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Handbook of Turbomachinery Second Edition Revised - Ventech!

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point in the flow as the fraction <strong>of</strong> time in which the flow is turbulent at that<br />

point. Where the flow is all laminar g is 0 and where it is fully turbulent g is<br />

1.<br />

As turbulent spots in the boundary layer move down stream and<br />

coalesce into full turbulence, intermittancy can be used to scale (or weight)<br />

the values <strong>of</strong> quantities <strong>of</strong> interest through transition. The non-dimensional<br />

heat transfer coefficient, St, may be given in this manner. If the momentum<br />

thickness Reynolds number (Re y) <strong>of</strong> 162 is used as the start <strong>of</strong> transition<br />

(Kays and Crawford [11]), and intermittancy is expressed by Emmon’s<br />

relationship<br />

Where<br />

gðxÞ ¼1 exp½ nsðRex RextÞ 2 Š ð1Þ<br />

Rext is the x (surface distance) Reynolds number at the start <strong>of</strong><br />

transition.<br />

n and s are experimentally determined parameters.<br />

Then we can write the heat-transfer coefficient as<br />

StðxÞ ¼ð1 gÞStlam þ gStturb ð2Þ<br />

In other words, the Stanton number in the transition zone is a linear<br />

combination <strong>of</strong> the fully laminar and fully turbulent heat-transfer<br />

coefficients at the same surface distance.<br />

While this approach serves well to estimate how the heat transfer and<br />

other quantities change through the transition zone, designers must still find<br />

a method to predict the intermittancy values from transition onset to finish.<br />

Clark et al. [12] is an example <strong>of</strong> this approach.<br />

LOW-SPEED, LARGE-SCALE EXPERIMENTS<br />

Virtually all <strong>of</strong> the turbine experimental heat-transfer studies through the<br />

mid-1970s were done either in flat-plate wind tunnels or in cascades <strong>of</strong> vanes<br />

or blades. The study <strong>of</strong> three-dimensional flow in a turbine cascade by<br />

Langston et al. [13] is typical <strong>of</strong> many similar investigations.<br />

The flow in these facilities could be compressible but more <strong>of</strong>ten was<br />

not because <strong>of</strong> the expense involved. Further, earlier experiments were most<br />

<strong>of</strong>ten steady and run at relatively low temperature differences between the<br />

wall and mainstream gas. The large scale <strong>of</strong> these facilities allowed matching<br />

<strong>of</strong> the Reynolds numbers in the experiments to the design Reynolds<br />

numbers <strong>of</strong> actual machines. But, as mentioned, Mach numbers could rarely<br />

Copyright © 2003 Marcel Dekker, Inc.

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