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Handbook of Turbomachinery Second Edition Revised - Ventech!

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above becomes a factor. This statement is sort <strong>of</strong> a ‘‘hybrid’’ <strong>of</strong> the<br />

above two observations but serves as an alternate way to picture the<br />

same process.<br />

An interested reader who researches the marketplace <strong>of</strong> positive displacement<br />

pump products will find variations on the simplified picture <strong>of</strong> Fig.<br />

15(a) which allow variations in pump flow rate. However, it should be<br />

understood that these are modifications <strong>of</strong> a machine whose basic tendencies<br />

are as described in the above paragraphs.<br />

Variable Displacement Pumping Elements<br />

Dominating the specific speed spectrum from a ‘‘low’’ value on the order <strong>of</strong><br />

200 (rpm-gpm-ft units) to values in excess <strong>of</strong> 10,000 is the class <strong>of</strong> pumping<br />

elements broadly known as variable displacement pumps. These machines are<br />

also referred to as ‘‘dynamic’’ or ‘‘rotodynamic pumps.’’ Centrifugal pumps<br />

and axial-flow pumps both fall into this general class, as well as a broad<br />

range <strong>of</strong> ‘‘in-between’’ pumps that are neither purely centrifugal or axial.<br />

These ‘‘in-between’’ pumps are <strong>of</strong>ten referred to as ‘‘mixed-flow’’ or<br />

‘‘Francis’’ pumps.<br />

Shown in Fig. 15(b) is ageneralized rotor <strong>of</strong> ahypothetical variable<br />

displacement pump. This rotor has a radius r1 at its inlet, and a radius r2 at<br />

its outlet. These radii may be equal, or the outlet radius r2 may be somewhat<br />

greater than r1. The rotor is being turned about the axis <strong>of</strong> rotation as<br />

shown, at an angular velocity o, requiring a torque T to maintain this<br />

velocity. For this example, our rotor is assumed to consist <strong>of</strong> a single row <strong>of</strong><br />

moving blades. In the case <strong>of</strong> multiple moving rows, most real machines<br />

intersperse stationary rows between the moving ones. In these cases, the<br />

accounting procedure is slightly more involved than that presented here, but<br />

not different in generality.<br />

Fluid is flowing steadily through this rotor at a mass rate _m. Fluid<br />

enters the rotor in the plane <strong>of</strong> the radius r1, with a ‘‘bulk’’ or ‘‘throughflow’’<br />

velocity Cm1. This velocity is also referred to as a ‘‘meridonal’’<br />

velocity. In addition to Cm1, a component exists in the tangential direction,<br />

Cu1. The velocity component Cu1 is <strong>of</strong>ten equal to zero. If not equal to zero,<br />

Cu1 is normally in the same direction as rotor rotation and is known as<br />

‘‘prewhirl.’’ In cases where prewhirl exists, it is normally generated by the<br />

designer for some particular reason. This topic will be discussed in more<br />

detail in a subsequent section.<br />

Fluid leaves the rotor in the plane <strong>of</strong> radius r2, with a ‘‘meridonal’’<br />

velocity Cm2 (note that Cm2 may have a radial component, depending on<br />

whether or not the inlet and exit radii are unequal). In addition, a tangential<br />

Copyright © 2003 Marcel Dekker, Inc.

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