Etude de la combustion de gaz de synthèse issus d'un processus de ...
Etude de la combustion de gaz de synthèse issus d'un processus de ... Etude de la combustion de gaz de synthèse issus d'un processus de ...
Experimental and numerical laminar syngas combustion conditions. Figures 4.40 – 4.42 shows experimental and numerical pressure and the heat flux for updraft syngas-air mixture at φ=0.8, φ=1.0 and φ=1.2, respectively. Pressure (bar) 7 6 5 4 3 2 1 Experimental P Numerical P Qw 500 400 300 200 100 Qw (kW/m 2 ) tel-00623090, version 1 - 13 Sep 2011 0 0 10 20 30 40 50 60 70 80 90 100 Time (ms) Figure 4.40 – Pressure and heat flux for updraft syngas-air at φ=0.8, P=1.0 bar, T= 293 K. Pressure (bar) 7 6 5 4 3 2 1 0 Experimental P Numerical P Qw 0 10 20 30 40 50 60 70 80 90 100 Time (ms) 0 500 400 300 200 100 0 Qw (kW/m 2 ) Figure 4.41– Pressure and heat flux for updraft syngas-air at φ=1.0, P=1.0 bar, T= 293 K. 130
Chapter 4 7 500 Pressure (bar) 6 5 4 3 2 1 Experimental P Numerical P Qw 400 300 200 100 Qw (kW/m 2 ) 0 0 10 20 30 40 50 60 70 80 90 100 Time (ms) 0 Figure 4.42 – Pressure and heat flux for updraft syngas-air at φ=1.2, P=1.0 bar, T= 293 K. tel-00623090, version 1 - 13 Sep 2011 From figures 4.40-4.42 one can conclude that pressure evolution of updraft syngas-air mixtures is accurately reproduced by the code for each equivalence ratio. However, pressure peak is always higher than the experimental measurement as well as in the cooling phase. It was found important chamber leakages at this stage, and so the chamber was repaired. The following results were obtained after the reparation. Figures 4.43 - 4.45 shows experimental and numerical pressure and the heat flux for downdraft syngas-air mixture at φ=0.8, φ=1.0 and φ=1.2, respectively. Pressure (bar) 7 6 5 4 3 2 1 500 Experimental P Numerical P 400 Qw 300 200 100 Qw (kW/m 2 ) 0 0 10 20 30 40 50 60 70 80 90 100 Time (ms) 0 Figure 4.43 – Pressure and heat flux for downdraft syngas-air at φ=0.8, P=1.0 bar, T= 293 K. 131
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Chapter 4<br />
7<br />
500<br />
Pressure (bar)<br />
6<br />
5<br />
4<br />
3<br />
2<br />
1<br />
Experimental P<br />
Numerical P<br />
Qw<br />
400<br />
300<br />
200<br />
100<br />
Qw (kW/m 2 )<br />
0<br />
0 10 20 30 40 50 60 70 80 90 100<br />
Time (ms)<br />
0<br />
Figure 4.42 – Pressure and heat flux for updraft syngas-air at φ=1.2, P=1.0 bar, T= 293 K.<br />
tel-00623090, version 1 - 13 Sep 2011<br />
From figures 4.40-4.42 one can conclu<strong>de</strong> that pressure evolution of updraft syngas-air<br />
mixtures is accurately reproduced by the co<strong>de</strong> for each equivalence ratio. However,<br />
pressure peak is always higher than the experimental measurement as well as in the<br />
cooling phase. It was found important chamber leakages at this stage, and so the<br />
chamber was repaired. The following results were obtained after the reparation.<br />
Figures 4.43 - 4.45 shows experimental and numerical pressure and the heat flux for<br />
downdraft syngas-air mixture at φ=0.8, φ=1.0 and φ=1.2, respectively.<br />
Pressure (bar)<br />
7<br />
6<br />
5<br />
4<br />
3<br />
2<br />
1<br />
500<br />
Experimental P<br />
Numerical P<br />
400<br />
Qw<br />
300<br />
200<br />
100<br />
Qw (kW/m 2 )<br />
0<br />
0 10 20 30 40 50 60 70 80 90 100<br />
Time (ms)<br />
0<br />
Figure 4.43 – Pressure and heat flux for downdraft syngas-air at φ=0.8, P=1.0 bar, T= 293 K.<br />
131