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Wake structure of an array of cylinders in shallow flow

Published online by Cambridge University Press:  10 May 2024

Fei He*
Affiliation:
School of Engineering, The University of Western Australia, 35 Stirling Highway, Crawley, WA 6009, Australia
Marco Ghisalberti*
Affiliation:
School of Engineering, The University of Western Australia, 35 Stirling Highway, Crawley, WA 6009, Australia Oceans Graduate School, The University of Western Australia, 35 Stirling Highway, Crawley, WA 6009, Australia
Hongwei An
Affiliation:
School of Engineering, The University of Western Australia, 35 Stirling Highway, Crawley, WA 6009, Australia
Scott Draper
Affiliation:
School of Engineering, The University of Western Australia, 35 Stirling Highway, Crawley, WA 6009, Australia Oceans Graduate School, The University of Western Australia, 35 Stirling Highway, Crawley, WA 6009, Australia
Paul Branson
Affiliation:
Oceans Graduate School, The University of Western Australia, 35 Stirling Highway, Crawley, WA 6009, Australia Environment, CSIRO, 35 Stirling Highway, Crawley, WA 6009, Australia
Chengjiao Ren
Affiliation:
School of Engineering, The University of Western Australia, 35 Stirling Highway, Crawley, WA 6009, Australia
Liang Cheng
Affiliation:
School of Engineering, The University of Western Australia, 35 Stirling Highway, Crawley, WA 6009, Australia Guangzhou International Campus, South China University of Technology, Guangzhou, 511442, PR China
*
†Email addresses for correspondence: fei.he@research.uwa.edu.au, marco.ghisalberti@uwa.edu.au
†Email addresses for correspondence: fei.he@research.uwa.edu.au, marco.ghisalberti@uwa.edu.au

Abstract

Although there is a range of approaches for classifying the wake structure behind an array of obstacles, these approaches provide inconsistent results across different array systems. This motivates the present study to integrate and reconcile these approaches into one that is consistent across different systems. This new, transferable classification approach is based on the dimensionless flow blockage of the array and the wake stability parameter. To demonstrate this approach, a series of laboratory experiments was conducted to characterise the wake structure behind an array of emergent cylinders across a practically relevant parameter space that has not previously been explored. Two arrays with the same values of flow blockage and wake stability parameters but different sizes display the same wake structure, demonstrating the controlling influence of these two parameters on the wake structure. This approach classifies four different wake structures, which are distinct in that they display differences in instantaneous and time-averaged flow fields, temporal velocity oscillations, shear layer growth and the length of the steady wake region. The dependence of the wake structure on the two parameters is a consequence of (i) the controlling influence of blockage on the fraction of incident flow passing through the array and (ii) the ability of shallowness to suppress wake instabilities and, to a lesser extent, also influence the velocity through the array. This paper provides a predictive framework for the wake structure based on knowledge of the array geometry, and the depth and velocity of incident flow across the entire relevant practical parameter space.

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), 2024. Published by Cambridge University Press.
Figure 0

Table 1. Summary of existing studies that investigated the wake structure behind obstacle systems. Note: Exp, laboratory experiment; Num, numerical simulation.

Figure 1

Figure 1. (a) Schematic diagram (plan view) of the experimental set-up; (b) photograph of a large array (D = 41 cm) in the flume and dye injection system, taken by camera A; (c) photograph of a small array (D = 16 cm) in a narrow channel created by an acrylic splitting plate; (d) photograph of the piezometer set-up. The velocity measurement locations for the transverse profiles (I, red hollow square), point sampling (II, green solid circle), streamwise profile (IV, blue solid square) described in § 2.3 are sketched in panel (a).

Figure 2

Table 2. Comparison between the measured and predicted (by Blasius equation) bed friction coefficients. Here, $\Delta h$ is the frictional change in water depth over 400 cm streamwise length, and h is the depth of incident flow at the upstream end of the testing section.

Figure 3

Table 3. Experimental conditions employed in this study. Testing cases numbered from ‘79’ to ‘83’ represent the dye visualisation cases without array models. Cases with numbered text (e.g. ‘A1’) are those for which wake velocity fields were measured and roman numeral (e.g. ‘I’) denotes the type of velocity measurement.

Figure 4

Figure 2. Variations of temporal standard deviation of (a) green colour intensity $({\sigma _G})$ and (b) transverse velocity $({\sigma _v})$ with sample length (t) in case H1 (table 3). The horizontal axis t represents the width of a time window (starting from zero) over which ${\sigma _G}$ and ${\sigma _v}$ were calculated. The convergence of ${\sigma _G}$ at a time of 45 seconds and of ${\sigma _v}$ at a time of 260 seconds suggests that sampling periods of 100 and 300 seconds for data from the flow visualisation and velocity measurements, respectively, met statistical convergence.

