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Basics of Fluid Mechanics, 2014a

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8.2. MASS CONSERVATION 233<br />

Equation (8.I.e) is first order ODE with the boundary condition U y (y =0)=0which<br />

can be arranged as<br />

(<br />

∂ U y α H (<br />

0−y<br />

))<br />

H 0<br />

1 − e<br />

−βt<br />

∂y<br />

= −αβ<br />

( )<br />

H0 − y<br />

e −βt<br />

H 0<br />

(8.I.f)<br />

U y is a function <strong>of</strong> the time but not y. Equation (8.I.f) holds for any time and thus, it<br />

can be treated for the solution <strong>of</strong> equation (8.I.f) as a constant 5 . Hence, the integration<br />

with respect to y yields<br />

(<br />

U y α H 0 − y (<br />

1 − e<br />

−βt )) ( ) 2 H0 − y<br />

= −αβ<br />

e −βt y + c (8.I.g)<br />

H 0<br />

2 H 0<br />

Utilizing the boundary condition U y (y =0)=0yields<br />

(<br />

U y α H 0 − y (<br />

1 − e<br />

−βt )) ( ) 2 H0 − y<br />

= −αβ<br />

e −βt (y − 1)<br />

H 0<br />

2 H 0<br />

(8.I.h)<br />

or the velocity is<br />

U y = β<br />

( )<br />

2 H0 − y e −βt<br />

2(H 0 − y) (1 − e −βt (1 − y) (8.I.i)<br />

)<br />

It can be noticed that indeed the velocity is a function <strong>of</strong> the time and space y.<br />

End Solution<br />

8.2.2 Simplified Continuity Equation<br />

A simplified equation can be obtained for a steady state in which the transient term is<br />

eliminated as (in a vector form)<br />

∇ · (ρU) =0 (8.19)<br />

If the fluid is incompressible then the governing equation is a volume conservation as<br />

∇ · U =0 (8.20)<br />

Note that this equation appropriate only for a single phase case.<br />

Example 8.2:<br />

In many coating processes a thin film is created by a continuous process in which liquid<br />

injected into a moving belt which carries the material out as exhibited in Figure 8.4.<br />

5 Since the time can be treated as a constant for y integration.

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