Coupled CFD-DEM Simulations for Modelling Non-Spherical Particles
被引:0
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作者:
Kiran, M. S.
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机构:
BITS Pilani, Dept Mech Engn, K K Birla Goa Campus, Pilani, IndiaBITS Pilani, Dept Mech Engn, K K Birla Goa Campus, Pilani, India
Kiran, M. S.
[1
]
Dutta, Rabijit
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h-index: 0
机构:
Virginia Commonwealth Univ, Dept Mech & Nucl Engn, Richmond, VA USABITS Pilani, Dept Mech Engn, K K Birla Goa Campus, Pilani, India
Dutta, Rabijit
[2
]
Ranjan, Pritanshu
论文数: 0引用数: 0
h-index: 0
机构:
BITS Pilani, Dept Mech Engn, K K Birla Goa Campus, Pilani, IndiaBITS Pilani, Dept Mech Engn, K K Birla Goa Campus, Pilani, India
Ranjan, Pritanshu
[1
]
机构:
[1] BITS Pilani, Dept Mech Engn, K K Birla Goa Campus, Pilani, India
[2] Virginia Commonwealth Univ, Dept Mech & Nucl Engn, Richmond, VA USA
来源:
INTERNATIONAL JOURNAL OF MECHANICAL ENGINEERING AND ROBOTICS RESEARCH
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2022年
/
11卷
/
09期
关键词:
discrete element modeling;
non-spherical particles;
CFD-DEM coupling;
turbulence modeling;
D O I:
10.18178/ijmerr.11.9.698-704
中图分类号:
TH [机械、仪表工业];
学科分类号:
0802 ;
摘要:
In the present work, single -spouted fluidized bed with non -spherical particle geometries was studied using Computational Fluid Dynamics - Discrete Element Modeling (CFD-DEM) coupling technique. CFD-DEM is an effective tool for modeling multi -phase flows in industrial applications such as fluidized bed reactors, spouted bed etc. Most DEM force -displacement models are based on particles with spherical geometry while many particles encountered in nature of non -spherical geometry. Three different shapes: Cylinder, Square and Hexagon were considered and the results are matched with the circular shaped particles. Multi -sphere method is used to model the force -displacement behavior. Open source software LIGGGHTS-DEM and OpenFOAM were used to perform the simulations. It was observed that the complex interactions of the multi -sphere particles give rise to greater instability in the fluidizing bed, as seen in strong fluctuations in particle properties. Also, these particles exhibited a tendency to agglomerate, thereby offering stronger resistance to shearing flows. As per the findings, it was concluded that the particle geometry has a significant influence on the performance of the fluidizing bed; failure to accurately represent an actual particle would result in erroneous results.