Issue
Korean Journal of Chemical Engineering,
Vol.28, No.3, 686-696, 2011
Experiment and 3D simulation of slugging regime in a circulating fluidized bed
A circulating fluidized bed (CFB) is widely applied in many industries because it has high efficiency. To develop and improve the process, an understanding of the hydrodynamics inside the CFB is very important. Computational fluid dynamics (CFD) represents a powerful tool for helping to understand the phenomena involved in the process. In this study, a CFD model was developed to represent a cold model of the laboratory scale CFB which was designed to study the hydrodynamics of a CFB using commercial CFD software. The Eulerian approach with kinetic theory of granular flow was used for simulating the hydrodynamics inside the system. After proper tuning of relevant parameters, the pressure profile along the equipment from the simulation was well agreed with that from the experiment. The simulation result expresses the hydrodynamic parameters of the slug flow such as solid volume fraction, gas and solid velocities and granular temperature in the riser.
[References]
  1. Kunii D, Levenspiel O, Fluidization engineering., Butterworth-Heinemann, New York, 1991
  2. Grace JR, Avidan AA, Knowlton TM, Circulating fluidized beds., Blackie Academic & Professional, London, 1997
  3. Geldart D, Powder Technol., 7, 285, 1973
  4. Lettieri P, Saccone G, Cammarata L, Chem. Eng. Res. Des., 82(8), 939, 2004
  5. Baeyens J, Geldart D, Chem. Eng. Sci., 29, 255, 1974
  6. Baker DGJ, Geldart D, Powder Technol., 19, 177, 1978
  7. De Luca L, Di Felice R, Foscolo PU, Boattini PP, Powder Technol., 69, 171, 1992
  8. Gidaspow D, Multiphase flow and fluidization: Continuum and kinetic theory description., Academic Press, Boston, 1994
  9. Fluent Inc., Fluent 6.2.16 User’s Guide, Fluent Inc., Lebanon, 2003
  10. Cabezas-Gomez L, Milioli FE, Powder Technol., 132(2-3), 216, 2003
  11. Mastellone ML, Arena U, Chem. Eng. Sci., 54(22), 5383, 1999
  12. Noymer PD, Hyre MR, Glicksman LR, Int. J. Heat Mass Transf., 43(19), 3641, 2000
  13. Wang XF, Jin BS, Zhong WQ, Chem. Eng. Process., 48(2), 695, 2009
  14. De Wilde J, Marin GB, Heynderickx GJ, Chem. Eng. Sci., 58(3-6), 877, 2003
  15. Johnson PC, Jackson R, J. Fluid Mech., 176, 67, 1987
  16. Cruz E, Steward FR, Pugsley T, Powder Technol., 169(3), 115, 2006
  17. Chalermsinsuwan B, Kuchonthara P, Piumsomboon P, Chem. Eng. Process., 48(1), 165, 2009
  18. Chalermsinsuwan B, Piumsomboon P, Gidaspow D, Chem. Eng. Sci., 64(6), 1195, 2009
  19. Clift R and Grace JR, in Fluidization II, Davidson JF, Clift R and Harrison D Eds., Academic Press, London, 1985
  20. Lee SH, Lee DH, Kim SD, Korean J. Chem. Eng., 19(2), 351, 2002