共 2 条
Particle-resolved simulation of packed beds by non-body conforming locally refined orthogonal hexahedral mesh
被引:0
|作者:
Bing Yuan
[1
,2
]
Junbo Xu
[2
]
Zaisha Mao
[2
]
Yongqiang Zhang
[3
]
Chao Yang
[1
,2
]
机构:
[1] College of Chemical Engineering, Sichuan University
[2] SINOPEC Research Institute of Petroleum Processing
[3] CAS Key Laboratory of Green Process and Engineering, Institute of Process Engineering, Chinese Academy of Sciences, University of Chinese Academy of Sciences
基金:
中国国家自然科学基金;
关键词:
CFD;
Packed bed;
Model;
Simulation;
Transport;
D O I:
暂无
中图分类号:
TQ021.1 [流体力学过程及原理];
学科分类号:
摘要:
The traditional fixed-bed reactor design is usually not suitable for the low tube-to-particle diameter ratios(N = D/d b 8) where the local phenomena of channeling near the wall and backflow in the bed are dominant. The recent"solid particle" meshing method is too complicated for mesh generation, especially for non-spherical particles in large random packed beds, which seriously hinders its development. In this work, a novel high-fidelity mesh model is proposed for simulation of fixed bed reactors by combining the immersed boundary and adaptive meshing methods. This method is suitable for different shapes of particles, which ingeniously avoids handling the complex "contact point" problem. Several packed beds with two different shapes of particles are investigated with this model, and the local flow in the bed is simulated without geometrical simplification. The predicted pressure drop across the fixed bed and heat transfer of the single particle are in good agreement with the corresponding empirical relations. Compared with spherical particles, the packed bed packing with pentaphyllous particles has lower pressure drop and better heat/mass transfer performance, and it shows that this method can be used for the screening of particle shapes in a fixed bed.
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页码:2635 / 2642
页数:8
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