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Handbook of Turbomachinery Second Edition Revised - Ventech!

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available to explore fully viscous solutions <strong>of</strong> the 3D Navier–Stokes<br />

equations in reasonable times. Because external surface heat transfer is<br />

essentially driven by the main stream flow conditions (through the structure<br />

<strong>of</strong> the intervening boundary layer), standard heat-transfer correlations<br />

could be used along the predicted streamlines to compute the heat transfer<br />

to the surface.<br />

Wu’s method was ‘‘packaged’’ and improved by researchers at what is<br />

now the USA’s NASA/Glenn Research Center as the well-known computer<br />

codes MERIDL and TSONIC [3, 4]. These codes are still used in many CFD<br />

calculations, for example, to quickly generate an approximate starting<br />

solution for more complex and time-consuming Navier–Stokes numerical<br />

solutions. A major drawback <strong>of</strong> Wu’s Quasi-3D method is that it is only<br />

approximate (by design, <strong>of</strong> course). The procedure also requires much<br />

human intervention and application <strong>of</strong> design experience during the iterative<br />

solution process to obtain the most useful results. Researchers therefore<br />

continued to look for both faster and more accurate methods, particularly<br />

those that incorporate viscosity and other effects naturally.<br />

The first major step for including viscosity became available in the late<br />

1960s and early 1970s through numerical analysis <strong>of</strong> flow-path boundary<br />

layers. The publication that started much <strong>of</strong> the work was by Patankar and<br />

Spalding [5] in which the authors numerically solved the 2D, steady<br />

boundary-layer equations (simplified forms <strong>of</strong> the Navier–Stokes equations)<br />

using a scaled coordinate system that adapts to the boundary-layer<br />

thickness as it grows downstream. The boundary-layer differential<br />

equations are <strong>of</strong> the parabolic type; thus only the values <strong>of</strong> the upstream<br />

independent variables are needed to solve for the downstream values.<br />

Variation in the solution is wholly determined by the variations in the free<br />

stream and the solid surface over which the fluid flows. This technique<br />

formed the vehicle for many, many studies <strong>of</strong> skin friction drag and heat<br />

transfer, for attached boundary layers. Patankar–Spalding also became the<br />

workhorse numerical technique for many studies <strong>of</strong> boundary-layer<br />

turbulence that popularized the k-e turbulence model [6] and others.<br />

Parabolic boundary-layer solvers using the Patankar–Spalding procedure<br />

were written by NASA and others under the names <strong>of</strong> STAN5 [7] and<br />

TEXSTAN [8]. Many others were developed in academia and industry.<br />

These codes were used with the TSONIC/MERDIL passage-flow solvers to<br />

give a technique fast and robust enough for design work but with greater<br />

accuracy than the part-calculation, part-correlation techniques used<br />

previously. Separation still had to be dealt with empirically because <strong>of</strong> the<br />

inability <strong>of</strong> the parabolic equations to be solved under conditions favoring<br />

separation, i.e., strong adverse pressure gradients. The transition starting<br />

point and transition lengths also need empirical expressions for their<br />

Copyright © 2003 Marcel Dekker, Inc.

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