3-D simulations of an internal airlift loop reactor using a steady two-fluid model
文献类型:期刊论文
作者 | Huang, Qingshan; Yang, Chao; Yu, Gengzhi; Mao, Zai-Sha |
刊名 | CHEMICAL ENGINEERING & TECHNOLOGY
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出版日期 | 2007-07-01 |
卷号 | 30期号:7页码:870-879 |
关键词 | airlift-reactor simulations two-fluid model two-phase flow |
ISSN号 | 0930-7516 |
其他题名 | Chem. Eng. Technol. |
中文摘要 | Three-dimensional (3-D) simulations of an internal airlift loop reactor in a cylindrical reference frame are presented, which are based on a two-fluid model with a revised k-epsilon turbulence model for two-phase bubbly flow. A steady state formulation is used with the purpose of time saving for cases with superficial gas velocity values as high as 0.12 m/s. Special 3-D treatment of the boundary conditions at the axis is undertaken to allow asymmetric gas-liquid flow. The simulation results are compared to the experimental data on average gas holdup, average liquid velocity in the riser and the downcomer, and good agreement is observed. The turbulent dispersion in the present two-fluid model has a strong effect on the gas holdup distribution and wall-peaking behavior is predicted. The CFD code developed has the potential to be applied as a tool for scaling up loop reactors. |
英文摘要 | Three-dimensional (3-D) simulations of an internal airlift loop reactor in a cylindrical reference frame are presented, which are based on a two-fluid model with a revised k-epsilon turbulence model for two-phase bubbly flow. A steady state formulation is used with the purpose of time saving for cases with superficial gas velocity values as high as 0.12 m/s. Special 3-D treatment of the boundary conditions at the axis is undertaken to allow asymmetric gas-liquid flow. The simulation results are compared to the experimental data on average gas holdup, average liquid velocity in the riser and the downcomer, and good agreement is observed. The turbulent dispersion in the present two-fluid model has a strong effect on the gas holdup distribution and wall-peaking behavior is predicted. The CFD code developed has the potential to be applied as a tool for scaling up loop reactors. |
WOS标题词 | Science & Technology ; Technology |
类目[WOS] | Engineering, Chemical |
研究领域[WOS] | Engineering |
关键词[WOS] | GAS-LIQUID FLOW ; STIRRED-TANK ; HYDRODYNAMICS ; COLUMN ; ALGORITHMS ; PHASE ; 2D |
收录类别 | SCI |
原文出处 | |
语种 | 英语 |
WOS记录号 | WOS:000248245000007 |
公开日期 | 2013-10-15 |
版本 | 出版稿 |
源URL | [http://ir.ipe.ac.cn/handle/122111/3344] ![]() |
专题 | 过程工程研究所_研究所(批量导入) |
作者单位 | Chinese Acad Sci, Inst Proc Engn, Beijing 100080, Peoples R China |
推荐引用方式 GB/T 7714 | Huang, Qingshan,Yang, Chao,Yu, Gengzhi,et al. 3-D simulations of an internal airlift loop reactor using a steady two-fluid model[J]. CHEMICAL ENGINEERING & TECHNOLOGY,2007,30(7):870-879. |
APA | Huang, Qingshan,Yang, Chao,Yu, Gengzhi,&Mao, Zai-Sha.(2007).3-D simulations of an internal airlift loop reactor using a steady two-fluid model.CHEMICAL ENGINEERING & TECHNOLOGY,30(7),870-879. |
MLA | Huang, Qingshan,et al."3-D simulations of an internal airlift loop reactor using a steady two-fluid model".CHEMICAL ENGINEERING & TECHNOLOGY 30.7(2007):870-879. |
入库方式: OAI收割
来源:过程工程研究所
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