Numerical approach for modeling particle transport phenomena in a closed loop of a circulating fluidized bed

被引:19
作者
Adamczyk, Wojciech P. [1 ]
Kozolub, Pawel [2 ]
Kruczek, Grzegorz [1 ]
Pilorz, Monika [1 ]
Klimanek, Adam [1 ]
Czakiert, Tomasz [3 ]
Wecel, Gabriel [1 ]
机构
[1] Silesian Tech Univ, Inst Thermal Technol, Gliwice, Poland
[2] AMEC Foster Wheeler, Staszica 31, PL-41200 Sosnowiec, Poland
[3] Czestochowa Tech Univ, Inst Adv Energy Technol, Czestochowa, Poland
来源
PARTICUOLOGY | 2016年 / 29卷
关键词
Fluidization; CFB; Numerical modeling; Multiphase flow; Particle transport; Cyclone; GAS-SOLID FLOW; IN-CELL MODEL; QUADRATURE METHOD; CFD-SIMULATION; MOMENTS; BOILER; EULER;
D O I
10.1016/j.partic.2015.12.006
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Numerical modeling of a large scale circulating fluidized bed (CFB") imposes many complexities and difficulties. Presence of a dense solid phase, a variety of spatial and time scales as well as complex model geometries requires advanced numerical techniques. Moreover, the appropriate selectionof a numerical model capable of solving granular flow, and geometrical model simplification can have a huge impact on the predicted flow field within the CFB boiler. In order to reduce the cost of the numerical simulations, the complex CFB boiler geometry is reduced to that of the combustion chamber. However, a question arises as to how much one can simplify the geometrical model without losing accuracy of numerical simulations. To accurately predict the gas-solid and solid-solid mixing processes within subsequent sections of the CFB boiler (combustion chamber, solid separator, drain section), a complete 3D geometrical model should be used. Nevertheless, because of the presence of various spatial and temporal scales within subsequent boiler sections, the complete model of the 3D CFB boiler is practically unrealizable in numerical simulations. To resolve the aforementioned problems, this paper describes a new approach that can be applied for complete boiler modeling. The proposed approach enables complex particle transport and gas flow problems within each of the boiler sections to be accurately resolved. It has been achieved by dividing the CFB boiler geometry into several subrnodels, where different numerical approaches van be used to resolve gas-solid transport. The interactions between computational domains were taken into account by connecting the inletsloutlets of each section using a set of user-defined functions implemented into the solution procedure. The proposed approach ensures stable and accurate solution within the separated boiler zones. (C) 2016 Chinese Society of Particuology and Institute of Process Engineering, Chinese Academy of Sciences. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:69 / 79
页数:11
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