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Near-bed velocity law and bed shear stress in vegetated flows

Published online by Cambridge University Press:  12 January 2026

Yuan Xu*
Affiliation:
State Key Laboratory of Estuarine and Coastal Research, East China Normal University , Shanghai 200241, PR ChinaState Key Laboratory of Hydroscience and Engineering, Tsinghua University , Beijing 100084, PR China
Siyuan Ma
Affiliation:
State Key Laboratory of Estuarine and Coastal Research, East China Normal University , Shanghai 200241, PR China
Qigang Chen
Affiliation:
School of Civil Engineering, Beijing Jiaotong University, Beijing 100044, PR China
Qiang Zhong
Affiliation:
College of Water Resource and Civil Engineering, China Agricultural University, Beijing 100083, PR China
Fan Xu*
Affiliation:
State Key Laboratory of Estuarine and Coastal Research, East China Normal University , Shanghai 200241, PR China
Qing He
Affiliation:
State Key Laboratory of Estuarine and Coastal Research, East China Normal University , Shanghai 200241, PR China
Heidi Nepf
Affiliation:
Department of Civil and Environmental Engineering, Massachusetts Institute of Technology, Cambridge, MA 02139, USA
*
Corresponding authors: Yuan Xu, yuanxu@sklec.ecnu.edu.cn; Fan Xu, fxu@sklec.ecnu.edu.cn
Corresponding authors: Yuan Xu, yuanxu@sklec.ecnu.edu.cn; Fan Xu, fxu@sklec.ecnu.edu.cn

Abstract

By generating drag and turbulence away from the bed, aquatic vegetation shapes the mean and turbulent velocity profile. However, the near-bed velocity distribution in vegetated flows has received little theoretical or experimental attention. This study investigated the near-bed velocity profile and bed shear stress using a coupled particle image velocimetry and particle tracking velocimetry system, which enabled the acquisition of flow-field measurements at very high spatial and temporal resolution. A viscous sublayer with a linear velocity profile was present, but this sublayer thickness was much smaller in vegetated flows than in bare flows with the same channel velocity. However, the dimensionless viscous sublayer thickness was the same in vegetated and bare flows, $z_v^+ = z_v \langle u_*\rangle / \nu = 6.1 \pm 0.7$. In addition, in vegetated flow, the horizontally averaged velocity profile above the viscous sublayer did not follow the classic logarithmic law found for bare beds. This deviation was attributed to the violation of two key assumptions in the classic Prandtl mixing length theory. By modifying the mixing length theory for vegetated conditions, a new theoretical power law profile for near-bed velocity was derived and validated with velocity data from both the present and previous studies, with mean percent errors of 4.9 % and 7.8 %, respectively. Using the new velocity law, the spatially averaged bed shear stress (and friction velocity) can be predicted from channel-average velocity, vegetation density and stem diameter, all of which are conveniently measured in the field.

Information

Type
JFM Papers
Copyright
© The Author(s), 2026. Published by Cambridge University Press
Figure 0

Figure 1.Schematic side view of the experimental flume. The figure is not to scale.

Figure 1

Figure 2.(a) Photograph of both cylinder sizes. (b) Schematic top view of the canopy. Black dots indicate the position of individual cylinders. Grey triangles are Vectrino measurement locations. Green dashed lines represent laser planes. The red dashed box locates a unit cell that represents the repeated velocity pattern within the array. (c) Schematic of the weighting scheme in (3.2). If the weight of each black box is 2, the weighted contribution of Y1, Y2, Y3 and Y4 to the average over unit cell (red box) is 1, 2, 2 and 1, respectively. (d) A particle image in the Y4 lateral section captured by the high-speed camera. (e) The instantaneous flow field obtained from a pair of images in the Y4 section using the PIV-PTV method. Red and green dots denote the particle centroids identified in the first and second frames, respectively. Yellow arrows indicate the corresponding velocity vectors obtained through particle tracking.

Figure 2

Table 1.Summary of experimental conditions and image resolution. The uncertainty in water depth $H$ arose from water surface fluctuations. Channel-average velocity $U$ was determined from the flow meter (i.e.discharge $Q$) and the uncertainty reflects small fluctuations in flow meter readings. The friction velocity $\langle u_*\rangle$ uncertainty stemmed from repeated velocity measurements and fitting of velocity gradients within the viscous sublayer.

Figure 3

Figure 3.(a) Comparisons of velocity, $\overline {u}$, at $z=0.5$ cm for four lateral sections measured from Vectrino and the PIV-PTV method for both bare and vegetated cases. Panels (b), (c) and (d) show bare bed cases O1 and O2. (b) Dimensionless velocity profiles of bare cases (without vegetation) measured with the PIV-PTV method. The dashed and solid lines represent the linear velocity distribution (2.10) in the viscous sublayer and logarithmic law (2.15) in the turbulent layer, respectively. (c) Dimensionless Reynolds stress profiles. The grey dashed line represents the theoretical linear distribution. (d) Dimensionless turbulent mixing length profiles. The grey dashed line is the linear law (2.14).

Figure 4

Figure 4.(a) Profiles of normalised velocity, $\langle \overline {u}\rangle /U$, in vegetated cases A1, D1, F1, D1H and F1D. Star markers are Vectrino measurements. Small dots close to the bed are the PIV-PTV measurements. (b) An expanded view of the near-bed region for case D1H. The grey area denotes the boundary layer. The red dashed line indicates the top of the viscous sublayer ($z=z_v$). (c) Profiles of stress gradients, $\partial \langle \tau _v \rangle /\partial z$, $\partial \langle \tau _{R} \rangle /\partial z$, $\partial \langle \tau _{d}\rangle /\partial z$ and vegetation drag, $F_{x}$, as in (2.5) for case D1H.

