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On the propagation of gravity currents over and through a submerged array of circular cylinders

Published online by Cambridge University Press:  13 October 2017

Jian Zhou
Affiliation:
Department of Civil and Environmental Engineering, Colorado State University, Fort Collins, CO 80523, USA
Claudia Cenedese
Affiliation:
Department of Physical Oceanography, Woods Hole Oceanographic Institution, Woods Hole, MA 02543, USA
Tim Williams
Affiliation:
Department of Civil and Natural Resources Engineering, University of Canterbury, Private Bag 4800, Christchurch 8140, New Zealand
Megan Ball
Affiliation:
Department of Civil and Natural Resources Engineering, University of Canterbury, Private Bag 4800, Christchurch 8140, New Zealand
Subhas K. Venayagamoorthy*
Affiliation:
Department of Civil and Environmental Engineering, Colorado State University, Fort Collins, CO 80523, USA
Roger I. Nokes
Affiliation:
Department of Civil and Natural Resources Engineering, University of Canterbury, Private Bag 4800, Christchurch 8140, New Zealand
*
†Email address for correspondence: vskaran@colostate.edu

Abstract

The propagation of full-depth lock-exchange bottom gravity currents past a submerged array of circular cylinders is investigated using laboratory experiments and large eddy simulations. Firstly, to investigate the front velocity of gravity currents across the whole range of array density $\unicode[STIX]{x1D719}$ (i.e. the volume fraction of solids), the array is densified from a flat bed ( $\unicode[STIX]{x1D719}=0$ ) towards a solid slab ( $\unicode[STIX]{x1D719}=1$ ) under a particular submergence ratio $H/h$ , where $H$ is the flow depth and $h$ is the array height. The time-averaged front velocity in the slumping phase of the gravity current is found to first decrease and then increase with increasing $\unicode[STIX]{x1D719}$ . Next, a new geometrical framework consisting of a streamwise array density $\unicode[STIX]{x1D707}_{x}=d/s_{x}$ and a spanwise array density $\unicode[STIX]{x1D707}_{y}=d/s_{y}$ is proposed to account for organized but non-equidistant arrays ( $\unicode[STIX]{x1D707}_{x}\neq \unicode[STIX]{x1D707}_{y}$ ), where $s_{x}$ and $s_{y}$ are the streamwise and spanwise cylinder spacings, respectively, and $d$ is the cylinder diameter. It is argued that this two-dimensional parameter space can provide a more quantitative and unambiguous description of the current–array interaction compared with the array density given by $\unicode[STIX]{x1D719}=(\unicode[STIX]{x03C0}/4)\unicode[STIX]{x1D707}_{x}\unicode[STIX]{x1D707}_{y}$ . Both in-line and staggered arrays are investigated. Four dynamically different flow regimes are identified: (i) through-flow propagating in the array interior subject to individual cylinder wakes ( $\unicode[STIX]{x1D707}_{x}$ : small for in-line array and arbitrary for staggered array; $\unicode[STIX]{x1D707}_{y}$ : small); (ii) over-flow propagating on the top of the array subject to vertical convective instability ( $\unicode[STIX]{x1D707}_{x}$ : large; $\unicode[STIX]{x1D707}_{y}$ : large); (iii) plunging-flow climbing sparse close-to-impermeable rows of cylinders with minor streamwise intrusion ( $\unicode[STIX]{x1D707}_{x}$ : small; $\unicode[STIX]{x1D707}_{y}$ : large); and (iv) skimming-flow channelized by an in-line array into several subcurrents with strong wake sheltering ( $\unicode[STIX]{x1D707}_{x}$ : large; $\unicode[STIX]{x1D707}_{y}$ : small). The most remarkable difference between in-line and staggered arrays is the non-existence of skimming-flow in the latter due to the flow interruption by the offset rows. Our analysis reveals that as $\unicode[STIX]{x1D719}$ increases, the change of flow regime from through-flow towards over- or skimming-flow is responsible for increasing the gravity current front velocity.

