CFD simulations of circulating fluidized bed risers, part II, evaluation of differences between 2D and 3D simulations

被引:66
|
作者
Li, Tingwen [1 ,2 ]
Pannala, Sreekanth [3 ]
Shahnam, Mehrdad [1 ]
机构
[1] Natl Energy Technol Lab, Morgantown, WV 26507 USA
[2] URS Corp, Morgantown, WV 26507 USA
[3] Oak Ridge Natl Lab, Oak Ridge, TN 37831 USA
关键词
Computational fluid dynamics; Numerical simulation; Circulating fluidized bed; Gas-solids flow; Riser flow; Pressure drop; MFIX-DEM SOFTWARE; VOIDAGE PROFILES; GAS; FLOWS; MODEL; HYDRODYNAMICS;
D O I
10.1016/j.powtec.2014.01.022
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Two-dimensional (2D) numerical simulations have been widely reported in the literature for qualitative, even quantitative, study of the complex gas-solids flow behavior in circulating fluidized bed (CFB) risers. It is generally acknowledged that there exist quantitative differences between 2D and three-dimensional (3D) numerical simulations. However, no detailed study evaluating such differences can be found for simulations of CFB risers. This paper presents 2D and 3D numerical simulations of three different CFB risers. Axial pressure gradients from both 2D and 3D simulations are compared with the experimental data. It has been clearly demonstrated that the 2D simulation cannot satisfactorily reproduce the 3D simulation results. A further comparison of radial profiles of void fraction and solids velocity for an axi-symmetric riser configuration is reported and the quantitative differences between 2D and 3D simulations are analyzed. In conclusion, 2D simulation is only recommended for qualitative evaluation and 3D modeling is recommended for predictive simulations. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:115 / 124
页数:10
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