Three-dimensional numerical simulation of a horizontal rotating fluidized bed

被引:7
作者
Ahmadzadeh, Azita [1 ]
Arastoopour, Hamid [1 ]
机构
[1] IIT, Dept Chem & Biol Engn, Chicago, IL 60616 USA
关键词
rotating fluidized bed; fluidized bed systems; numerical simulation; computational fluid dynamics; solid particles; gas-solid interaction; multi-phase flow;
D O I
10.1016/j.powtec.2008.01.023
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Three-dimensional numerical simulations of a horizontal rotating fluidized bed (RFB) containing glass bead particles (d(s) = 82 mu m, rho(s) = 2450 kg/m(3)) and washed alumina (d(s) = 89 mu m, rho(s) = 1550 kg/m(3)) were performed. FLUENT 6.1 software was used to carry out our simulation. The numerical results were compared with the experimental data of Qian and Pfeffer et al. [G.H. Qian, I. Bagyi, I.W. Burdick, R. Pfeffer, H. Shaw, Gas-Solid Fluidization in a Centrifugal Field." AIChE J. 47 (5) (2001) 1022-1034]. The rotating speed of the RFB was set at 325 rpm (34 rad/s), which is equivalent to a centrifugal acceleration of 7 g. The flow behavior of the solid particles was analyzed; the bed thickness and the calculated pressure drop were compared with the experimental results. Our calculated pressure drop agreed very well with the experimental results. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:410 / 416
页数:7
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