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Mechanics of Fluids

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156 The momentum equation<br />

✷<br />

(b) F = ϱAu2 (u1 − u4) = ϱA (u1 + u4)<br />

2<br />

(u1 − u4)<br />

= 1.2 kg · m −3 × π<br />

4 × (12 m)2 (20 + 8) m · s−1<br />

× × 12 m · s<br />

2<br />

−1<br />

= 22.8 × 10 3 N<br />

�<br />

u2 1<br />

(c) P = ϱQ<br />

2 − u2 � �<br />

4<br />

u2 1<br />

= ϱAu2<br />

2<br />

= ϱA (u1<br />

�<br />

+ u4) u2 1<br />

2 2 − u2 �<br />

4<br />

2<br />

2 − u2 4<br />

2<br />

= 1.2 kg · m −3 × π<br />

4 (12 m)2 (20 + 8) m · s−1<br />

×<br />

2<br />

��<br />

20 m · s−1 �2 �<br />

8m· s−1 �2 �<br />

×<br />

2<br />

−<br />

= 319 000 W = 319 kW<br />

PROBLEMS<br />

2<br />

4.1 A stationary curved vane deflects a 50 mm diameter jet <strong>of</strong> water<br />

through 150 ◦ . Because <strong>of</strong> friction over the surface, the water<br />

leaving the vane has only 80% <strong>of</strong> its original velocity. Calculate<br />

the volume flow rate necessary to produce a fluid-dynamic force<br />

<strong>of</strong> 2000 N on the vane.<br />

4.2 The diameter <strong>of</strong> a pipe-bend is 300 mm at inlet and 150 mm at<br />

outlet and the flow is turned through 120 ◦ in a vertical plane.<br />

The axis at inlet is horizontal and the centre <strong>of</strong> the outlet section<br />

is 1.4 m below the centre <strong>of</strong> the inlet section. The total volume<br />

<strong>of</strong> fluid contained in the bend is 0.085 m 3 . Neglecting friction,<br />

calculate the magnitude and direction <strong>of</strong> the net force exerted<br />

on the bend by water flowing through it at 0.23 m 3 · s −1 when<br />

the inlet gauge pressure is 140 kPa.<br />

4.3 Air at constant density 1.22 kg · m −3 flows in a duct <strong>of</strong> internal<br />

diameter 600 mm and is discharged to atmosphere. At the outlet<br />

end <strong>of</strong> the duct, and coaxial with it, is a cone with base diameter<br />

750 mm and vertex angle 90 ◦ . Flow in the duct is controlled<br />

by moving the vertex <strong>of</strong> the cone into the duct, the air then<br />

escaping along the sloping sides <strong>of</strong> the cone. The mean velocity<br />

in the duct upstream <strong>of</strong> the cone is 15 m · s −1 and the air leaves<br />

the cone (at the 750 mm diameter) with a mean velocity <strong>of</strong><br />

60 m · s −1 parallel to the sides. Assuming temperature changes<br />

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