48 research outputs found
Evidence of reverse and intermediate size segregation in dry granular flows down a rough incline
In a dry granular flow, size segregation behave differently for a mixture
containing a few large beads with a size ratio (S) above 5 (Thomas, Phys.Rev.E
62,96(2000)). For moderate large S, large beads migrate to an intermediate
depth in the bed: this is called intermediate segregation. For the largest S,
large beads migrate to the bottom: this is called reverse segregation (in
contrast with surface segregation). As the reversal and intermediate depth
values depend on the bead fraction, this numerical study mainly uses a single
large tracer. Small fractions are also computed showing the link between a
tracer behavior and segregation process. For half-filled rotating drum and for
rough incline, two and three (3D) dimensional cases are studied. In the
tumbler, trajectories of a large tracer show that it reaches a constant depth
during the flow. For large S, this depth is intermediate with a progressive
sinking when S increases. Largest S correspond to tracers at the bottom of the
flow. All 3D simulation are in quantitative agreement with the experiments. In
the flow down an incline, a large tracer reaches an equilibrium depth during
flow. For large S, its depth is intermediate, inside the bed. For the largest
S, its depth is reverse, near the bottom. Results are slightly different for
thin or thick flow. For 3D thick flows, the reversal between surface and bottom
positions occurs within a short range of S: no tracer stabilizes near
mid-height and two reachable intermediate depth layers exist, below the surface
and above the bottom. For 3D thin flows, all intermediate depths are reachable,
depending on S. The numerical study of larger tracer fractions (5-10%) shows
the 3 segregation patterns (surface, intermediate, reverse) corresponding to
the 3 types of equilibrium depth. The reversal is smoother than for a single
tracer. It happens around S=4.5, in agreement with experiments.Comment: 18 pages, 27 figure
Influence of Rough and Smooth Walls on Macroscale Flows in Tumblers
Walls in discrete element method simulations of granular flows are sometimes
modeled as a closely packed monolayer of fixed particles, resulting in a rough
wall rather than a geometrically smooth wall. An implicit assumption is that
the resulting rough wall differs from a smooth wall only locally at the
particle scale. Here we test this assumption by considering the impact of the
wall roughness at the periphery of the flowing layer on the flow of
monodisperse particles in a rotating spherical tumbler. We find that varying
the wall roughness significantly alters average particle trajectories even far
from the wall. Rough walls induce greater poleward axial drift of particles
near the flowing layer surface, but decrease the curvature of the trajectories.
Increasing the volume fill level in the tumbler has little effect on the axial
drift for rough walls, but increases the drift while reducing curvature of the
particle trajectories for smooth walls. The mechanism for these effects is
related to the degree of local slip at the bounding wall, which alters the
flowing layer thickness near the walls, affecting the particle trajectories
even far from the walls near the equator of the tumbler. Thus, the proper
choice of wall conditions is important in the accurate simulation of granular
flows, even far from the bounding wall.Comment: 32 pages, 19 figures, regular article, accepted for publication in
Physical Review E 200
Why antiplectic metachronal cilia waves are optimal to transport bronchial mucus
International audienceThe coordinated beating of epithelial cilia in human lungs is a fascinating problem from the hydrodynamics perspective. The phase lag between neighboring cilia is able to generate collective cilia motions, known as metachronal waves. Different kinds of waves can occur, antiplectic or symplectic, depending on the direction of the wave with respect to the flow direction. It is shown here, using a coupled lattice Boltzmann-immersed boundary solver, that the key mechanism responsible for their transport efficiency is a blowing-suction effect that displaces the interface between the periciliary liquid and the mucus phase. The contribution of this mechanism on the average flow generated by the cilia is compared to the contribution of the lubrication effect. The results reveal that the interface displacement is the main mechanism responsible for the better efficiency of antiplectic metachronal waves over symplectic ones to transport bronchial mucus. The conclusions drawn here can be extended to any two-layer fluid configuration having different viscosities, and put into motion by cilia-shaped or comb-plate structures, having a back-and-forth motion with phase lags
