13.02.2013 Views

Mechanics of Fluids

Mechanics of Fluids

Mechanics of Fluids

SHOW MORE
SHOW LESS

Create successful ePaper yourself

Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.

316 Boundary layers, wakes and other shear layers<br />

To sum up, the principal characteristics <strong>of</strong> the turbulent boundary layer<br />

on a flat plate with zero pressure gradient and moderate Reynolds number<br />

are these:<br />

1. The thickness <strong>of</strong> the boundary layer increases approximately as the 4 5<br />

power <strong>of</strong> the distance from the leading edge (compared with the power<br />

1<br />

2 for a laminar layer).<br />

2. The shear stress τ0 at the boundary is approximately inversely proportional<br />

to the fifth root <strong>of</strong> the local Reynolds number (compared with the<br />

square root for a laminar layer).<br />

3. The total friction drag is approximately proportional to 9 5 power <strong>of</strong> the<br />

velocity <strong>of</strong> the main flow and 4 3<br />

5 power <strong>of</strong> the length (compared with 2<br />

and 1<br />

2 powers respectively for the laminar layer).<br />

Example 8.5 A train is 100 m long, 2.8 m wide and 2.75 m high.<br />

The train travels at 180 km · h −1 through air <strong>of</strong> density 1.2 kg · m −3<br />

and kinematic viscosity 1.5 × 10 −5 m 2 · s −1 . You may assume that<br />

the frictional drag <strong>of</strong> the train is equivalent to the drag <strong>of</strong> a turbulent<br />

boundary layer on one side <strong>of</strong> a flat plate <strong>of</strong> length l = 100 m and<br />

breadth b = 8.3 m. Taking the constant in equation 8.24 equal to<br />

0.37, calculate<br />

(a) the boundary layer thickness at the rear <strong>of</strong> the train<br />

(b) the frictional drag acting on the train, DF<br />

(c) the power required to overcome the frictional drag.<br />

Solution<br />

(a) um = 180 km · h−1 × 103 m · km −1<br />

3600 s · h−1 50 m · s −1<br />

Substituting in equation 8.24, with x = l<br />

� �1/5 ν<br />

δ = 0.37 l<br />

um<br />

4/5 �<br />

(1.5 × 10<br />

= (0.37)<br />

−5 ) m2 · s−1 50 m · s−1 = 0.73 m<br />

(b) Rel = uml<br />

ν = 50 m · s−1 × 100 m<br />

(1.5 × 10−5 ) m2 = 3.333 × 108<br />

· s−1 From equation 8.25<br />

CF = 2F<br />

ϱu 2 m l = 0.074(Re l) −1/5<br />

� 1/5<br />

(100 m) 4/5

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!