Knowledge Management System Of Institute of process engineering,CAS
A new drag model for TFM simulation of gas-solid bubbling fluidized beds with Geldart-B particles | |
Alternative Title | Particuology |
Wang, Yingce1,2; Zou, Zheng1,2; Li, Hongzhong1; Zhu, Qingshan1 | |
2014-08-01 | |
Source Publication | PARTICUOLOGY
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ISSN | 1674-2001 |
Volume | 15Issue:S1Pages:151-159 |
Abstract | 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.; 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. |
Keyword | Fluidization Bubbling Fluidized Bed Cfd Geldart-b Particles Drag Model |
Subtype | Article |
WOS Headings | Science & Technology ; Technology |
DOI | 10.1016/j.partic.2013.07.003 |
URL | 查看原文 |
Indexed By | SCI |
Language | 英语 |
WOS Keyword | NUMERICAL-SIMULATION ; KINETIC-THEORY ; GRANULAR FLOW ; REACTORS ; CFD ; HYDRODYNAMICS |
WOS Research Area | Engineering ; Materials Science |
WOS Subject | Engineering, Chemical ; Materials Science, Multidisciplinary |
WOS ID | WOS:000340329500021 |
Citation statistics | |
Document Type | 期刊论文 |
Version | 出版稿 |
Identifier | http://ir.ipe.ac.cn/handle/122111/11546 |
Collection | 研究所(批量导入) |
Affiliation | 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 |
Recommended Citation 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. |
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