Analysis of hydrodynamic forces on solid particles in mixing tanks using coupled CFD–DEM method: Influence of impeller pumping direction and speed on mixing dynamics

This study presents a comprehensive analysis of hydrodynamic forces acting on particles in a three-phase (gas–liquid–solid) mixing tank using a coupled Computational Fluid Dynamics–Discrete Element Method (CFD–DEM) approach. A baffled cylindrical tank equipped with a Pitched Blade Turbine (PBT45) impeller is simulated under both upward and downward pumping directions over a range of speeds (300–800 rpm). Key particle–fluid forces — including drag, lift, pressure gradient, virtual mass, and flow-induced torque — are modeled to assess their individual and collective impacts on particle suspension and mixing dynamics. The simulations capture temporal evolution, spatial distributions, and time-averaged behavior of forces, providing insight into flow regime transitions and solid dispersion characteristics. Experimental validation is performed using both torque measurements and Electrical Resistance Tomography (ERT), showing good agreement between CFD–DEM predictions and experimental observations. Results indicate that pressure gradient and drag forces dominate particle–fluid momentum exchange, while virtual mass forces play secondary but directionally significant roles. Lift force and fluid-generated torque exhibit minor contributions across most operating conditions. Furthermore, comparison of impeller pumping directions reveals that upward pumping facilitates early suspension but shows diminishing force effectiveness at higher speeds, whereas downward pumping supports sustained force growth and more efficient suspension at high rotational speeds. These findings establish a quantitative and qualitative framework for comparing all major hydrodynamic forces in stirred tanks, offering both fundamental insight and practical recommendations for optimizing multiphase mixing simulations. • Utilization of the CFD–DEM framework to investigate the hydrodynamics of mixing systems. • Quantitative evaluation of key fluid–particle interaction forces. • Examination of the role of fluid-generated torque on particle behavior. • Recommendations for reducing computational cost in CFD–DEM simulations. • Practical insights for selecting impeller configurations in multiphase mixing processes.

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Publication Details

Journal
Powder Technology
Published
2025-09-08
DOI
https://doi.org/10.1016/j.powtec.2025.121609
Citations
3
Primary Topic
Granular flow and fluidized beds
Type
article
Field-Weighted Citation Impact
4.00
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article

Analysis of hydrodynamic forces on solid particles in mixing tanks using coupled CFD–DEM method: Influence of impeller pumping direction and speed on mixing dynamics

Farhad Ein‐Mozaffari, Simant R. Upreti, Pouya Ranjbari
3 citations
Powder Technology
Granular flow and fluidized beds
4.00
article

Analysis of hydrodynamic forces on solid particles in mixing tanks using coupled CFD–DEM method: Influence of impeller pumping direction and speed on mixing dynamics

Farhad Ein‐Mozaffari, Simant R. Upreti, Pouya Ranjbari
article en
3 citations

Abstract

This study presents a comprehensive analysis of hydrodynamic forces acting on particles in a three-phase (gas–liquid–solid) mixing tank using a coupled Computational Fluid Dynamics–Discrete Element Method (CFD–DEM) approach. A baffled cylindrical tank equipped with a Pitched Blade Turbine (PBT45) impeller is simulated under both upward and downward pumping directions over a range of speeds (300–800 rpm). Key particle–fluid forces — including drag, lift, pressure gradient, virtual mass, and flow-induced torque — are modeled to assess their individual and collective impacts on particle suspension and mixing dynamics. The simulations capture temporal evolution, spatial distributions, and time-averaged behavior of forces, providing insight into flow regime transitions and solid dispersion characteristics. Experimental validation is performed using both torque measurements and Electrical Resistance Tomography (ERT), showing good agreement between CFD–DEM predictions and experimental observations. Results indicate that pressure gradient and drag forces dominate particle–fluid momentum exchange, while virtual mass forces play secondary but directionally significant roles. Lift force and fluid-generated torque exhibit minor contributions across most operating conditions. Furthermore, comparison of impeller pumping directions reveals that upward pumping facilitates early suspension but shows diminishing force effectiveness at higher speeds, whereas downward pumping supports sustained force growth and more efficient suspension at high rotational speeds. These findings establish a quantitative and qualitative framework for comparing all major hydrodynamic forces in stirred tanks, offering both fundamental insight and practical recommendations for optimizing multiphase mixing simulations. • Utilization of the CFD–DEM framework to investigate the hydrodynamics of mixing systems. • Quantitative evaluation of key fluid–particle interaction forces. • Examination of the role of fluid-generated torque on particle behavior. • Recommendations for reducing computational cost in CFD–DEM simulations. • Practical insights for selecting impeller configurations in multiphase mixing processes.

Powder TechnologyVol. 468
Toronto Metropolitan University (CA)
Openalex Percentile: Top 6%
Granular flow and fluidized beds
4.00
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