Applying a CFD-PBM approach to modeling the flow behavior in pressurized bubbling fluidized beds

被引:1
|
作者
Zang, Hongyang [1 ,2 ]
Hu, Shanwei [1 ,3 ]
Liu, Xinhua [1 ,3 ]
Du, Wei [1 ,2 ]
机构
[1] Chinese Acad Sci, Inst Proc Engn, State Key Lab Mesosci & Engn, Beijing 100190, Peoples R China
[2] China Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
[3] Univ Chinese Acad Sci, Sch Chem Engn, Beijing 100049, Peoples R China
基金
中国国家自然科学基金;
关键词
Pressurized fluidized bed; Bubble; Two-fluid model; Population balance model; EMMS model; STRUCTURE-DEPENDENT DRAG; ELEVATED PRESSURE; GAS; DYNAMICS; VELOCITY; HYDRODYNAMICS; SIZE; PARTICLES;
D O I
10.1016/j.powtec.2024.120541
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Pressurized fluidization is an important technology for process intensification. In this research, we introduce a CFD-PBM approach coupled with the EMMS model to investigate the flow behavior in pressurized fluidized beds across a pressure range of 0.1 to 1.0 MPa. By comparing with experiments, it is evident that the CFD-PBM-EMMS approach can reasonably capture the flow characteristics and bubble behavior under various operating pressures. The prediction errors of the expansion height and bubble diameter are less than 5 % and 25 %, respectively. The breakage kernel accurately predicts the increasing bubble breakage frequency as pressure rises. Under high pressures, the gas-solid flow becomes more uniform, and the fluidization behavior of Geldart B particles transitions towards that of Geldart A ones. The effect of pressure on process intensification exhibits a marginal decreasing effect beyond 0.6 Mpa, suggesting that there may exist an optimal operating state that balances energy consumption and fluidization quality.
引用
收藏
页数:12
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