Low Reynolds number modeling of turbulent flows with and without wall transpiration

A full Reynolds-stress closure that is capable of describing the flow all the way to the wall is formulated. The closure is based on the conventional high Reynolds number form of the redistribution model, the inclusion of molecular diffusion, and a modified dissipation model to account for viscous effects near a wall. Two dissipation models are investigated along with two gradient diffusion and two redistribution models. Their respective effects on the calculated flow properties are assessed by comparing them with the data of fully developed turbulent flows and a developing pipe flow with wall transpiration. The near-wall behavior is very well predicted; however, the wall correction to the redistribution modeling is found to have little effect on the calculated results. The overall behavior of the fully developed turbulent flows is best described by a nonisotropic gradient diffusion model, a return-to-isotropy redistribution model, and a dissipation model that accounts for viscous behavior near a wall. This same closure also gives the best prediction of the axial pressure drop behavior along a pipe with a uniform wall suction. Furthermore, the near-wall behavior of such a flow is very well predicted by this closure.

[1]  Wolfgang Rodi,et al.  Prediction of free shear flows: A comparison of the performance of six turbulence models , 1972 .

[2]  Wolfgang Rodi,et al.  A Reynolds-stress closure model of turbulence applied to the calculation of a highly curved mixing layer , 1981, Journal of Fluid Mechanics.

[3]  B. Stratford An experimental flow with zero skin friction throughout its region of pressure rise , 1959, Journal of Fluid Mechanics.

[4]  B. Launder,et al.  Ground effects on pressure fluctuations in the atmospheric boundary layer , 1978, Journal of Fluid Mechanics.

[5]  P. A. Smith,et al.  Prediction of the effect of streamline curvature on turbulence , 1975 .

[6]  George L. Mellor,et al.  A survey of the mean turbulent field closure models. , 1973 .

[7]  D. Spalding,et al.  A calculation procedure for heat, mass and momentum transfer in three-dimensional parabolic flows , 1972 .

[8]  A. J. Reynolds,et al.  Turbulence in plane channel flows , 1981, Journal of Fluid Mechanics.

[9]  M. R. Head,et al.  Some observations on skin friction and velocity profiles in fully developed pipe and channel flows , 1969, Journal of Fluid Mechanics.

[10]  G. Meier,et al.  The influence of suction on the structure of turbulence in fully developed pipe flow , 1979, Journal of Fluid Mechanics.

[11]  N. Afzal,et al.  Analysis of turbulent pipe and channel flows at moderately large Reynolds number , 1973, Journal of Fluid Mechanics.

[12]  W. Jones,et al.  Some properties of sink-flow turbulent boundary layers , 1972, Journal of Fluid Mechanics.

[13]  K. Chien,et al.  Predictions of Channel and Boundary-Layer Flows with a Low-Reynolds-Number Turbulence Model , 1982 .

[14]  G. Mellor,et al.  A Hierarchy of Turbulence Closure Models for Planetary Boundary Layers. , 1974 .

[15]  A. J. Reynolds,et al.  Velocity distributions in plane turbulent channel flows , 1980, Journal of Fluid Mechanics.

[16]  B. Launder,et al.  Progress in the development of a Reynolds-stress turbulence closure , 1975, Journal of Fluid Mechanics.

[17]  Brian Launder,et al.  A Reynolds stress model of turbulence and its application to thin shear flows , 1972, Journal of Fluid Mechanics.

[18]  J. Rotta,et al.  Statistische Theorie nichthomogener Turbulenz , 1951 .

[19]  Luc R. Bissonnette,et al.  Experiments on the behaviour of an axisymmetric turbulent boundary layer with a sudden circumferential strain , 1974, Journal of Fluid Mechanics.

[20]  K.-Y. Chien,et al.  Predictions of channel and boundary-layer flows with a low-Reynolds-number two-equation model of turbulence , 1980 .

[21]  Brian Launder,et al.  Contribution towards a Reynolds-stress closure for low-Reynolds-number turbulence , 1976, Journal of Fluid Mechanics.

[22]  J. Laufer,et al.  The Structure of Turbulence in Fully Developed Pipe Flow , 1953 .

[23]  T. Y. Na,et al.  Computational methods in engineering boundary value problems , 1979 .

[24]  Francis H. Harlow,et al.  Transport Equations in Turbulence , 1970 .

[25]  W. Jones,et al.  The prediction of laminarization with a two-equation model of turbulence , 1972 .

[26]  W. C. Reynolds,et al.  Asymptotic near‐wall stress dissipation rates in a turbulent flow , 1983 .

[27]  Brian Launder,et al.  Numerical computation of convective heat transfer in complex turbulent flows: time to abandon wall functions? , 1984 .