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Large Eddy Simulation of Horizontal Particle-Laden Channel<br />
Flows with Effect of Wall Roughness<br />
A. Konan ∗ , O. Simonin ∗ and K. D. Squires †<br />
Detailed analysis of the particle behaviour in horizontal channel in experimental<br />
works by Schade et al. 1 , Sommerfeld et al. 2, 3 show that the wall roughness<br />
affects strongly the particle transport. They observed a modification of pressure loss,<br />
particle mass flux, particle mean and fluctuating velocities along a narrow channel,<br />
due to the roughness effect on the particle-wall interaction mechanism. Such an effect<br />
4, 5,<br />
has been accounted for in several numerical studies based on RANS approaches<br />
6, 7 leading to very convincing results. In particular, according to Sommerfeld, the<br />
roughness effect may be accounted for by assuming that any incident particle collides<br />
with a virtual wall with a random inclination obeying a given truncated Gaussian<br />
probability distribution function satifying the realisability of the particle bouncing<br />
angle.<br />
We have carried out Large-Eddy Simulation (LES) of the carrier phase flow coupled<br />
with Discrete Particle Simulation (DPS) using the Sommerfeld’s virtual wall<br />
model. Lagrangian particle tracking is computed by assuming only gravity and drag<br />
forces. Simulations are performed in the dilute limit in which particle-particle collisions<br />
are accounted for, using a deterministic approach (hard-sphere model), but<br />
neglecting the modification of the underlying carrier flow by momentum exchange<br />
with the particles. Computations were performed for spherical glass beads with diameters<br />
between 130µm and 195µm and different wall roughness standard deviations<br />
(1.2 ◦ and 7.0 ◦ ). The numerical predictions (mass flux, mean and turbulent velocities)<br />
are compared with Sommerfeld’s experimental results 8 .<br />
In addition, statistical properties of the incident and bouncing particle velocities<br />
are measured from the simulations and used for the theoretical derivation of particulate<br />
eulerian wall boundary conditions 9 .<br />
∗ Institut de Mécanique des Fluides, Allée du Professeur Camille Soula, 31400 Toulouse, France.<br />
† Department of Mechanical and Aerospace Engineering, Arizona State University, Tempe, Ari-<br />
zona 85287, USA<br />
1 K.-P Schade and Th. Hädrich, 3th International conference on multiphase flow, ICMF’98,<br />
Lyon,France, June 8-12 ,(1998).<br />
2 M. Sommerfeld and N. Huber, Int. J. Multiphase Flow 25,(1999).<br />
3 J. Kussin and M. Sommerfeld, Experiments in Fluids 33,(2002).<br />
4 Y. Tsuji, T. Oshima and Y. Morikawa, KONA 3,(1985).<br />
5 M. Sommerfeld, Int. J. Multiphase Flow 18,(1992).<br />
6 M. Sommerfeld and J. Kussin, Powder Technology 142, 180-192 (2004).<br />
7 Xia Zhang and Lixing Zhou, 5th International conference on multiphase flow, ICMF’04, Yokohama,<br />
Japan, May 30 - June 4, 162 (2004).<br />
8 Sommerfeld, 11th Workshop on two-phase flow predictions, Merseburg, Germany, April 5-<br />
8 ,(2005).<br />
9 A. Konan, O. Simonin and J. Adou, 11th Workshop on two-phase flow predictions, Merseburg,<br />
Germany, April 5-8, (2005).<br />
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