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Quantifying wall turbulence via a symmetry approach. Part 2. Reynolds stresses

Published online by Cambridge University Press:  05 July 2018

Xi Chen
Affiliation:
State Key Laboratory for Turbulence and Complex Systems and Department of Mechanics, College of Engineering, Peking University, Beijing, 100871, China Department of Mechanical Engineering, Texas Tech University, TX 79409-1021, USA
Fazle Hussain
Affiliation:
State Key Laboratory for Turbulence and Complex Systems and Department of Mechanics, College of Engineering, Peking University, Beijing, 100871, China Department of Mechanical Engineering, Texas Tech University, TX 79409-1021, USA
Zhen-Su She*
Affiliation:
State Key Laboratory for Turbulence and Complex Systems and Department of Mechanics, College of Engineering, Peking University, Beijing, 100871, China
*
Email address for correspondence: she@pku.edu.cn

Abstract

We present new scaling expressions, including high-Reynolds-number ($Re$) predictions, for all Reynolds stress components in the entire flow domain of turbulent channel and pipe flows. In Part 1 (She et al., J. Fluid Mech., vol. 827, 2017, pp. 322–356), based on the dilation symmetry of the mean Navier–Stokes equation a four-layer formula of the Reynolds shear stress length $\ell _{12}$ – and hence also the entire mean velocity profile (MVP) – was obtained. Here, random dilations on the second-order balance equations for all the Reynolds stresses (shear stress $-\overline{u^{\prime }v^{\prime }}$, and normal stresses $\overline{u^{\prime }u^{\prime }}$, $\overline{v^{\prime }v^{\prime }}$, $\overline{w^{\prime }w^{\prime }}$) are analysed layer by layer, and similar four-layer formulae of the corresponding stress length functions $\ell _{11}$, $\ell _{22}$, $\ell _{33}$ (hence the three turbulence intensities) are obtained for turbulent channel and pipe flows. In particular, direct numerical simulation (DNS) data are shown to agree well with the four-layer formulae for $\ell _{12}$ and $\ell _{22}$ – which have the celebrated linear scalings in the logarithmic layer, i.e. $\ell _{12}\approx \unicode[STIX]{x1D705}y$ and $\ell _{22}\approx \unicode[STIX]{x1D705}_{22}y$. However, data show an invariant peak location for $\overline{w^{\prime }w^{\prime }}$, which theoretically leads to an anomalous scaling in $\ell _{33}$ in the log layer only, namely $\ell _{33}\propto y^{1-\unicode[STIX]{x1D6FE}}$ with $\unicode[STIX]{x1D6FE}\approx 0.07$. Furthermore, another mesolayer modification of $\ell _{11}$ yields the experimentally observed location and magnitude of the outer peak of $\overline{u^{\prime }u^{\prime }}$. The resulting $-\overline{u^{\prime }v^{\prime }}$, $\overline{u^{\prime }u^{\prime }}$, $\overline{v^{\prime }v^{\prime }}$ and $\overline{w^{\prime }w^{\prime }}$ are all in good agreement with DNS and experimental data in the entire flow domain. Our additional results include: (1) the maximum turbulent production is located at $y^{+}\approx 12$; (2) the location of peak value $-\overline{u^{\prime }v^{\prime }}_{p}$ has a scaling transition from $5.7Re_{\unicode[STIX]{x1D70F}}^{1/3}$ to $1.5Re_{\unicode[STIX]{x1D70F}}^{1/2}$ at $Re_{\unicode[STIX]{x1D70F}}\approx 3000$, with a $1+\overline{u^{\prime }v^{\prime }}_{p}^{+}$ scaling transition from $8.5Re_{\unicode[STIX]{x1D70F}}^{-2/3}$ to $3.0Re_{\unicode[STIX]{x1D70F}}^{-1/2}$ ($Re_{\unicode[STIX]{x1D70F}}$ the friction Reynolds number); (3) the peak value $\overline{w^{\prime }w^{\prime }}_{p}^{+}\approx 0.84Re_{\unicode[STIX]{x1D70F}}^{0.14}(1-48/Re_{\unicode[STIX]{x1D70F}})$; (4) the outer peak of $\overline{u^{\prime }u^{\prime }}$ emerges above $Re_{\unicode[STIX]{x1D70F}}\approx 10^{4}$ with its location scaling as $1.1Re_{\unicode[STIX]{x1D70F}}^{1/2}$ and its magnitude scaling as $2.8Re_{\unicode[STIX]{x1D70F}}^{0.09}$; (5) an alternative derivation of the log law of Townsend (1976, The Structure of Turbulent Shear Flow, Cambridge University Press), namely, $\overline{u^{\prime }u^{\prime }}^{+}\approx -1.25\ln y+1.63$ and $\overline{w^{\prime }w^{\prime }}^{+}\approx -0.41\ln y+1.00$ in the bulk.

