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12.9 Compressible Flow Turbomachines 685<br />

F l u i d s i n t h e N e w s<br />

Cavitation damage in hydraulic turbines The occurrence of<br />

cavitation in hydraulic pumps seem to be an obvious possibility<br />

since low suction pressures are expected. Cavitation damage can<br />

also occur in hydraulic turbines even though they do not seem<br />

obviously prone to this kind of problem. Local acceleration of<br />

liquid over blade surfaces can be sufficient to result in local pressures<br />

low enough to cause <strong>fluid</strong> vaporization or cavitation.<br />

Further along the flow path, the <strong>fluid</strong> can decelerate rapidly<br />

enough with accompanying increase in local pressure to make<br />

cavitation bubbles collapse with enough intensity to cause blade<br />

surface damage in the form of material erosion. Over time, this<br />

erosion can be severe enough to require blade repair or replacement<br />

which is very expensive. (See Problem 12.80.)<br />

E XAMPLE 12.9<br />

Use of Specific Speed to Select Turbine Type<br />

GIVEN A hydraulic turbine is to operate at an angular velocity<br />

of 6 revs, a flowrate of 10 ft 3 s, and a head of 20 ft.<br />

SOLUTION<br />

The most efficient type of turbine to use can be obtained by calculating<br />

the specific speed, , and using the information of Fig.<br />

12.32. To use the dimensional form of the specific speed indicated<br />

in Fig. 12.32 we must convert the given data into the appropriate<br />

units. For the rotor speed we get<br />

To estimate the shaft power, we assume all of the available head<br />

is converted into power and multiply this amount by an assumed<br />

efficiency 194%2.<br />

W # shaft 21.3 hp<br />

Thus for this turbine,<br />

N¿ sd v2W# shaft<br />

1h a 2 5 4<br />

According to the information of Fig. 12.32,<br />

<br />

A mixed-flow Francis turbine would<br />

probably give the highest efficiency and<br />

an assumed efficiency of 0.94 is appropriate.<br />

(Ans)<br />

COMMENT What would happen if we wished to use a Pelton<br />

wheel for this application? Note that with only a 20-ft head, the<br />

maximum jet velocity, V 1 , obtainable 1neglecting viscous effects2<br />

would be<br />

As shown by Eq. 12.52, for maximum efficiency of a Pelton<br />

wheel the jet velocity is ideally two times the blade velocity.<br />

Thus, V 1 2vR, or the wheel diameter, D 2R, is<br />

N¿ sd<br />

FIND What type of turbine should be selected? Explain.<br />

v 6 revs 60 smin 360 rpm<br />

W # 20 ft10.942<br />

shaft gQzh 162.4 lbft 3 2110 ft 3 s2c<br />

550 ft # lbs # hp d<br />

1360 rpm2 221.3 hp<br />

120 ft2 5 4<br />

39.3<br />

V 1 12 gz 22 32.2 fts 2 20 ft 35.9 fts<br />

To obtain a flowrate of Q 10 ft 3 s at a velocity of<br />

V 1 35.9 fts, the jet diameter, d 1 , must be given by<br />

or<br />

D V 1<br />

v 35.9 fts<br />

0.952 ft<br />

16 revs 2p radrev2<br />

Q p 4 d 2 1 V 1<br />

d 1 c 4Q 12<br />

d c 4110 ft3 12<br />

s2<br />

pV 1 p135.9 fts2 d 0.596 ft<br />

A Pelton wheel with a diameter of D 0.952 ft supplied with<br />

water through a nozzle of diameter d 1 0.596 ft is not a practical<br />

design. Typically d 1 66 D 1see Fig. 12.222. By using<br />

multiple jets it would be possible to reduce the jet diameter.<br />

However, even with 8 jets, the jet diameter would be 0.211 ft,<br />

which is still too large 1relative to the wheel diameter2 to be<br />

practical. Hence, the above calculations reinforce the results<br />

presented in Fig. 12.32—a Pelton wheel would not be practical<br />

for this application. If the flowrate were considerably smaller,<br />

the specific speed could be reduced to the range where a Pelton<br />

wheel would be the type to use 1rather than a mixed-flow reaction<br />

turbine2.<br />

12.9 Compressible Flow Turbomachines<br />

Compressible flow turbomachines are in many ways similar to the incompressible flow pumps and<br />

turbines described in previous portions of this chapter. The main difference is that the density of<br />

the <strong>fluid</strong> 1a gas or vapor2 changes significantly from the inlet to the outlet of the compressible flow<br />

machines. This added feature has interesting consequences, benefits, and complications.

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