06.09.2021 Views

Basics of Fluid Mechanics, 2014a

Basics of Fluid Mechanics, 2014a

Basics of Fluid Mechanics, 2014a

SHOW MORE
SHOW LESS

You also want an ePaper? Increase the reach of your titles

YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.

5.6. THE DETAILS PICTURE – VELOCITY AREA RELATIONSHIP 167<br />

For constant density (conservation <strong>of</strong> volume) equation 6 and (h >z) reduces to<br />

∫<br />

U rn ρdA=0 (5.35)<br />

In the container case for uniform velocity equation 5.35 becomes<br />

A<br />

U z A = U e A e =⇒ U z = − A e<br />

A U e (5.36)<br />

It can be noticed that the boundary is not moving and the mass inside does not change<br />

this control volume. The velocity U z is the averaged velocity downward.<br />

The x component <strong>of</strong> velocity is obtained<br />

by using a different control volume.<br />

into the page<br />

Y control Volume<br />

The control volume is shown in Figure 5.9.<br />

The boundary are the container far from<br />

A<br />

−<br />

the flow exit with blue line projection into y<br />

page (area) shown in the Figure 5.9. The<br />

mass conservation for constant density <strong>of</strong><br />

this control volume is<br />

∫<br />

−<br />

A<br />

∫<br />

U bn ρdA+<br />

A<br />

U rn ρdA=0<br />

(5.37)<br />

X control Volume<br />

A<br />

− x into the page<br />

x y<br />

Ue A e<br />

Fig. -5.9. Control volume and system before<br />

and after the motion.<br />

Usage <strong>of</strong> control volume not included in the previous analysis provides the velocity at<br />

the upper boundary which is the same as the velocity at y direction. Substituting into<br />

(5.37) results in<br />

∫<br />

∫<br />

A e<br />

A − x<br />

A U e ρdA+ U x ρdA=0 (5.38)<br />

A yz<br />

Where A x − is the area shown the Figure under this label. The area A yz referred to<br />

area into the page in Figure 5.9 under the blow line. Because averaged velocities and<br />

constant density are used transformed equation (5.38) into<br />

A yz<br />

A { }} {<br />

e<br />

A A x − U e + U x Y (x) h =0 (5.39)<br />

Where Y (x) is the length <strong>of</strong> the (blue) line <strong>of</strong> the boundary. It can be notice that the<br />

velocity, U x is generally increasing with x because A − x increase with x.<br />

The calculations for the y directions are similar to the one done for x direction.<br />

The only difference is that the velocity has two different directions. One zone is right<br />

to the exit with flow to the left and one zone to left with averaged velocity to right.<br />

If the volumes on the left and the right are symmetrical the averaged velocity will be<br />

zero.<br />

6 The point where (z = h) the boundary term is substituted the flow in term.

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

Saved successfully!

Ooh no, something went wrong!