 21 (4B), 627-651. [Google Scholar]
  • Johnson, A.R., Letzsch, W.L. and Silverman, M.A. (1994) Upgrade Residues with FCCU’s Designed for High Severity Operation. Fuel Reformul., Nov.-Dec., 61-65. [Google Scholar]
  • Avidan, A.A., Owen, H. and Schipper, P. (1990) FCC Closed Cyclone System. Oil & Gas J., March 26, 56-62. [Google Scholar]
  • Galtier, P., Pontier, R. and Patureaux, T. (1989) Near Full Scale Cold Flow Model for the R2R Catalytic Process. Proceedings of the 6th Fludization Conference, Banff, Canada, Engineering Foundation, New York, 17-23. [Google Scholar]
  • Maul议, J.L. and Sigaud, J.B. (1987) Mix Temperature Control Enhances FCC. Oil & Gas J., Feb. 23, 52-55. [Google Scholar]
  • Heinrich, G., Gauthier, T.A. and Del Pozo, M. (1997) R2R, a Suite of Technologies for Residue Catalytic Cracking. Upgrading Heavy Ends with IFP: 30th anniversary CEDI Ren笎avarre, IFP, Rueil-Malmaison, France, 113-125. [Google Scholar]
  • Gauthier, T.A. and Bonifay, R.R. (1999) Catatalytic Cooler Scale-up and Operation. Proceedings of the 2nd European Congress of Chemical Engineering conference, Montpellier, France, October 5-7. [Google Scholar]
  • Gauthier, T.A. and Ross, J. (1999) Controling Gas Flow in Standpipe Systems. Proceedings of the 6th International Conference on Circulating Fluidized Beds, Würzburg, Germany, August 22-27, Dechema, Frankfurt am Main, Germany, 483-488. [Google Scholar]
  • King, D., Forde, R., Leaney P. and Zenz, F. (1989) FCC Cold Modeling Helps Solve FCC Standpipe Flow. Proceedings of the 6th Fluidization Conference, Banff, Canada, Engineering Foundation, New York, 145-152. [Google Scholar]
  • Jones, P.J. and Leung, L.S. (1985) Downflow of Solids Through Pipes and Valves. Fluidization, 2nd ed., Davidson, J.F., Clift, R. and Harrisson, D. (eds.), Academic Press. [Google Scholar]
  • Karri, R.S.B. and Knowlton, T.M. (1993) The Effect of Fines Content on the Flow of FCC Catalyst in Standpipes. Proceedings of the 4th International Conference on Circulating Fluidized Beds, Hidden Valley Conference and Mountain Resort Somerset, Pennsylvania, USA, Avidan, A. (ed.), 490-493. [Google Scholar]
  • Mott, R.W. (1992) Troubleshooting FCC Standpipe Flow Problems. Davidson Catagram, 83, 25-35. [Google Scholar]
  • Abrahmsen, A.R. and Geldart, D. (1980) Behaviour of Gaz- Fluidized Beds of Fine Powders. Powder Technol., 26, 35-46. [CrossRef] [Google Scholar]
  • Kuipers, J.A.M. and Van Swaaij, W.P.M. (1998) CFD Applied to Chemical Reaction Engineering. Adv. Chem. Eng., 24, 227-327. [Google Scholar]
  • Ferschneider, G. and M禥, P. (1996) Eulerian Simulation of Dense Phase Fluidized Beds. Revue de l’Institut français du pétrole, 51, 2, 301-307. [Google Scholar]
  • Boelle, A. (1997) Validation d’un modèle à deux fluides appliqué à la simulation des lits fluidisés denses. Thèse, Paris VI. [Google Scholar]
  • Patureaux, T. and Barthod, D. (2000) These proceedings. [Google Scholar]
  • Fiorentino, M. and Newton, D. (1998) Application of X-Ray Imaging to Fluidized Bed Scale-up. Proceedings of the 9th Fluidization Conference, Durango, Colorado, Engineering Foundation, New York, 589-596. [Google Scholar]
  • Werther, J.,Hartge, E.U. and Rensner, D. (1993) Measurement Techniques for Gas-Solid Fluidized Beds Reactors. Int. Chem. Eng., 33, 1, 18-26. [Google Scholar]
  • Herbert, P.M., Gauthier, T.A., Briens, C.L. and Bergougnou M.A. (1994) Application of Optic Fiber Probes to the Measurement of Local Particle Velocity and Concentration in Gas-Solid Flow. Powder Technol., 80, 243-252. [CrossRef] [Google Scholar]
  • Taxil, I.P., Guigon, P., Archimbault, F. and Gauthier, T.A. (1998) Gas Flow Characterization in Turbulent Fluidization for FCC Catalyst. Proceedings of the 9th Fluidization Conference, Durango, Colorado, Engineering Foundation, New York, 69-76. [Google Scholar]
  • Smith, M., Bayle, J. and Gauthier, T.A. (1999) Bubble Flow Study in a Turbulent FCC Fluidized Bed. Proceedings of the 2nd European Congress of Chemical Engineering Conference, Montpellier, France, October 5-7. [Google Scholar]
  • Derouin, C.,Nevicato, D.,Forissier, M.,Wild, G. and Bernard, J.R. (1997) Hydrodynamics of Riser Units and their Impact on FCC Operation. Ind. Eng. Chem. Res., 36, 11, 4504-4516 [CrossRef] [Google Scholar]
  • Knowlton, T.M., Hirsan, I. and Leung, L.S. (1978) The Effect of Aeration Tap Location on a Non-Mechanical J-Valve. Proceedings of the International Fluidization Conference, Cambridge, Davidson, J.F. (ed.), University Press, Cambridge. [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.