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Direct numerical simulations of turbulent pipe flow up to $Re_\tau \approx 5200$

Published online by Cambridge University Press:  02 February 2023

Jie Yao
Affiliation:
Department of Mechanical Engineering, Texas Tech University, Lubbock, TX 79409, USA
Saleh Rezaeiravesh
Affiliation:
Department of Engineering Mechanics, KTH Royal Institute of Technology, SE-100 44 Stockholm, Sweden
Philipp Schlatter
Affiliation:
Department of Engineering Mechanics, KTH Royal Institute of Technology, SE-100 44 Stockholm, Sweden
Fazle Hussain*
Affiliation:
Department of Mechanical Engineering, Texas Tech University, Lubbock, TX 79409, USA
*
Email address for correspondence: fazlehussain@gmail.com

Abstract

Well-resolved direct numerical simulations (DNS) have been performed of the flow in a smooth circular pipe of radius $R$ and axial length $10{\rm \pi} R$ at friction Reynolds numbers up to $Re_\tau =5200$ using the pseudo-spectral code OPENPIPEFLOW. Various turbulence statistics are documented and compared with other DNS and experimental data in pipes as well as channels. Small but distinct differences between various datasets are identified. The friction factor $\lambda$ overshoots by $2\,\%$ and undershoots by $0.6\,\%$ the Prandtl friction law at low and high $Re$ ranges, respectively. In addition, $\lambda$ in our results is slightly higher than in Pirozzoli et al. (J. Fluid Mech., vol. 926, 2021, A28), but matches well the experiments in Furuichi et al. (Phys. Fluids, vol. 27, issue 9, 2015, 095108). The log-law indicator function, which is nearly indistinguishable between pipe and channel up to $y^+=250$, has not yet developed a plateau farther away from the wall in the pipes even for the $Re_\tau =5200$ cases. The wall shear stress fluctuations and the inner peak of the axial turbulence intensity – which grow monotonically with $Re_\tau$ – are lower in the pipe than in the channel, but the difference decreases with increasing $Re_\tau$. While the wall value is slightly lower in the channel than in the pipe at the same $Re_\tau$, the inner peak of the pressure fluctuation shows negligible differences between them. The Reynolds number scaling of all these quantities agrees with both the logarithmic and defect-power laws if the coefficients are properly chosen. The one-dimensional spectrum of the axial velocity fluctuation exhibits a $k^{-1}$ dependence at an intermediate distance from the wall – also seen in the channel. In summary, these high-fidelity data enable us to provide better insights into the flow physics in the pipes as well as the similarity/difference among different types of wall turbulence.

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, provided the original article is properly cited.
Copyright
© The Author(s), 2023. Published by Cambridge University Press
Figure 0

Table 1. Summary of simulation parameters. The axial length of the pipe ($L_z$) is $10{\rm \pi} R$, with $R$ being the pipe radius. Here, $Re_\tau (\equiv u_\tau R/\nu )$ and $Re_b (\equiv 2U_b R/\nu )$ are the frictional and bulk Reynolds numbers, respectively; $N_z$ and $N_\theta$ are the number of dealiased Fourier modes in the axial and azimuthal directions, and $N_r$ is the number of grid points in the radial direction; $\Delta z$ and $\Delta (R\theta )$ are the grid spacings in the axial and azimuthal directions, defined in terms of the Fourier modes. In the radial direction, $\Delta r^+_w$ represents the grid spacing at the wall, and $\Delta r^+_{max}$ denotes the maximum grid spacing. Also, $T u_\tau /R$ is the total eddy-turnover time without the initial transient phase.

Figure 1

Table 2. List of references of data used. FD denotes (second order) finite difference, SE denotes spectral element, SB denotes spectral/B-spline, SC denotes spectral/compact finite difference, and LDV represents laser Doppler velocimetry. $L_z$ is the axial (streamwise) length, $\Delta z$ and $\Delta (R\theta )$ are the grid spacing in the axial and azimuthal directions, defined in terms of the Fourier modes. In the radial direction, $\Delta r^+_w$ represents the grid spacing at the wall, and $\Delta r^+_{max}$ denotes the maximum grid spacing.

Figure 2

Figure 1. Comparison of the residual in the mean momentum equation (2.1) among different high-$Re$ simulations. The black solid line with a star denotes our $Re_\tau =5200$ result.

Figure 3

Figure 2. Visualization of the instantaneous axial velocity $u_z/U_b$ in the $(r,\theta )$ plane for $Re_\tau$ values (a) $180$, (b) $550$, (c) 1000, (d) 2000, and (e) 5200; and inner-scaled instantaneous axial velocity fluctuations $u'_z/u_\tau$ on a cylindrical surface $(z - r\theta )$ for $Re_\tau =5200$ at ( f) $y^+=15$ and (g) $y/R=0.5$.

Figure 4

Figure 3. (a) Friction factor $\lambda$ as a function of $Re_b$, and (b) the relative deviations from the Prandtl friction law.

