Construction of drag coefficient models of flake particles with different sectional shapes

The driving force for the settling motion of particles is the difference between the trailing force of the fluid and the effective force of gravity. The drag coefficient is an important parameter for predicting the drag force on an object in a fluid. Although the drag coefficients of spherical and regular non-spherical particles have been studied more, there are fewer studies on flake particles with different cross-sectional shapes. In this study, we analyzed the effects of thickness-to-diameter ratio and circularity on settling velocity by using a self-designed monitoring system, constructed a new model Z=0.7815λ2+0.0176c2+0.1 for describing the shape of flake particles, and obtained a new drag coefficient model Cd=0.0451Z−2.6438Re(−0.9236Z0.1102+1)+A containing Z and the Reynolds number Re, with an average relative error of 8.97%. Based on this model, the settling end velocity of flake particles with different cross-sectional shapes was predicted using MATLAB, with an average relative error of 5.52%, which is a good prediction. This study provides a theoretical basis for the settling behavior of flake particles.

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Publication Details

Journal
Physics of Fluids
Published
2024-12-01
DOI
https://doi.org/10.1063/5.0237702
Primary Topic
Granular flow and fluidized beds
Type
article
Field-Weighted Citation Impact
0.00

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article

Construction of drag coefficient models of flake particles with different sectional shapes

Chengyi Zhang, Liqiang Ma, Yiding Zhu, Wen‐Quan Tao et al.
Physics of Fluids
Granular flow and fluidized beds
article

Construction of drag coefficient models of flake particles with different sectional shapes

Chengyi Zhang, Liqiang Ma, Yiding Zhu, Wen‐Quan Tao, Jilin Li, Jihui Li, Qiao Guo, Gen Huang
article en

Abstract

The driving force for the settling motion of particles is the difference between the trailing force of the fluid and the effective force of gravity. The drag coefficient is an important parameter for predicting the drag force on an object in a fluid. Although the drag coefficients of spherical and regular non-spherical particles have been studied more, there are fewer studies on flake particles with different cross-sectional shapes. In this study, we analyzed the effects of thickness-to-diameter ratio and circularity on settling velocity by using a self-designed monitoring system, constructed a new model Z=0.7815λ2+0.0176c2+0.1 for describing the shape of flake particles, and obtained a new drag coefficient model Cd=0.0451Z−2.6438Re(−0.9236Z0.1102+1)+A containing Z and the Reynolds number Re, with an average relative error of 8.97%. Based on this model, the settling end velocity of flake particles with different cross-sectional shapes was predicted using MATLAB, with an average relative error of 5.52%, which is a good prediction. This study provides a theoretical basis for the settling behavior of flake particles.

Physics of FluidsVol. 36(12)
Peking University (CN), China University of Mining and Technology (CN)
National Natural Science Foundation of China, Fundamental Research Funds for the Central Universities
Openalex Percentile: Top 75%
Granular flow and fluidized beds
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