2013
DOI: 10.1016/j.powtec.2013.08.033
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The rheology of dense granular flows in a disc impeller high shear granulator

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Cited by 13 publications
(9 citation statements)
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“…They showed that the powder rheology was mainly determined by the content of fines, and proposed a rheological model using mathematical modelling based on continuum mechanics. Based on experiments and CFD simulations, Khalilitehrani et al (2013;2015) studied the rheology of dense granular flows in a disc impeller high shear granulator. Remy et al (2009Remy et al ( , 2011 carried out stress analyses of particle flow in a rotating blade mixer using DEM.…”
Section: Introductionmentioning
confidence: 99%
“…They showed that the powder rheology was mainly determined by the content of fines, and proposed a rheological model using mathematical modelling based on continuum mechanics. Based on experiments and CFD simulations, Khalilitehrani et al (2013;2015) studied the rheology of dense granular flows in a disc impeller high shear granulator. Remy et al (2009Remy et al ( , 2011 carried out stress analyses of particle flow in a rotating blade mixer using DEM.…”
Section: Introductionmentioning
confidence: 99%
“…However, in this work a new modeling framework is developed and the method it is not dependent on the specific choice of flow model. More accurate models for dense granular flows are needed and under development [13][14][15][16] for more reliable results. The present modeling framework is, however, not affected by the detailed flow modeling and in future work more accurate flow simulations can easily be incorporated.…”
Section: Figure 1 Side and Top View Of The Two Regions In The Granulmentioning
confidence: 99%
“…The continuum approach to particle flows in high shear granulation was first used by Darelius et al [9] and Ng et al [10]. This has further been studied by Abrahamsson et al [11][12][13] and developed by Khalilitehrani et al [14][15][16] which shows promising results but also a need for further development. The HSG process is a continuously changing system where the continuous changes in particle properties are bound to affect the flow field and vice versa.…”
Section: Introductionmentioning
confidence: 99%
“…As indicated above, in a typical HSG equipment there is coexistence of relatively dilute (solid volume fractions ranging from 0 to 0.5) and very dense regions (ranging from a volume fraction of 0.5 to the maximum packing of the material) [8,9]. The flow situation in the former region is most often described by the rapid flow theory, whereas in the latter, the quasi-static flow regime is assumed.…”
Section: Introductionmentioning
confidence: 99%
“…This approach focuses on the transition regime capturing the liquid-solid transition with a pressure-dependent yield stress determined for individual particle types and sizes from a set of flow experiments. The results show good potential, but the model is not capable of treating the rapid regime [8]. In Khalilitehrani et al [17], the framework was extended and combined with a rapid regime, kinetic theory of granular flow (KTGF), model with a transition criterion based on a regime determining inertial number.…”
Section: Introductionmentioning
confidence: 99%