Granular mixing and flow dynamics in horizontal stirred bed reactors
Sahar Pourandi, Igor Ostanin, Thomas Weinhart

TL;DR
This study uses DEM simulations to analyze how rotation speed and fill level affect granular flow, mixing, and axial transport in horizontal stirred bed reactors, providing insights for optimizing industrial processes.
Contribution
It offers a detailed DEM-based analysis of the effects of operating conditions on granular flow and mixing in HSBRs, which was previously not well understood.
Findings
Higher rotation speeds accelerate mixing and circulation.
Higher fill levels slow axial mixing but increase circulation.
Axial dispersion increases with rotation speed and decreases with fill level.
Abstract
Horizontal stirred bed reactors (HSBRs) are used in gas--phase polyolefin production, where efficient solids mixing and controlled residence time distributions are essential for product quality and stability. Despite their industrial relevance, the influence of operating conditions on granular flow and mixing in HSBRs is not well understood. Discrete Element Method (DEM) simulations are used to study the effects of rotation speed and fill level on particle motion, mixing, and axial transport in a lab--scale HSBR. An industrial--grade polypropylene powder is modelled using calibrated contact parameters. Mixing is quantified using the Lacey index in axial (z) and cross--sectional (xy) directions. Particle circulation is characterised via cycle--time analysis and a coarse--grained angular velocity field. Axial dispersion coefficients are obtained from particle trajectories using both…
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