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Untitled - Aerobib - Universidad Politécnica de Madrid

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12.3. BOUNDARY CONDITIONS ON THE FLAME 291<br />

The previous system together with the a<strong>de</strong>quate boundary conditions <strong>de</strong>termine<br />

the values for p, ρ, T , ¯v and for the mass fractions Y i at each point as well as the shape<br />

of the flame which so far is unknown.<br />

12.3 Boundary conditions on the flame<br />

Chemical species A i forming the mixture can be classified into three different groups:<br />

a) Reacting species A r i , which diffuses towards the flame where they burn. These<br />

species are unable to cross Σ f .<br />

b) Reaction products A p i , which produce at the flame and diffuse from it towards<br />

both si<strong>de</strong>s.<br />

c) Inert species A d i , which dilute reacting species. These species can cross Σ f .<br />

According to Burke and Schumann’s mo<strong>de</strong>l mass fractions Yi<br />

r<br />

species must be zero on the flame surface, that is<br />

of the reacting<br />

Y r<br />

1 = Y r<br />

2 = · · · = Y r<br />

l r<br />

= 0 (12.10)<br />

on Σ f , where l r is the number of reacting species. 5<br />

position of the flame surface.<br />

These conditions <strong>de</strong>termine the<br />

Let m r i be the mass of species Ar i that reaches Σ f per unit surface and per unit<br />

time. m r i is given by m r i = −ρY i¯v i · ¯n i , (12.11)<br />

where ¯n i is the unit vector normal to Σ f at A r i si<strong>de</strong>. mr i is consumed by the chemical<br />

reactions taking place at Σ f . Let<br />

∑<br />

ν ijA ′ r i → ∑ ν ijA ′′ p i , (j = 1, 2, . . . , r), (12.12)<br />

i<br />

i<br />

be one of these reactions, which transforms reacting species A r i into reaction products<br />

A p i . Since the thickness of the reaction zone is assumed to be zero, it becomes necessary<br />

to <strong>de</strong>fine a surface reaction rate for each reaction. Such rate gives the masses of<br />

the species consumed or produced by the reaction per unit surface and per unit time.<br />

Be r j the value of such surface reaction rate for reaction j. The fraction m r ij of mr i<br />

consumed by this reaction is<br />

where M r i is the molar mass of species Ar i .<br />

m r ij = M r i ν ′ ijr j , (j = 1, 2, . . . , r), (12.13)<br />

5 Actually, these mass fractions are very small but not strictly zero. Their values are practically those of<br />

the equilibrium of species un<strong>de</strong>r the prevailing conditions at the flame.

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