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grains are not spherical and so must have defined separation<br />

points depending on their instantaneous orientations to the local<br />

flows. This is not the case for spherical particles which are<br />

<strong>of</strong>ten used as model substitutes for such grains, so we might<br />

argue that it is a reasonable compromise to use cylinders falling<br />

somewhere between these two extremes, perhaps even that our model<br />

particles may be more appropriate than spheres?<br />

The methods employed in the trajectory experiments <strong>of</strong> section 3<br />

were described in chapter 2; recall that the landing position and<br />

flight time <strong>of</strong> individual particles was recorded from video<br />

records <strong>of</strong> the trajectories <strong>of</strong> particles released on the upstream<br />

stoss slope.<br />

Their contribution to the particle concentration<br />

C in the lee fluid was measured by following individual<br />

particles. The time averaged relative concentration C ± /C 0<br />

in any<br />

reference mesh is then related to the number <strong>of</strong> particles N ± that<br />

have passed through at mean velocity Vpi by the expression (Sene,<br />

1985) .<br />

Vpi<br />

(1)<br />

where N 0 is the total number <strong>of</strong> particles tracked, C 0 is total<br />

particle concentration in the measurement grid and Vp0<br />

is mean<br />

velocity <strong>of</strong> the particles travelling through the grid. Vpi is<br />

related to the number <strong>of</strong> times that any single particle is<br />

counted in a square, here termed the number <strong>of</strong> footprints F ±<br />

that<br />

it leaves.<br />

For a square grid <strong>of</strong> side L(m) and time step t(sec)<br />

3-5

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