Hydrodynamic performance and structural optimization of a slurry bubble column with vertical tube internals

被引:12
作者
Duan, Jihai [1 ]
Li, Guiyong [1 ]
Shen, Zongwang [1 ]
Zhang, Xiaoxu [1 ]
Zou, Yuanqiang [1 ]
Pan, Qingpeng [1 ]
Wang, Wenze [1 ]
Li, Chaojie [2 ]
机构
[1] Qingdao Univ Sci & Technol, Coll Chem Engn, Qingdao 266042, Peoples R China
[2] Qingdao Univ Sci & Technol, Coll Environm & Safety Engn, Qingdao 266042, Peoples R China
关键词
HIGH GAS TEMPERATURE; LIQUID-SOLID FLOW; CFD SIMULATION; HEAT-TRANSFER; NUMERICAL-SIMULATION; TURBULENCE MODELS; MASS-TRANSFER; REACTOR; HOLDUP; VALIDATION;
D O I
10.1063/5.0151385
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
The slurry bubble column, as a multiphase reactor, is widely used in chemical, biological, petroleum refining, environmental, and other fields. However, most published studies of the hydrodynamic performance of slurry bubble columns have been carried out on empty columns without internal components, and recent studies on columns with vertical heat exchange tubes have been limited. In this study, the hydrodynamic performance of a laboratory-scale slurry bubble column with vertical tube bundles was studied, and a new vertical tube structure with fins was proposed. The effect of the new structure on the hydrodynamic performance of the laboratory-scale slurry bubble column was studied via a combination of experimental and numerical simulations. The results of these simulations showed that the vertical heat exchange tube structure with fins was helpful for improving fluid flow, exerted a certain fragmentation effect on large bubbles, and could strengthen mass transfer between gas and liquid, thereby improving the hydrodynamic performance.
引用
收藏
页数:17
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