2006
DOI: 10.1016/j.powtec.2006.08.002
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Determination of coalescence kernels for high-shear granulation using DEM simulations

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Cited by 86 publications
(34 citation statements)
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“…The aggregation kernel has been defined as a function of the collision frequency (C) and collision efficiency ψ. The collision frequency (which is a function of particle size [46]) is calculated based on the number of collisions occurring between the particle groups which can be obtained from EDEM TM based on the particle properties.…”
Section: Population Balance Model For Fbgmentioning
confidence: 99%
“…The aggregation kernel has been defined as a function of the collision frequency (C) and collision efficiency ψ. The collision frequency (which is a function of particle size [46]) is calculated based on the number of collisions occurring between the particle groups which can be obtained from EDEM TM based on the particle properties.…”
Section: Population Balance Model For Fbgmentioning
confidence: 99%
“…Gant et.al. [8] used DEM simulations to extract collision rates and energies in a disc-impeller granulator to use for PBM kernels. The disadvantage of the DEM method is that it becomes impractical for industrial size granulators where the number of particles may, by orders of magnitude, exceed 10 6 .…”
Section: Introductionmentioning
confidence: 99%
“…Although the underlying mechanisms of such processes are yet to be thoroughly grasped, granulation, a particle design process, is one such area where substantial progress has been made over the years [5]. The approaches for modeling such systems are as numerous as they are varied: Discrete Element Modeling (DEM) [6], Population Balance Modeling (PBM) [3,[7][8][9][10][11][12][13], hybrid models by combining PBM with DEM [14], PBM with Volume of Fluid (VoF) methods [15], and PBM with Computational Fluid Dynamics (CFD) [16], to name a few. Of the aforementioned, the most widely used are the DEM and PBM methods.…”
Section: Introductionmentioning
confidence: 99%