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x1/B<br />

0.3 0.5 0.8 1.0<br />

9 Pollutant Dispersion in Flow Around Bluff-Bodies Arrangement 51<br />

a<br />

0.5 1.5 2.5 3.0<br />

−1.5 −1.0 −0.5 0.0 0.5 1.0 1.5 −1.5 −1.0 −0.5 0.0 0.5 1.0 1.5 −1.5 −1.0 −0.5 0.0 0.5 1.0 1.5<br />

x2/B x2 /B<br />

x2/B<br />

Fig. 9.2. Isolines of mean concentration in the inter-obstacle gap a) S/B = 2,<br />

b) S/B =4,c)S/B =6<br />

C k[%]<br />

0.9<br />

0.8<br />

0.7<br />

0.6<br />

0.5<br />

0.4<br />

0.3<br />

0.2<br />

0.1<br />

0.0<br />

−2 −1<br />

0<br />

x 2/B<br />

b<br />

1.0 2.0 3.0 4.0 5.0<br />

1<br />

s/B = 6<br />

s/B = 4<br />

s/B = 2<br />

x1/B = 1<br />

Fig. 9.3. Mean concentration profiles for various inter-obstacle gap width<br />

case concentration peaks are distinctly moving towards the flow axis and for<br />

the distances x1/B > 0.75 maximum values of mean concentration are in the<br />

centreline of the wake. The region of higher CO2 concentration is noticeable<br />

in the whole inter-obstacle gap.<br />

Mean concentration profiles for various inter-obstacle gaps and for the<br />

same position of x1/B = 1 behind the upstream cylinder are presented in the<br />

Fig. 9.3. As one can notice, in the case of S/B =2andS/B = 6 maximum<br />

values of mean concentration are outside of the gap region, while for the gap<br />

width S/B = 4 maximum value of mean concentration is in the centreline<br />

of the wake. Computational profiles of the mean velocity components and<br />

numerical distribution of turbulence energy for the same cross section (x1/B =<br />

1) were used to find explanation. It was revealed that velocity distributions<br />

are similar so the question arises why the concentration profiles are different.<br />

To find an explanation the results of computational modelling of velocity<br />

field performed by Gnatowska & Jar˙za [1] have been used. The numerical<br />

2<br />

c<br />

2.60<br />

2.49<br />

2.38<br />

2.27<br />

2.16<br />

2.05<br />

1.94<br />

1.83<br />

1.72<br />

1.61<br />

1.50

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