Figure 5

Figure 5.Plots of $z_\delta /d$ versus $1/\sqrt {\textit{Re}_d C_d a d}$ from (a) the present study and (b) the previous study (Conde-Frias et al.2023). Best fit shown with the dashed grey line in (a).

Figure 6

Figure 6.Vertical profiles of time- and horizontal-mean velocity ($\langle \overline {u} \rangle$) near the bed ($z \lt 2.5$ mm) measured from the PIV–PTV method. The blue and red markers indicate velocity ranges 5.5–6.3 cm s−1 and 16.4–18.4 cm s−1, respectively. Increasing SVF noted with a dashed arrow. The blue and red dashed lines indicate the velocity gradients in the viscous sublayer. The grey dashed line indicates the top of the viscous sublayer for case O1.

Figure 7

Figure 7.(a) The variation in the sublayer thickness, $z_v$, with SVF, $\phi$. Bare bed conditions correspond to $\phi = 0$ (star symbol). Blue and red markers indicate velocity ranges from 5.5 to 6.3 cm s−1 and from 16.4 to 18.4 cm s−1, respectively. The dashed lines are fitted curves between sublayer thickness and $\phi$ at similar velocity. (b) The variation of the normalised friction velocity, $\langle u_* \rangle /U$, with SVF, $\phi$. The legend is the same as figure 6.

Figure 8

Figure 8.(a) Dimensionless velocity profiles in the very near-bed region ($z^+\lt 30$) for all cases. Grey symbols correspond to bare bed conditions and coloured symbols correspond to vegetated conditions. The grey shaded area indicates the viscous sublayer, where the mean velocity distribution is linear. The black dashed line represents the linear velocity law, $u^+=z^+$. (b) Dimensionless velocity profiles over $z^+\lt 300$. The data are presented on a log-linear scale. For vegetated cases, only measured data in the boundary layer ($z \lt z_\delta$) are shown. The black dashed-dotted line indicates the classic logarithmic law.

Figure 9

Figure 9.Vertical profiles of the three stress components ($\langle \tau _v \rangle = \rho \nu \partial \langle \overline {u} \rangle / \partial z$, $\langle \tau _R \rangle = -\rho \langle \overline {u' w'} \rangle$, $\langle \tau _d \rangle = -\rho \langle \overline {u}'' \overline {w}'' \rangle$) normalised by bed stress $\langle \tau _b \rangle$ within the near-bed region of (a) bare bed (cases O1 and O2), and (b) vegetated bed with all densities (cases A1–F1). The blue, red and grey markers represent viscous, Reynolds and dispersive stresses, respectively. The thick dashed line in (b) indicates the top of the boundary layer ($z^+ =z_\delta ^+=38$) for case A1; and $z_\delta ^+ = 18$ for case F1. Note that, since the friction velocity was lower for bare cases, for the same physical distance from the bed ($z$), the values of $z^+$ attain larger values, as reflected in the vertical axis range.

Figure 10

Figure 10.Schematic classification of the velocity layers for (a) emergent vegetated flows (layer thickness not shown to scale), and (b) bare flows. Here $z_\delta$ is the height of the boundary layer. In fully developed bare flows the boundary layer extends up to the water surface.

Figure 11

Figure 11.Variation of dimensionless turbulent mixing length $l_r^+$ with $z^+$ in bare flow.

Figure 12

Figure 12.Vegetated flow: dimensionless mixing length $l_r^+$ versus dimensionless distance from the bed $z^+$. (a) All vegetated cases, with $z_\delta ^+$ ranged from 18 to 98. The grey and green dashed lines represent the linear and quadratic power law (4.5), respectively. The black dashed line represents the van Driest (1956) function (4.4) with $\kappa =1.05$ and $B=92$. (b) Lowest density case, case A. (c) Excluding case A. (d) Schematic of the mixing length variation with distance above the bed in bare ($\phi =0$) and vegetated ($\phi \gt 0$) flows.

Figure 13

Figure 13.(a) Dimensionless dispersive length $l_d^+$ in the boundary layer versus $z^+$ for vegetated cases. The black dashed line represents a quadratic relationship between $l_d^+$ and $z^+$. (b) The relationship between $l_d^+/l_r^+$ and $z^+$ in the boundary layer. The horizontal line indicates the average value of $l_d^+/l_r^+$ for all vegetated cases.

Figure 14

Figure 14.Comparison of measured velocity over the entire boundary layer ($z\le z_\delta$) from (a) the present study and (b) previous studies with the new velocity law (4.13). The values of $z_\delta ^+$ in the present study ranges from 18 to 98. The black and grey dashed lines represent (4.13) and (2.10), respectively. The new power law (i.e. 4.13) applies to the region of $z^+\gt 13$ and $z\lt z_\delta$.

Figure 15

Figure 15.(a) Measured (this study) and predicted bed shear stress. (c) Measured (previous studies) and predicted bed shear stress. Prediction from (4.17).

Figure 16

Figure 16.Mean percentage error between predicted $\langle \tau _{b,p}\rangle$ and measured $\langle \tau _{b,m}\rangle$ with variation in parameter $C_d$ for the sparest (A1) and densest (F1) cases.

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