2006
DOI: 10.1088/1742-5468/2006/07/p07019
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Transport of small particles through a 3D packing of spheres: experimental and numerical approaches

Abstract: In this paper, we study the transport of particles through a porous structure. Experimentally, we focus our attention on the dependence of the mean transit time on some parameters like the number of small particles injected in the structure, and the height of the packing. We have developed a numerical model, based on a DEM method, to simulate the experiment. This model is useful for accessing the internal structure of the packing and for analysing precisely the influence of the restitution coefficient and the … Show more

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Cited by 23 publications
(15 citation statements)
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References 8 publications
(12 reference statements)
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“…5 cially for larger expansions (x > 0.6). Thus, if the pellets bounce more they can more easily find their way into the space between coke particles, giving an increase in f. This observation is consistent with the results of the study of Lomine and Oger: 6) Pellets with higher restitution coefficients spend less time to percolate through coke layer, which means that the total number of pellet particles that percolate throughout the coke layer to the bottom plate, depicted in Fig. 6, is higher.…”
Section: Coefficient Of Restitutionsupporting
confidence: 87%
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“…5 cially for larger expansions (x > 0.6). Thus, if the pellets bounce more they can more easily find their way into the space between coke particles, giving an increase in f. This observation is consistent with the results of the study of Lomine and Oger: 6) Pellets with higher restitution coefficients spend less time to percolate through coke layer, which means that the total number of pellet particles that percolate throughout the coke layer to the bottom plate, depicted in Fig. 6, is higher.…”
Section: Coefficient Of Restitutionsupporting
confidence: 87%
“…The difference in percolation between pellets of diameters 3 mm and 4 mm is, however, rather small. It should be noted that the condition for Dpe = 4 mm still exceeds the critical ratio 6,29) of bed (coke) particle diameter to percolating (pellet) particle diameter, which expresses the lowest value of Dco/Dpe at which the smaller particle can drain through the bed. The results indicate that increasing the size of the percolating particles is a feasible method to reduce inter-particle percolation.…”
Section: Pellet Diametermentioning
confidence: 99%
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“…A rough estimate of the drainage speed of these particles is about 1 mm/sec, although some particles travel through the bed several times faster whereas others never make it out of the bed. Comparison with drainage experiments of Lomine and Oger [34] without shearing is difficult because different bead size ratios were used; however, shearing significantly accelerates the drainage rate (factor of five or more).…”
Section: Drainage Out Of the Bedmentioning
confidence: 99%
“…Segregation studies by Lominé and Oger [34,35] examined the percolation of smaller particles, diameter d 1 , draining through a static, dense granular bed of larger particles, diameter d 0 . If they are sufficiently small, d 1 ≤ d 0 /6.46, the small beads poured onto a granular bed percolate through the bed similar to a pachinko gaming machine.…”
mentioning
confidence: 99%