Competing flow and collision effects in a monodispersed liquid-solid fluidized bed at a moderate Archimedes number
Yinuo Yao, Craig S. Criddle, Oliver B. Fringer

TL;DR
This study investigates how fluid-particle and particle-particle interactions influence flow regimes in a liquid-solid fluidized bed, identifying an optimal particle Reynolds number for mixing efficiency at a specific Archimedes number.
Contribution
The paper introduces a detailed simulation analysis of flow regimes in a fluidized bed, highlighting the transition point where hydrodynamic effects dominate over collisions.
Findings
Flow regimes depend on particle Reynolds number.
Maximum mixing occurs near Re_p of 40.
Transition from collision-dominated to hydrodynamic-dominated flow at Re_p ~50.
Abstract
We study the effects of fluid-particle and particle-particle interactions in a three-dimensional monodispersed reactor with unstable fluidization. Simulations were conducted using the Immersed Boundary Method (IBM) for particle Reynolds numbers of 20-70 with an Archimedes number of 23600. Two different flow regimes were identified as a function of the particle Reynolds number. For low particle Reynolds numbers (), the porosity is relatively low and the particle dynamics are dominated by interparticle collisions that produce anisotropic particle velocity fluctuations. The relative importance of hydrodynamic effects increases with increasing particle Reynolds number, leading to a minimized anisotropy in the particle velocity fluctuations at an intermediate particle Reynolds number. For high particle Reynolds numbers (), the particle dynamics are dominated by…
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Taxonomy
TopicsGranular flow and fluidized beds · Particle Dynamics in Fluid Flows · Fluid Dynamics and Heat Transfer
