Simulation of mass transfer in downer fluidized beds with a structure-based consideration

被引:9
|
作者
Yan, Dong [1 ]
Li, Hongzhong [1 ]
Hu, Chaoquan [1 ]
Zhu, Qingshan [1 ,2 ]
Xie, Zhaohui [1 ]
机构
[1] Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, POB 353, Beijing 100190, Peoples R China
[2] Univ Chinese Acad Sci, Beijing 100049, Peoples R China
基金
中国国家自然科学基金;
关键词
Mass transfer; Downer reactor; Heterogeneous structure; Computational fluid dynamics; SOLID RISER FLOWS; TRANSFER MODEL; GAS; DOWNFLOW; HYDRODYNAMICS; REACTOR; PERFORMANCE;
D O I
10.1016/j.ces.2019.115235
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The gas-solid mass transfer in the downer fluidized bed is analyzed theoretically in this work. Compared to the homogeneous assumption in each calculating grid, a structure-based model was proposed that the process was divided into the mass transfer in the cluster and dispersed phases. Simulations were performed with the cooperation of the Euler-Euler two-fluid method. The model predictions are in good agreement with the previous reported experimental measurements under a wide range of operating conditions. Simulated ozone profiles show a sharp conversion in the acceleration region, and a gentle conversion in the fully developed region. The transition point is well consistent with the boundary measured experimentally. These results show that the consideration of the heterogeneous structure results in a better understanding and prediction of mass transfer in downers. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页数:9
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