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Mechanics of Fluids

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where 0 ≤ θ ≤ 90 ◦ and sin θ = b2/b1. Ifb1 is large compared with b2, r<br />

becomes equal to 1.5 and eqn 10.35 may then be written<br />

Q = b2g1/2h 3/2<br />

1<br />

(1.5) 3/2<br />

The occurrence <strong>of</strong> critical conditions 453<br />

(10.36)<br />

This equation may be derived alternatively by substituting for h2 from<br />

eqn 10.33 into eqn 10.32:<br />

Q = b2g 1/2<br />

� � �<br />

3/2<br />

2<br />

3<br />

h1 + u2 1<br />

2g<br />

� 3/2<br />

(10.37)<br />

when b1 is very large, u1 is small and u2 1 /2g may be neglected. Even for<br />

b2/b1 = 1/3, r = 1.474 and so the error involved in neglecting the velocity<br />

<strong>of</strong> approach and using eqn 10.36 would be only 1.7% in r and 2.54% in Q.<br />

Corrections for velocity <strong>of</strong> approach may be applied in the same manner<br />

as for the broad-crested weir (Section 10.11.1). If u1 is at first neglected<br />

in eqn 10.37 an approximate value <strong>of</strong> Q may be calculated from which<br />

u1 = Q/b1h1 can be estimated for use in a second approximation. For a<br />

flume that has already been calibrated, however, this arithmetical process is<br />

not necessary as the cubic equation for r will have been solved once for all.<br />

A coefficient <strong>of</strong> discharge Cd is required to account for the small amount<br />

<strong>of</strong> friction between inlet and throat and for the effects <strong>of</strong> curvature <strong>of</strong> the<br />

streamlines which the given theory ignores. In practice, values <strong>of</strong> Cd are<br />

typically between 0.95 and 0.99.<br />

All the foregoing applies to a flume under conditions <strong>of</strong> free discharge,<br />

that is, where the liquid surface downstream is not maintained at too high a<br />

level. The level in the outlet from the flume continues to fall and thus rapid<br />

flow exists where the width <strong>of</strong> the passage again increases. If conditions<br />

downstream <strong>of</strong> the flume are such that the velocity is greater than the critical,<br />

the surface <strong>of</strong> the liquid issuing from the flume gradually merges into the<br />

normal depth <strong>of</strong> flow in the downstream channel, and any excess energy<br />

possessed by the liquid emerging from the flume is dissipated by friction.<br />

On the other hand, if conditions downstream are such as to demand a<br />

velocity less than the critical, the flow has to change from rapid to tranquil.<br />

This change normally takes place through a hydraulic jump (Fig. 10.38). The<br />

jump occurs at a point where the depth <strong>of</strong> the rapid flow is such as to give<br />

the correct depth <strong>of</strong> subsequent tranquil flow (according to eqn 10.25 if the<br />

section is rectangular). A limiting position is that in which the jump – then<br />

Fig. 10.38 Flow through venturi flume. The critical depth at the throat is greater<br />

because the narrowing <strong>of</strong> the channel increases the discharge divided by width q and<br />

for rectangular section hc = (q 2 /g) 1/3 .

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