Figure 5

Figure 3. Evolution of dye streaks in the flow (h = 7 cm) with no array. (a) Instantaneous streak structure; (b) the spatial distribution of CV. The array diameter D used for normalisation is equal to 43 cm. There is lateral spreading of dye streaks due to ‘background’ diffusion, which will be used as a point of comparison for dye streaks in the presence of cylinder arrays.

Figure 6

Figure 4. Wake regimes are well distinguished by the instantaneous wake structure (snapshot of dye streaks), the time-averaged flow structure (field of CV) and power spectral density (Svv) of transverse velocity. The incoming flow is directed upwards. Transverse velocities v for calculating the spectra were sampled at (x/D, y/D) = (8.5, 0.5). The four rows present (in order) cases H1, F1, C1 and A1. The steady wake region in panel (e) is roughly indicated by the black arrow. The series of KH vortices formed in the array shear layer in regime KH in panel (g) is marked by grey arrows.

Figure 7

Table 4. Characteristic flow features of the four wake regimes behind an array of cylinders. Dashed circle represents the edge of a cylinder array, and the incident flow points upwards. Shear layers are considered ‘unstable’ when they generate coherent vortex structures.

Figure 8

Figure 5. Separation, in the ${\textrm{S}_C}\unicode{x2013} {\varGamma _D}$ parameter space, of wake regimes in flows through an array of cylinders. Filled and unfilled markers represent data from this work and previous studies, respectively. Six filled symbols with black edges represent the pairs of cases tested with arrays of both large and small dimensionless array sizes (D/d). The dashed ellipses denote two cases with close values of ${\varGamma _D}$ or SC, but with an approximately 50 % difference in D/d. This chart shows that a wake transition can be caused by variation of either ${\varGamma _D}$ or SC and allows prediction of the wake regime behind an array of cylinders.

Figure 9

Table 5. Comparison of visualised wake regimes for pairs of cases with the same values of ${\varGamma _D}$ and SC, but different size (D/d). Note that the cylinder diameters for all cases are d = 1 cm. In all pairs, there is no change of wake form when the array diameter is halved, confirming that the wake structure is primarily controlled by ${\varGamma _D}$ and SC.

Figure 10

Figure 6. Comparison of wake profiles of $\bar{u}/{U_\infty }$ at x/D = 1 between the cases of large and small D/d values. The pair of cases in each panel have the same values of ${\varGamma _D}$ and SC, but an approximately 50 % difference in D/d. There is negligible difference between the pair of velocity profiles in panels (a)–(d), demonstrating the independence of wake structure on the array size.

Figure 11

Table 6. Summary of array size (D/d), Reynolds number defined based on element diameter (Red), array diameter (ReD) and water depth (Reh) for different studies shown in figure 5. Note that the velocity upstream of the obstacle is used in the definitions of different Reynolds numbers. Despite the broad range of Red, ReD and Reh, the data points with the same value of ${\varGamma _D}$ and SC but different D/d from these different studies lie in the same wake regimes in figure 5.

Figure 12

Figure 7. Comparison of measured mean velocity profiles at x/D = 3 (all cases in regime KH) to the function presented in (3.6). Here, $\bar{y}$ occurs at $y/D \approx \mathrm{\ \pm 0}\textrm{.5}$ in all cases. The agreement between the measured velocity profiles and the hyperbolic tangent profile of a mixing layer is strong, highlighting the validity of the mixing layer analogy for the array shear layers.

Figure 13

Figure 8. Collapse of spectrum of transverse velocity for three regime KH flows. The power spectral density is normalised by its maximum, and the frequency is normalised as ${f^\ast } = f\theta /\bar{U}$. All the spectra were sampled at y/D = 0.5 upstream of where two array shear layers merge. The horizontal dashed line represents the chosen critical value of Svv/(Svv)max (= 0.2) to determine the upper and lower bounds $(f_1^\ast ,f_2^\ast )$ of the observed KH frequency. The observed broadband peaks always span the normalised natural frequency $(f_{KH}^\ast= 0.032)$, indicating the occurrence of KH instability in these three cases.

Figure 14

Figure 9. Variation of the velocity spectrum with time. The colour bar represents the amplitude of $v^{\prime}(t)$ with units of cm s$^{-1}$. The spectrograms are separated into two groups, i.e. (a,c) upstream and (b,d) downstream of the merging of array shear layers at the centreline. The velocities upstream and downstream of the merging point were sampled at y/D = 0.5, 0, respectively. x/D = (a) 5, (b) 8.5, (c) 1 and (d) 5. The solid lines in panels (a,c) denote the predicted values from linear stability theory $(\,{f_{KH}}D/{U_\infty })$ and the dashed lines in panels (a–d) represent the typical Strouhal number 0.2 of an isolated solid cylinder. Whilst the von Kármán vortex street is characterised by a constant frequency and oscillation amplitude downstream of the merging point in panel (b), the dominant frequencies associated with KH vortices are intermittent over time regardless of location in panels (c,d).

