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

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Chapter 2<br />

This is compatible with the assumption that the (mass averaged) burned temperature<br />

does not vary over time in this mo<strong>de</strong>l. O’Donovan and Rallis agree that this is a severe<br />

simplification, and suggest to measure the burned temperature at the centre of the<br />

bomb T b,c immediately after the start of <strong>combustion</strong> to evaluated T e /T b .<br />

- Lewis and von Elbe (1987)<br />

The most cited x(p) re<strong>la</strong>tion in literature equates the burnt mass fraction to the<br />

fractional pressure rise originally proposed by Lewis and von Elbe, (1987):<br />

p − pi<br />

x =<br />

p − p<br />

e<br />

i<br />

(2.66)<br />

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

Because its appealing simplicity and reasonable accuracy, the linear re<strong>la</strong>tion has been<br />

used a lot for obtaining <strong>la</strong>minar burning velocities. Dahoe et al., (1996) give a <strong>de</strong>rivation<br />

simi<strong>la</strong>r to the above, but immediately start from the linear re<strong>la</strong>tion (2.66). Eq. (2.62)<br />

then turns into<br />

2<br />

1 3<br />

⎡<br />

⎤<br />

dp 3( p ) u<br />

e<br />

−pi ⎛ pi<br />

⎞γ<br />

( pe<br />

−p)<br />

⎛ p ⎞<br />

= ⎢1− ⎥<br />

dt R ⎢ ⎜ ⎟<br />

⎜ ⎟<br />

⎝ p ⎠ ( pe − pi)<br />

⎥<br />

⎝pi<br />

⎢<br />

⎥<br />

⎠<br />

⎣<br />

⎦<br />

1<br />

γu<br />

S<br />

u<br />

(2.67)<br />

- Nagy et al., (1969)<br />

Nagy et al., (1969) assume isentropic compression of the burned mixture and have<br />

used the following x(p) expression:<br />

p − p<br />

xp ( ) =<br />

p p p<br />

1/ γu<br />

1/ γu<br />

i<br />

1/ γ b (1/ γu−1/ γb) 1/ γu<br />

e<br />

−<br />

i<br />

(2.68)<br />

- Luijten et al., (2009)<br />

Luijten et al. proposed an exten<strong>de</strong>d linear analytical two-zone mo<strong>de</strong>l, where both the<br />

burned and unburned zones have uniform temperatures and compositions.<br />

Conservation of specific volume v and internal energy e is expressed by<br />

v = xv + ( 1− x)<br />

v<br />

(2.69)<br />

t b u<br />

e = xe + ( 1− x)<br />

e<br />

(2.70)<br />

t b u<br />

55

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