Information

Type
JFM Papers
Creative Commons
Creative Common License - CCCreative Common License - BY
This is an Open Access article, distributed under the terms of the Creative Commons Attribution licence (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted re-use, distribution, and reproduction in any medium, provided the original work is properly cited.
Copyright
© 2018 Cambridge University Press
Figure 0

Figure 1. (a) Budget of $\overline{u^{\prime }u^{\prime }}$ (2.1b). (b) Compensated plot of $\ell _{11}$, $\ell _{12}$, $\ell _{22}$ and $\ell _{33}$ (normalized by the half-channel height) divided by $1-r^{4}$ (Part 1). Note that the bulk layer (between $y_{buf}^{+}$ and $r_{core}$) has nearly constant values. Thicknesses of viscous sublayer ($y_{sub}^{+}=9.7$), buffer layer ($y_{buf}^{+}=41$) and core layer ($r_{core}=0.27$) shown by dashed lines. Data from DNS channel flow at $Re_{\unicode[STIX]{x1D70F}}=940$ (Hoyas & Jimenez 2006).

Figure 1

Table 1. A summary of the canonical scaling in the four layers of turbulent channels. Note that the log layer is contained in the bulk layer since $1-r^{4}\propto y$ as $r=1-y\rightarrow 1$ (towards the wall). For pipe flows, the scalings are the same as for channels except for $\ell _{ij}\propto 1-r^{5}$ in the bulk layer of pipes.

Figure 2

Figure 2. Reynolds shear stress profiles by (3.2) (solid lines) compared with DNS data (symbols) for channel flows in coordinates $y^{+}$ (a) and $y^{+}/Re_{\unicode[STIX]{x1D70F}}$ (b). The departure between data and our theory (i.e. $W_{12}^{+Theory}-W_{12}^{+DNS}$) is shown in (c,d), which is bounded within $\pm 0.01$. DNS channel data from Iwamoto, Suzuki & Kasagi (2002) for $Re_{\unicode[STIX]{x1D70F}}=300,650$, Hoyas & Jimenez (2006) for $Re_{\unicode[STIX]{x1D70F}}=940,2000$; Lee & Moser (2015) at $Re_{\unicode[STIX]{x1D70F}}=5200$. Also included are the prediction of $W_{12}^{+}$ for $Re_{\unicode[STIX]{x1D70F}}=50\,000$, awaiting future verification.

Figure 3

Figure 3. Scaling for the peak of Reynolds shear stress: (a) location; (b) magnitude defect. Solid lines denote (3.9a) and (3.10a) for low $Re$, and dashed lines denote (3.9b) and (3.10b) for high $Re$. Symbols are DNS data: squares from Iwamoto et al. (2002) for $Re_{\unicode[STIX]{x1D70F}}=300,400$ and 650 (channel); circles from Hoyas & Jimenez (2006) for $Re_{\unicode[STIX]{x1D70F}}=940$ and 2000 (channel); stars from Wu & Moin (2008) for $Re_{\unicode[STIX]{x1D70F}}=1142$ (pipe); cross from Ahn et al. (2015) for $Re_{\unicode[STIX]{x1D70F}}=3008$ (pipe); and diamonds from Lee & Moser (2015) for $Re_{\unicode[STIX]{x1D70F}}=550$, 1000 and 5200 (channel).

Figure 4

Figure 4. Validation of (2.33) against DNS data for $\ell _{22}^{+}$ as a function of $y^{+}$ (a) and $y^{+}/Re_{\unicode[STIX]{x1D70F}}$ (b) with $y_{sub}^{+}=9.7$, $y_{buf}^{+}=41$ (the same as for $\ell _{12}^{+}$), $\unicode[STIX]{x1D705}_{22}=0.52$ and $r_{22core}=0.3$. Inset of (a) shows the compensated plot of $\ell _{22}^{Theory}/\ell _{22}^{DNS}$ using (2.33) and DNS data, which are close to the unity in almost the entire flow region.

Figure 5

Figure 5. Wall-normal Reynolds stress profiles by (4.1) compared with data. Also included are predictions at $Re_{\unicode[STIX]{x1D70F}}=50\,000$. The departure between data and our theory (i.e. $W_{22}^{+Theory}-W_{22}^{+DNS}$) is shown in (c,d), which is bounded within $\pm 0.1$. For legend, see figure 2.

Figure 6

Figure 6. Canonical four-layer $\ell _{33}$ of (2.37) compared with data: (a) compensated plot of $\ell _{33}$ divided by $1-r^{4}$; (b) compensated plot of $\ell _{33}$ divided by $\ell _{12}$ showing an anomalous scaling in the bulk flow region. As explained in the text, the anomalous scaling exponent 0.07 results from (5.5). Symbols denote DNS channel data at $Re_{\unicode[STIX]{x1D70F}}=940$ (Hoyas & Jimenez 2006) and $Re_{\unicode[STIX]{x1D70F}}=5200$ (Lee & Moser 2015).

