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BSA Flow Software Installation and User's Guide - CSI

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π<br />

d<br />

6<br />

considering the instantaneous velocity V ≡ Up - Uf, of the particle relative to<br />

the fluid. (From Durst, Melling & Whitelaw, 1981):<br />

t<br />

dU<br />

p<br />

π dUfπdV<br />

3<br />

dV<br />

ρ =− 3πµ<br />

dp V + dpρf<br />

− d pρf − d p πµρf<br />

dt<br />

6 dt 12 dt 2 ∫ dξ<br />

3 3 3 2<br />

p p<br />

142 3<br />

Accelerating<br />

force<br />

44 142 34 1 24<br />

1 24<br />

1 2<br />

Stokes<br />

viscous<br />

drag<br />

Lorenz-Mie light scattering theory<br />

4 3<br />

Pressure<br />

gradient<br />

force on<br />

fluid<br />

4 3<br />

Fluid<br />

resistance to<br />

accelerating<br />

sphere<br />

t<br />

0<br />

dξ<br />

t − ξ<br />

4444 44443<br />

Drag force<br />

associated with<br />

unsteady motion<br />

-where subscript p refer to the seeding particle, <strong>and</strong> subscript f refer to the<br />

fluid.<br />

(7-15)<br />

The first term in this equation represent the force required to accelerate the<br />

particle, <strong>and</strong> the second term describe the viscous drag as given by Stokes<br />

law. Acceleration of the fluid produce a pressure gradient in the vicinity of<br />

the particle, <strong>and</strong> hence additional force on the particle as described by the<br />

third term. The fourth term is the resistance of an inviscid fluid to<br />

acceleration of the sphere, <strong>and</strong> is predicted by potential flow theory. The last<br />

term is the “Basset history integral” representing the drag force arising from<br />

derivation of the flow pattern from that occurring in steady flow.<br />

Note that when the first, third <strong>and</strong> fourth terms are combined, the<br />

accelerating force is equivalent to that of a sphere whose mass is increased<br />

by an additional “virtual mass” equal to half the mass of the displaced fluid.<br />

The above equation is valid within the following assumptions:<br />

• The turbulence is homogeneous <strong>and</strong> time-invariant.<br />

• Particles are smaller than the turbulence microscale<br />

• Stokes drag law applies (particles are spherical)<br />

• Particles are always surrounded by the same fluid molecules<br />

• There is no interaction between particles.<br />

Furthermore external forces, such as gravitational, centrifugal <strong>and</strong><br />

electrostatic forces have been ignored.<br />

Depending on the nature of the flow, seeding particles used for LDAmeasurements<br />

usually have particle diameters ranging from 0.1 to 50 µm.<br />

This is comparable to the wavelength of the light used, which for a He-Ne<br />

laser is 632.8 nm.<br />

With particle sizes comparable to the wavelength of light, the Lorenz-Mie<br />

light scattering theory apply. This theory consider spherical particles, <strong>and</strong><br />

thus describe only the dependency on particle size, but in practice also the<br />

shape <strong>and</strong> orientation of seeding particles play a major role in the scattering<br />

of light.<br />

In general large particles scatter more light than smaller ones, but particle<br />

size also affect the spatial distribution of the scattered light as shown in<br />

Figure 7-13. For large particles the ratio of forward to backward scattered<br />

light can be in the order of 10 2 to 10 3 , while smaller particles scatter more<br />

evenly.<br />

7-18 <strong>BSA</strong> <strong>Flow</strong> <strong>Software</strong>: Reference guide

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