A new drag model for TFM simulation of gas-solid bubbling fluidized beds with Geldart-B particles
文献类型:期刊论文
作者 | Wang, Yingce1,2; Zou, Zheng1,2; Li, Hongzhong1; Zhu, Qingshan1 |
刊名 | PARTICUOLOGY
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出版日期 | 2014-08-01 |
卷号 | 15期号:S1页码:151-159 |
关键词 | Fluidization Bubbling fluidized bed CFD Geldart-B particles Drag model |
ISSN号 | 1674-2001 |
其他题名 | Particuology |
中文摘要 | In this work, a new drag model for TFM simulation in gas solid bubbling fluidized beds was proposed, and a set of equations was derived to determine the meso-scale structural parameters to calculate the drag characteristics of Geldart-B particles under low gas velocities. In the new model, the meso-scale structure was characterized while accounting for the bubble and meso-scale structure effects on the drag coefficient. The Fluent software, incorporating the new drag model, was used to simulate the fluidization behavior. Experiments were performed in a Plexiglas cylindrical fluidized bed consisting of quartz sand as the solid phase and ambient air as the gas phase. Comparisons based on the solids hold-up inside the fluidized bed at different superficial gas velocities, were made between the 2D Cartesian simulations, and the experimental data, showing that the results of the new drag model reached much better agreement with experimental data than those of the Gidaspow drag model did. (C) 2013 Chinese Society of Particuology and Institute of Process Engineering, Chinese Academy of Sciences. Published by Elsevier BAT. All rights reserved. |
英文摘要 | In this work, a new drag model for TFM simulation in gas solid bubbling fluidized beds was proposed, and a set of equations was derived to determine the meso-scale structural parameters to calculate the drag characteristics of Geldart-B particles under low gas velocities. In the new model, the meso-scale structure was characterized while accounting for the bubble and meso-scale structure effects on the drag coefficient. The Fluent software, incorporating the new drag model, was used to simulate the fluidization behavior. Experiments were performed in a Plexiglas cylindrical fluidized bed consisting of quartz sand as the solid phase and ambient air as the gas phase. Comparisons based on the solids hold-up inside the fluidized bed at different superficial gas velocities, were made between the 2D Cartesian simulations, and the experimental data, showing that the results of the new drag model reached much better agreement with experimental data than those of the Gidaspow drag model did. (C) 2013 Chinese Society of Particuology and Institute of Process Engineering, Chinese Academy of Sciences. Published by Elsevier BAT. All rights reserved. |
WOS标题词 | Science & Technology ; Technology |
类目[WOS] | Engineering, Chemical ; Materials Science, Multidisciplinary |
研究领域[WOS] | Engineering ; Materials Science |
关键词[WOS] | NUMERICAL-SIMULATION ; KINETIC-THEORY ; GRANULAR FLOW ; REACTORS ; CFD ; HYDRODYNAMICS |
收录类别 | SCI |
原文出处 | |
语种 | 英语 |
WOS记录号 | WOS:000340329500021 |
公开日期 | 2014-09-30 |
版本 | 出版稿 |
源URL | [http://ir.ipe.ac.cn/handle/122111/11546] ![]() |
专题 | 过程工程研究所_研究所(批量导入) |
作者单位 | 1.Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, Beijing 100190, Peoples R China 2.Chinese Acad Sci, Grad Sch, Beijing 100049, Peoples R China |
推荐引用方式 GB/T 7714 | Wang, Yingce,Zou, Zheng,Li, Hongzhong,et al. A new drag model for TFM simulation of gas-solid bubbling fluidized beds with Geldart-B particles[J]. PARTICUOLOGY,2014,15(S1):151-159. |
APA | Wang, Yingce,Zou, Zheng,Li, Hongzhong,&Zhu, Qingshan.(2014).A new drag model for TFM simulation of gas-solid bubbling fluidized beds with Geldart-B particles.PARTICUOLOGY,15(S1),151-159. |
MLA | Wang, Yingce,et al."A new drag model for TFM simulation of gas-solid bubbling fluidized beds with Geldart-B particles".PARTICUOLOGY 15.S1(2014):151-159. |
入库方式: OAI收割
来源:过程工程研究所
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