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Optimization and Computational Fluid Dynamics - Department of ...

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46 Gábor Janiga<br />

Temperature variations [K]<br />

50<br />

40<br />

30<br />

20<br />

10<br />

0<br />

0.006 0.007 0.008 0.009 0.01 0.011 0.012<br />

Average mass flow-rate <strong>of</strong> CO [g/s]<br />

Fig. 2.16 Feasible configurations for Case B. To improve clarity only a part <strong>of</strong> the results<br />

are shown here<br />

erable variations have been tested by the optimization procedure, exploring<br />

the whole parameter space before identifying the best solution. Such large<br />

variations would certainly not have been considered by a human being carrying<br />

out a manual optimization. The automatic optimization requires in this<br />

case a considerable computing time but leads to a reduction <strong>of</strong> the pollutant<br />

emission (CO) by a factor 2.5 <strong>and</strong> <strong>of</strong> the temperature variation by a factor<br />

exceeding 20, compared to the worst feasible configuration (Fig. 2.18).<br />

2.5 <strong>Optimization</strong> <strong>of</strong> the St<strong>and</strong>ard k–ω Turbulence<br />

Model Parameters (Case C)<br />

Numerical simulations based on RANS are widely used for engineering problems<br />

<strong>and</strong> complex geometries, due to a high computational efficiency. The<br />

determination <strong>of</strong> the closure constants for RANS turbulence models is based<br />

on dimensional analysis, theoretical observations or experiments for some<br />

special cases like channel or pipe flows. Such experiments <strong>of</strong>ten consider twodimensional<br />

flows, so that most model developments are originally suited for<br />

two-dimensional situations. Nevertheless, these models are mostly used in<br />

quite different – usually complex three-dimensional – configurations so that

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