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Basics of Fluid Mechanics, 2014a

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9.3. NUSSELT’S TECHNIQUE 301<br />

boundary conditions are<br />

U x (y =0)<br />

U 0x<br />

= f(x)<br />

μ ∂U x<br />

∂x (y = h) =τ 0 g(x)<br />

Now it is very convenient to define several new variables:<br />

(9.22)<br />

U =<br />

where :<br />

U x(x)<br />

U 0x<br />

(9.23)<br />

x =<br />

x h<br />

y<br />

= y h<br />

The length h is chosen as the characteristic length since no other length is provided.<br />

It can be noticed that because the units consistency, the characteristic length can be<br />

used for “normalization” (see Example 9.11). Using these definitions the boundary and<br />

initial conditions becomes<br />

U x(y=0)<br />

U 0x<br />

= f ′ (x)<br />

hμ<br />

U 0x<br />

∂U x<br />

∂x (y =1)=τ 0 g ′ (x)<br />

(9.24)<br />

It commonly suggested to arrange the second part <strong>of</strong> equation (9.24) as<br />

∂U x<br />

∂x (y =1)=τ 0 U 0x<br />

hμ g′ (x) (9.25)<br />

Where new dimensionless parameter, the shear stress number is defined as<br />

τ 0 = τ 0 U 0x<br />

hμ<br />

(9.26)<br />

With the new definition equation (9.25) transformed into<br />

∂U x<br />

∂x (y =1)=τ 0 g ′ (x) (9.27)<br />

Example 9.11:<br />

Non–dimensionalize the following boundary condition. What are the units <strong>of</strong> the coefficient<br />

in front <strong>of</strong> the variables, x. What are relationship <strong>of</strong> the typical velocity, U 0 to<br />

U max ?<br />

(<br />

U x (y = h) =U 0 ax 2 + b exp(x) )<br />

(9.XI.a)

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