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

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Bibliographic revision<br />

Since n is a unit normal vector, we have:<br />

<br />

( )<br />

2<br />

∂n<br />

1 ∂n<br />

. n = = 0<br />

∂t<br />

2 ∂t<br />

<br />

∇ = ∇ ⎜ ⎟ = 0<br />

⎝ 2 ⎠<br />

2<br />

n<br />

W. n . n W.<br />

⎛ ⎞<br />

(2.12)<br />

(2.13)<br />

Therefore, the transport equation (2.11) can be written as follows:<br />

d<br />

dt<br />

∫<br />

<br />

dA = ⎡−n n : ∇ W +∇.<br />

W ⎤<br />

∫ ⎣<br />

⎦<br />

dA<br />

At ( ) At ( )<br />

(2.14)<br />

Note that in tensor notation, the first term of the right si<strong>de</strong> of the Eq. (2.14) can be<br />

written as:<br />

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

<br />

−nn:<br />

∇ W = −n n<br />

i<br />

j<br />

∂w<br />

∂x<br />

j<br />

i<br />

(2.15)<br />

If we consi<strong>de</strong>r a surface element, then A(t) can be substituted by δΑ. The f<strong>la</strong>me stretch<br />

rate κ can be expressed as:<br />

1 d( δ A)<br />

<br />

κ = = −nn: ∇ W +∇.<br />

W<br />

(2.16)<br />

δ A dt<br />

The general velocity W can be consi<strong>de</strong>red to have two components: one in the normal<br />

direction at a speed S u and the other is the local fluid velocity. Thus:<br />

<br />

W = S + S n<br />

u<br />

(2.17)<br />

Several vector operations can be applied to Eq. (2.17) to give:<br />

<br />

∇ W = ∇ S + Su<br />

∇ n+ n∇Su<br />

<br />

nn : ∇ W = nn : ∇ S + n∇Su<br />

<br />

∇ . W = ∇ . S + S ∇ . n+ n.<br />

∇S<br />

u<br />

u<br />

(2.18)<br />

(2.19)<br />

(2.20)<br />

Substituting these expressions in the Eq. (2.16), we have:<br />

1 d( δA)<br />

∂Si<br />

1 ∂ρ<br />

S<br />

κ = = −nn: ∇ S+∇ . S+ Su∇ . n = − ni nj<br />

+− +<br />

δA dt ∂x ρ ∂t r<br />

j<br />

u<br />

c<br />

(2.21)<br />

44

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