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Shallow mixing layers over hydraulically smooth bottom in a tilted open channel

Published online by Cambridge University Press:  08 November 2022

Sébastien Proust*
Affiliation:
INRAE, RiverLy, 69100 Villeurbanne, France
Céline Berni
Affiliation:
INRAE, RiverLy, 69100 Villeurbanne, France
Vladimir I. Nikora
Affiliation:
School of Engineering, University of Aberdeen, Aberdeen AB24 3UE, UK
*
Email address for correspondence: sebastien.proust@inrae.fr

Abstract

Shallow mixing layers (SMLs) behind a splitter plate were studied in a tilted rectangular open-channel flume for a range of flow depths and the initial shear parameter ${\lambda = (U_{2}-U_{1})/(U_{2}+U_{1})}$, where $U_1$ and $U_2$ are streamwise velocities of the slow and fast streams, respectively. The main focus of the study is on (i) key parameters controlling the time-averaged SMLs; and (ii) the emergence and spatial development of Kelvin–Helmholtz coherent structures (KHCSs) and large- and very-large-scale motions (LSMs and VLSMs) and associated turbulence statistics. The time-averaged flow features of the SMLs are mostly controlled by bed-friction length scale $h/c_f$ and shear parameter $\lambda$ as well as by time-averaged spanwise velocities $V$ and momentum fluxes $UV$, where $h$ and $c_f$ are flow depth and bed-friction coefficient, respectively. For all studied cases, the effect of shear layer turbulence on the SML growth is comparatively weak, as the fluxes $UV$ dominate over the spanwise turbulent fluxes. Initially, the emergence of KHCSs and their length scales largely depend on $\lambda$. The KHCSs cannot form if ${\lambda \lessapprox 0.3}$ and the turbulence behind the splitter plate resembles that of free mixing layers. Further downstream, shear layer turbulence becomes dependent on the bed-friction number $S = c_f \delta _v /(4 h \lambda )$, where $\delta _v$ is vorticity thickness. When $S \gtrapprox 0.01$, the KHCSs are longitudinally stretched and the scaled transverse turbulent fluxes decrease with increasing $S$. The presence and streamwise development of LSMs/VLSMs away from the splitter plate depends on the $\lambda$-value, particularly when $\lambda > 0.3$, resembling LSMs/VLSMs in conventional open-channel flows when $\lambda$ is small.

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JFM Papers
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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), 2022. Published by Cambridge University Press.
Figure 0

Figure 1. Key parameters of the shallow mixing layers (SMLs), with free mixing layers (FMLs) serving as reference flows: (a) spanwise profile of the time-averaged streamwise velocity $U$, where $U_1$ and $U_2$ are characteristic velocities of the two ambient streams, $U_i$ is velocity at the inflection point that equals average velocity $U_c =(U_1+U_2)/2$ for FMLs, $y_i$ is the spanwise position of $U_i$, $\delta _v =(U_2-U_1)/({\rm d} U/{{\rm d} y})_{max}$ is the vorticity thickness; (b) streamwise evolution of $\delta _v$; and (c) streamwise evolutions of $y_i$, spanwise position $y_c$ of $U_c$ and spanwise position $y_t$ of the extreme in turbulent shear stress $\overline {-u'v'}$.

Figure 1

Figure 2. Open-channel flume: (a) view downstream (experiments with a working length $= 18\ {\rm m}$ and a working width $= 2\ {\rm m}$ (right-hand 2/3 of the total flume width) with bed and sidewalls made of glass); (b) sketch of a cross-section (view downstream), in which $h_1$ and $h_2$ are the flow depths at $y = 0.5\ {\rm m}$ and 1.5 m, respectively; (c) sketch of the inlet flow conditions viewed from upstream, in which $Q_1$ and $Q_2$ are the inflow discharges in the right-hand and left-hand tanks; (d) flow near the splitter plate for $Q_1= 5$ l s$^{-1}$ and $Q_2 = 55$ l s$^{-1}$, view upstream; (e) flow near the splitter plate for $Q_1 = 3$ l s$^{-1}$ and $Q_2 = 27$ l s$^{-1}$, top view.

