An Inlet Area for Particle Mixing in a Two-Dimensional Fluidized Bed Using a CFD-DEM Model

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Fluidized beds are widely used in many industries since they are effective in mixing process. The distinct element method (DEM) has recently received more attention for investigating the phenomena of multiphase flow because the technique is effective in gathering detailed information on the complex phenomena without physically disturbing the flows. A CFD-DEM model has been developed for calculating the minimum fluidization velocity and particle mixing in a two-dimensional fluidized bed. In this research, the inlet area on the particle mixing was investigated. From the result, it was indicated that the developed CFD-DEM model was performed adequately in predicting the phenomena in a two dimensional fluidized bed. The minimum fluidization velocity predicted by the developed model agreed well with the theory and correlation of Grace. Based on Lacey mixing index, it was found that the mixing index increased with an increase in time and superficial gas velocity. In addition, the inlet area of 20% gave a good mixing.

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367-373

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December 2013

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[1] P.A. Cundall and O.D.L. Strack: A Discrete Numerical Model for Granular Assemblies, Geotechnique, Vol. 29 (1979), pp.47-65.

DOI: 10.1680/geot.1979.29.1.47

Google Scholar

[2] M.J. Rhodes, W.S. Wang, M. Nguyen, P. Stewart and K. Liffman: Onset of Cohesive Behavior in Gas Fluidized Beds: a Numerical Study using DEM Simulation, Chemical Engineering Science, Vol. 56 No. 14 (2001), pp.4433-4438.

DOI: 10.1016/s0009-2509(01)00146-4

Google Scholar

[3] Y. Tsuji, T. Kawaguchi and T. Tanaka: Discrete Particle Simulation of Two-Dimensional Fluidized Bed, Powder Technology, Vol. 77 (1993), pp.79-87.

DOI: 10.1016/0032-5910(93)85010-7

Google Scholar

[4] Y. Tsuji, T. Tanaka and T. Ishida: Lagrangian Numerical Simulation of Plug Flow of Cohesionless Particles in a Horizontal Pipe, Powder Technology, Vol. 71 (1992), pp.239-250.

DOI: 10.1016/0032-5910(92)88030-l

Google Scholar

[5] B.H. Xu and A.B. Yu: Numerical Simulation of the Gas-Particle Flow in a Fluidized Bed by Discrete Particle Method with Computational Fluid Dynamics, Chemical Engineering Science, Vol. 52 (1997), p.2785.

DOI: 10.1016/s0009-2509(97)00081-x

Google Scholar

[6] T. Kawaguchi, T. Tanaka and Y. Tsuji: Numerical Simulation of Two-Dimensional Fluidized Beds using the Discrete Element Method (Comparison between the Two-and Three-Dimensional Models), Powder Technology, Vol. 96 No. 2 (1998), pp.129-138.

DOI: 10.1016/s0032-5910(97)03366-4

Google Scholar

[7] Y. Kaneko, T. Shiojima and M. Horio: DEM Simulation of Fluidized Beds for Gas-Phase Olefin Polymerization, Chemical Engineering Science, Vol. 54 No. 24 (1999), pp.5809-5821.

DOI: 10.1016/s0009-2509(99)00153-0

Google Scholar

[8] S. Limtrakul, A. Boonsrirat and T. Vatanatham: DEM Modeling Simulation of a Catalytic Gas-Solid Fluidized Bed Reactor: a Spouted Bed as a Case Study, Chemical Engineering Science, Vol. 59 No. 22-23 (2004), pp.5225-5231.

DOI: 10.1016/j.ces.2004.09.020

Google Scholar

[9] T. Swasdisevi, W. Tanthapanichakoon, T. Kawaguchi, T. Tanaka and Y. Tsuji: Investigation of Fluid and Coarse-Particle Dynamics in a Two- Dimensional Spouted Bed, Chemical Engineering Technology, Vol. 27 (2004), pp.971-981.

DOI: 10.1002/ceat.200401918

Google Scholar

[10] T. Swasdisevi, W. Tanthapanichakoon, T. Charinpanitkul, T. Kawaguchi, T. Tanaka and Y. Tsuji: Prediction of Gas-Particle Dynamics and Heat Transfer in a Two- Dimensional Spouted Bed, Advanced Powder Technology, Vol. 16 (2005), pp.275-293.

DOI: 10.1002/ceat.200401918

Google Scholar

[11] S. Ergun: Fluid Flow through Packed Columns, Chemical Engineering Progress, Vol. 48 (1952), pp.89-94.

Google Scholar

[12] P.M.C. Lacey: Developments in the Theory of Particulate Mixing, Journal of Applied Chemistry, Vol. 4, pp (1954), p.257–268.

Google Scholar

[13] C.Y. Wen and Y.H. Yu: A Generalized Method for Predicting the Minimum Fluidization Velocity, AIChE Journal, Vol. 12 (1996), pp.610-612.

DOI: 10.1002/aic.690120343

Google Scholar

[14] J.R. Grace and H. Bi: Introduction to Circulating Fluidized Bed, In Circulating Fluidized Beds, Grace, J.R., et al., (Eds. ), Chap & Hall, London, (1997), pp.1-19.

DOI: 10.1007/978-94-009-0095-0_1

Google Scholar