Figure 15

Figure 10. Characteristics of secondary vortex street for case D3* with (${\varGamma _D}$, SC) = (8.12, 0.06) in regime KH. (a) Instantaneous wake structure; (b) the time history of $v^{\prime}$ sampled at (x/D, y/D) = (8, 0) (located at the blue dot in panel a). Although the secondary vortex street in panel (a) is similar to the von Kármán vortex street in figure 4(a) in terms of meandering form, the secondary vortex street is generated irregularly over time as indicated by discontinuous oscillations in panel (b).

Figure 16

Figure 11. Comparison of the growth of array shear layers in (a) the SS regime (case F1), (b) the KH regime (case C1) and (c) the CI regime (case A1). The red dashed lines mark the edges of shear layers, which are defined by the transverse location where the Reynolds shear stress is less than 20 % of the maximum in the profile. Hashed region represents the steady wake region in the field of view. The shear layer growth rate decreases as the wake flow varies from regime SS to KH and to CI.

Figure 17

Figure 12. Agreement between the measured and modelled (by (3.9)) development of array shear layer for the cases A1 (regime CI) and C1 (regime KH) both at SC = 0.04. Superscripts ‘m’ and ‘p’ represents measurements and predictions, respectively.

Figure 18

Figure 13. Comparison between the streamwise variations of (a) normalised Reynolds shear stress $- \overline {u^{\prime}v^{\prime}} /U_\infty ^2$, (b) normalised mean streamwise velocity $\bar{u}/{U_\infty }$ and (c) coefficient of variation CV for a regime SS flow (case F1). All the data points in panels (a–c) were sampled along the line of y/D = 0.05. The end of the steady wake region is identified as the points where values of $- \overline {u^{\prime}v^{\prime}} /U_\infty ^2$, $\bar{u}/{U_\infty }$ and CV start to increase in the streamwise direction.

Figure 19

Figure 14. (a) Variation of the steady region length L as a function of ${\varGamma _D}$ and SC. Hexagons, the present study; symbols denoting other studies refer to figure 5. Cases in regime KH are in the hashed region; (b) the comparison of measured values of L with the predictions by (3.10). Some cases in panel (a) are not shown in panel (b) due to lack of velocity measurements for these cases. The steady region length generally increases with increasing SC in panel (a) and is largely underpredicted by (3.10) in panel (b), highlighting the role of shallowness in controlling shear layer growth.

Figure 20

Figure 15. Variation of normalised bleeding velocity ${\bar{u}_b}/{U_\infty }$ with ${\varGamma _D}$. While the bleeding velocity is chiefly controlled by, and decreases with, ${\varGamma _D}$, there is a secondary influence of SC.

Figure 21

Figure 16. Stabilising effects of SC on wake instability in two flows (cases D2, D3) at the same ${\varGamma _D}$ (= 6.5) but different SC (= 0.06, 0.17). The velocity profiles shown in panel (a) were sampled at x/D = 1 and the Reynolds shear stress profiles are shown for x/D = 1 in panel (b) and 8.5 in panel (c). Hollow and solid squares in panels (a, b, c) denote the cases with SC = 0.06 (regime KH), 0.17 (regime CI), respectively. The wake instability is growing (from panel b to panel c) within array shear layers for the regime KH flow with low SC = 0.06 but is stabilised for the regime CI flow with high SC = 0.17 despite the same bleeding flow for the two cases in panel (a).

Figure 22

Figure 17. Comparison of profile of Reynolds shear stress at x/D = 1 between a cylinder array and an isolated cylinder in regime VS. (${\varGamma _D}$, SC) = (308.5, 0.04) for the cylinder array and (${\varGamma _D}$, SC) = (∞, 0.04) for the solid cylinder. The array has the same diameter as the solid cylinder (D = 41.3 cm). The peak value of $- \overline {u^{\prime}v^{\prime}} /U_\infty ^2$ for the cylinder array is much lower and the peak location is far away from the wake centreline (y/D = 0), suggesting weaker array shear layers and wider separation angle of array shear layers in comparison to these of the isolated solid cylinder.

Supplementary material: File

He et al. supplementary movie 1

Regime VS_case_H1
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File 7.2 MB
Supplementary material: File

He et al. supplementary movie 2

Regime SS_case_F1
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Supplementary material: File

He et al. supplementary movie 3

Regime_KH_case_C1
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He et al. supplementary movie 4

Regime KH_case_D2
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Supplementary material: File

He et al. supplementary movie 5

Regime CI_case_A1
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