2014
DOI: 10.1016/j.ces.2014.04.040
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Forces acting on a single introduced particle in a solid–liquid fluidised bed

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Cited by 44 publications
(10 citation statements)
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“…Therefore, a constant solid concentration of ( ϕ m1 + ϕ m2 )/2 along the bed height is obtained. However, in the real liquid fluidized beds that operate under superficial liquid velocities smaller than the particle terminal settling velocity, the complete mixing status of the particle species might be hardly observed due to the local turbulence of the liquid flow and the resultant large liquid bubbles under high superficial liquid velocities …”
Section: Resultsmentioning
confidence: 99%
“…Therefore, a constant solid concentration of ( ϕ m1 + ϕ m2 )/2 along the bed height is obtained. However, in the real liquid fluidized beds that operate under superficial liquid velocities smaller than the particle terminal settling velocity, the complete mixing status of the particle species might be hardly observed due to the local turbulence of the liquid flow and the resultant large liquid bubbles under high superficial liquid velocities …”
Section: Resultsmentioning
confidence: 99%
“…Moreover, they were able to successfully reproduce the particle velocity distributions. Alternatively, Peng et al [124] studied the forces acting on a foreign particle that was introduced into a fluidized bed containing particles with a lower density. Employing their validated CFD-DEM model, they evaluated this system based on the foreign particle's collision frequency and classification velocity.…”
Section: Fluidized Bedsmentioning
confidence: 99%
“…To avoid the incorrect void fractions, several approaches have been applied. Peng et al [21] used a particle meshing method (PMM) in which the particle is meshed to the small parts before each sub-part is mapped to cells according to the location of their centroids. In the offset method, used by Alobaid et al [60] with a momentum and void fraction grid, the void fraction is defined with the Eulerian cell displacements and averaged across the calculated void fractions.…”
Section: Nomenclaturementioning
confidence: 99%
“…Computational fluid dynamics-discrete element method (CFD-DEM), also referred to as a combined continuum and discrete model (CCDM) ( [19] and [17]), is commonly used to obtain detailed information of the flow fields and the particle-particle interactions in gas-solid fluidized beds and pneumatic conveying ( [20]). Liquid fluidized beds have been also studied with good agreement ( [21], [22], [23], [24] and [25]). In the resent years, CFD-DEM has also been used to study particle batch settling ( [26] and [27]), sediment transport ( [28], [29], [30] and [31]), solid-liquid mixing ( [32]) and slurry transport in pipes ( [33], [34] and [35]).…”
Section: Introductionmentioning
confidence: 99%