2007
DOI: 10.1590/s0104-66322007000400007
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A study of the pneumatic conveying of non-spherical particles in a turbulent horizontal channel flow

Abstract: In this work, the pneumatic conveying of non-spherical isometric particles with different degrees of non-sphericity is studied. The solids mass loading fraction is small enough in order to have a dilute flow, so inter-particle collisions can be neglected. As a first approximation, only the aerodynamic drag force acting on the particles is considered, neglecting the lift forces and the particle rotation. The drag coefficient is calculated using the correlations of Haider and Levenspiel (1989) and Ganser (1993).… Show more

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Cited by 23 publications
(15 citation statements)
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“…Note that this method is different from common practice, e.g. 43,44 , where the inclusion of an equivalent diameter alone as the geometric parameter and optionally a shape factor, e.g. the sphericity, in the empirical drag coefficient is used to account for the departure in shape from a sphere, but the orientation dependency is ignored.…”
Section: Rementioning
confidence: 99%
“…Note that this method is different from common practice, e.g. 43,44 , where the inclusion of an equivalent diameter alone as the geometric parameter and optionally a shape factor, e.g. the sphericity, in the empirical drag coefficient is used to account for the departure in shape from a sphere, but the orientation dependency is ignored.…”
Section: Rementioning
confidence: 99%
“…The literature contains no information about the carrier phase turbulence modulation due to non-spherical particles [27]. Therefore, the conventional k- turbulence model was applied in the simulations without alteration.…”
Section: Turbulence Modellingmentioning
confidence: 99%
“…Particle shape is known to play a significant role on the particle-fluid interaction and particle dispersion in a two-phase flow and has been the subject of investigation in literature [24][25][26][27].…”
Section: Introductionmentioning
confidence: 99%
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“…First, in the dilute phase, a reduction in the pressure is observed due to the settling of the particles in the lower half of the pipe line [18]. The settling is a consequence of the dominant gravity effect and particles inertia that is leading to the particles separation [19]. The pressure reduction continues until it reaches a minimum pressure point which is corresponding to saltation velocity of the carrier phase.…”
Section: Introductionmentioning
confidence: 99%