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

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Chapter 4<br />

P i = 1.0 bar, Ti = 293 K, φ=0.6<br />

Time (ms) 5.0 6.0 7.0 8.0 9.0 10.0 11.0 12.0 13.0 14.0 15.0<br />

Radius (mm) 6.4 7.4 8.5 9.4 10.5 11.5 12.4 13.3 14.2 15.1 15.9<br />

16.0 17.0 18.0 19.0 20.0<br />

16.7 17.6 18.5 19.3 20.1<br />

P i = 1.0 bar, Ti = 293 K, φ=0.8<br />

Time (ms) 3.5 4.5 5.5 6.5 7.5 8.5 9.5 10.5 11.5 12.5 13.5<br />

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

Radius (mm) 6.0 7.6 9.2 10.8 12.4 13.9 15.5 17.0 18.4 19.7 21.0<br />

P i = 1.0 bar, T i = 293 K, φ=1.0<br />

Time (ms) 4.0 5.0 6.0 7.0 8.0 9.0 10.0 11.0<br />

Radius (mm) 6.6 8.7 10.9 13.0 15.0 17.1 19.1 21.0<br />

P i = 1.0 bar, Ti = 293 K, φ=1.2<br />

Time (ms) 4.0 5.0 6.0 7.0 8.0 9.0 10.0 11.0<br />

Radius (mm) 6.4 8.5 10.4 12.5 14.5 16.6 18.6 20.5<br />

Figure 4.3 - Schlieren images of downdraft syngas-air mixture f<strong>la</strong>mes at 1.0 bar.<br />

2.5<br />

1.4<br />

Sn<br />

2.2<br />

P<br />

1.3<br />

Sn (m/s)<br />

1.9<br />

1.6<br />

1.3<br />

1.2<br />

1.1<br />

Pressure (bar)<br />

1.0<br />

0 5 10 15 20 25 30 35<br />

Radius (mm)<br />

1.0<br />

Figure 4.4- F<strong>la</strong>me speed and pressure versus radius for stoichiometric downdraft syngas-air<br />

mixture at 1.0 bar.<br />

91

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