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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 />

1.4<br />

1.2<br />

Su/S 0 u<br />

1.0<br />

0.8<br />

φ<br />

1.0<br />

0.8<br />

0.6<br />

0.00 0.05 0.10 0.15 0.20 0.25 0.30<br />

Karlovitz number<br />

Figure 4.22 – Evolution of the <strong>la</strong>minar burning velocity versus Karlovitz number for fluidized bed<br />

syngas-air mixture at different equivalence ratios and 1.0 bar.<br />

The linear behavior of the normalized burning velocity with Karlovitz number supports<br />

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

that the Markstein number is in<strong>de</strong>pen<strong>de</strong>nt of the Karlovitz number as it was verified by<br />

Aung et al. (1997). Also the generally low Karlovitz numbers obtained for all the typical<br />

syngas compositions and equivalence ratios indicates small influence of stretch rate on<br />

the syngas-air f<strong>la</strong>mes.<br />

As it was pointed out by Aung at al., (1997) and Bradley et al., (1996) the Markstein<br />

length is a fundamental property of premixed <strong>la</strong>minar f<strong>la</strong>mes and it is necessary to<br />

measure it precisely. Table 4.2 shows Markstein lengths and Markstein numbers for<br />

syngas-air mixture at various equivalence ratios. If Ma0, It is in the stable regime (Law,<br />

2006). If Ma=0, the f<strong>la</strong>me is neutrally stable, and S u = S 0 u<br />

at all values of stretch rate.<br />

Table 4.2– Markstein lengths and Markstein numbers versus equivalence ratio of syngas-air<br />

mixtures at 1.0 bar and 293 K.<br />

Eq.<br />

Updraft Downdraft Fluidized bed<br />

Ratio L b L u Ma L b L u Ma L b L u Ma<br />

φ=0.6 -2×10 -3 -4.1×10 -4 -1.55 -9×10 -4 -1.9×10 -4 -1.4 n.d. n.d. n.d.<br />

φ=0.8 -7×10 -4 -1.3×10 -4 -1.21 -4×10 -4 -7.4×10 -5 -0.84 -4×10 -4 -7.5×10 -5 -0.5<br />

φ=1.0 -7×10 -4 -1.2×10 -4 -1.39 -5×10 -4 -8.7×10 -5 -1.17 8×10 -4 1.4×10 -4 1.18<br />

φ=1.2 -5×10 -4 -8.9×10 -5 -0.90 -4×10 -4 -7.4×10 -5 -0.94 n.d. n.d. n.d.<br />

Updraft and downdraft syngas shows to be in the preferential diffusion instability<br />

regime as the Markstein number is negative for all cases. The f<strong>la</strong>me can be seen to be<br />

neutrally stable for fluidized bed syngas somewhat between φ=0.8 and φ =1.0 as the<br />

Markstein number changes from a negative to a positive value.<br />

108

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