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1. Thermo-physical properties 2. Radiation properties - nptel - Indian ...

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Mechanical Measurements Prof S.P.Venkatesan<br />

<strong>Indian</strong> Institute of Technology Madras<br />

Figure 21 Schematic of a rotating cylinder viscometer<br />

The nomenclature used in the following derivation is given in Figure 2<strong>1.</strong> If the<br />

gap a between the two cylinders is very small compared to the radius of any of<br />

the cylinders we may approximate the flow between the two cylinders to be<br />

coquette flow familiar to us from fluid mechanics. The velocity distribution across<br />

2<br />

the gap a is linear and the constant velocity gradient is given by<br />

r du ω<br />

= . The<br />

dr b<br />

uniform shear stress acting on the surface of the inner cylinder all along its length<br />

L is then given by<br />

due to this is<br />

r du ω<br />

dr b<br />

2<br />

τ=μ =μ . The torque experienced by the inner cylinder<br />

2<br />

2<br />

1 2<br />

μωr 2πμωr r<br />

TL = × 2π rL 1 × r1<br />

=<br />

b <br />

<br />

b<br />

Shear stress<br />

Liquid<br />

film<br />

L<br />

Surface area<br />

Moment arm<br />

Stationary<br />

cylinder<br />

Constant<br />

rotational<br />

speed ω<br />

Rotating<br />

cylinder<br />

There is another contribution to the torque due to the shear stress at the bottom<br />

of the cylinder due to the liquid film of thickness a. At a radial distance r from the<br />

center of the stationary cylinder the shear stress is given by<br />

a<br />

r1<br />

r2<br />

b<br />

(17)<br />

ωr<br />

τ=μ . Consider<br />

a

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