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( a ) Isolines of normalized downstream velocity, v s / U . ( b ) Normalized depth-averaged downstream velocity, U s / U ; normalized unit discharge, ( U s Bh ) / Q . ( c ) Vertical profiles of 

( a ) Isolines of normalized downstream velocity, v s / U . ( b ) Normalized depth-averaged downstream velocity, U s / U ; normalized unit discharge, ( U s Bh ) / Q . ( c ) Vertical profiles of 

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Secondary currents are a characteristic feature of flow in open-channel bends. Besides the classical helical motion (centre-region cell), a weaker and smaller counter-rotating circulation cell (outer-bank cell) is often observed near the outer bank, which is believed to play an important role in bank erosion processes. The mechanisms underlying the...

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Context 1
... outer-bank cell comes into existence when the v s -profiles are so strongly deformed that the driving term changes sign in the upper part of the water column (cf. figure 3c in § 6). For the axisymmetric curved flows investigated in these numerical models, the outer-bank cell was only slightly weaker than the centre-region cell. ...
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... vectorial representation of the measured cross-stream velocity field, (v n , v z ), normalized by the overall mean velocity U = Q/(BH ), is shown in figure 3(d). The centre-region cell reflects the 'classical' helical motion that is characteristic of flow in bends. ...
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... circulatory part of the cross-stream motion is reflected by the downstream vorticity, ω s , which is shown in figure 3(e). The centre-region cell and the outer-bank cell, separated by the (ω s = 0)-contour, are clearly visible in the vorticity field. ...
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... distribution of the normalized downstream velocity component, v s /U , is given in figure 3(a). Its depth-averaged value is nearly constant over most of the measuring area: U s /U ≈ 1.35 (figure 3b), which means that the depth-averaged velocity there is well above the overall mean velocity. ...
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... depth-averaged value is nearly constant over most of the measuring area: U s /U ≈ 1.35 (figure 3b), which means that the depth-averaged velocity there is well above the overall mean velocity. Figure 3(b) also shows that the distribution of the normalized unit discharge, U s Bh/Q, with h denoting the local water depth, is concentrated in the deep outer part of the cross-section. Integration of this profile shows that about 80% of the discharge passes through the investigated outer half of the cross-section. ...
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... of this profile shows that about 80% of the discharge passes through the investigated outer half of the cross-section. The core of maximum velocity, marked by in figure 3(a, b), is found near the transition between the two circulation cells. Figure 3(c) compares some measured v s / U s -profiles with a logarithmic profile for a friction factor C f = 0.008, which corresponds to the value in the experiment as estimated by Blanckaert & Graf (2001). ...
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... core of maximum velocity, marked by in figure 3(a, b), is found near the transition between the two circulation cells. Figure 3(c) compares some measured v s / U s -profiles with a logarithmic profile for a friction factor C f = 0.008, which corresponds to the value in the experiment as estimated by Blanckaert & Graf (2001). The profiles shown are averaged over the outer-bank region (n = −20 to −14 cm), the transition zone (n = −14 to −8 cm) and the centre region (n = −8 to 0 cm). ...
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... (figures 3e, 5 and 6) Integrated over the water depth, the centrifugal term in the vorticity equations (4)- (6) is always positive, which complies with the sense of rotation of the centre-region cell. Due to advective momentum transport by the centre-region cell, the velocity maximum in the present experiments is in the lower part of the water column ( figure 3c). As a consequence, the centrifugal term -(∂/∂z)(v 2 s /R) in the vorticity equation is negative in a significant part of the water column (figure 5a), thus opposing the observed sense of rotation of the centre-region cell. ...

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Secondary currents are a characteristic feature of flow in open-channel bends. Besides the classical helical motion (centre-region cell), a weaker and smaller counter-rotating circulation cell (outer-bank cell) is often observed near the outer bank, which is believed to play an important role in bank erosion processes. The mechanisms underlying the...

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Confluences of open-channel flows commonly occur in natural and artificial water networks and in hydraulic structures. The flow in these junctions is complex, three-dimensional and is steered by the shape of the bed. This research focuses on schematized confluences with a T-shaped planform in which the bed level of the tributary channel is higher than the one in the main channel. This phenomenon is ubiquitous in natural river confluences, but also frequently occurs in human-made configurations. The effect on the flow of such a difference in bed elevations between the two channels is investigated by means of numerical simulations and laboratory experiments. Also, the effect on the mixing of suspended or dissolved substances in merging water streams is explored. The applied Large Eddy Simulations allow not only the study of the time-averaged flow features but also their time-dependent behaviour. Besides providing fundamental knowledge, this work also contributes to the optimization of artificial confluences.
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Large-eddy simulations of turbulent flow in partially filled pipes are conducted to investigate the effect of secondary currents on the friction factor, first- and second-order statistics and large-scale turbulent motion. The method is validated first and simulated profiles of the mean streamwise velocity, normal stresses and turbulent kinetic energy (TKE) are shown to be in good agreement with experimental data. The secondary flow is stronger in half- and three-quarters full pipes compared with quarter full or fully filled pipe flows, respectively. The origin of the secondary flow is examined by both the TKE budget and the steamwise vorticity equation, providing evidence that secondary currents originate from the corner between the free surface and the pipe walls, which is where turbulence production is larger than the sum of the remaining terms of the TKE budget. An extra source of streamwise vorticity production is found at the free surface near the centreline bisector, due to the two-component asymmetric turbulence there. The occurrence of dispersive stresses (due to secondary currents) reduces the contribution of the turbulent shear stress to the friction factor, which results in a reduction of the total friction factor of flows in half and three-quarters full pipes in comparison to a fully filled pipe flow. Furthermore, the presence of significant secondary currents inhibits very-large-scale motion (VLSM), which in turn reduces the strength and scales of near-wall streaks. Subsequently, near-wall coherent structures generated by streak instability and transient growth are significantly suppressed. The absence of VLSM and less coherent near-wall turbulence structures is supposedly responsible for the drag reduction in partially filled pipe flows relative to a fully filled pipe flow at an equivalent Reynolds number.