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simulation numerique de la combustion diphasique - cerfacs

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2<br />

Masse volumique (kg.m -3 )<br />

4<br />

Vitesse (m.s -1 )<br />

1.5<br />

3<br />

1<br />

2<br />

0.5<br />

1<br />

101350<br />

0<br />

-0.01 -0.005 0 0.005 0.01<br />

x (m)<br />

Pression (Pa)<br />

3000<br />

0<br />

-0.01 -0.005 0 0.005 0.01<br />

x (m)<br />

Temperature (K)<br />

101345<br />

101340<br />

101335<br />

101330<br />

101325<br />

2500<br />

2000<br />

1500<br />

1000<br />

500<br />

101320<br />

-0.01 -0.005 0 0.005 0.01<br />

x (m)<br />

5e+09<br />

Degagement <strong>de</strong> chaleur (J.m -3 .s -1 )<br />

4000<br />

0<br />

-0.01 -0.005 0 0.005 0.01<br />

x (m)<br />

Taux <strong>de</strong> reaction (mol.m -3 .s -1 )<br />

4e+09<br />

3e+09<br />

2e+09<br />

1e+09<br />

3000<br />

2000<br />

1000<br />

0<br />

-0.01 -0.005 0 0.005 0.01<br />

x (m)<br />

0<br />

-0.01 -0.005 0 0.005 0.01<br />

x (m)<br />

Fig. B.1 – Comparaison <strong>de</strong>s profils spatiaux <strong>de</strong>s variables <strong>de</strong> <strong>la</strong> f<strong>la</strong>mme prémé<strong>la</strong>ngée d’éthanol<br />

obtenus par PREMIX et AVBP (Schéma Lax-Wendroff).<br />

60

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