Figure 5

Table 3. Summary of values and standard deviations of some key parameters: the friction factor $\lambda =8\tau _{z,w}/(\rho U^2_b)$; the peak of axial velocity variance $\langle{u'^2_z}\rangle^{+}_p$; the peak of the Reynolds shear stress $-\langle{u'_ru'_z}\rangle^{+}_p$; the axial $\langle{\tau '^2_{z,w}}\rangle^+$ and azimuthal $\langle{\tau '^2_{\theta,w} }\rangle^+$ wall shear stress fluctuations; and the wall ($p'^+_{w,rms}$) and peak ($p'^+_{p,rms}$) values of root-mean-square (r.m.s.) pressure fluctuations.

Figure 6

Figure 4. (a) Axial ($\langle \tau '^2_{z,w}\rangle ^+$) and (b) azimuthal ($\langle \tau '^2_{\theta,w}\rangle ^+$) wall shear stress fluctuations as a function of $Re_\tau$. The dotted, dashed and dashed-dotted lines in the inset of (a) denote $\langle \tau '^2_{z,w}\rangle ^+=(0.225+0.0264 \ln (Re_\tau ))^2$, $\langle \tau '^2_{z,w}\rangle ^+=0.016+0.0218 \ln (Re_\tau )$ and $\langle \tau '^2_{z,w}\rangle ^+=0.255-0.477\,Re^{-1/4}_\tau$, respectively.

Figure 7

Figure 5. (a) Mean velocity profiles $U^+$ and (b) log-law diagnostic function $\beta$. Profiles in (a) are offset vertically by two wall units, and the shaded area in (b) represents the standard deviation of our data at $Re_\tau =5200$.

Figure 8

Figure 6. (a) Axial velocity variance $\langle{ u'^2_z}\rangle ^+$ as a function of $y^+$; (b) the diagnostic plot depicting $u'_{z,rms}/U_c$ as a function of $U^+/U_c$; and (c) the inner peak of axial velocity variance $\langle{ u'^2_z}\rangle ^+_p$ as a function of $y^+$. The dashed and dashed-dotted lines in the inset of (c) denote $\langle{u'^2_z}\rangle^{+}_p=3.251+0.687\ln (Re_\tau )$ and $\langle{u'^2_z}\rangle^{+}_p=11.132-17.402\,Re^{-1/4}_\tau$, respectively.

Figure 9

Figure 7. (a) Radial velocity variance $\langle u'^2_r \rangle ^+$, and (b) Reynolds shear stress $\langle u'_r u'_z \rangle ^+$, as functions of $y^+$.

Figure 10

Figure 8. Reynolds number dependence of (a) the peak of the Reynolds shear stress $\langle u'_r u'_z \rangle ^+$, and (b) the corresponding peak location in wall units.

Figure 11

Figure 9. Indicator function for Townsend's prediction among different high-$Re$ simulations: (a) axial velocity variance $y\,\partial _y\langle{ u'^2_z}\rangle ^+$, and (b) azimuthal velocity variance $y\,\partial _y\langle u'^2_\theta \rangle ^+$.

Figure 12

Figure 10. Azimuthal velocity variance $\langle u'^2_\theta \rangle ^+$ as a function of (a) $y^+$ and (b) $y/R$. Only the two highest $Re_\tau$ cases are included in (b).

Figure 13

Figure 11. (a) Production $P^+_k$ and dissipation $\epsilon ^+_k$ of the turbulent kinetic energy, and (b) balance of production and dissipation $P^+_k/\epsilon ^+_k-1$, as functions of $y^+$.

Figure 14

Figure 12. (a) Mean pressure ($P^+$) and (b) r.m.s. pressure fluctuation ($P^{\prime+}_{rms}$), as functions of $y^+$.

Figure 15

Figure 13. Reynolds number dependence of (a) peak ($P^{\prime+}_{p,rms}$) and (b) wall ($P'^+_{w,rms}$) values of r.m.s. pressure fluctuations.

Figure 16

Figure 14. Wavenumber pre-multiplied energy spectra for $Re_\tau =5200$: (a) $k_zE_{zz}/u^2_\tau$, (b) $k_\theta E_{zz}/u^2_\tau$, (c) $k_zE_{rz}/u^2_\tau$, and (d) $k_\theta E_{rz}/u^2_\tau$.

Figure 17

Figure 15. Comparison of the pre-multiplied energy spectra between pipe (solid) and channel (dashed) for $Re_\tau =5200$: (a) $k_zE_{zz}/u^2_\tau$, and (b) $k_\theta E_{zz}/u^2_\tau$.

Figure 18

Figure 16. Comparison of the grid resolution in radial direction $\Delta r^+$ among different high-$Re$ simulations. The black solid line with a star denotes our $Re_\tau \approx 5200$ result.

Figure 19

Table 4. Summary of the sampling of the flow variables used in the UQ analyses.

Figure 20

Figure 17. Estimated standard deviation of different statistical quantities: (a) $U^+$, (b) $\partial U^+/\partial y^+$, (c) $\langle{u'^2_z}\rangle^{+}$, (d) $\langle{u'^2_r}\rangle^{+}$, (e) $\langle{u'^2_\theta}\rangle^{+}$, ( f) $\langle{u'_ru'_z}\rangle^{+}$.