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Mechanics of Fluids

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126 The principles governing fluids in motion<br />

Fig. 3.23<br />

✷<br />

Since<br />

�h = p1 − p2<br />

ϱ fg<br />

the volumetric flow rate is obtained by substituting in the relation<br />

�<br />

2g�h<br />

Q = CA0<br />

1 − (Ao/A1) 2<br />

�1/2 = 0.62 × π<br />

�<br />

6<br />

4 100 m<br />

� �<br />

2<br />

2 × 12 500 N · m−2 0.86 × 103 kg · m−3 ×[1− (6/12) 4 ]<br />

= 0.00976 m 3 · s −1<br />

Hence<br />

� 1/2<br />

m = ϱ fQ = 0.86 × 10 3 kg · m −3 × 0.00976 m 3 · s −1 = 8.39 kg · s −1<br />

3.7.5 Notches and sharp-crested weirs<br />

A notch may be defined as a sharp-edged obstruction over which flow <strong>of</strong> a<br />

liquid occurs. As the depth <strong>of</strong> flow above the base <strong>of</strong> the notch is related to<br />

the discharge, the notch forms a useful measuring device. It is formed in a<br />

smooth, plane, vertical plate and its edges are bevelled on the downstream<br />

side so as to give minimum contact with the fluid. The area <strong>of</strong> flow is most<br />

commonly either rectangular or V-shaped. A large rectangular notch is more<br />

<strong>of</strong>ten termed a sharp-crested weir.<br />

The pattern <strong>of</strong> flow over a notch is quite complex. Owing to the curvature<br />

<strong>of</strong> the streamlines (Fig. 3.23) there is no cross-section <strong>of</strong> the flow over which<br />

the pressure is uniform. Any attempt, therefore, to discover analytically<br />

the relation between the rate <strong>of</strong> flow and the depth at the notch can be<br />

based only on drastic simplifying assumptions. It is nevertheless useful in

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