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Mechanics of Fluids

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∴ Velocity <strong>of</strong> approach = 0.0660 m3 · s−1 0.26 m2 = 0.254 m · s −1<br />

u2 1<br />

2g = (0.254 m · s−1 ) 2<br />

19.62 m · s−2 = 3.28 × 10−3 m<br />

∴ H + u 2 1 /2g = (0.155 + 0.00328) m = 0.1583 m<br />

Second approximation: Q = 2<br />

3 0.61� (19.62)0.6(0.1583) 3/2 m 3 · s −1<br />

= 0.0681 m 3 · s −1<br />

Further refinement <strong>of</strong> the value could be obtained by a new calculation<br />

<strong>of</strong> u1(0.0681 m 3 · s −1 ÷0.26 m 2 ), a new calculation <strong>of</strong> H +u 2 1 /2g<br />

and so on. One correction is usually sufficient, however, to give a value<br />

<strong>of</strong> Q acceptable to three significant figures. ✷<br />

PROBLEMS<br />

3.1 A pipe carrying water tapers from a cross-section <strong>of</strong> 0.3 m 2 at<br />

A to 0.15 m 2 at B which is 6 m above the level <strong>of</strong> A. AtA<br />

the velocity, assumed uniform, is 1.8 m · s −1 and the pressure<br />

117 kPa gauge. If frictional effects are negligible, determine the<br />

pressure at B.<br />

3.2 A long bridge with piers 1.5 m wide, spaced 8 m between<br />

centres, crosses a river. The depth <strong>of</strong> water before the bridge is<br />

1.6 m and that between the piers is 1.45 m. Calculate the volume<br />

rate <strong>of</strong> flow under one arch assuming that the bed <strong>of</strong> the river is<br />

horizontal, that its banks are parallel and that frictional effects<br />

are negligible.<br />

3.3 A pipe takes water from a reservoir where the temperature is<br />

12 ◦ C to a hydro-electric plant 600 m below. At the 1.2 m<br />

diameter inlet to the power house the gauge pressure <strong>of</strong> the<br />

water is 5.5 MPa and its mean velocity 2 m · s −1 . If its temperature<br />

there is 13.8 ◦ C at what rate has heat passed into<br />

the pipe as a result <strong>of</strong> hot sunshine? (Note: The change <strong>of</strong><br />

atmospheric pressure over 600 m must be accounted for: mean<br />

atmospheric density = 1.225 kg · m −3 . Specific heat capacity <strong>of</strong><br />

water = 4.187 kJ · kg −1 · K −1 .)<br />

3.4 In an open rectangular channel the velocity, although uniform<br />

across the width, varies linearly with depth, the value at the free<br />

surface being twice that at the base. Show that the value <strong>of</strong> the<br />

kinetic energy correction factor is 10/9.<br />

3.5 From a point 20 m away from a vertical wall a fireman directs<br />

a jet <strong>of</strong> water through a window in the wall at a height <strong>of</strong><br />

15 m above the level <strong>of</strong> the nozzle. Neglecting air resistance<br />

Problems 131

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