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.

Fundamentals <strong>of</strong> the theory <strong>of</strong> hydrodynamic lubrication 225<br />

overcome the viscous resistance is dissipated as heat, and the consequent<br />

variations in the viscosity and density <strong>of</strong> the lubricant cause the centre <strong>of</strong><br />

pressure to move forward. A centrally pivoted slipper is <strong>of</strong> course suitable<br />

for movement in either direction.<br />

We have seen that the heel <strong>of</strong> the slipper should not touch the bearing<br />

plate because lubrication would then break down entirely. In practice there<br />

is a lower limit, greater than zero, to the clearance at the heel. This limit is<br />

largely governed by the inevitable lack <strong>of</strong> perfect smoothness <strong>of</strong> the surfaces<br />

and the probable size <strong>of</strong> solid particles (e.g. grit) in the lubricant. If these<br />

particles are unable to escape under the heel <strong>of</strong> the bearing, they collect at<br />

this point and score the surfaces.<br />

The tangential force (i.e. the resistance to the relative movement between<br />

the slipper and the bearing plate) may also be calculated. The viscous shearing<br />

stress at any point in the film <strong>of</strong> lubricant is given by τ = µ(∂u/∂y). The<br />

velocity u is given by eqn 6.18<br />

�<br />

δp∗ �<br />

y2 = µu + Ay + B<br />

δx 2<br />

It is again permissible to drop the asterisk from the symbol p ∗ since we consider<br />

a horizontal slipper bearing, and again the inclination <strong>of</strong> the slipper is<br />

assumed so small that any component <strong>of</strong> velocity in the vertical direction is<br />

negligible. Since the rate <strong>of</strong> change <strong>of</strong> pressure with x is not constant, the<br />

differential dp/dx must be used instead <strong>of</strong> the ratio δp/δx. The integration<br />

constants A and B are determined by the conditions at the boundaries. Referring<br />

to Fig. 6.19, the velocity <strong>of</strong> the lubricant must equal the velocity <strong>of</strong> the<br />

bearing plate when y = 0. Substituting u = V and y = 0 gives B =−µV.<br />

If the clearance is h at a particular value <strong>of</strong> x, the other boundary condition<br />

is that u = 0 when y = h (since the slipper is considered stationary).<br />

∴ dp h<br />

dx<br />

2<br />

dp<br />

= 0 + Ah − µV whence A =<br />

2 dx<br />

Thus the expression for velocity at any point becomes<br />

h<br />

2<br />

+ µ<br />

h V<br />

dp y<br />

dx<br />

2 dp h µ<br />

= µu + y + Vy − µV<br />

2 dx 2 h<br />

and differentiation with respect to y then gives an expression for the viscous<br />

stress in the x direction at any value <strong>of</strong> y<br />

µ ∂u<br />

∂y =−dp<br />

� �<br />

h<br />

− y −<br />

dx 2 µV<br />

(6.41)<br />

h<br />

The stress at the bearing plate is given by the value <strong>of</strong> this expression when<br />

y = 0, that is, −(dp/dx)(h/2)−µV/h. (The sign convention for stress shows<br />

that the stress on the bearing plate is given by µ(∂u/∂y) since the plate faces<br />

the direction <strong>of</strong> increase <strong>of</strong> y.) Thus the total tangential force on the bearing<br />

plate divided by the width <strong>of</strong> the plate is<br />

� l�<br />

�<br />

dp h µV<br />

− + dx<br />

dx 2 h<br />

0

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

Saved successfully!

Ooh no, something went wrong!