Figure 2

Table 1. Inflow conditions of the test cases: total flow rate $Q$ and right-hand and left-hand inflow discharges $Q_1$ and $Q_2$. Flow parameters measured at $x = 1.65\ {\rm m}$: flow depths $h_{1}$ and $h_{2}$ at $y = 0.5\ {\rm m}$ and 1.5 m respectively, time-averaged streamwise velocities $U_{2}$ and $U_{1}$ measured at $z/h=0.5$, average velocity ${U_{c}=(U_{2}+U_{1})/2}$, velocity shear ${U_{s}=U_{2}-U_{1}}$, shear parameter ${\lambda =(U_2-U_1)/(U_2+U_1)}$, bed-friction coefficients in the slow and fast streams $c_{f1}$ (with $1/\sqrt {c_{f1}} = -4 \log (1.25/(4Re_1 \sqrt {c_{f1}}))$) and $c_{f2}$ (with $1/\sqrt {c_{f2}} = -4 \log (1.25/(4Re_2 \sqrt {c_{f2}}))$) , Froude numbers $Fr_1 = |U_{1}|/\sqrt {gh_{1}}$ and ${Fr_2 = |U_{2}|/\sqrt {gh_{2}}}$, Reynolds numbers ${Re_1 = |U_{1}|h_{1}/\nu }$ and ${Re_2 = |U_{2}|h_{2}/\nu }$. Here, WSF, MSF and HSF refer to weakly, moderately and highly sheared flow, respectively (see § 2.2).

Figure 3

Table 2. Variation ranges of the flow depths $h_1$ and $h_2$, velocity shear ${U_{s}=U_2-U_1}$, average velocity $U_c = (U_2+U_1)/2$, shear parameter $\lambda =(U_2-U_1)/(U_2+U_1)$, vorticity thickness to flow depth ratio ${\delta _v/h}$ (with $\delta _v=(U_2-U_1)/({\rm d} U/{{\rm d} y})_{{max}}$ and $h = (h_1+h_2)/2$), bed-friction coefficients $c_f = (c_{f1}+c_{f2})/2$, $c_{f1}$ (with $1/\sqrt {c_{f1}} = -4 \log (1.25/(4Re_1 \sqrt {c_{f1}}))$) and $c_{f2}$ (with $1/\sqrt {c_{f2}} = -4 \log (1.25/(4Re_2 \sqrt {c_{f2}}))$), ratio ${h/c_f}$, bed-friction number $S = c_f \delta _v/ (4h \lambda$), maximum value of the spanwise velocity $|V^*|=|V|/U_c$ across the channel and maximum value of root mean square of the streamwise velocity fluctuation $\sqrt {\overline {{u^{'}}^{2}}}^*=\sqrt {\overline {{u^{'}}^{2}}}/U_c$. Here, N.D.: not defined.

Figure 4

Figure 3. Examples of spatial correlation functions of the spanwise velocity fluctuations $v'$. The fixed probe is located at $x = 3.65\ {\rm m}$ and $z/h = 0.5$ and the second probe is moving point by point at the same elevation (a) along the streamwise direction (2.1) or (b) along the spanwise direction (2.2), the horizontal continuous line indicating $R_{yy}^y$ = 0.10.

Figure 5

Figure 4. Shear parameter ${\lambda = (U_{2}-U_{1})/(U_{2}+U_{1})}$ as a function of the streamwise position $x$ (a); the dashed line indicates ${\lambda _c = 0.3}$. Detection of KHCSs using dye tracer injected at the inflection point in the $U$-profile, at $x = 3.65\ {\rm m}$ (b) and $x = 5.65\ {\rm m}$ (c) for representative test cases $Q_1$-$Q_2$ (e.g. 03-11 refers to inlet discharges ${Q_1 = 3 \, \rm {l\, s}^{-1}}$ and ${Q_2 = 11\ \text {l s}^{-1}}$).

Figure 6

Figure 4 (cntd). Shear parameter ${\lambda = (U_{2}-U_{1})/(U_{2}+U_{1})}$ as a function of the streamwise position $x$ (a); the dashed line indicates ${\lambda _c = 0.3}$. Detection of KHCSs using dye tracer injected at the inflection point in the $U$-profile, at $x = 3.65\ {\rm m}$ (b) and $x = 5.65\ {\rm m}$ (c) for representative test cases $Q_1$-$Q_2$ (e.g. 05-55 refers to inlet discharges $Q_1 = 5\ \rm {l\, s}^{-1}$ and $Q_2 = 55\ \text {l s}^{-1}$).

