Modeling of Turbulent Fluid Flow Over a Rough Wall With or Without Suction

[+] Author and Article Information
G. Grégoire, M. Favre-Marinet

Laboratory of Geophysical and Industrial Flows, Grenoble University, UJF-INPG-CNRS, BP 53X, 38041 Grenoble Cedex 9, France

F. Julien Saint Amand

Center Technique du Papier, BP 251, 38044 Grenoble Cedex 9, France

J. Fluids Eng 125(4), 636-642 (Aug 27, 2003) (7 pages) doi:10.1115/1.1593705 History: Received November 21, 2000; Revised February 12, 2003; Online August 27, 2003
Copyright © 2003 by ASME
Your Session has timed out. Please sign back in to continue.


Patel,  V. C., 1998, “Perspective: Flow at High Reynolds Number and Over Rough Surfaces-Achilles Heel of CFD,” ASME J. Fluids Eng., 120, pp. 434–444.
Clauser, F. H., 1956, “The Turbulent Boundary Layer,” Advances in Applied Mechanics, 4 , Academic Press, New York.
White, F. M., 1991, Viscous Fluid Flow, McGraw-Hill, New York.
Stevenson, T. N., 1963, “A Law of the Wall for Turbulent Boundary Layers With Suction or Injection,” Cranfield College, Aero. Report 166.
Simpson,  R. L., Whitten,  D. C., and Moffat,  R. J., 1970, “An Experimental Study of the Turbulent Prandtl Number of Air With Injection or Suction,” Int. J. Heat Mass Transfer, 13, pp. 125–143.
Wilcox, D. C., 1993, “Turbulence Modeling for CFD,” DCW Industries Inc., La Canada, CA.
Andersen, P. S., Kays, W. M., and Moffat, R. J., 1972, “The Turbulent Boundary Layer on a Porous Plate: An Experimental Study of the Fluid Mechanics for Adverse Free-Stream Pressure Gradients,” Report No. HMT-15, Department of Mechanical Engineering, Stanford University, CA.
Marko, J. J., and LaRiviere, C. J., 1999, “The Use of Computational Fluid Dynamics (CFD) in Pressure Screen Design,” Tappi 99 Proceedings, pp. 1477–1482.
Wolfstein,  M., 1969, “The Velocity and Temperature Distribution of One-Dimensional Flow With Turbulence Augmentation and Pressure Gradient,” Int. J. Heat Mass Transfer, 12, pp. 301–318.
Chen,  H. C., and Patel,  V. C., 1988, “Near-Wall Turbulence Models for Complex Flows Including Separation,” AIAA J., 26(6), pp. 641–648.
Taylor,  R. P., Coleman,  H. W., and Hodge,  B. K., 1985, “Prediction of Turbulent Rough-Wall Skin Friction Using a Discrete Element Approach,” ASME J. Fluids Eng., 107, pp. 251–257.
Webb, R. L., 1994, Principles of Enhanced Heat Transfer, John Wiley and Sons, New York.


Grahic Jump Location
Pattern of streamlines close to the screen basket. Vp/Vt=1/3.
Grahic Jump Location
Influence of the position of the virtual wall on the mean velocity profile at x=0
Grahic Jump Location
Mean velocity profiles at different positions along the wall
Grahic Jump Location
Influence of suction on the friction velocity
Grahic Jump Location
Mean velocity profile at x=0 for a moderate suction ratio. Vpor/Vt=0.0073.
Grahic Jump Location
Mean velocity profile at x=0 for a high suction ratio. Vpor/Vt=0.0104.
Grahic Jump Location
Mean velocity profile at x=0 plotted with internal variables. Vpor/Vt=0.0073.



Some tools below are only available to our subscribers or users with an online account.

Related Content

Customize your page view by dragging and repositioning the boxes below.

Related Journal Articles
Related eBook Content
Topic Collections

Sorry! You do not have access to this content. For assistance or to subscribe, please contact us:

  • TELEPHONE: 1-800-843-2763 (Toll-free in the USA)
  • EMAIL: asmedigitalcollection@asme.org
Sign In