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12.4 The Centrifugal Pump 655<br />

Centrifugal pump<br />

impellers involve an<br />

increase in blade<br />

velocity along the<br />

flow path.<br />

As discussed in Section 12.3, the moment-of-momentum equation indicates that the shaft<br />

torque, required to rotate the pump impeller is given by equation Eq. 12.2 applied to a pump<br />

with m # T shaft<br />

1 m # ,<br />

2 m # . That is,<br />

or<br />

(12.9)<br />

T shaft rQ1r 2 V u2 r 1 V u1 2<br />

(12.10)<br />

where V u1 and V u2 are the tangential components of the absolute velocities, V 1 and V 2 1see Figs.<br />

12.8b,c2.<br />

For a rotating shaft, the power transferred, W # shaft, is given by<br />

and therefore from Eq. 12.10<br />

Since U 1 r 1 v and U 2 r 2 v we obtain<br />

T shaft m # 1r 2 V u2 r 1 V u1 2<br />

W # shaft T shaft v<br />

W # shaft rQv1r 2 V u2 r 1 V u1 2<br />

W # shaft rQ1U 2 V u2 U 1 V u1 2<br />

(12.11)<br />

Equation 12.11 shows how the power supplied to the shaft of the pump is transferred to the flowing<br />

<strong>fluid</strong>. It also follows that the shaft power per unit mass of flowing <strong>fluid</strong> is<br />

w shaft W# shaft<br />

rQ<br />

For incompressible pump flow, we get from Eq. 5.82<br />

U 2V u2 U 1 V u1<br />

w shaft a p out<br />

r V 2<br />

out<br />

2 gz outb a p in<br />

r V in 2<br />

2 gz inb loss<br />

(12.12)<br />

W 2<br />

β 2<br />

V 2<br />

V θ 2<br />

α 2<br />

Vr2<br />

(c)<br />

U 2<br />

W 2<br />

β 2<br />

V 2<br />

U 2<br />

α 2<br />

W 1<br />

V 1<br />

r 2<br />

1<br />

W 1<br />

V 1<br />

r 1<br />

β 1<br />

β<br />

α 1<br />

U 1<br />

(a)<br />

+<br />

ω<br />

V θ 1<br />

α 1<br />

Vr1<br />

U 1<br />

(b)<br />

F I G U R E 12.8<br />

centrifugal pump impeller.<br />

Velocity diagrams at the inlet and exit of a

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