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12.5 Dimensionless Parameters and Similarity Laws 667<br />

Head, ft<br />

100%<br />

Efficiency<br />

80<br />

60<br />

80<br />

70<br />

40<br />

20<br />

Head<br />

60<br />

50<br />

40<br />

30<br />

20<br />

10<br />

0<br />

Horsepower<br />

0<br />

100<br />

80<br />

60<br />

40<br />

20<br />

0<br />

0 1000 2000 3000 4000 5000<br />

Capacity, gal/min<br />

Brake horsepower Efficiency<br />

0.25<br />

0.20<br />

0.15<br />

C H<br />

0.10<br />

0.05<br />

0<br />

C P (pump)<br />

C H<br />

η<br />

100%<br />

80<br />

60<br />

40<br />

20<br />

0<br />

0 0.025 0.050 0.075 0.100<br />

C Q<br />

0<br />

0.016<br />

0.012<br />

0.008<br />

0.004<br />

η<br />

CP<br />

(a)<br />

(b)<br />

F I G U R E 12.17 Typical performance data for a centrifugal pump: (a) characteristic curves for<br />

a 12-in. centrifugal pump operating at 1000 rpm, (b) dimensionless characteristic curves. (Data from Ref. 8,<br />

used by permission.)<br />

The dimensionless parameter C Q QvD 3 is called the flow coefficient. These three equations<br />

provide the desired similarity relationships among a family of geometrically similar pumps. If<br />

two pumps from the family are operated at the same value of flow coefficient<br />

it then follows that<br />

a Q<br />

vD 3b a Q<br />

1 vD 3b 2<br />

(12.32)<br />

a gh a<br />

v 2 D 2b a gh a<br />

1 v 2 D 2b 2<br />

(12.33)<br />

Pump scaling laws<br />

relate geometrically<br />

similar pumps.<br />

a W# shaft<br />

(12.34)<br />

rv 3 D 5b a W# shaft<br />

1 rv 3 D 5b 2<br />

h 1 h 2<br />

(12.35)<br />

where the subscripts 1 and 2 refer to any two pumps from the family of geometrically similar<br />

pumps.<br />

With these so-called pump scaling laws it is possible to experimentally determine the performance<br />

characteristics of one pump in the laboratory and then use these data to predict the corresponding<br />

characteristics for other pumps within the family under different operating conditions.<br />

Figure 12.17a shows some typical curves obtained for a centrifugal pump. Figure 12.17b shows<br />

the results plotted in terms of the dimensionless coefficients, C Q , C H , C p , and h. From these curves<br />

the performance of different-sized, geometrically similar pumps can be predicted, as can the effect<br />

of changing speeds on the performance of the pump from which the curves were obtained. It is to<br />

be noted that the efficiency, h, is related to the other coefficients through the relationship<br />

h C Q C H C 1 p . This follows directly from the definition of h.<br />

E XAMPLE 12.5<br />

Use of Pump Scaling Laws<br />

GIVEN An 8-in.-diameter centrifugal pump operating at 1200<br />

rpm is geometrically similar to the 12-in.-diameter pump having<br />

the performance characteristics of Figs. 12.17a and 12.17b while<br />

operating at 1000 rpm. The working <strong>fluid</strong> is water at 60 °F.<br />

FIND For peak efficiency, predict the discharge, actual head<br />

rise, and shaft horsepower for this smaller pump.

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