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Optimization and Computational Fluid Dynamics - Department of ...

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44 Gábor Janiga<br />

Air mass flow-rate in primary inlet [g/s]<br />

1.5<br />

1<br />

0.5<br />

0<br />

0.04 0.06 0.08<br />

Methane mass flow-rate in primary inlet [g/s]<br />

1.5 × 10 −2<br />

1.4 × 10 −2<br />

1.3 × 10 −2<br />

1.2 × 10 −2<br />

1.1 × 10 −2<br />

1.0 × 10 −2<br />

9.0 × 10 −3<br />

8.0 × 10 −3<br />

7.0 × 10 −3<br />

6.0 × 10 −3<br />

Fig. 2.14 Contour plot <strong>of</strong> the average mass fraction <strong>of</strong> CO (in g/s) as function <strong>of</strong> the<br />

input parameters<br />

Table 2.4 Parameters <strong>of</strong> the EA for the laminar burner optimization (Case B)<br />

Parameter Value<br />

Population size, N 20<br />

Generations 14<br />

Survival probability 10%<br />

Average probability 40%<br />

Crossover probability 50%<br />

Mutation probability 100%<br />

Mutation magnitude 50% a (i.e., ±25%)<br />

a This value is multiplied by 0.85 at each generation. For example, the mutation magnitude<br />

is 11.6% (±5.8%) after 10 generations. Mutation magnitude must be decreased during the<br />

optimization process to stabilize the population.<br />

figure shows again that both objectives improve roughly in the same direction<br />

in parameter space <strong>and</strong> converge to an almost identical optimal solution.<br />

Figure 2.16 does not contain any information on the corresponding input<br />

parameters. The relation between the input parameters <strong>and</strong> the objectives are<br />

demonstrated in Fig. 2.17 using parallel coordinates. In this figure, only good<br />

configurations are shown to improve readability. The optimal configurations<br />

correspond to two almost identical fully premixed <strong>and</strong> nearly stoichiometric<br />

0.1

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