Study of dynamic multi-dimensional temperature and concentration distributions in liquid-sprayed fluidized beds

被引:51
作者
Heinrich, S
Blumschein, J
Henneberg, M
Ihlow, M
Peglow, M
Mörl, L
机构
[1] Univ Magdeburg, Inst Proc Equipment & Environm Technol, D-39106 Magdeburg, Germany
[2] Max Planck Inst Dynam Complex Tech Syst, D-39106 Magdeburg, Germany
关键词
fluidized bed; drying; evaporation; heat transfer; mass transfer; dynamic simulation; fluidization;
D O I
10.1016/j.ces.2003.08.010
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A physically based model was developed for heat and mass transfer processes in liquid-sprayed fluidized beds. Such fluidized beds are used for granulation, coating and agglomeration. The complex correlations of a number of microprocesses, spraying, wetting, drop deposition, heat transfer, drying and mass transfer were studied, and transient three-dimensional distributions of air humidity, air temperature, particle wetting efficiency, liquid film temperature, particle temperature, local liquid loading and local evaporation rate were calculated. For the evaluation of the model, the stationary spatial air temperature distributions were measured at a fluidized bed pilot plant of the institute. The fluidized bed of monodisperse wood- or glass beads was sprayed with clear water. Conclusions are drawn on the relevance of particle dispersion, spraying and drying to simulating temperature and concentrations distributions. (C) 2003 Elsevier Ltd. All rights reserved.
引用
收藏
页码:5135 / 5160
页数:26
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