Hostname: page-component-6898cfcb55-w5hgh Total loading time: 0 Render date: 2026-11-11T06:33:38.075Z Has data issue: false hasContentIssue false

Mean flow structure and velocity–bed shear stress maxima phase difference in smooth wall, transitionally turbulent oscillatory boundary layers: direct numerical simulations

Published online by Cambridge University Press:  21 October 2021

Dimitrios K. Fytanidis*
Affiliation:
Ven Te Chow Hydrosystems Laboratory, Department of Civil and Environmental Engineering, The Grainger College of Engineering, University of Illinois at Urbana-Champaign, Urbana, IL 61801, USA
Marcelo H. García
Affiliation:
Ven Te Chow Hydrosystems Laboratory, Department of Civil and Environmental Engineering, The Grainger College of Engineering, University of Illinois at Urbana-Champaign, Urbana, IL 61801, USA
Paul F. Fischer
Affiliation:
Department Computer Science, The Grainger College of Engineering, University of Illinois at Urbana-Champaign, Urbana, IL 61801, USADepartment Mechanical Science and Engineering, The Grainger College of Engineering, University of Illinois at Urbana-Champaign, Urbana, IL 61801, USA
*
†Email address for correspondence: fytanid2@illinois.edu

Abstract

Direct numerical simulations of oscillatory boundary-layer flows in the transitional regime were performed to explain discrepancies in the literature regarding the phase difference ${\rm \Delta} \phi$ between the bed-shear stress and free-stream velocity maxima. Recent experimental observations in smooth bed oscillatory boundary-layer (OBL) flows, showed a significant change in the widely used ${\rm \Delta} \phi$ diagram (Mier et al., J. Fluid Mech., vol. 922, 2021, A29). However, the limitations of the point-wise measurement technique did not allow us to associate this finding with the turbulent kinetic energy budget and to detect the approach to a ‘near-equilibrium’ condition, defined in a narrow sense herein. Direct numerical simulation results suggest that a phase lag occurs as the result of a delayed and incomplete transition of OBL flows to a stage that mimics the fully turbulent regime. Data from the literature were also used to support the presence of the phase lag and propose a new ${\rm \Delta} \phi$ diagram. Simulations performed for ${\textit {Re}}_{\delta }=671$ confirmed the sensitivity in the development of self-sustained turbulence on the background disturbances ($\textit{Re}_{\delta}=U_{o}\delta/\nu$, where $\delta=[2\nu/\omega]^{1/2}$ is the Stokes' length, $U_{o}$ is the maximum free stream velocity of the oscillation, $\nu$ is the kinematic viscosity and $\omega=2{\rm \pi}/T$ is the angular velocity based on the period of the oscillation T). Variations of the mean velocity slope and intersect values for oscillatory flows are also explained in terms of the proximity to near-equilibrium conditions. Relaminarization and transition effects can significantly delay the development of OBL flows, resulting in an incomplete transition. The shape and defect factors are examined as diagnostic parameters for conditions that allow the formation of a logarithmic profile with the universal von Kármán constant and intersect. These findings are of relevance for environmental fluid mechanics and coastal morphodynamics/engineering applications.

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
© The Author(s), 2021. Published by Cambridge University Press
Figure 0

Figure 1.Computational domain and boundary conditions.

Figure 1

Table 1.Summary of simulations conducted in the present study. Here, $L$ is the streamwise length, $H$ is the height and $W$ is the width of the domain; $E_{x}$, $E_{y}$ and $E_{z}$ are the number of elements used in each direction, $n_{x}$, $n_{y}$ and $n_{z}$ are the number of computational points/degrees of freedom in each direction ($n_{i}=E_{i}p$), $n_{p}$ is the total number of computational points for each simulation; ${\textrm {d}\kern0.7pt x}^{+}$ and $\textrm {d} z^{+}$ are resolutions in the streamwise and spanwise directions normalized using the maximum shear velocity $u_{*_{max}}$ over the period and the kinematic viscosity $\nu$. $\textrm {d} y_{min}^{+}$ is the first point location in wall units; $n_{T}$ is the number of periods used to compute statistics. Letters A, B and C correspond to the computations using the small, medium and large domain sizes, respectively.

