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Etude de la combustion de gaz de synthèse issus d'un processus de ...

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Experimental and numerical <strong>la</strong>minar syngas <strong>combustion</strong><br />

40<br />

1000<br />

Pressure (bar)<br />

30<br />

20<br />

10<br />

Experimental P<br />

Numerical P<br />

Qw<br />

800<br />

600<br />

400<br />

200<br />

Qw (kW/m 2 )<br />

0<br />

0 30 60 90 120 150<br />

Time (ms)<br />

0<br />

Figure 4.48 – Pressure and heat flux for updraft syngas-air at 5.0 bar and 293 K.<br />

tel-00623090, version 1 - 13 Sep 2011<br />

Pressure (bar)<br />

40<br />

30<br />

20<br />

10<br />

0<br />

Experimental P<br />

Numerical P<br />

Qw<br />

0 10 20 30 40 50 60 70 80 90 100<br />

Time (ms)<br />

1000<br />

800<br />

600<br />

400<br />

200<br />

0<br />

Qw (kW/m 2 )<br />

Figure 4.49 – Pressure and heat flux for downdraft syngas-air at 5.0 bar and 293 K.<br />

As reported in 4.1.1.1 cellu<strong>la</strong>r f<strong>la</strong>me are present in syngas-air f<strong>la</strong>mes for initial<br />

pressures higher than 2.0 bar. Therefore, pressure curves of 5.0 bar are not perfectly<br />

spherical, which makes the f<strong>la</strong>me to reach the wall non-uniformly. Thus, the heat flux<br />

peak is not synchronized in the entire chamber surface, which exp<strong>la</strong>ins that the<br />

pressure peak is reached after some re<strong>la</strong>xation. This behavior was also observed by<br />

Boust, (2006) when <strong>de</strong>aling with lean (φ=0.7) methane-air mixtures.<br />

Notice that the co<strong>de</strong> reproduces well the pressure evolution beyond the validity of the<br />

burning velocity corre<strong>la</strong>tion established in 4.1.2.3 for updraft and downdraft syngas<br />

compositions. For these syngas compositions, the experimental corre<strong>la</strong>tion is valid up<br />

to 20 bar, however we show numerically that value could be used beyond 33 bar.<br />

134

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