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Untitled - Aerobib - Universidad Politécnica de Madrid

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146 CHAPTER 6. LAMINAR FLAMES<br />

In this expression, n is the or<strong>de</strong>r of reaction and k a function of temperature, which,<br />

generally, is of the form<br />

k = A<br />

( T<br />

T f<br />

) δ<br />

e −E/RT , (6.56)<br />

where A is a constant and E is the activation energy of the reaction.<br />

It is convenient to eliminate the <strong>de</strong>nsity from Eq. (6.55) so that only two variables<br />

appear explicitly: the temperature and the mass fraction of products.<br />

Let M r and M p be the molar masses of reactants and products, respectively,<br />

and a the relation<br />

Then, the mean molar mass of the mixture is 4<br />

a = M r<br />

M p<br />

− 1. (6.57)<br />

M =<br />

M r<br />

1 + aY , (6.58)<br />

and the <strong>de</strong>nsity of the mixture may be expressed as a function of pressure and temperature<br />

in the form<br />

By taking now Eq. (6.56) and (6.59) into (6.55), we finally obtain for the reaction<br />

velocity<br />

ρ = pM r<br />

RT<br />

1<br />

1 + aY . (6.59)<br />

w = A<br />

( ) n ( ) n ( ) δ pMr 1 − Y T<br />

e −E/RT . (6.60)<br />

RT 1 + aY T f<br />

It is advantageous to bring forth in Eq. (6.60) the dimensionless temperature θ =<br />

T/T f as <strong>de</strong>fined in the preceding paragraph, and to introduce dimensionless activation<br />

temperature θ a as <strong>de</strong>fined by<br />

Now, Eq. (6.60) may be written<br />

θ a =<br />

E<br />

RT f<br />

. (6.61)<br />

( ) n 1 − Y<br />

w = Bθ δ−n e −θ a/θ , (6.62)<br />

1 + aY<br />

where<br />

( ) n pMr<br />

B = A<br />

(6.63)<br />

RT f<br />

is a constant of the process. Eq. (6.62) is the form of the reaction velocity that will be<br />

used in the following.<br />

4 See Chap. 1, Eq. (1.36).

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