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Scale invariance in finite Reynolds number homogeneous isotropic turbulence

Published online by Cambridge University Press:  07 February 2019

L. Djenidi
Affiliation:
Discipline of Mechanical Engineering, School of Engineering, University of Newcastle, Newcastle, 2308 NSW, Australia
R. A. Antonia
Affiliation:
Discipline of Mechanical Engineering, School of Engineering, University of Newcastle, Newcastle, 2308 NSW, Australia
S. L. Tang*
Affiliation:
Institute for Turbulence-Noise-Vibration Interaction and Control, Shenzhen Graduate School, Harbin Institute of Technology, Shenzhen518055, PR China
*
†Email address for correspondence: shunlin.tang88@gmail.com

Abstract

The problem of homogeneous isotropic turbulence (HIT) is revisited within the analytical framework of the Navier–Stokes equations, with a view to assessing rigorously the consequences of the scale invariance (an exact property of the Navier–Stokes equations) for any Reynolds number. The analytical development, which is independent of the 1941 (K41) and 1962 (K62) theories of Kolmogorov for HIT for infinitely large Reynolds number, is applied to the transport equations for the second- and third-order moments of the longitudinal velocity increment, $(\unicode[STIX]{x1D6FF}u)$. Once the normalised equations and the constraints required for complying with the scale-invariance property of the equations are presented, results derived from these equations and constraints are discussed and compared with measurements. It is found that the fluid viscosity, $\unicode[STIX]{x1D708}$, and the mean kinetic energy dissipation rate, $\overline{\unicode[STIX]{x1D716}}$ (the overbar denotes spatial and/or temporal averaging), are the only scaling parameters that make the equations scale-invariant. The analysis further leads to expressions for the distributions of the skewness and the flatness factor of $(\unicode[STIX]{x1D6FF}u)$ and shows that these distributions must exhibit plateaus (of different magnitudes) in the dissipative and inertial ranges, as the Taylor microscale Reynolds number $Re_{\unicode[STIX]{x1D706}}$ increases indefinitely. Also, the skewness and flatness factor of the longitudinal velocity derivative become constant as $Re_{\unicode[STIX]{x1D706}}$ increases; this is supported by experimental data. Further, the analysis, backed up by experimental evidence, shows that, beyond the dissipative range, the behaviour of $\overline{(\unicode[STIX]{x1D6FF}u)^{n}}$ with $n=2$, 3 and 4 cannot be represented by a power law of the form $r^{\unicode[STIX]{x1D701}_{n}}$ when the Reynolds number is finite. It is shown that only when $Re_{\unicode[STIX]{x1D706}}\rightarrow \infty$ can an $n$-thirds law (i.e. $\overline{(\unicode[STIX]{x1D6FF}u)^{n}}\sim r^{\unicode[STIX]{x1D701}_{n}}$, with $\unicode[STIX]{x1D701}_{n}=n/3$) emerge, which is consistent with the onset of a scaling range.

Information

Type
JFM Papers
Copyright
© 2019 Cambridge University Press 
Figure 0

Table 1. Comparison of theoretical results. The $2/3$ law is obtained if one assumes that $S$ is constant in the inertial range. Both $\unicode[STIX]{x1D707}$ and $\unicode[STIX]{x1D708}$ are supposed to be positive numbers ($0<\unicode[STIX]{x1D707},\unicode[STIX]{x1D708}<1$).

Figure 1

Table 2. Testing the K41 and K62 predictions for the skewness and flatness factor of ($\unicode[STIX]{x2202}u/\unicode[STIX]{x2202}x$) against the NSEq-based results.

Figure 2

Figure 1. Dependence of $-S_{0}$ and $F_{0}$ on $Re_{\unicode[STIX]{x1D706}}$ in a plane jet. ▴, Antonia, Anselmet & Chambers (1986); ▾, Sreenivasan & Antonia (1997); ●, Antonia et al. (2017). Blue symbols are reproduced from figure 4 of Tang et al. (2018) without identifying the data sources. The blue and red dashed lines correspond to magnitudes of 0.53 and 10, respectively.

Figure 3

Figure 2. Distributions of Kolmogorov normalised $\overline{(\unicode[STIX]{x1D6FF}u)^{2}}$ on the centreline of a turbulent round jet for two $Re_{\unicode[STIX]{x1D706}}$. For each $Re_{\unicode[STIX]{x1D706}}$, several distributions along the jet axis over a range of positions between 30 and 60 times the jet nozzle diameter are reported.

Figure 4

Figure 3. Effect of the Reynolds number on the distributions of $\overline{(\unicode[STIX]{x1D6FF}u^{\ast })^{2}}$ in various flows normalised by $(\unicode[STIX]{x1D702},v_{K})$ (top) and $(u^{\prime },L)$. Black lines: grid turbulence (Zhou & Antonia (2000), $Re_{\unicode[STIX]{x1D706}}=25$–99); red lines: circular cylinder wake (Antonia, Zhou & Romano (2002), $Re_{\unicode[STIX]{x1D706}}=160$–280); pink lines: plane jet (Antonia et al. (2017), $Re_{\unicode[STIX]{x1D706}}=550$–1067); green lines: round jet (Xu, Antonia & Rajagopalan (2001), $Re_{\unicode[STIX]{x1D706}}=235$–545). The blue dashed line represents $r^{\ast 2}/15$.

Figure 5

Figure 4. Distributions of $-\overline{(\unicode[STIX]{x1D6FF}u)^{3}}/(\overline{\unicode[STIX]{x1D716}}r)$ at $Re_{\unicode[STIX]{x1D706}}=72$ (▪), $144$ (●) and 2260 (♦) in grid turbulence (Gagne et al.2004).

Figure 6

Figure 5. The $Re_{\unicode[STIX]{x1D706}}$ variation of the second term on the right-hand side of (3.15) (red curve) and the third term on the right-hand side of (3.16) (blue curve), divided by $r^{\ast }$ and $r^{\ast 4/3}$, respectively, for $r=\unicode[STIX]{x1D706}$ in grid turbulence. The red curve has already been reported in Tang et al. (2017) (see their figure 7).