THESE de DOCTORAT - cerfacs
THESE de DOCTORAT - cerfacs
THESE de DOCTORAT - cerfacs
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88 Chapter 5: Assessment of combustion noise in a premixed swirled combustor<br />
u ′ i,LES = u′ i,hyd + u′ i,ac (5.6)<br />
Appling the operator ∂/∂t to Eq. (5.6) leads to<br />
∂u ′ i,LES<br />
∂t<br />
= ∂u′ i,hyd<br />
∂t<br />
+ ∂u′ i,ac<br />
∂t<br />
(5.7)<br />
From linear acoustics, the momentum equation is given by<br />
¯ρ ∂u′ i,ac<br />
∂t<br />
= − ∂p′ ac<br />
∂x i<br />
(5.8)<br />
where ¯[] and [] ′ represent respectively the mean and fluctuating flow. Combining Eq. (5.8) and<br />
Eq. (5.7) leads to<br />
− 1¯ρ<br />
∂p ′ ac<br />
∂x i<br />
+ ∂u′ i,hyd<br />
∂t<br />
= ∂u′ i,LES<br />
∂t<br />
(5.9)<br />
Finally the divergence operator to this equation is applied to yield<br />
− ∂ (<br />
∂p<br />
∂x i<br />
1¯ρ<br />
′ ) ( )<br />
ac<br />
+ ∂ ∂u<br />
′<br />
i,hyd<br />
= ∂2 u<br />
i,LES<br />
′<br />
∂x i ∂x i ∂t ∂x i ∂t<br />
(5.10)<br />
5.4.1 Finding ∂u i,hyd<br />
∂x i<br />
Neglecting viscosity, species diffusion and heat conduction, the Navier-Stokes equations for<br />
reacting flows read<br />
∂ρ<br />
∂t + ρ ∂u j<br />
∂x j<br />
+ u j<br />
∂ρ<br />
∂x j<br />
= 0 (5.11)<br />
ρ ∂u i<br />
∂t + ρu ∂u i<br />
j = − ∂p<br />
(5.12)<br />
∂x j ∂x i<br />
ρc p<br />
∂T<br />
∂t + ρc pu j<br />
∂T<br />
∂x j<br />
= ˙ω T (5.13)<br />
In the low-Mach number approximation, the thermodynamic pressure ¯p only <strong>de</strong>pends on tem-