Direct Numerical Simulation of Sediment Transport in Turbulent Open Channel Flow

Direct numerical simulations of interface-resolved sediment transport in horizontal open-channel flow are currently being performed on the XC-4000. The channel bottom boundary is roughened with a fixed layer of spheres and about 9000 particles are allowed to move within the computational domain. The density ratio of the solid and fluid phase is 1.7 and the bulk Reynolds number of the flow is 2880. In the present configuration, the particles tend to accumulate near the bed because of gravity, but due to the turbulent motions, a cycle of resuspension and deposition is produced. This leads to a particle concentration profile which decreases with the distance from the bed. The preliminary results show that the presence of particles strongly modifies the mean fluid velocity and turbulent fluctuation profiles. The dispersed phase lags the carrier phase on average across the whole channel height. Both observations confirm previous experimental evidence. The different observations suggest that particle inertia, finite-size and finite-Reynolds effects together with gravity play an important role in this flow configuration. Several potential mechanisms of turbulence-particle interaction are discussed.

[1]  禰津 家久,et al.  Turbulence in open-channel flows , 1993 .

[2]  K. Kiger,et al.  Suspension and turbulence modification effects of solid particulates on a horizontal turbulent channel flow , 2002 .

[3]  H. C. Simpson Bubbles, drops and particles , 1980 .

[4]  A. Tanière,et al.  On the behaviour of solid particles in a horizontal boundary layer with turbulence and saltation effects , 1997 .

[5]  Markus Uhlmann,et al.  Experience with DNS of particulate flow using a variant of the immersed boundary method , 2006 .

[6]  R. Verzicco,et al.  A Finite-Difference Scheme for Three-Dimensional Incompressible Flows in Cylindrical Coordinates , 1996 .

[7]  C. Peskin The immersed boundary method , 2002, Acta Numerica.

[8]  Sanjoy Banerjee,et al.  Particle behavior in the turbulent boundary layer. II. Velocity and distribution profiles , 1995 .

[9]  M. Uhlmann,et al.  Direct Numerical Simulation of Sediment Transport in a Horizontal Channel , 2006 .

[10]  R. Glowinski,et al.  A distributed Lagrange multiplier/fictitious domain method for particulate flows , 1999 .

[11]  Christof Hinterberger,et al.  Dreidimensionale und tiefengemittelte Large-Eddy-Simulation von Flachwasserströmungen , 2004 .

[12]  Markus Uhlmann,et al.  Interface-resolved direct numerical simulation of vertical particulate channel flow in the turbulent regime , 2008, 1108.6233.

[13]  C. Peskin Flow patterns around heart valves: A numerical method , 1972 .

[14]  Giovanni Paolo Romano,et al.  Particle–fluid interactions in a plane near-wall turbulent flow , 2004, Journal of Fluid Mechanics.

[15]  W. Rodi,et al.  Large Eddy Simulation for Complex Turbulent Flows of Practical Interest , 1996 .

[16]  M. Uhlmann An immersed boundary method with direct forcing for the simulation of particulate flows , 2005, 1809.08170.

[17]  Sanjoy Banerjee,et al.  Numerical investigation of the effects of large particles on wall-turbulence , 1997 .

[18]  Charles S. Peskin,et al.  Flow patterns around heart valves: a digital computer method for solving the equations of motion , 1973 .

[19]  C. Peskin Acta Numerica 2002: The immersed boundary method , 2002 .

[20]  O. Daube,et al.  A finite difference method for 3D incompressible flows in cylindrical coordinates , 2005 .

[21]  Ernst Heinrich Hirschel,et al.  Flow Simulation with High-Performance Computers II , 1996 .

[22]  Marcelo Horacio Garcia,et al.  Sedimentation engineering : processes, measurements, modeling, and practice , 2008 .

[23]  M. I. Yudine Physical Considerations on Heavy-particle Diffusion , 1959 .

[24]  Marian Muste,et al.  Two-phase flow insights into open-channel flows with suspended particles of different densities , 2009 .