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Untitled - Aerobib - Universidad Politécnica de Madrid

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2.2. DIFFUSION 47<br />

coefficients. 14 The values of k T are generally small. Normally they do not exceed 0.1.<br />

Thereby thermal diffusion is of secondary importance in Aerothermochemistry and its<br />

influence is, usually, disregar<strong>de</strong>d.<br />

In Refs. [8], [9], [10] and [11] recent information on theoretical and experimental<br />

values of transport coefficients can be found.<br />

For mixtures containing more than two components, the problem has been<br />

solved by Curtiss and Hirschfel<strong>de</strong>r [2], [12]. In such case, the aforementioned three<br />

causes of diffusion, namely, differences in composition, pressure and temperature, still<br />

hold. Yet in this case diffusion flux of each species <strong>de</strong>pends not only on the gradient<br />

of its molar fraction but is a linear function of the gradients of all molar fractions.<br />

Diffusion flux ¯f i of species A i (i = 1, 2, . . . , l) is<br />

¯f i = ρY i¯v di = ρ M i<br />

M 2 m<br />

∑<br />

M j D ij<br />

′<br />

j≠i<br />

(<br />

∇X j + (X j − Y j ) ∇p<br />

p<br />

)<br />

− D T i<br />

∇T<br />

T . (2.26)<br />

Here D ′ ij is the diffusion coefficient of species A i and A j in the mixture. For a binary<br />

mixture, D ′ ij is diffusion coefficient D ij previously <strong>de</strong>fined. For the case of more than<br />

two components it differs. D T i is the thermal diffusion coefficient of species A i in<br />

the mixture.<br />

The l equations (2.26) are not in<strong>de</strong>pen<strong>de</strong>nt from each other. In fact, diffusion<br />

fluxes of l species must satisfy the condition<br />

∑<br />

¯f i = ¯0. (2.27)<br />

i<br />

Diffusion coefficients D ij ′ in system (2.26) can be expressed as a function of<br />

binary diffusion coefficients D ij of the species taken in couples. Ref. [2], pp. 541<br />

and 543, and Ref. [12] contain expressions for these coefficients as well as for those<br />

of thermal diffusion. Expressions for D ′ ij and D T i are too complicated for practical<br />

computations. Then it is advantageous to eliminate D ij ′ by substituting system (2.26)<br />

with the following that makes explicit the influence of binary diffusion coefficients 15<br />

∑ X i X j<br />

(¯v dj − ¯v di ) =∇X i + (X i − Y i ) ∇p<br />

D ij<br />

p<br />

j≠i<br />

− ∑ (<br />

X i X j DT j<br />

− D ) (2.28)<br />

T i ∇T<br />

ρD ij Y j Y i T . j≠i<br />

As was done for the case of binary diffusion, it is also convenient to eliminate<br />

molar fractions of the species by introducing their corresponding mass fractions.<br />

14 A critical study on the subject will be found in Ref. [6], p. 492 and following, as well as bibliography.<br />

15 See Ref. [2]. p. 517.

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