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BSA Flow Software Installation and User's Guide - CSI

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7.1.8 Seeding<br />

Seeding as flow field tracers<br />

In LDA it is not actually the velocity of the flow that is measured, but the<br />

velocity of particles suspended in the flow. In this respect these seeding<br />

particles can be considered to be the actual velocity probes, <strong>and</strong> seeding<br />

considerations are thus important in LDA.<br />

The particles must be small enough to track the flow accurately, yet large<br />

enough to scatter sufficient light for the photodetector to be able to detect the<br />

Doppler frequency. Ideally, the particles should also be neutrally buoyant in<br />

the fluid, that is they should have approximately the same density as the<br />

fluid itself, but in many experiments this is a secondary consideration.<br />

Durst, Melling & Whitelaw (1981) state the following desired properties of<br />

seeding particles:<br />

Particles whose motion is used to represent that of a fluid should be:<br />

• Able to follow the flow.<br />

• Good light scatterers.<br />

• Conveniently generated.<br />

• Cheap.<br />

• Non-toxic, non-corrosive, non-abrasive.<br />

• Non-volatile, or slow to evaporate.<br />

• Chemically inactive.<br />

• Clean.<br />

In general the motion of particles suspended in a fluid is affected by<br />

• Particle shape.<br />

• Particle size.<br />

• Relative density of particle <strong>and</strong> fluid.<br />

• Concentration of particles in the fluid.<br />

• Body forces.<br />

The shape of the seeding particles affect the drag exerted on the particle by<br />

the surrounding fluid, <strong>and</strong> the size of the particles along with their relative<br />

density influence their response to velocity changes of the surrounding fluid.<br />

The concentration of particles affect particle motion through interaction<br />

between different particles. In practice the concentrations used are normally<br />

so low, that particle interaction can be neglected.<br />

Also body forces, such as gravity, can normally be ignored, except in very<br />

slow flows, where buoyancy of the seeding particles may be an issue. Also<br />

in experiments including for example electrostatic fields, body forces may be<br />

of importance, but in such cases, they will probably be part of the<br />

experiment, <strong>and</strong> as such they can not really be considered a disturbance.<br />

Particle motion Since the analysis of particle motion is rather complicated even for spherical<br />

particles, <strong>and</strong> “real” particles can’t be modelled properly anyway, only<br />

spherical particles in an infinite fluid have been analysed. It is assumed, that<br />

the results apply qualitatively also for particles of more irregular shape. This<br />

assumption is good for liquid particles <strong>and</strong> fair for monodisperse solid<br />

particles, but poor for other solid particles, such as agglomerates.<br />

Basset derived the equation of motion for a sphere relative to an infinite,<br />

stagnant fluid in 1888, <strong>and</strong> in 1959 Hinze exp<strong>and</strong>ed this to a moving fluid,<br />

<strong>BSA</strong> <strong>Flow</strong> <strong>Software</strong>:Reference guide 7-17

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