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Handbook of Turbomachinery Second Edition Revised - Ventech!

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alternative frequently employed. If the relative angle <strong>of</strong> the flow leaving an<br />

impeller were parallel to the impeller blades at the trailing edge, the absolute<br />

value <strong>of</strong> the tangential component <strong>of</strong> the exit velocity would be Vy;i. The<br />

ratio <strong>of</strong> Vy;2, the tangential velocity actually realized, to Vy;i is called the slip<br />

factor. Various formulas for estimating slip factor have been published, but<br />

most are unreliable. Most <strong>of</strong> the values were deduced by measuring the<br />

temperature rise in the impeller and calculating the value <strong>of</strong> DH and the<br />

value <strong>of</strong> Vy;2 by using Eq. (7). In nearly all impellers, however, some flow is<br />

recirculated between stations somewhere between the inlet and discharge.<br />

The actual value <strong>of</strong> Vy;2 is lower than that calculated. In fact, slip factors<br />

greater than unity have been reported, and this is absurd. A practical<br />

solution is to estimate the slip factor by Eq. (22), and then increase the<br />

impeller diameter by about 5%. The impeller tip is gradually cut back to the<br />

proper value during development testing. Chapter 4 <strong>of</strong> Balje [19] has a good<br />

discussion about slip factor. One <strong>of</strong> the equations noted there is<br />

Slip factor ¼ 1 ð3sinb b;2Þ=Z ð22Þ<br />

STATORS OR DIFFUSERS<br />

Four types <strong>of</strong> stators or diffusers have been used. They have been designated<br />

as vaneless, vane island, cascade, and pipe diffusers. Most <strong>of</strong>ten, nearly all<br />

the diffusion takes place while the gas velocity has a significant radial<br />

component. The flow then is usually either turned to the axial direction, as<br />

shown in Figs. 1–4, or collected by ascroll, which changes the flow direction<br />

to a tangential one. Chapter 6 <strong>of</strong> Balje [19] reviews the design <strong>of</strong> scrolls.<br />

Vaneless Diffusers<br />

These diffusers are rarely used in industry except when some efficiency can<br />

be sacrificed to reduce manufacturing costs, when size is not a criterion, or if<br />

a wide range <strong>of</strong> flow rates between the maximum flow and surge is<br />

mandatory. Scrolls are generally used with these diffusers. Chapter 6 <strong>of</strong><br />

Balje [19] reviews the design <strong>of</strong> these diffusers. As previously noted,<br />

deceleration <strong>of</strong> the tangential component <strong>of</strong> velocity leaving the impeller is<br />

automatically accomplished as the radius <strong>of</strong> the flow increases. Deceleration<br />

<strong>of</strong> the radial and axial components, which is controlled by the space between<br />

the two walls, must be kept small.<br />

Short, vaneless diffusers also <strong>of</strong>fer a cost-effective way to execute part<br />

<strong>of</strong> the development testing <strong>of</strong> centrifugal and mixed-flow compressors. The<br />

Copyright © 2003 Marcel Dekker, Inc.

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