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6.2.5. Stokes' Law<br />

When a sphere of radius R moves with velocity V through a<br />

stationary fluid and if the motion is nonturbulent, then the<br />

viscous drag (F) on the sphere is given by Stokes' law:<br />

F s=61r1]RV<br />

(6.12)<br />

where TJ is the viscosity of the fluid.<br />

6.2.6. Erythrocyte Sedimentation Rate<br />

The coefficient of viscosity (TJ) depends on temperature; the<br />

approximate viscosity-temperature relation is:<br />

b<br />

1]=a.eT (6.13)<br />

where a and b are constants and T is the absolute temperature.<br />

The erythrocyte sedimentation rate (ESR) measures the distance<br />

red blood cells will fall along the length of a vertical tube<br />

over a given time period (e.g., I hour).<br />

Sedimentation is normally accelerated as the temperature rises<br />

and the viscosity decreases [see equation (6.13)]:<br />

I<br />

V==- (6.14)<br />

1]<br />

Sedimentation of red cells depends on the forces resisting<br />

sedimentation (e.g. negative charges on the red cells surface, the<br />

opposite stream of plasma, rigidity of the red cells) and the<br />

forces accelerating sedimentation (e.g. anemia, plasma proteins).<br />

Changes ESR values are associated with changes in plasma<br />

proteins with can be caused with various diseases (e.g. rheumatoid<br />

arthritis, temporal arteritis, polymyalgia rheumatica, tuberculosis<br />

and Hodgkin's).<br />

6.2.7. PoiseuiIle's Law of Flow<br />

The French physicist Poiseuille showed experimentally that the<br />

volume (Q) of liquid flowing through a tube of length I is directly<br />

proportional to the pressure difference (p J - p) driving the liquid, and<br />

proportional to the fourth power of the tube radius (R). The laminar<br />

flow of liquids in pi pes is described by Poiseuille's Law 0/Flow:<br />

54<br />

I 1r·R 4<br />

Q =--;]'8T'(PI - pz)· (6.15)<br />

Poiseuille's law of flow can be used to quantitative measure<br />

the viscosity (TJ) of liquids.<br />

6.2.8. Sedimentation<br />

When a sphere falls in a viscous medium, it reaches a terminal<br />

velocity when the retarding forces, viscosity (F, = 6·1r·TJ·R· V) and<br />

buoyancy (FA =pm-V· g =~ .n.R 3 p m·g) equal the weight (m- g =<br />

=~ .n.R 3 p s p<br />

• g) of the sphere:<br />

f.n . R 3 • Psp • g = ~ . tt . R 3 • Pm' g + 6 . n . 1] . R . V (6.16)<br />

where m is the mass of sphere, R = ~ -<br />

the radius of sphere, P sp<br />

and Pm - the density of the sphere and medium, and TJ - the<br />

viscosity of the medium.<br />

2· g . R Z • t . (p - P )<br />

Hence. · 1] - Sp m (6 • 17)<br />

9·/<br />

and the terminal velocity (also called sedimentation velocity) can<br />

be determined as:<br />

V = g. P sp -<br />

Pm<br />

2. R Z<br />

1] 9<br />

6.2.9. Physical Principles of Ultracentrifugation<br />

(6.18)<br />

The movement of spherical particles in a centrifuge tube<br />

(fig. 6.8) eventually reach a terminal velocity determined<br />

by the frictional force (F; = 6·n·TJ·R· V), centripetal force<br />

mmV 2 2 V 2 )<br />

( Fcp = .---- = m 11/UJ r = Pm UJ r<br />

r<br />

55

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