Slow axial drift in three-dimensional granular tumbler flow
Models of monodisperse particle flow in partially filled three-dimensional
tumblers often assume that flow along the axis of rotation is negligible. We
test this assumption, for spherical and double cone tumblers, using experiments
and discrete element method simulations. Cross sections through the particle
bed of a spherical tumbler show that, after a few rotations, a colored band of
particles initially perpendicular to the axis of rotation deforms: particles
near the surface drift toward the pole, while particles deeper in the flowing
layer drift toward the equator. Tracking of mm-sized surface particles in
tumblers with diameters of 8-14 cm shows particle axial displacements of one to
two particle diameters, corresponding to axial drift that is 1-3% of the
tumbler diameter, per pass through the flowing layer. The surface axial drift
in both double cone and spherical tumblers is zero at the equator, increases
moving away from the equator, and then decreases near the poles. Comparing
results for the two tumbler geometries shows that wall slope causes axial
drift, while drift speed increases with equatorial diameter. The dependence of
axial drift on axial position for each tumbler geometry is similar when both
are normalized by their respective maximum values
Écoulement granulaire et ségrégation en tambour tournant lisse ou rugueux
La ségrégation axiale en tambour tournant sphérique est étudiée à travers l'influence du taux de remplissage et de la rugosité des parois. L'étude des écoulements monodisperses a mis en évidence la courbure des trajectoires des particules et l'existence de cellules de convection. Nous montrons comment ces deux caractéristiques, couplées à la ségrégation amène à une organisation axiale en trois bandes petites/grandes/petites ou grandes/petites/grandes selon le phénomène dominant
Profils de vitesse des Ă©coulements granulaires
Nous présentons une étude expérimentale et
numérique de l'écoulement sur plan incliné de milieux granulaires monodisperse et
bidisperse ségrégé. Après présentation des profils de vitesse théoriques attendus, et
ceux observés expérimentalement et numériquement, que l'augmentation de la vitesse
d'écoulement par la présence de grandes particules à la surface a lieu sur les
écoulements de faibles épaisseurs. Dès que l'écoulement est plus épais, on retrouve
numériquement la superposition des deux profils monodisperses, contrairement au cas
expérimental
Comparaison de différentes méthodes numériques pour l'étude de la collision dipôle-paroi
Nous présentons une confrontation entre
différentes méthodes numériques pour résoudre les équation de Navier-Stokes : Volumes
Finis, Différences Finies, Fourier, Tchebyshev, Gaz de Boltzmann, Ondelettes, ... pour
l'étude de la collision entre un dipôle et une paroi non glissante. La précision obtenue
en fonction de la résolution, l'ordre des méthodes, les temps de calculs requis seront
présentés pour toutes les méthodes
Instabilité dans les écoulements granulaires ségrégés
National audienceL'écoulement sur plan incliné d'un milieux granulaire sec constitué de deux types de particules est étu-dié. Les particules présentent un rapport de taille et de densité (les grandes particules sont plus denses). Pour un système initialement bi-couche (particules denses en surface), une instabilité de Rayleigh-Taylor se développe pendant l'écoulement. Dans le cas d'un système initialement homogène, la ségrégation va induire la formation d'une couche de particules grandes et denses à la surface qui se déstabilisera dans un second temps. Dans les deux cas, l'écoulement granulaire converge vers un système de bandes alternées avec des cellules de recirculation analogues aux cellules de convection de Rayleigh-Bénard. Abstract : Dry granular flow made of two types of particle over a rough incline is studied. Particles have a size and a density ratio (large particles are denser). When the system is initially made of two layers (dense particles above), a Rayleigh-Taylor instability develops during the flow. In the case of an initially homogeneous system, the granular segregation will lead to the formation of a layer of dense and large particles at the surface which will destabilise in a second time. For both cases, the granular flow evolves toward a pattern of alternating bands with recirculation cells analogous to Rayleigh-Bénard convection cells
Rayleigh-Taylor and Rayleigh-BĂ©nard like instabilities in two-size two-densities granular flow
International audienc