Information

Type
Papers
Copyright
© 2017 Cambridge University Press 
Figure 0

Figure 1. Schematic diagram showing the full-depth lock-exchange set-up used in this study. (a) Elevation view of the channel; (b) plan view of the in-line arrangement; (c) plan view of the staggered arrangement. The vertical dashed line in (a) indicates the gate position at $x=0$. The rightmost end of the array is far from the channel extremity. Circular cylinders (when present) with a diameter of $d$ and a height of $h$ are mounted on the channel bed, with their axes parallel to the vertical direction. The streamwise and spanwise centre-to-centre cylinder spacings are denoted as $s_{x}$ and $s_{y}$, respectively. In the staggered case, the offset rows are shifted by $s_{y}/2$ along the spanwise direction. Not to scale.

Figure 1

Figure 2. Comparison of experimental and numerical instantaneous laterally averaged density fields of a gravity current propagating past a sparse and a dense array. The submergence condition is fixed at $H/h=4$. (a) Sparse, experimental; (b) dense, experimental; (c) sparse, LES; (d) dense, LES. For the sparse array, $\unicode[STIX]{x1D707}_{x}=0.361$, $\unicode[STIX]{x1D707}_{y}=0.313$ and $\unicode[STIX]{x1D719}=0.09$. For the dense array, $\unicode[STIX]{x1D707}_{x}=0.722$, $\unicode[STIX]{x1D707}_{y}=0.626$ and $\unicode[STIX]{x1D719}=0.36$. The experimental density fields are from Cenedese et al. (2016).

Figure 2

Figure 3. Comparison of the time-averaged Froude number between the laboratory experiments and the numerical simulations for different array densities and submergence conditions (black: $H/h=3$; red: $H/h=4$; green: $H/h=5.4$; blue: $H/h=7$). Error bars are included to account for the range of $\overline{Fr}$ in 4–6 different experimental runs for measuring the front velocity for each case due to the unsteady nature of the flow. For in-line arrays, the mean values of experimental and LES results are linearly interpolated by solid lines. The data between in-line and staggered arrays are interpolated using dashed lines. Experimental data of the smooth ($\unicode[STIX]{x1D719}=0$) and the densest cases ($\unicode[STIX]{x1D719}=0.36$) are from Cenedese et al. (2016).

Figure 3

Table 1. List of simulations performed for the parametric study.

Figure 4

Figure 4. Froude number versus streamwise (spanwise) array density at fixed spanwise (streamwise) array densities. (a,b) In-line arrays; (c,d) staggered arrays. Circles show the values of $\overline{Fr}^{\ast }$ in the slumping phase and solid lines are the best fitting curves with $R^{2}\geqslant 0.98$. The two limiting cases are included in each panel: flat-bed case F-0 (- - - -); solid-slab case F-1 ($\cdots \,\cdot$). The submergence ratio is fixed at $H/h=5.4$.

Figure 5

Figure 5. Variation of $\unicode[STIX]{x1D716}$ using the $\unicode[STIX]{x1D707}_{x}$–$\unicode[STIX]{x1D707}_{y}$ space. (a) In-line arrays; (b) staggered arrays. Solid curves indicate contours of $\unicode[STIX]{x1D719}=(\unicode[STIX]{x03C0}/4)\unicode[STIX]{x1D707}_{x}\unicode[STIX]{x1D707}_{y}$ with their values marked on the right-hand side of (b). Approximate regions corresponding to different flow regimes are annotated in both panels. Different paths of flow regime change are shown by dashed arrows. The submergence ratio is fixed at $H/h=5.4$.