Figure 7

Figure 7. (a) Peak value $W_{33p}^{+}$ of DNS data compared with prediction by (5.10) (line) showing good agreement. Symbols are the same as in figure 3. (b) Diagnostic function $\unicode[STIX]{x1D6E4}_{33}=-y\text{d}W_{33}^{+}/\text{d}y$ showing an approximate plateau $\unicode[STIX]{x1D6E4}_{33}=0.41\pm 0.04$ for $0.02\leqslant y\leqslant 0.14$. Symbols are DNS data at $Re_{\unicode[STIX]{x1D70F}}=5200$ (Lee & Moser 2015). Solid line indicates (5.12), whose minimum value $\unicode[STIX]{x1D6E4}_{33min}\approx 0.41$ obtained in (5.15) – dashed line – represents well the plateau value.

Figure 8

Figure 8. Validation of (5.3) – solid lines – for spanwise Reynolds stress profiles compared with data. Also included is the prediction of $W_{33}^{+}$ at $Re_{\unicode[STIX]{x1D70F}}=50\,000$. Note the log profile (1.4) – dotted line in (b) – agreeing well with data and with (5.3); its slope $A_{33}\approx 0.41$ and the additive constant $B_{33}\approx 1.00$ are theoretically determined in (5.16). The departure between data and our theory (i.e. $W_{33}^{+Theory}-W_{33}^{+DNS}$) is shown in (c,d), which is bounded within $\pm 0.15$. For legend, see figure 2.

Figure 9

Figure 9. Canonical four-layer formula (2.32) (a) and the resulting $W_{11}^{+}$ profiles (6.1) (b) compared with data, showing an underestimation in the bulk flow region at $Re_{\unicode[STIX]{x1D70F}}=5200$.

Figure 10

Figure 10. (a) Measurement of $\unicode[STIX]{x1D705}_{11}$ by the inner peak value $W_{11pi}^{+}$ using (6.4). Dashed line denotes $\unicode[STIX]{x1D705}_{11}=1.02$ resulting from $W_{11pi}^{+}=9.2$ for Princeton pipe; solid line results from the empirical observation $W_{11pi}^{+}=3.66+0.642\ln Re_{\unicode[STIX]{x1D70F}}$ (Lee & Moser 2015). Data: hexagon – Princeton pipe (Hultmark et al.2012); other symbols are the same as in figure 3 for DNS data. (b) Predictions of outer peak location $y_{11po}^{+}$ (left axis) using (6.13a) – dashed line – and of peak value $W_{11po}^{+}$ (right axis) using (6.13b) – solid line; circles are Princeton pipe data and triangles are CICLoPE data; open – $y_{11po}^{+}$, solid – $W_{11po}^{+}$.

Figure 11

Figure 11. Inner profile by (6.2) – dash-dotted line – and the outer profile by (6.9) – solid line – compared with high $Re$ data in (a) Princeton pipe (Hultmark et al.2012) and (b) CICLoPE (Willert et al.2017). Note that $y^{\ast }$ in (6.2), and $c$ and $\unicode[STIX]{x1D6FE}_{m}$ in (6.9) are slightly different between Princeton and CICLoPE datasets. Also included in (a) are log profiles of (1.3) – dashed lines – with $A_{11}=1.25$ and $B_{11}=1.63$ theoretically determined in (6.17).

Figure 12

Figure 12. (a) EXP pipe data (Hultmark et al.2012) denoted by symbols compared with (6.19) denoted by solid lines for $Re_{\unicode[STIX]{x1D70F}}=10\,481$ (downward triangle), 37 450 (leftward triangle) and 98 187 (square) – showing good agreement. Our log profile $W_{11}^{+}=-1.25\ln (y^{+}/Re_{\unicode[STIX]{x1D70F}})+1.63$ from (6.17) is marked in dash-dotted line. Also included are predictions for $Re_{\unicode[STIX]{x1D70F}}=3\times 10^{5}$ and $10^{6}$, awaiting future data for validation. (b) The logarithmic diagnostic function $\unicode[STIX]{x1D6E4}_{11}=-yd_{y}W_{11}^{+}$ for data (symbol) and using (6.19) (solid line) showing good agreement in the entire flow domain. The dashed line marks the log profile slope $-1.25$ given in (6.17); also included is the prediction of $\unicode[STIX]{x1D6E4}_{11}$ at $Re_{\unicode[STIX]{x1D70F}}=3\times 10^{5}$.

Figure 13

Figure 13. $W_{11}^{+}$ obtained by anomalous scaling modification compared with data of (a) DNS (each profile has been vertically shifted by one unit for better display) and (b) Princeton pipe experiment (EXP) (Hultmark et al.2012). The departure between data and our theory is shown in (c) (for DNS) and (d) (for EXP) – all bounded within $\pm 1$. In addition to the DNS channel data in figure 2, DNS pipe data are also included in (a,c) at $Re_{\unicode[STIX]{x1D70F}}=1142$ by Wu & Moin (2008) (diamonds) and at $Re_{\unicode[STIX]{x1D70F}}=3008$ by Ahn et al. (2015) (leftward triangles).