A theory for turbulent pipe and channel flows

A theory for fully developed turbulent pipe and channel flows is proposed which extends the classical analysis to include the effects of finite Reynolds number. The proper scaling for these flows at finite Reynolds number is developed from dimensional and physical considerations using the Reynolds-averaged Navier–Stokes equations. In the limit of infinite Reynolds number, these reduce to the familiar law of the wall and velocity deficit law respectively. The fact that both scaled profiles describe the entire flow for finite values of Reynolds number but reduce to inner and outer profiles is used to determine their functional forms in the ‘overlap’ region which both retain in the limit. This overlap region corresponds to the constant, Reynolds shear stress region (30 < y+ < 0.1R+ approximately, where R+ = u*R/v). The profiles in this overlap region are logarithmic, but in the variable y + a where a is an offset. Unlike the classical theory, the additive parameters, Bi, Bo, and log coefficient, 1/κ, depend on R+. They are asymptotically constant, however, and are linked by a constraint equation. The corresponding friction law is also logarithmic and entirely determined by the velocity profile parameters, or vice versa. It is also argued that there exists a mesolayer near the bottom of the overlap region approximately bounded by 30 < y+ < 300 where there is not the necessary scale separation between the energy and dissipation ranges for inertially dominated turbulence. As a consequence, the Reynolds stress and mean flow retain a Reynolds number dependence, even though the terms explicitly containing the viscosity are negligible in the single-point Reynolds-averaged equations. A simple turbulence model shows that the offset parameter a accounts for the mesolayer, and because of it a logarithmic behaviour in y applies only beyond y+ > 300, well outside where it has commonly been sought. The experimental data from the superpipe experiment and DNS of channel flow are carefully examined and shown to be in excellent agreement with the new theory over the entire range 1.8 × 102 < R+ < 5.3 × 105. The Reynolds number dependence of all the parameters and the friction law can be determined from the single empirical function, H = A/(ln R+)α for α > 0, just as for boundary layers. The Reynolds number dependence of the parameters diminishes very slowly with increasing Reynolds number, and the asymptotic behaviour is reached only when R+ [Gt ] 105.

[1]  G. I. Barenblatt,et al.  Scaling of the intermediate region in wall-bounded turbulence: The power law , 1998 .

[2]  F. Fendell,et al.  Asymptotic analysis of turbulent channel and boundary-layer flow , 1972, Journal of Fluid Mechanics.

[3]  J. Lumley,et al.  A First Course in Turbulence , 1972 .

[4]  W. Reynolds Computation of Turbulent Flows , 1975 .

[5]  K. Stewartson Mechanics of fluids , 1978, Nature.

[6]  F. Durst,et al.  LDA measurements in the near-wall region of a turbulent pipe flow , 1995, Journal of Fluid Mechanics.

[7]  G. I. Barenblatt,et al.  Scaling laws for fully developed turbulent shear flows. Part 1. Basic hypotheses and analysis , 1993, Journal of Fluid Mechanics.

[8]  A. Perry,et al.  Scaling laws for pipe-flow turbulence , 1975, Journal of Fluid Mechanics.

[9]  Robert R. Long,et al.  Experimental evidence for the existence of the ‘mesolayer’ in turbulent systems , 1981, Journal of Fluid Mechanics.

[10]  B. Massey,et al.  Mechanics of Fluids , 2018 .

[11]  Luciano Castillo,et al.  Zero-Pressure-Gradient Turbulent Boundary Layer , 1997 .

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

[13]  John Kim,et al.  On the structure of pressure fluctuations in simulated turbulent channel flow , 1989, Journal of Fluid Mechanics.

[14]  Response to “Scaling of the intermediate region in wall-bounded turbulence: The power law” [Phys. Fluids 10, 1043 (1998)] , 1998 .

[15]  G. I. Barenblatt,et al.  Scaling laws for fully developed turbulent shear flows. Part 2. Processing of experimental data , 1993, Journal of Fluid Mechanics.

[16]  Alexander J. Smits,et al.  A NEW MEAN VELOCITY SCALING FOR TURBULENT BOUNDARY LAYERS , 1998 .

[17]  H. Weitzner,et al.  Perturbation Methods in Applied Mathematics , 1969 .

[18]  Boundary Layers with Pressure Gradient: Another Look at the Equilibrium Boundary Layer. , 1993 .

[19]  A. Smits,et al.  Mean-flow scaling of turbulent pipe flow , 1998, Journal of Fluid Mechanics.

[20]  P. Moin,et al.  Turbulence statistics in fully developed channel flow at low Reynolds number , 1987, Journal of Fluid Mechanics.

[21]  G. I. Barenblatt Scaling: Self-similarity and intermediate asymptotics , 1996 .

[22]  G. I. Barenblatt,et al.  Scaling laws for fully developed turbulent flow in pipes: discussion of experimental data. , 1997, Proceedings of the National Academy of Sciences of the United States of America.

[23]  J. R. Pannell,et al.  Similarity of Motion in Relation to the Surface Friction of Fluids , 1914 .

[24]  H. Squire I. Reconsideration of the theory of free turbulence , 1948 .

[25]  R. Panton Scaling Turbulent Wall Layers , 1990 .

[26]  H. Tennekes,et al.  Outline of a second-order theory of turbulent pipe flow. , 1968 .