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Untitled - Aerobib - Universidad Politécnica de Madrid

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164 CHAPTER 6. LAMINAR FLAMES<br />

which is the form that will be used is the following. In the equation it has been taken<br />

B j = A j<br />

( p<br />

R<br />

) nj<br />

. (6.113)<br />

As aforesaid said in chapter 3, §8, even when there exist l reaction equations (6.109)<br />

corresponding to i chemical species they are not all in<strong>de</strong>pen<strong>de</strong>nt from one another.<br />

In fact, the number of in<strong>de</strong>pen<strong>de</strong>nt equations is the smallest of the following two: 1)<br />

number of chemical reactions; 2) number of in<strong>de</strong>pen<strong>de</strong>nt components of the mixture,<br />

in the sense of the rule of phases.<br />

If we take (6.111.a) into (6.109), the latter may be written in the form<br />

m dε i<br />

dx =<br />

r∑<br />

j=1<br />

M i B j (ν ′′<br />

ij − ν ′ ij)T δj−nj e −E j/RT<br />

which is the form that will be used in the following.<br />

l ∏<br />

s=1<br />

X ν′ sj<br />

s , (6.109.a)<br />

Diffusion equations<br />

Since it is evi<strong>de</strong>nt that<br />

ρv = m, (6.114)<br />

equation (3.68) of Chap. 3 may be written<br />

ρY j v dj = m(ε j − Y j ), (j = 1, 2, . . . , l). (6.115)<br />

If we now take this expression of the diffusion velocities into the equations of system<br />

(3.75) (which in this case still holds if we nullify the term corresponding to pressure<br />

diffusion since it is neglectable), we shall obtain the <strong>de</strong>sired system of diffusion equations.<br />

However, when written in this form, the said system has the inconvenient that<br />

the <strong>de</strong>rivatives of the mass fractions dY j / dx do not appear explicit as it would be<br />

necessary in or<strong>de</strong>r to obtain the system of equations for the flame in the canonical<br />

form. Such an inconvenience can be easily avoi<strong>de</strong>d by simply expressing the result<br />

as a function of molar fractions X i in lieu of the mass fractions. In fact, in this case<br />

the system of diffusion equations to be used is the one given by Eq. (2.28), which<br />

after applied to the one-dimensional flow and neglecting the pressure and temperature<br />

diffusions takes the form<br />

dX i<br />

dx =<br />

l∑<br />

j=1<br />

X i X j<br />

D ij<br />

(v dj − v di ). (6.116)

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