Figure 2

Figure 2.Reynolds number effect. Ensemble-average velocity profiles in wall units for (a) $\omega t={\rm \pi} /4$, (b) $\omega t={\rm \pi} /2$, (c) $\omega t=3{\rm \pi} /4$. Ensemble-average velocity defect profile normalized with free-stream velocity $U_{\infty }$ and $\delta$ for (d) $\omega t={\rm \pi} /4$, (e) $\omega t={\rm \pi} /2$, ( f) $\omega t=3{\rm \pi} /4$. Ensemble-average velocity defect profile normalized with shear velocity $u_{*}$ for (h) $\omega t={\rm \pi} /4$, (i) $\omega t={\rm \pi} /2$, (g) $\omega t=3{\rm \pi} /4$. Dashed orange lines show logarithmic fit for the cases with ${\textit {Re}}_{\delta } \geq 763$. The arrows show the increasing ${\textit {Re}}_{\delta }$ path.

Figure 3

Figure 3.Reynolds number effect. Ensemble-average $\overline {u^{'2}}^{+}$ profiles for (a) $\omega t={\rm \pi} /4$, (b) $\omega t={\rm \pi} /2$, (c) $\omega t=3{\rm \pi} /4$. Ensemble-average $\overline {w^{'2}}^{+}$ profiles for (d) $\omega t={\rm \pi} /4$, (e) $\omega t={\rm \pi} /2$, ( f) $\omega t=3{\rm \pi} /4$. Ensemble-average $\overline {v^{'2}}^{+}$ profiles for (h) $\omega t={\rm \pi} /4$, (i) $\omega t={\rm \pi} /2$, (g) $\omega t=3{\rm \pi} /4$.

Figure 4

Figure 4.Friction coefficient as a function of ${\textit {Re}}_{\delta }$ and ${\textit {Re}}_{w}$.

Figure 5

Table 2.Friction factor $f_{w}$ and phase difference ${\rm \Delta} \phi$ (in degrees) computations: comparison between experimental observations and DNS results. Indices A, B and C correspond to the computations using the small, medium and large domain sizes, respectively.

Figure 6

Figure 5.Normalized bed-shear stress variation for various ${\textit {Re}}_{\delta }$.

Figure 7

Figure 6.Phase difference ${\rm \Delta} \phi$ diagram as a function of ${\textit {Re}}_{\delta }$ and ${\textit {Re}}_{w}$.

Figure 8

Figure 7.Variation of (a) ${\textit {Re}}_{\delta *}$, (b) ${\textit {Re}}_{\theta }$ and (c) ${\textit {Re}}_{\tau }$ over the period.

Figure 9

Figure 8.Development of flow structures. Coherent structures visualized using $\lambda _{2}=-0.0025$ and coloured using the normalized velocity magnitude $u/U_{o}$ at (a) $\omega t = {\rm \pi}/2$ (b) $\omega t = 7{\rm \pi} /12$ and (c) $\omega t = 2{\rm \pi} /3$.

Figure 10

Figure 9.Development of flow structures. Coherent structures visualized using $\lambda _{2}=-0.005$ and coloured with the normalized velocity magnitude $u/U_{o}$ at $\omega t = 3 {\rm \pi}/ 4$.

Figure 11

Figure 10.Ensemble-average velocity profiles $\overline {{u}^{+}}$ and logarithmic fit for ${\textit {Re}}_{\delta }=763$ (case $763B$).

Figure 12

Figure 11.Ensemble-average velocity profiles $\overline {{u}^{+}}$ and logarithmic fit for ${\textit {Re}}_{\delta }=1315$ (case $1315B$).

