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Untitled - Aerobib - Universidad Politécnica de Madrid

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292 CHAPTER 12. DIFFUSION FLAME<br />

Therefore m r i<br />

is given by<br />

∑<br />

m r i = Mi<br />

r ν ijr ′ j , (i = 1, 2, . . . , l r ). (12.14)<br />

j<br />

Likewise if m p i is the mass of species Ap i produced per unit surface and per<br />

unit time one has<br />

m p i = M p i<br />

∑<br />

j<br />

ν ′′<br />

ijr j , (i = l r + 1, l r + 2, . . . , l a ), (12.15)<br />

where l a = l r + l p is the number of active species (reactants plus products) and l p is<br />

the number of products.<br />

Reaction rates r j are unknown “a priori”. Elimination of the same between<br />

equations (12.14) and (12.15) gives l a −r relations between Yi<br />

r and Y p<br />

i which enables<br />

to express all mass fractions of active species as functions of r selected from them.<br />

Thus the variables of the problem reduce in l a − r.<br />

So far no solutions have been obtained for this general system of equations.<br />

In or<strong>de</strong>r to make computation available, additional assumptions must be introduced<br />

to simplify consi<strong>de</strong>rably the problem. Such simplifications will be performed in the<br />

following paragraph.<br />

12.4 Simplified equations<br />

In this approximate study the number of species is assumed to be three. Namely, fuel<br />

A 1 , oxidizer A 3 and products A 2 . Products inclu<strong>de</strong> not only species resulting from<br />

reactions, but also diluents of fuel and oxidizer initially mixed with them. 6 Flame surface<br />

divi<strong>de</strong>s space into two regions: an interior region at the fuel si<strong>de</strong> and an exterior<br />

one at the oxidizer si<strong>de</strong>. Only A 1 and A 2 species exist within the interior region. In<br />

the exterior one only A 2 and A 3 . Therefore, the composition of the mixture within the<br />

interior region is <strong>de</strong>termined by the value of Y 1 which must satisfy equation (12.2)<br />

ρ(¯v · ∇)Y 1 + ∇ · (ρY 1¯v d1 ) = 0. (12.16)<br />

Similarly in the exterior region one has for Y 3<br />

ρ(¯v · ∇)Y 3 + ∇ · (ρY 3¯v d3 ) = 0. (12.17)<br />

6 A larger number of species could easily be inclu<strong>de</strong>d by distinguishing, for example , between diluents<br />

and products. Such is done, among others, by Zeldovich [17] and Fay [15]. However, this does not represent<br />

any fundamental advantage and computations become more elaborate. A differentiation between products<br />

and diluent can be done once the problem is solved.

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