Hostname: page-component-78c5997874-v9fdk Total loading time: 0 Render date: 2024-11-11T03:01:23.342Z Has data issue: false hasContentIssue false

Coefficients of Time and Length Scales of Turbulent Eddies

Published online by Cambridge University Press:  05 May 2011

Keh-Chin Chang*
Affiliation:
Department of Aeronautics and Astronautics, National Cheng Kung University, Tainan, Taiwan 70101, R.O.C.
Shih-Shiang Jeng*
Affiliation:
Department of Aeronautics and Astronautics, National Cheng Kung University, Tainan, Taiwan 70101, R.O.C.
*
*Professor
**Graduate student
Get access

Abstract

The turbulence time and length scales representing the energy containing eddies are by Tt = CtT k/ε and ℓt = Ct k32/ε, respectively, while the Kolmogorov time and length scales representing the energy dissipative eddies are expressed by Tk = CkT (ν/ε)1/2 and ℓk = Ck3/ε)1/4, respectively. The available DNS data for fully developed channel flows with and without wall injection / suction are used to determine the coefficients. It is found that, with the typical values of CtT = Ct = 1 which are usually adopted in the turbulence study, ckT = 2 and Ck = 3. However, this set of coefficients lead to underprediction of the thickness of viscous sublayer . By relaxing the usual assumption of CtT = Ct= 1, a new set of coefficients: CtT = Ct = 0.8, CkT = 4, and Ck = 9 is suggested. The calculated with this set of coefficients becomes more physically reasonable.

Type
Articles
Copyright
Copyright © The Society of Theoretical and Applied Mechanics, R.O.C. 2002

Access options

Get access to the full version of this content by using one of the access options below. (Log in options will check for institutional or personal access. Content may require purchase if you do not have access.)

References

REFERENCES

1Bejan, A., Convection Heat Transfer, 2nd Edition, John Wiley, New York, pp. 303310 (1995).Google Scholar
2Shih, T. H. and Lumley, J. L., “Kolmogorov Behavior of New-wall Turbulence and Its Application in Turbulence Modelin.” Int. J. Computational Fluid Dynamics, 1, pp. 4356 (1993).CrossRefGoogle Scholar
3Patel, V. C., Rodi, W. and Scheuerer, G., “Turbulence Models for Near-wall and Low Reynolds Number Flows: a Review,” AIAA J., 23, pp. 13081319 (1985).CrossRefGoogle Scholar
4Chen, C. J. and Jaw, S. Y., Fundamentals of Turbulence Modeling, Taylor & Francis, Washington, D. C., pp. 115119 (1998).Google Scholar
5Yang, Z. and Shih, H. T., “New Time Scale B1ased k – ε Model for Near-wall Turbulence,” AIAA J., 31, pp. 11911198 (1993).Google Scholar
6Rahman, M. M. and Siikonen, T., “Improved Low Reynolds Number k –ε Model,” AIAA J., 38, pp. 12981300 (2000).CrossRefGoogle Scholar
7Shyu, M. J. and Chang, K. C., “Limit of Eddy Length Scales in Use of Low-Reynolds-Number k – ε Models,” The Chinese J. Mechanics, B, 16, pp. 109118 (2000).Google Scholar
8Durbin, P. A., “Near-wall Turbulence Closure Modeling without Damping Functions,” Theoretical Computational Fluid Dynamics, 3, pp. 113 (1991).Google Scholar
9Durbin, P. A., “Separated Flow Computations with the k – ε – V 2 Model,” AIAA J., 33, pp. 659664 (1995).Google Scholar
10Sumitani, Y. and Kasagi, N., “Direct Numerical Simulation of Turbulent Transport with Uniform Wall Injection and Suction,” AIAA J., 33, pp. 12201228 (1995).CrossRefGoogle Scholar
11Kim, J., Moin, P. and Moser, R., “Turbulence Statistics in Fully Developed Channel Flow at Low-Reynolds-Number,” J. Fluid Mech., 177, pp. 133166 (1987).Google Scholar
12Kim, J., “Collaborative Testing of Turbulence Models,” ERCOFTAC Fluid Dynamics Database www Services, http://fluindigo.mech.surrey.ac.uk/.Google Scholar
13Moser, R. D., Kim, J. and Mansour, N. N., “Direct Numerical Simulation of Turbulent Channel Flow up to Reτ = 590,” Physics Fluids, 11, pp. 943945 (1999).Google Scholar
14Schildknecht, M., Miller, J. A. and Meier, G. E. A., “The Influence of Suction on the Structure of Turbulence in Fully Developed Pipe Flow,” J. Fluid Mech., 90, pp. 67107 (1979).CrossRefGoogle Scholar
15Julien, H. L., Kays, W. M. and Moffat, R. J., “Experimental Hydrodynamics of the Accelerated Turbulent Boundary Layer with and without Mass Injection,” J. Heat Transfer, 93, pp. 373379 (1971).Google Scholar