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Handbook of Turbomachinery Second Edition Revised - Ventech!

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stable operation is assured. In some aggressive engine system designs (i.e.,<br />

those possessing low starting energy to minimize system weight), the effect<br />

<strong>of</strong> the H–Q curve shape (as influenced by head coefficient) should be<br />

evaluated for its effect on the system’s transient starting performance. Note<br />

that while the exactitude <strong>of</strong> results <strong>of</strong> these types <strong>of</strong> analyses is questionable,<br />

trends and relative margins can certainly be determined.<br />

The number <strong>of</strong> blades used in a centrifugal stage impeller can be<br />

readily approximated from a number <strong>of</strong> correlations that are in general use.<br />

The number <strong>of</strong> impeller blades can be expected to vary from 5 or 6 to as<br />

many as 24 or 25. However, the combination <strong>of</strong> high suction-performance<br />

requirements and the desire to highly load the pump stage (for weight<br />

reduction) leads to the use <strong>of</strong> impeller blades called ‘‘splitters’’ in many<br />

propellant pumps for liquid rocket engine systems. If we refer to Fig. 15(c),<br />

we can see that the required number <strong>of</strong> blades for a particular pump has<br />

been determined as eight. However, if all eight blades extend into the<br />

impeller eye, the amount <strong>of</strong> flow area that is ‘‘blocked’’ by the blades causes<br />

flow to accelerate to the point where substantial cavitation is encountered.<br />

This difficulty is dealt with by placing the leading edges <strong>of</strong> a number <strong>of</strong> the<br />

blades (perhaps half <strong>of</strong> them, perhaps more) significantly downstream <strong>of</strong> the<br />

impeller inlet. Of course, these blades extend all the way to the impeller exit,<br />

and thus the solidity criterion at the impeller exit for achieving the design<br />

head coefficient is met. It should be noted that a uniform criterion for<br />

placement <strong>of</strong> the splitter leading edges does not exist to this author’s<br />

knowledge. A technique <strong>of</strong>ten used to determine this is simply to place the<br />

leading edges <strong>of</strong> the splitters at 50% <strong>of</strong> the meridonal distance through the<br />

impeller flow passage, and then to simulate the resulting flow with any <strong>of</strong> a<br />

number <strong>of</strong> computer programs available. The results <strong>of</strong> these simulations<br />

can then be used to determine the point in the passage where loading <strong>of</strong> the<br />

full-length blades becomes excessive, requiring the placement <strong>of</strong> the splitter<br />

leading edges somewhat upstream <strong>of</strong> that point. For propellant pumps that<br />

must operate over a significant flow range, these computations should<br />

be carried out at the operating point consistent with the highest blade<br />

loading.<br />

The angle <strong>of</strong> the impeller vanes at the impeller inlet can be determined<br />

easily from geometry and bulk flow considerations. Referring to Fig. 15(e),<br />

flow is approaching the impeller inlet at a velocity C. The impeller blade is<br />

moving as shown with a velocity U. The combination <strong>of</strong> these vectors<br />

produces the vector W, or the fluid inlet velocity vector as seen from a point<br />

on the impeller. The angle <strong>of</strong> the blade centerline is normally set to the<br />

expected angle <strong>of</strong> the W vector, to minimize the losses associated with<br />

negotiating the blade leading edge (referred to as incidence losses). It should<br />

be noted that if the pump must operate over a significant range <strong>of</strong> inlet flow<br />

Copyright © 2003 Marcel Dekker, Inc.

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