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Untitled - Aerobib - Universidad Politécnica de Madrid

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2.2. DIFFUSION 39<br />

Hereinafter, notation in chapter 1 will be kept, adopting the vectorial and tensorial<br />

notation <strong>de</strong>fined in the Appendix to chapter 3.<br />

2.2 Diffusion<br />

Let ¯v i be the velocity of species A i at P . 4 ¯v i is generally different from velocity ¯v of<br />

the mixture. The difference ¯v di is called diffusion velocity of A i<br />

¯v di = ¯v i − ¯v. (2.2)<br />

The following relations exist between ¯v, ¯v i and ¯v di<br />

¯v = ∑ i<br />

Y i¯v i , (2.3)<br />

∑<br />

Y i¯v di = ¯0. (2.4)<br />

i<br />

Flux dm i of A i through dσ during time dt, when P moves at velocity ¯v of the<br />

mixture, is obviously<br />

dm i = ρ i¯v di · ¯n dσ dt. (2.5)<br />

The problem lies in calculating flux vector ¯f i ,<br />

¯f i = ρ i¯v di . (2.6)<br />

Let us first consi<strong>de</strong>r the case of a binary mixture formed by species A 1 and A 2 .<br />

The problem has been solved by Enskog [3] and Chapman [4]. The flux of A 1 is<br />

¯f 1 = ρY 1¯v d1 = −ρ M (<br />

1M 2<br />

Mm<br />

2 D 12 ∇X 1 − (Y 1 − X 1 ) ∇p )<br />

∇T<br />

− D T 1<br />

p T . (2.7)<br />

Here D 12 and D T 1 are, respectively, the coefficients of diffusion and thermal diffusion<br />

5 of the mixture. Flux ¯f 2 of A 2 is, from (2.4) and (2.6),<br />

¯f 2 = − ¯f 1 . (2.8)<br />

4¯v i is <strong>de</strong>fined as follows: taking a volume element dV around P and forming the mean value of velocities<br />

¯v i , of the molecules A i on it. Such value is ¯v i<br />

¯v i =<br />

1 X<br />

¯v j i<br />

N ,<br />

i<br />

where N i is the number of molecules of A i on dV . If dV is large respect to the molecular scale and<br />

small respect to the macroscopic scale, the value ¯v i thus <strong>de</strong>fined is in<strong>de</strong>pen<strong>de</strong>nt from size and shape of dV .<br />

Velocity ¯v of the mixture is, by <strong>de</strong>finition<br />

¯v = X i<br />

j<br />

Y i¯v i .<br />

5 The coefficient of thermal diffusion must not be confused with the thermal diffusivity, Ed.

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