Investigation of heat transfers with particle-resolved simulations: From Stokes flow to fluidized bed

Particle-Resolved Simulations (PRS) of fluid–solid particles are conducted to study fluid–particle heat transfers and wall-to-bed heat transfers in an anisothermal liquid–solid fluidized bed. An overview of existing PRS methods to study anisothermal fluid–solid flows is presented. In the framework of fluidized bed simulations, the collision detection method is optimized using Verlet tables. The overall computation time is reduced by 20%. An original Lagrangian method to compute the fluid–particle heat transfers is presented for an isolate particle. A parametric study on the fluid–particle heat transfer is performed to assess well-known correlations of the literature for a settling particle in a quiescent fluid. 77 PRS are performed for Reynolds numbers between 1 and 32 and Prandtl number between 0.1 and 10 for a grid resolution of 20 meshes per particle diameter. For two of three correlations considered, the predicted heat flow is within 10% error. An anisothermal fluidized bed of 2 134 particles is finally studied. Four fluidization velocities are considered for a solid fraction comprised between 0.13 and 0.35. Three grid resolutions are carried out to assess the sensitivity of the mesh for the lowest fluidization velocity (12, 24 and 36 meshes per particle diameter). Results show that the macroscopic behavior of the bed is well retrieved even with a coarser grid as the solid fraction is well predicted. However, strong effects of the grid resolution are observed on the fluid–particle and the wall-to-bed heat transfers. The study of the velocity–temperature correlation shows that the parietal heat transfer is driven by the turbulent heat flow near the wall ( x + ∼ 30 ). • Particle-Resolved Simulations are performed to study anisothermal fluidized beds. • An original Lagrangian method is developed to compute fluid–particle heat transfer. • Heat transfer correlations assessed for a wide range of Reynolds and Prandtl numbers. • Wall-to-bed heat transfer is confronted to an empirical correlation. • Velocity–temperature and temperature–temperature correlations are investigated.

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Publication Details

Journal
International Journal of Heat and Mass Transfer
Published
2025-01-27
DOI
https://doi.org/10.1016/j.ijheatmasstransfer.2025.126687
Citations
4
Primary Topic
Granular flow and fluidized beds
Type
article
Field-Weighted Citation Impact
5.34
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article

Investigation of heat transfers with particle-resolved simulations: From Stokes flow to fluidized bed

Edouard Butaye, Samuel Mer, Françoise Bataille, Rolando Quintana et al.
4 citations
International Journal of Heat and Mass Transfer
Granular flow and fluidized beds
5.34
article

Investigation of heat transfers with particle-resolved simulations: From Stokes flow to fluidized bed

Edouard Butaye, Samuel Mer, Françoise Bataille, Rolando Quintana, Adrien Toutant
article en
4 citations

Abstract

Particle-Resolved Simulations (PRS) of fluid–solid particles are conducted to study fluid–particle heat transfers and wall-to-bed heat transfers in an anisothermal liquid–solid fluidized bed. An overview of existing PRS methods to study anisothermal fluid–solid flows is presented. In the framework of fluidized bed simulations, the collision detection method is optimized using Verlet tables. The overall computation time is reduced by 20%. An original Lagrangian method to compute the fluid–particle heat transfers is presented for an isolate particle. A parametric study on the fluid–particle heat transfer is performed to assess well-known correlations of the literature for a settling particle in a quiescent fluid. 77 PRS are performed for Reynolds numbers between 1 and 32 and Prandtl number between 0.1 and 10 for a grid resolution of 20 meshes per particle diameter. For two of three correlations considered, the predicted heat flow is within 10% error. An anisothermal fluidized bed of 2 134 particles is finally studied. Four fluidization velocities are considered for a solid fraction comprised between 0.13 and 0.35. Three grid resolutions are carried out to assess the sensitivity of the mesh for the lowest fluidization velocity (12, 24 and 36 meshes per particle diameter). Results show that the macroscopic behavior of the bed is well retrieved even with a coarser grid as the solid fraction is well predicted. However, strong effects of the grid resolution are observed on the fluid–particle and the wall-to-bed heat transfers. The study of the velocity–temperature correlation shows that the parietal heat transfer is driven by the turbulent heat flow near the wall ( x + ∼ 30 ). • Particle-Resolved Simulations are performed to study anisothermal fluidized beds. • An original Lagrangian method is developed to compute fluid–particle heat transfer. • Heat transfer correlations assessed for a wide range of Reynolds and Prandtl numbers. • Wall-to-bed heat transfer is confronted to an empirical correlation. • Velocity–temperature and temperature–temperature correlations are investigated.

International Journal of Heat and Mass TransferVol. 241
Centre National de la Recherche Scientifique (FR), Université de Perpignan (FR), Laboratoire Procédés, Matériaux et Energie Solaire (FR)
Openalex Percentile: Top 5%
Granular flow and fluidized beds
5.34
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