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WARNING Stand clear of<br />

Hazard areas while engine is<br />

running<br />

454 Chapter 8 ■ Viscous Flow in Pipes<br />

Estimate the extra pressure drop between points (1) and (2) caused<br />

by these straws.<br />

C1130F<br />

(1)<br />

Tightly packed 0.25-in.-diameter,<br />

12-in.-long straws<br />

(2)<br />

12 in.<br />

WARNING Stand clear of<br />

Hazard areas while engine is<br />

running<br />

F I G U R E P8.66<br />

8.67 Repeat Problem 8.66 if the straws are replaced by a piece of<br />

porous foam rubber that has a loss coefficient equal to 5.4.<br />

F I G U R E P8.63<br />

8.64 (See Fluids in the News article titled “New hi-tech fountains,”<br />

Section 8.5.) The fountain shown in Fig. P8.64 is designed<br />

to provide a stream of water that rises h 10 ft to<br />

h 20 ft above the nozzle exit in a periodic fashion. To do this<br />

the water from the pool enters a pump, passes through a pressure<br />

regulator that maintains a constant pressure ahead of the<br />

flow control valve. The valve is electronically adjusted to provide<br />

the desired water height. With h 10 ft the loss coefficient<br />

for the valve is K L 50. Determine the valve loss coefficient<br />

needed for h 20 ft. All losses except for the flow control valve<br />

are negligible. The area of the pipe is 5 times the area of the exit<br />

nozzle.<br />

8.68 As shown in Fig. P8.68, water flows from one tank to another<br />

through a short pipe whose length is n times the pipe diameter.<br />

Head losses occur in the pipe and at the entrance and exit.<br />

(See Video V8.10.) Determine the maximum value of n if the major<br />

loss is to be no more than 10% of the minor loss and the friction<br />

factor is 0.02.<br />

D<br />

= nD<br />

F I G U R E P8.68<br />

h<br />

8.69 Air flows through the fine mesh gauze shown in Fig. P8.69<br />

with an average velocity of 1.50 m/s in the pipe. Determine the<br />

loss coefficient for the gauze.<br />

4 ft<br />

Gauze over<br />

end of pipe<br />

V = 1.5 m/s<br />

Pump<br />

Flow control valve<br />

Pressure regulator<br />

F I G U R E P8.64<br />

8 mm<br />

Water<br />

*8.65 Water flows from a large open tank through a sharp-edged<br />

entrance and into a galvanized iron pipe of length 100 m and diameter<br />

10 mm. The water exits the pipe as a free jet at a distance<br />

h below the free surface of the tank. Plot a log–log graph of the<br />

flowrate, Q, as a function of h for 0.1 h 10 m.<br />

8.66 Air flows through the mitered bend shown in Fig. P8.66 at<br />

a rate of 5.0 cfs. To help straighten the flow after the bend, a set<br />

of 0.25-in.-diameter drinking straws is placed in the pipe as shown.<br />

F I G U R E P8.69<br />

8.70 Water flows steadily through the 0.75-in-diameter galvanized<br />

iron pipe system shown in Video V8.14 and Fig. P8.70 at<br />

a rate of 0.020 cfs. Your boss suggests that friction losses in the<br />

straight pipe sections are negligible compared to losses in the<br />

threaded elbows and fittings of the system. Do you agree or disagree<br />

with your boss? Support your answer with appropriate calculations.

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