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Section 3.4 considers suspension from the stoss slope downstream<br />

<strong>of</strong> the crest. However, the interaction between shear layer<br />

vortices and the stoss slope downstream <strong>of</strong> the trough was<br />

particularly difficult to study here because <strong>of</strong> bedload motion<br />

during start-up. Thus, particles pre-spread over the stoss slope<br />

were washed away during the start-up flows in our flume, even<br />

when the flume was full before the flow was started and<br />

regardless <strong>of</strong> the rate <strong>of</strong> increase in flow velocity. A partial<br />

solution was secured by attaching a grid <strong>of</strong> galvanised meshing<br />

to the centreline <strong>of</strong> the bedform. The height <strong>of</strong> the grid above<br />

the perspex bedform was about 4mm.<br />

Even with the grid present the starting flow washed away most <strong>of</strong><br />

the particles at higher flow velocities, however enough remained<br />

to allow reasonable estimation <strong>of</strong> the suspension fluxes. No<br />

estimates were made <strong>of</strong> the concentration distribution due to lack<br />

<strong>of</strong> particle numbers so we give a brief description here <strong>of</strong> the<br />

seven runs in which the flow velocity U and particle fall speed<br />

V were varied through U=0.20-0.36m/s at V=0.034m/s and U=0.20-<br />

0.43m/s at V=0.60m/s.<br />

3 EXPERIMENTAL RESULTS<br />

3.1 Visualisation <strong>of</strong> the Coanda-flapping events<br />

The series <strong>of</strong> plates in figure 2 show the Coanda-flapping<br />

phenomenon with great clarity. This sequence was taken over the<br />

bedforms described above at a flow velocity <strong>of</strong> about 0.6m/s<br />

4-10

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