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Untitled - Aerobib - Universidad Politécnica de Madrid

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10.3. METHOD OF FABRI-SIESTRUNCK-FOURÉ 255<br />

10.3 Method of Fabri-Siestrunck-Fouré<br />

The flow in the combustion chamber is two dimensional and stationary. Therefore, a<br />

stream function ψ exists. This function is <strong>de</strong>fined by the following relations<br />

ρu =ρ 0 u 0 h ∂ψ<br />

∂y , (10.18)<br />

ρv =ρ 0 u 0 h ∂ψ<br />

∂x . (10.19)<br />

Thus <strong>de</strong>fined, ψ is non-dimensional.<br />

The x axis is a streamline to which the value ψ = 0 is assigned. The upper<br />

wall of the chamber, y = h, is also a streamline for which ψ = 1, as results from the<br />

integration of (10.18). Therefore, in the upper half of the chamber, ψ varies from the<br />

value zero, at the axis, to the value one, at the wall.<br />

A linearization of the problem, by assuming that all velocities are small compared<br />

to u, leads to the conclusion that pressure is constant at each cross section of<br />

the chamber. Therefore, since the flow of unburnt gases is isentropic, their <strong>de</strong>nsity,<br />

temperature and velocities are equally constant at each cross section. Moreover, the<br />

value of either one of these magnitu<strong>de</strong>s <strong>de</strong>termines the values for the others.<br />

ψ<br />

ψ’<br />

D u’<br />

ρ<br />

1<br />

B<br />

C<br />

ρ’’<br />

E<br />

u<br />

u’’<br />

ψ<br />

ψ’<br />

0<br />

x<br />

A<br />

Figure 10.9: Notation for the method of Fabri-Siestrunck-Fouré.<br />

Let us consi<strong>de</strong>r a cross section AB, at a distance x from the stabilizer, as shown<br />

in Fig. 10.9. Here, evi<strong>de</strong>ntly<br />

∫<br />

1 h<br />

dy = 1, (10.20)<br />

h 0<br />

which, by virtue of (10.18), can be written in the following form<br />

∫ 1<br />

0<br />

ρ 0 u 0<br />

ρu<br />

dψ = 1. (10.21)

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