Figure 13

Figure 12.Effect of ${\textit {Re}}_{\delta }$ on the variation over $\omega t$ of (a) $c_{f}$ (b) $y_{max}/\delta$, $\delta _{*}/\delta$ and $\theta /\delta$, (c) $H$, (d) $G$, (e) $\kappa$ and ( f) $A_{s}$.

Figure 14

Figure 13.TKE budget for ${\textit {Re}}_{\delta }=763$. Terms are normalized using $\delta /U_{o}^{3}$. Also plotted are the time variation of the ratio between the integral of production and the integral of the dissipation rate $I_{Pr}/I_{\epsilon }$, the normalized bed-shear stress $\tau _{b}/\tau _{b_{max}}$ and the normalized TKE integral $I_{k}/I_{k_{max}}$.

Figure 15

Figure 14.TKE budget for ${\textit {Re}}_{\delta }=1315$. Terms are normalized using $\delta /U_{o}^{3}$. Also plotted are the time variation of the ratio between the integral of production and the integral of the dissipation rate $I_{Pr}/I_{\epsilon }$, the normalized bed-shear stress $\tau _{b}/\tau _{b_{max}}$ and the normalized TKE integral $I_{k}/I_{k_{max}}$.

Figure 16

Figure 15.TKE budget for ${\textit {Re}}_{\delta }=1315$. Terms are normalized using $\nu /u_{*}^{4}$. Also plotted are the time variation of the ratio between the integral of production and the integral of dissipation rate $I_{Pr}/I_{\epsilon }$, the normalized bed-shear stress $\tau _{b}/\tau _{b_{max}}$ and the normalized TKE integral $I_{k}/I_{k_{max}}$.

Figure 17

Figure 16.TKE production to absolute dissipation rate ratio $Pr/|\epsilon |$ for the examined flows.

Figure 18

Figure 17.Normalized $\epsilon ^{+}=\epsilon /(u_{*}^{4}/\nu )$ for ${\textit {Re}}_{\delta }=819$.

Figure 19

Figure 18.Normalized $\epsilon ^{+}=\epsilon /(u_{*}^{4}/\nu )$ for ${\textit {Re}}_{\delta }=1036$.

Figure 20

Figure 19.Normalized $\epsilon ^{+}=\epsilon /(u_{*}^{4}/\nu )$ for ${\textit {Re}}_{\delta }=1315$.

Figure 21

Figure 20.Comparison of the results for the small (case $763A$), medium (case $763B$) and large domain (case $763C$).

Figure 22

Figure 21.Comparison of the Reynolds stress results for the small (case 763$A$), medium (case 763$B$) and large domain (case 763$C$).

Figure 23

Figure 22.Grid convergence of mean velocity profile for case 1316B for polynomial orders 6, 7 and 8.

Figure 24

Figure 23.Convergence of TKE budgets: typical results for ${\textit {Re}}_{\delta }=1315$. Continuous lines represent results averaged over 5 periods. Symbols show results averaged over 10 periods and exploiting the symmetry between $\omega t$ and $\omega t + {\rm \pi}$ (i.e. 20 realizations).

Fytanidis at al. Supplementary Movie 1

Variation of + proles over time for Re = 819. Comparison between the present data and data by Wu et al. (2017) is shown. Re and b variations are also shown.

Download Fytanidis at al. Supplementary Movie 1(Video)
Video 190.2 KB

Fytanidis at al. Supplementary Movie 2

Variation of + proles over time for Re = 1036. Comparison between the present data and data by Wu et al. (2017) is shown. Re and b variations are also shown.

Download Fytanidis at al. Supplementary Movie 2(Video)
Video 198.1 KB

Fytanidis at al. Supplementary Movie 3

Variation of + proles over time for Re = 1315. Comparison between the present data and data by Wu et al. (2017) is shown. Re and b variations are also shown.

Download Fytanidis at al. Supplementary Movie 3(Video)
Video 196.7 KB