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Basics of Fluid Mechanics, 2014a

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234 CHAPTER 8. DIFFERENTIAL ANALYSIS<br />

H 0<br />

T 0<br />

T 0 T(x)<br />

T∞<br />

x<br />

Fig. -8.4. Mass flow in coating process<br />

for example 8.2.<br />

The temperature and mass transfer taking<br />

place which reduces (or increases) the<br />

thickness <strong>of</strong> the film. For this example, assume<br />

that no mass transfer occurs or can<br />

be neglected and the main mechanism is<br />

heat transfer. Assume that the film temperature<br />

is only a function <strong>of</strong> the distance<br />

from the extraction point. Calculate the<br />

film velocity field if the density is a function<br />

<strong>of</strong> the temperature. The relationship between the density and the temperature is<br />

linear as<br />

( )<br />

ρ − ρ ∞ T − T∞<br />

= α<br />

(8.II.a)<br />

ρ 0 − ρ ∞ T 0 − T ∞<br />

State your assumptions.<br />

Solution<br />

This problem is somewhat similar to Example 8.1 6 , however it can be considered as<br />

steady state. At any point the governing equation in coordinate system that moving<br />

with the belt is<br />

∂ (ρU x )<br />

∂x<br />

+ ∂ (ρU y)<br />

∂y<br />

=0 (8.II.b)<br />

At first, it can be assumed that the material moves with the belt in the x direction<br />

in the same velocity. This assumption is consistent with the first solution (no stability<br />

issues). If the frame <strong>of</strong> reference was moving with the belt then there is only velocity<br />

component in the y direction 7 . Hence equation (8.II.b) can be written as<br />

∂ρ<br />

U x<br />

∂x = −∂ (ρU y)<br />

(8.II.c)<br />

∂y<br />

Where U x is the belt velocity.<br />

See the resembles to equation (8.I.b). The solution is similar to the previous<br />

Example 8.1 for a general function T = F (x).<br />

∂ρ<br />

∂x = α ∂F(x)<br />

U x ∂x (ρ 0 − ρ ∞ ) (8.II.d)<br />

Substituting this relationship in equation (8.II.d) into the governing equation results in<br />

∂U y ρ<br />

∂y<br />

= α U x<br />

∂F(x)<br />

∂x (ρ 0 − ρ ∞ ) (8.II.e)<br />

6 The presentation <strong>of</strong> one dimension time dependent problem to two dimensions problems can be<br />

traced to heat and mass transfer problems. One <strong>of</strong> the early pioneers who suggest this idea is Higbie<br />

which Higbie’s equation named after him. Higbie’s idea which was rejected by the scientific establishment.<br />

He spend the rest <strong>of</strong> his life to pro<strong>of</strong> it and ending in a suicide. On personal note, this author<br />

Master thesis is extension Higbie’s equation.<br />

7 In reality this assumption is correct only in a certain range. However, the discussion about this<br />

point is beyond the scope <strong>of</strong> this section.<br />

x

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