Multi-scale heat transfer in fluidized bed reactors by Eulerian CFD modeling

被引:14
作者
Wang Shuai [1 ]
Zhang Tianyu [1 ]
Liu Guodong [1 ]
Lu Huilin [1 ]
Sun Liyan [1 ]
机构
[1] Harbin Inst Technol, Sch Energy Sci & Engn, Harbin 150001, Peoples R China
基金
中国国家自然科学基金;
关键词
Multi-scale structure; Heat transfer; Computational fluid dynamics; Fluidized bed; CHEMICAL LOOPING COMBUSTION; MASS-TRANSFER MODEL; SOLID RISER FLOWS; KINETIC-THEORY; GRANULAR FLOW; GAS; SIMULATION; PARTICLES; CLUSTER; DRAG;
D O I
10.1016/j.fuel.2014.09.027
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In the previous work, the multi-scale chemical reaction model was developed by Wang et al. (2014) to consider the impact of the meso-scale structure on reaction performance. This paper incorporates multi-scale heat transfer to further improve the previous multi-scale chemical reaction model. The temperature field in the cluster phase and the dispersed phase is predicted. A cluster structure-dependent (CSD) drag model is used to obtain local structural parameters. By comparison with experimental data, there is a slight improvement on predicted results with consideration of the multi-scale heat transfer. Meanwhile, the inter-phase heat transfer between the cluster phase and the dispersed phase is evaluated. The results indicate that the effect of the inter-phase heat transfer on the temperature field is less significant than the effect of the inter-phase mass transfer on gas components. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:646 / 651
页数:6
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