TY - JOUR
T1 - Quantifying wall turbulence via a symmetry approach. Part 2. Reynolds stresses
AU - Chen, Xi
AU - Hussain, Fazle
AU - She, Zhen Su
N1 - Funding Information:
The authors thank C. E. Willert for sharing the CICLoPE data with us. This work is initially supported by the MOST 973 project 2009CB724100 of China, and then by National Nature Science Foundation of China with nos. 11452002, 11221062.
Publisher Copyright:
Cambridge University Press 2018
PY - 2017
Y1 - 2017
N2 - 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 `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 −u0v0, and normal stresses u0u0, v0v0, w0w0) are analysed layer by layer, and similar four-layer formulae of the corresponding stress length functions `11, `22, `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 `12 and `22 – which have the celebrated linear scalings in the logarithmic layer, i.e. `12 ≈ κy and `22 ≈ κ22y. However, data show an invariant peak location for w0w0, which theoretically leads to an anomalous scaling in `33 in the log layer only, namely `33 ∝ y1−γ with γ ≈ 0.07. Furthermore, another mesolayer modification of `11 yields the experimentally observed location and magnitude of the outer peak of u0u0. The resulting −u0v0, u0u0, v0v0 and w0w0 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+ ≈ 12; (2) the location of peak value −u0v0p has a scaling transition from 5.7Re1τ/3 to 1.5Reτ1/2 at Reτ ≈ 3000, with a 1 + u0v0+p scaling transition from 8.5Re−τ2/3 to 3.0Re−τ1/2 (Reτ the friction Reynolds number); (3) the peak value w0w0+p ≈ 0.84Re0τ14(1 − 48/Reτ); (4) the outer peak of u0u0 emerges above Reτ ≈ 104 with its location scaling as 1.1Reτ1/2 and its magnitude scaling as 2.8Re0τ09; (5) an alternative derivation of the log law of Townsend (1976, The Structure of Turbulent Shear Flow, Cambridge University Press), namely, u0u0+ ≈ −1.25 ln y + 1.63 and w0w0+ ≈ −0.41 ln y + 1.00 in the bulk.
AB - 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 `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 −u0v0, and normal stresses u0u0, v0v0, w0w0) are analysed layer by layer, and similar four-layer formulae of the corresponding stress length functions `11, `22, `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 `12 and `22 – which have the celebrated linear scalings in the logarithmic layer, i.e. `12 ≈ κy and `22 ≈ κ22y. However, data show an invariant peak location for w0w0, which theoretically leads to an anomalous scaling in `33 in the log layer only, namely `33 ∝ y1−γ with γ ≈ 0.07. Furthermore, another mesolayer modification of `11 yields the experimentally observed location and magnitude of the outer peak of u0u0. The resulting −u0v0, u0u0, v0v0 and w0w0 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+ ≈ 12; (2) the location of peak value −u0v0p has a scaling transition from 5.7Re1τ/3 to 1.5Reτ1/2 at Reτ ≈ 3000, with a 1 + u0v0+p scaling transition from 8.5Re−τ2/3 to 3.0Re−τ1/2 (Reτ the friction Reynolds number); (3) the peak value w0w0+p ≈ 0.84Re0τ14(1 − 48/Reτ); (4) the outer peak of u0u0 emerges above Reτ ≈ 104 with its location scaling as 1.1Reτ1/2 and its magnitude scaling as 2.8Re0τ09; (5) an alternative derivation of the log law of Townsend (1976, The Structure of Turbulent Shear Flow, Cambridge University Press), namely, u0u0+ ≈ −1.25 ln y + 1.63 and w0w0+ ≈ −0.41 ln y + 1.00 in the bulk.
KW - pipe flow boundary layer
KW - turbulence theory
KW - turbulent boundary layers
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U2 - 10.1017/jfm.2018.405
DO - 10.1017/jfm.2018.405
M3 - Article
AN - SCOPUS:85049600477
SN - 0022-1120
VL - 850
SP - 401
EP - 438
JO - Journal of Fluid Mechanics
JF - Journal of Fluid Mechanics
ER -