CFD investigation of the cold hydrodynamics of a laboratory scale CFB furnace

Authors

  • A.Mercy Vasan Saranathan College of Engineering,Tiruchirapalli,India
  • N. Prasanna Kongu College of Engineering,Perundurai, India
  • M. Vivekanandan National Institute of Technology,Tiruchirapalli,India
  • V. Gopalakrishnan M.A.M.College of Engineering, Tiruchirapalli,India

DOI:

https://doi.org/10.24297/jac.v12i9.4092

Keywords:

CFB, CFD, simulation, volume fraction, particle velocity

Abstract

This investigation presents a computational and experimental study of the flow characteristics of a laboratory scale CFB cold model riser. i) The first part of the work deals with 2D, CFD validation of a literature based CFB riser of circular cross section of 1m height. Simulation results showed good agreement with experimental literature data for radial profiles of volume fraction and particle velocity. ii) The second part is a work on simulation and experimental verification of a CFB riser flow characteristics of a CFB riser of rectangular cross section (400mm x 550mm x2000mm). An experimental run on the test rig was conducted for sand of 300 micron size at a fluidization velocity of 4 m/s and the fluidization behavior was captured on a high speed camera. For simulation, 3D, transient, Euler-ian approach combined with the Kinetic theory of Granular flow and Gidaspow drag model was used to describe the gas–particle behavior. A frame by frame visual comparison of instantaneous volume fraction distribution was made between camera images and 3D simulated profiles. A further graphical comparison between experimental literature data and simulated 3D profiles of volume fraction and particle velocity profiles yielded fairly good results. It was observed that, in spite of non inclusion of turbulence factor in the current 3D simulation, no significant influence was observed in the results

Downloads

Download data is not yet available.

References

I. Grace, JR., Bi, H.T., Golriz, M.,in: Wen-Ching Yang (Ed.),2003, Circulating fluidized beds, in handbook of fluidization and fluid–particle systems, Marcel Dekker Inc., New York, pp. 485–531. II. Samuelsberg, Hjertager , BH., Computational modeling of gas–particle flow in a riser, AIChE J. 42 (1996) 1536–1546. III. Spalding, D.B., 1983, Developments in the IPSA procedure for numerical computation of multiphase-Flow phenomena with interphase slip, unequal temperatures, etc. In: Numerical Properties and Methodologies in Heat Transfer. Hemisphere, Washington DC, pp. 421-476. IV. Mathiesen,V., Solberg,T., Hjertager, B.H.,2000, An experimental and computational study of multiphase flow behavior in a circulating fluidized bed, International Journal of Multiphase Flow,Vol. 26 , 387-419. V. Armstrong, L.M., Luo, Gu, S.,2010, Two-dimensional and three-dimensional computational studies of hydrodynamics in the transition from bubbling to circulating fluidised bed, Chemical Engineering Journal ,Vol.160 ,pp 239–248. VI. Gidaspow, D., Bezburuah, R., Ding, J.,1992, Hydrodynamics of circulating fluidized beds, kinetic theory approach, Fluidization VII, Proceedings of the 7th Engineering Foundation Conference on Fluidization, pp. 75–82. VII. Ding, J. , Gidaspow,1990, D.A. Bubbling fluidization model using kinetic theory of granular flow, AIChE J. 36 (4) 523–538. VIII. Schaeffer, D. G.,1987, Instability in the evolution equations describing incompressible granular flow . Journal of Differential Equations,Volume 6(1), pages 19 – 50. ISSN 0022-0396. doi:10.1016/0022-0396(87)90038-6. IX. Gidaspow , D., 1994, Multiphase Flow and Fluidization - Continuum and Kinetic Theory Descriptions. Academic Press, ISBN 0-12-282470-9. X. Ergun, S., 1952, „„Fluid Flow Through Packed Columns,‟‟ Chem. Eng. Prog., Vol.48, pp. 245. XI. Wen, Y. C., and Y. H. Yu, 1966, „„Mechanics of Fluidization,‟‟ Chem. Eng.Prog. Symp. Ser., Vol.62, pp.100. XII.Suhas V.Patankar, 1980, Numerical heat transfer and fluid flow, CRC Press. XIII P. Johnson, R. Jackson, Frictional-collisional constitutive relations for granular materials, with application to plane shearing, J.Fluid Mech. 176 (1987)67–93. XIV. Zhang N, Lu B, Wang W, Li J.,2010, “3D CFD simulation of hydrodynamics of a 150 MW circulating fluidized bed boiler”, Chem.Eng J., Vol.162, pp.821 –828. XV. Wang C., Zhu J., Li C.,Bargh S., 2014,”Detailed measurements of particle velocity and solids flux in a high density circulating fluidized bed riser”, Chemical Engineering Science, Vol.114, pp.9-20.

Downloads

Published

2016-11-02

How to Cite

Vasan, A., Prasanna, N., Vivekanandan, M., & Gopalakrishnan, V. (2016). CFD investigation of the cold hydrodynamics of a laboratory scale CFB furnace. JOURNAL OF ADVANCES IN CHEMISTRY, 12(9), 4330–4340. https://doi.org/10.24297/jac.v12i9.4092

Issue

Section

Articles