Figure 6

Figure 6. Visualization of representative flow structures using instantaneous density isosurfaces, $\unicode[STIX]{x1D70C}\geqslant 0.5$. (a) F-0 (unobstructed flat bed, $\unicode[STIX]{x1D719}=0$); (b) S-0.363-0.363 (equidistant and sparse, $\unicode[STIX]{x1D719}=0.103$); (c) S-0.636-0.636 (equidistant and dense, $\unicode[STIX]{x1D719}=0.318$); (d) S-1.000-1.000 (highest density achievable for circular cylinders, $\unicode[STIX]{x1D719}=\unicode[STIX]{x03C0}/4$); ($e$) I-0.090-1.000 (impermeable fences, $\unicode[STIX]{x1D719}=0.071$); ($f$) I-1.000-0.272 (channelization, $\unicode[STIX]{x1D719}=0.214$). The arrows mark the unobstructed nose (N), through-nose within the array (TN), over-nose above the array (ON) and the vertical convection within the pore regions (VC), respectively.

Figure 7

Figure 7. Instantaneous fluid density fields along the channel centreline at $t=21.5t_{0}$ showing the $T\Rightarrow O$ regime change. (a) F-0; (b) S-0.272-0.272; (c) S-0.636-0.636; (d) S-1.000-1.000; ($e$) F-1. Roughness elements are shown in dark grey. The lock region ($-L_{lock}\leqslant x<0$) is not shown.

Figure 8

Figure 8. Time-averaged and laterally averaged horizontal velocity profiles showing the $T\Rightarrow O$ regime change. The velocity data are recorded at a distance of $H/2$ behind the current nose by moving with the gravity current’s front frame. The horizontal grey line marks the array top.

Figure 9

Figure 9. Instantaneous density isosurface at $\unicode[STIX]{x1D70C}=0.5$ for different array densities. (a) S-0.272-0.272; (b) S-0.636-0.636; (c) S-1.000-1.000. The horizontal dashed lines roughly divide the array region into a longitudinal propagation zone ($0\leqslant z<\unicode[STIX]{x1D6FF}$, encompassed by the green window) and a vertical convection zone ($\unicode[STIX]{x1D6FF}\leqslant z, encompassed by the red window). Arrows indicate the ejection of the lighter ambient fluid from underneath, with their length signifying the strength of the vertical exchange. Note, the vertical convection is more pronounced near the over-nose, and vanishes far upstream where the water column within the array is largely homogenized.

Figure 10

Figure 10. Instantaneous fluid density fields at $t=21.5t_{0}$ showing the $T\Rightarrow S\Rightarrow O$ regime change. (a,f) F-0; (b,g) I-0.636-0.272; (c,h) I-1.000-0.272; (d,i) S-0.636-0.272; (e,j) I-0.636-0.636. The left panels are plotted in the $x$–$z$ plane along the array centreline, and the right panels are plotted in the $x$–$y$ plane located $0.2h$ above the channel bed. Roughness elements are shown in dark grey. Note that in (d) the centreline density data are not available at every other cylinder in the streamwise direction due to the staggered arrangement.

Figure 11

Figure 11. Time-averaged and laterally averaged horizontal velocity profiles showing the $T\Rightarrow S\Rightarrow O$ regime change. The velocity data are recorded at a distance of $H/2$ behind the current nose by moving with the gravity current’s front frame. The horizontal grey line marks the array top.

Figure 12

Figure 12. Instantaneous fluid density fields along the channel centreline at $t=21.5t_{0}$ showing the $T\Rightarrow P\Rightarrow O$ regime change. (a) I-0.090-0.636; (b) I-0.090-1.000; (c) I-0.545-1.000; (d) I-1.000-1.000. Frontal cylinder configurations as seen by the current are shown on the right.

Figure 13

Figure 13. Time-averaged and laterally averaged horizontal velocity profiles showing the $T\Rightarrow P\Rightarrow O$ regime change. The velocity data are recorded at a distance of $H/2$ behind the current nose by moving with the gravity current’s front frame. The horizontal grey line marks the array top.