Figure 7

Figure 5. Spanwise profile of the time-averaged streamwise velocity $U^*=U/U_c$ at $z/h=0.5$ at $x = 0.65\ {\rm m}$ (a), $x = 3.65\ {\rm m}$ (b) and $x = 11.65\ {\rm m}$ (c). All cases with total discharge $Q = 14$, 30, 60 and 120 l s$^{-1}$. The standard error in $U$ is approximately 1 $\%$.

Figure 8

Figure 6. Spanwise profiles of the time-averaged spanwise velocity $V^*=V/U_c$ at $z/h=0.5$ at: $x = 0.65\ {\rm m}$ (a), $x = 3.65\ {\rm m}$ (b) and $x = 11.65\ {\rm m}$ (c). The standard error in $V$ is approximately 9 $\%$.

Figure 9

Figure 7. Peak value of the time-averaged spanwise velocity $|V^*=V/U_c|$ across the SMLs at $x = 0.65\ {\rm m}$ as a function of shear parameter $\lambda$ (a) and normalized flow depth difference $|h_2-h_1|/[(h_2+h_1)/2]$ (b) for $Q = 14$ l s$^{-1}$ ($*$), 30 l s$^{-1}$ ($\bullet$), 60 l s$^{-1}$ ($\Box$) and 120 l s$^{-1}$ ($\triangle$).

Figure 10

Figure 8. Spanwise exchange of streamwise momentum by the time-averaged flow $|{U}^*{V}^*|$ and Reynolds shear stress $-\overline {u'v'}^*=-\overline {u'v'}/U_c^{2}$ at $z/h=0.5$, at $x = 0.65\ {\rm m}$ (a), $x = 3.65\ {\rm m}$ (b) and $x = 11.65\ {\rm m}$ (c), for cases with total discharge $Q = 120$ l s$^{-1}$ and 30 l s$^{-1}$. The standard error in $\overline {u'v'}$ is approximately 10 $\%$.

Figure 11

Figure 9. Streamwise profiles of the Froude numbers in the slow stream ${Fr_{1}=|U_1|/\sqrt {gh_1}}$ and in the fast stream ${Fr_{2}=|U_2|/\sqrt {gh_2}}$ from $x = 0.65\ {\rm m}$ to $x = 15.65\ {\rm m}$.

Figure 12

Figure 10. Streamwise changes in the normalized flow depth $h^*$ (3.1) from $x = 0.5\ {\rm m}$ to $x = 16.5\ {\rm m}$ at spanwise positions $y = 0.5\ {\rm m}$ ($\times$) and $y =1.5\ {\rm m}$ ($\circ$). The standard error in flow depth $h$ is approximately 0.2 mm.

Figure 13

Figure 11. Vertical distributions of the time-averaged spanwise velocity $V$ for uniform flow 60-60 (a) and HSF 35-85 (b). The standard error in $V$ is approximately 9 $\%$.

Figure 14

Figure 12. Streamwise changes in the shear parameter ${\lambda =(U_{2}-U_{1})/(U_{2}+U_{1})}$ from $x = 0.06\ {\rm m}$ to $15.65\ {\rm m}$ at elevation ${z/h=0.5}$. The dashed line indicates ${\lambda _c = 0.3}$.

Figure 15

Figure 13. Longitudinal decay of $(U_{2}^2-U_{1}^2)^{*}= (U_{2}^2-U_{1}^2)/(U_{2,0}^2-U_{1,0}^2)$ as a function of $x^*=x c_f/h$. Comparison with the law (1.3) of Chu & Babarutsi (1988).

