Description of Simplified Models

  • Robert W. Lyczkowski
  • Walter F. Podolski
  • Jacques X. Bouillard
  • Stephen M. Folga
Chapter
Part of the SpringerBriefs in Applied Sciences and Technology book series (BRIEFSAPPLSCIENCES)

Abstract

This section summarizes the simplified monolayer energy dissipation (MED) erosion model and a suggested empirical complementary approach that relies upon data correlations. Also included is a brief description of the input parameters required for each approach.

Keywords

Metal wastage Monolayer energy dissipation Correlations Erosion models Scaling parameters Operating parameters Design parameters Hydrodynamics 

References

  1. 1.
    R.W. Lyczkowski, J.X. Bouillard, Scaling and guidelines for erosion in fluidized beds. Powder Technol. 125, 217–225 (2002)CrossRefGoogle Scholar
  2. 2.
    F.W. Staub, Solids circulation in turbulent fluidized beds and heat transfer to immersed tube banks. ASME. J. Heat Transfer 70(3), 391–396 (1979). AugCrossRefGoogle Scholar
  3. 3.
    S.L. Soo, A note on moving dust particles. Powder Technol. 77, 259–263 (1977)CrossRefGoogle Scholar
  4. 4.
    R.T. Wood, D.A. Woodford, Tube Erosion in Fluidized Beds, General. (Electric Co. Report 11/ET-FUC79, U.S. Energy Research and Development Administration Report 81-12, Dec 1980)Google Scholar
  5. 5.
    R.R. Gansley, T.J. O’Brien, A model for bubble-induced erosion in fluidized-bedcombustors and comparison with experiment. Wear 137, 107–127 (1990)CrossRefGoogle Scholar
  6. 6.
    R.W. Lyczkowski, J.X. Bouillard, D. Gidaspow, G.F. Berry, Computer Modeling ofErosion in Fluidized Beds. (Argonne National Laboratory Report ANL/ESD/TM-1, Argonne, IL, July 1986, Jan 1990)Google Scholar
  7. 7.
    M.J. Parkinson, A.W. Jury, B.A. Napier, T.J. Kempton, J.C. Holder, Cold Model Erosion Studies in Support of Pressurized Fluidized Bed Combustion. (Electric Power Research Institute Draft Final Report for Project 1337-2, April 1986)Google Scholar
  8. 8.
    J.X. Bouillard, R.W. Lyczkowski, S. Folga, D. Gidaspow, G.F. Berry, Hydrodynamics of erosion of heat exchanger tubes in fluidized-bed combustors. Can. J. Chem. Eng. 67, 218–229 (1989)CrossRefGoogle Scholar
  9. 9.
    J.X. Bouillard, R.W. Lyczkowski, On the erosion of heat exchanger tube banks in fluidized-bed combustors. Powder Technol. 68, 37–51 (1991)CrossRefGoogle Scholar
  10. 10.
    R.W. Lyczkowski, S. Folga, S.L. Chang, J.X. Bouillard, C.S. Wang, G.F. Berry, D.Gidaspow, State-of-the-Art Computation of Dynamics and Erosion in Fluidized Bed Tube Banks, ed.by A.M. Manaker in Proceedings of the 10th International Conference on Fluidized Bed Combustion, Vol. 1, (American Society of Mechanical Engineers, NY 1989) pp. 465–478Google Scholar
  11. 11.
    R.W. Lyczkowski, J.X. Bouillard, State-of-the-art review of erosion modeling in fluid/solids systems. Prog. Energy Combust. Sci. 28(6), 543–602 (2002)CrossRefGoogle Scholar
  12. 12.
    J.G. Yates, On the erosion of metal tubes in fluidized beds. Chem. Eng. Sci. 42, 379–380 (1987)CrossRefGoogle Scholar
  13. 13.
    E.K. Levy, J.W. Stallings, Tube Erosion in Bubbling Fluidized Beds, ed.by E.J. Anthony. 11th Conference on Fluidized Bed Combustion, Vol. 3, (American Society of Mechanical Engineers, NY 1991) pp. 1139–1144Google Scholar
  14. 14.
    J. Zhu, Tube Erosion in Fluidized Beds, Ph.D Thesis, Department of Chemical Engineering, The University of British Columbia, 1988Google Scholar
  15. 15.
    J. Zhu, C.J. Liu, J.R. Grace, J.A. Lund, Tube wear in gas fluidized beds–11. Low-velocity impact erosion and semi-empirical model for bubbling and slugging fluidizedbeds. Chem. Eng. Sci. 46(4), 1151–1156 (1991)Google Scholar
  16. 16.
    R.W. Lyczkowski, J.X. Bouillard, Scaling and guidelines for erosion in fluidized beds. Powder Technol. 125, 217–225 (2002)CrossRefGoogle Scholar

Copyright information

© The Author(s) 2012

Authors and Affiliations

  • Robert W. Lyczkowski
    • 1
  • Walter F. Podolski
    • 1
  • Jacques X. Bouillard
    • 2
  • Stephen M. Folga
    • 1
  1. 1.Argonne National LaboratoryArgonneUSA
  2. 2.INERIS, Parc Technologique ALATA, BP 2Verneuil-en-HalatteFrance

Personalised recommendations