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Mechanics of Fluids

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The torque T on the cylinder <strong>of</strong> radius b<br />

= stress × area × radius<br />

= (µr∂ω/∂r) r=b × 2πbh × b<br />

where h represents the height <strong>of</strong> the cylinder in contact with the fluid, and<br />

end effects are assumed negligible.<br />

∴ T = 2πµb 3 � �<br />

∂ω<br />

h = 2πµb<br />

∂r<br />

3 � �<br />

A<br />

h (from eqn 6.30)<br />

r=b<br />

µb 3<br />

= 2πhA = 4πha2b2 µ�<br />

a2 = kµ� (6.32)<br />

− b2 where k is a constant for any given apparatus.<br />

It may readily be shown that the torque on the rotating cylinder is the<br />

same. Equation 6.32 applies whether the inner cylinder is stationary while<br />

the outer one rotates, or the outer cylinder is stationary while the inner one<br />

rotates.<br />

In the derivation <strong>of</strong> eqn 6.32 it was assumed that h was large enough to<br />

render negligible any special effects at the ends. In practice, however, the<br />

cylinders are <strong>of</strong> moderate length and some account must therefore be taken<br />

<strong>of</strong> effects produced by the ends. The end effects are very similar to that <strong>of</strong><br />

an additional length <strong>of</strong> the cylinder in contact with the fluid, in other words<br />

(h + l) rather than h would arise in eqn 6.32. By using two, or preferably<br />

more, values <strong>of</strong> the liquid depth, and therefore <strong>of</strong> h, simultaneous equations<br />

are obtained from which l may be eliminated.<br />

If the radii <strong>of</strong> the two cylinders are closely similar eqn 6.32 may be slightly<br />

simplified. Putting the annular clearance c = a − b and (a + b) = 2 × (mean<br />

radius) = mean diameter = D, we obtain<br />

a<br />

T = 4πhµ�<br />

2b2 � �<br />

D + c<br />

2� �<br />

D − c<br />

2�<br />

= 4πhµ�<br />

Dc<br />

(a + b)(a − b) 2 2<br />

= πhµ�<br />

4Dc (D2 − c 2 ) 2<br />

Then neglecting c 2 in comparison with D 2 , we have<br />

T = πhµ�D3<br />

4c<br />

The measurement <strong>of</strong> viscosity 217<br />

(6.33)<br />

A simple laboratory viscometer <strong>of</strong> this type is that devised by G. F. C. Searle<br />

(1864–1954).<br />

It is important to remember that neither eqn 6.32 nor eqn 6.33 is applicable<br />

if the motion <strong>of</strong> the fluid is turbulent. Moreover, the assumption has been<br />

made throughout that the two cylinders are concentric. The formulae are<br />

therefore not applicable (except in very rare instances) to journal bearings,<br />

for, as we shall see in Section 6.7.3, a journal bearing supports a load only<br />

if the journal and bearing are not concentric.

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