Figure 16

Figure 14. Growth rate of the vorticity thickness $\delta _v$ against shear parameter $\lambda$ at $x = 0.36\ {\rm m}$ for total flow rates $Q = 14$ l s$^{-1}$ ($*$), 30 l s$^{-1}$ ($\bullet$), 60 l s$^{-1}$ ($\Box$) and 120 l s$^{-1}$ ($\triangle$). Comparison with relationships (1.8) of Brown & Roshko (1974) for FMLs and (1.7) of Chu & Babarutsi (1988) for SMLs. The standard error in $\delta _v$ ranges approximately from 5 (HSFs) to 10 cm (WSFs).

Figure 17

Figure 15. Streamwise evolution of the relative vorticity thickness. The solid lines indicate the relationship (1.4) after Van Prooijen & Uijttewaal (2002) using $\alpha = 0.09$ (FML behaviour when $x \longrightarrow 0$, with ${{\rm d} \delta _v/{{\rm d}\kern0.06em x} = 0.18 \lambda }$ after Brown & Roshko 1974). The standard error in $\delta _v$ ranges approximately from 5 (HSFs) to 10 cm (WSFs).

Figure 18

Figure 16. Mixing layer width based on the bed-friction number $\delta ^* = c_f \delta _v / (h 2 \lambda ) = 2S$ vs $x^* = x (c_f /h)$. The continuous and dotted lines indicate the relationships $\delta ^*= 0.09 x^*$ (for $x^* < 1.5$) and $\delta ^*= 0.0364 {x^*}^3$ (for $x^* > 2$) of Cheng & Constantinescu (2020). Note that $\delta ^*= 0.09 x^*$ is equivalent to $\delta _v= 0.18\lambda x$ for FMLs (Brown & Roshko 1974).

Figure 19

Figure 17. Various definitions of the SML centre: (i) spanwise position $y_m$ ($-$) of the border between fast and slow flows that preserves initial discharges $Q_1$ and $Q_2$ calculated from (1.9) proposed by Cushman-Roisin & Constantinescu (2020); (ii) position $y_c$ ($\bullet$) of the measured average velocity $U_c$; (iii) position $y_i$ ($\circ$) of the velocity measured at the inflection point $U_i$; and (iv) position $y_t$ ($\ast$) of the measured peak Reynolds stress.

Figure 20

Figure 18. Longitudinal and spanwise length scales of the KHCSs, $\delta _x^{CS}$ and $\delta _y^{CS}$, against shear parameter $\lambda$, at three streamwise positions, for total discharges $Q = 14$ l s$^{-1}$ ($*$), 30 l s$^{-1}$ ($\bullet$), 60 l s$^{-1}$ ($\Box$) and 120 l s$^{-1}$ ($\triangle$). Vertical dashed line indicates $\lambda _c = 0.3$. The standard errors in $\delta _x^{CS}$ and $\delta _y^{CS}$ are approximately 10 cm and 2.5 cm, respectively.

Figure 21

Figure 19. Maximum value of Reynolds stress $-\overline {u'v'}^{*} = -\overline {u'v'}/U_c^2$ across the SML at $x = 3.65\ {\rm m}$ against (a) local shear parameter $\lambda$ and (b) local bed-friction number $S =c_f \delta _v / (4h \lambda )$ for $Q = 14$ l s$^{-1}$ ($*$), 30 l s$^{-1}$ ($\bullet$), 60 l s$^{-1}$ ($\Box$) and 120 l s$^{-1}$ ($\triangle$). Dashed line indicates $\lambda _c =0.3$ in panel (a).

Figure 22

Figure 20. The data for the WSFs ($\times$), MSFs ($\square$) and HSFs ($\triangledown$). Ratio of the 3-D bed-induced turbulence production $P_{\rm 3D}$ to the 2-D shear layer turbulence production $P_{\rm 2D}$ weighted with $\lambda$ and $\gamma$ (a), ratio $P_{\rm 3D}/P_{\rm 2D}$ (b), ratio of the lateral Reynolds stress to the streamwise turbulence intensity $\overline {u'v'}/\overline {u'^{2}}$ (c) (horizontal line corresponding to 0.38 is proposed for FMLs by Townsend 1976) and ratio of the KHCS spanwise length scale measured at position $x$ to the furthest downstream measured spanwise scale (d), as a function of the bed-friction number $S=c_f \delta _v/(4h\lambda )$.

