Computational Investigation of Liquid Holdup and Wetting Efficiency Inside Trickle Bed Reactors with Different Catalyst Particle Shapes

被引:10
作者
Deng, Hao [1 ,2 ,3 ]
Guo, Baoqi [1 ,2 ,3 ]
Dong, He [1 ,2 ,3 ]
Liu, Cheng [1 ,2 ,3 ]
Geng, Zhongfeng [1 ,2 ,3 ]
机构
[1] Tianjin Univ, Key Lab Green Chem Technol, Minist Educ, Tianjin 300072, Peoples R China
[2] Tianjin Univ, R&D Ctr Petrochem Technol, Tianjin 300072, Peoples R China
[3] Collaborat Innovat Ctr Chem Sci & Engn, Tianjin 300072, Peoples R China
来源
APPLIED SCIENCES-BASEL | 2020年 / 10卷 / 04期
关键词
liquid holdup; wetting efficiency; trickle bed reactor; CFD; VOF; CFD SIMULATIONS; FLUID-DYNAMICS; 2-PHASE FLOW; HYDRODYNAMICS; SURFACE; DROP; TUBE;
D O I
10.3390/app10041436
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Liquid holdup and wetting efficiency are essential parameters for design of trickle bed reactors. Both parameters play an important role in reactor performance including pressure drop, conversion, and heat transfer. Empirical formulas are usually employed to calculate liquid holdup and wetting efficiency. However, factors such as particle shape and the wetting ability of liquid on the particle surface are not described clearly in traditional formulas. In this paper, actual random packing was built by DEM and CFD simulations were performed to investigate the factors affecting liquid holdup and wetting efficiency in trickle bed reactors, including particle shape, surface tension, contact angle, liquid viscosity, liquid density, liquid, and gas superficial velocity. Detailed fluid flow and liquid-solid interaction were described by VOF model. Four different particle shapes were investigated. It showed the particle shape has great effect and the 4-hole cylinder packing gained both highest liquid holdup and wetting efficiency. The overall simulations gave a detailed description of phase interactions and fluid flow in the voids between catalyst particles and these results could give further guidance for the design and operation of trickle bed reactors.
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页数:18
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