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Mechanics of Fluids

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132 The principles governing fluids in motion<br />

determine the angle at which the nozzle must be held when the<br />

supply pressure at the nozzle is only just sufficient, and calculate<br />

this minimum pressure if Cv for the nozzle is 0.95. (The velocity<br />

head in the hose may be neglected.)<br />

3.6 The air supply to an oil-engine is measured by being taken<br />

directly from the atmosphere into a large reservoir through a<br />

sharp-edged orifice 50 mm diameter. The pressure difference<br />

across the orifice is measured by an alcohol manometer set at<br />

a slope <strong>of</strong> arcsin 0.1 to the horizontal. Calculate the volume<br />

flow rate <strong>of</strong> air if the manometer reading is 271 mm, the relative<br />

density <strong>of</strong> alcohol is 0.80, the coefficient <strong>of</strong> discharge for<br />

the orifice is 0.602 and atmospheric pressure and temperature<br />

are respectively 755 mm Hg and 15.8 ◦ C. (You may assume<br />

R = 287 J · kg −1 · K −1 .)<br />

3.7 Oil <strong>of</strong> relative density 0.85 issues from a 50 mm diameter orifice<br />

under a pressure <strong>of</strong> 100 kPa (gauge). The diameter <strong>of</strong> the vena<br />

contracta is 39.5 mm and the discharge is 18 L · s −1 . What is<br />

the coefficient <strong>of</strong> velocity?<br />

3.8 A submarine, submerged in sea-water, travels at 16 km · h −1 .<br />

Calculate the pressure at the front stagnation point situated<br />

15 m below the surface. (Density <strong>of</strong> sea-water =<br />

1026 kg · m −3 .)<br />

3.9 A vertical venturi-meter carries a liquid <strong>of</strong> relative density 0.8<br />

and has inlet and throat diameters <strong>of</strong> 150 mm and 75 mm<br />

respectively. The pressure connection at the throat is 150 mm<br />

above that at the inlet. If the actual rate <strong>of</strong> flow is 40 L · s −1<br />

and the coefficient <strong>of</strong> discharge is 0.96, calculate (a) the pressure<br />

difference between inlet and throat, and (b) the difference<br />

<strong>of</strong> levels in a vertical U-tube mercury manometer connected<br />

between these points, the tubes above the mercury being full <strong>of</strong><br />

the liquid. (Relative density <strong>of</strong> mercury = 13.56.)<br />

3.10 A servo-mechanism is to make use <strong>of</strong> a venturi contraction in<br />

a horizontal 350 mm diameter pipe carrying a liquid <strong>of</strong> relative<br />

density 0.95. The upper end <strong>of</strong> a vertical cylinder 100 mm<br />

diameter is connected by a pipe to the throat <strong>of</strong> the venturi<br />

and the lower end <strong>of</strong> the cylinder is connected to the inlet.<br />

A piston in the cylinder is to be lifted when the flow rate<br />

through the venturi exceeds 0.15 m 3 · s −1 . The piston rod is<br />

20 mm diameter and passes through both ends <strong>of</strong> the cylinder.<br />

Neglecting friction, calculate the required diameter <strong>of</strong><br />

the venturi throat if the gross effective load on the piston rod<br />

is 180 N.<br />

3.11 A sharp-edged notch is in the form <strong>of</strong> a symmetrical trapezium.<br />

The horizontal base is 100 mm wide, the top is 500 mm wide<br />

and the depth is 300 mm. Develop a formula relating the discharge<br />

to the upstream water level, and estimate the discharge<br />

when the upstream water surface is 228 mm above the level

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