Figure 23

Figure 21. Longitudinal evolution of the streamwise and spanwise length scales of the KHCSs, $\delta _x^{CS}$ (a) and $\delta _y^{CS}$ (b), with normalization by flow depth $h$, and ratio $\delta _y^{CS}/\delta _x^{CS}$ (c) for flow rates $Q$ = 14 l s$^{-1}$ ($*$), 30 l s$^{-1}$ ($\bullet$), 60 l s$^{-1}$ ($\Box$) and 120 l s$^{-1}$ ($\triangle$), and distinguishing the MSFs (blue markers) and HSFs (pink markers). The lines in (a) and (b) correspond to (1.11).

Figure 24

Figure 22. Cross-sectional distribution of the time-averaged streamwise velocity $U$, root mean square of the spanwise velocity fluctuation $\sqrt {\overline {v'^{2}}}$, and Reynolds stress $-\rho \overline {u'v'}$ for the HSF case 35-85 at: $x = 3.65\ {\rm m}$ (ac) and $x = 11.65\ {\rm m}$ (df). (a) $U$ (cm s$^{-1}$), $x=3.65$ m, (b) $\sqrt {\overline {v'^{2}}}$ (cm s$^{-1}$), $x=3.65$ m, (c) $-\rho\overline {u'v'}$ (Pa), $x=3.65$ m, (d) $U$ (cm s$^{-1}$), $x=11.65$ m, (e) $\sqrt {\overline {v'^{2}}}$ (cm s$^{-1}$), $x=11.65$ m and ( f) $-\rho\overline {u'v'}$ (Pa), $x=11.65$ m.

Figure 25

Figure 23. Vertical distributions of the KHCS length scales (ac). Spatial correlation function of the spanwise velocity fluctuations $v'$ along the vertical direction, with a reference point at mid-depth (d). Vertical distributions of turbulence statistics (ef), shear parameter $\lambda$ (g), vorticity thickness $\delta _v$ (h), and bed-friction number $S = c_f \delta _v/(4h \lambda )$ (i). Measurements at the inflection point of the $U$-profile at $z/h =0.5$ for 35–85 at $x = 3.65\ {\rm m}$ and $y_i = 0.90\ {\rm m}$ (empty markers) and $x = 11.65\ {\rm m}$ and $y_i = 0.85\ {\rm m}$ (filled markers).

Figure 26

Figure 24. Pre-multiplied auto-spectra of streamwise velocity (left-hand column) and co-spectra of streamwise and vertical velocities (right-hand column) for uniform flows of 30, 60 and 120 l s$^{-1}$ at three $x$-locations. Black line shows spectra reported by Zampiron et al. (2020) for an OCF with conventional entrance condition (i.e. without a splitter plate). The data shown represent averaged values at two symmetrical locations, i.e. $y=0.5\ {\rm m}$ and $y=1.5\ {\rm m}$. The 95 $\%$ confidence intervals for the shown spectral curves are comparable to the curve thickness (see text for details).

Figure 27

Figure 25. Pre-multiplied auto-spectra of streamwise velocity for non-uniform flows (WSFs) of 30 l s$^{-1}$ and 120 l s$^{-1}$ at three $x$-locations. Black line shows spectra for corresponding uniform flows at $x=11.65\ {\rm m}$. Panels (a) and (b) relate to $Q_1 = 13$ l s$^{-1}$ ($y = 0.5\ {\rm m}$) and $Q_2 = 17$ l s$^{-1}$ ($y = 1.5\ {\rm m}$), respectively. Panels (c) and (d) relate to $Q_1 = 50$ l s$^{-1}$ ($y = 0.5\ {\rm m}$) and $Q_2 = 70$ l s$^{-1}$ ($y = 1.5\ {\rm m}$), respectively. The 95 $\%$ confidence intervals for the shown spectral curves are comparable to the curve thickness (see text for details).

Figure 28

Figure 26. Dominant physical mechanisms in (a) WSFs (initial $\lambda < 0.3$) and (b) MSFs and HSFs (initial ${\lambda > 0.3}$). Focus on the effects of shear parameter $\lambda$ and bed-friction number $S$ on the emergence and development of the KHCSs, respectively, and on the turbulence bulk statistics (c). SC refers to secondary currents.