Characterization and CFD-modeling of the hydrodynamics of a prismatic spouted bed apparatus

被引:67
|
作者
Gryczka, O. [1 ,2 ]
Heinrich, S. [1 ]
Deen, N. G. [3 ]
Annaland, M. van Sint [3 ]
Kuipers, J. A. M. [3 ]
Jacob, M. [4 ]
Moerl, L. [2 ]
机构
[1] Hamburg Univ Technol, Inst Solids Proc Engn & Particle Technol, D-21073 Hamburg, Germany
[2] Otto VonGuericke Univ Magdegurg, Inst Proc Equipment & Environm Technol, D-39106 Magdeburg, Germany
[3] Univ Twente, Fac Sci & Technol, NL-7500 AE Enschede, Netherlands
[4] Glatt Ingenieurtech GmbH, D-99427 Weimar, Germany
关键词
Spouted bed; CFD; Simulation; Multiphase flow; SOLID FLUIDIZED-BEDS; GRANULAR FLOW; BIDISPERSE ARRAYS; DISCRETE PARTICLE; KINETIC-THEORY; DRAG FORCE; COEFFICIENT; DYNAMICS; RESTITUTION; VALIDATION;
D O I
10.1016/j.ces.2009.04.020
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Recently the importance of spouted bed technology has significantly increased in the context of drying processes as well as granulation, agglomeration or coating processes. However, the understanding of the complex interactions within and between the single phases is still low and needs further improvement. Several research groups apply both continuum as well as discrete element simulations to understand the hydrodynamics of the spouting process. This work focuses on the simulation of the hydrodynamic behavior of a prismatic spouted bed apparatus by applying the Euler/Euler continuum approach in the commercial computational fluid dynamics (CFD) software package FLUENT 6.2. The simulations are validated by experiments. Calculated and experimental (by PIV-measurements) obtained velocity vector maps, as well as measured and calculated gas phase pressure fluctuations over the entire bed are compared. The aim of this work is to improve the understanding of the hydrodynamics of the spouting process. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:3352 / 3375
页数:24
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