Page 192 - Tribology in Machine Design
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Sliding-elemen t be a rings  17 7

                                 U 2(dh/dx) normal to the top area, that may be taken as dx dz because of its
                                very small inclination in bearings. In Fig. 5.3, case (b), flow at velocity U 2 is
                                shown through the projected area (dh/dx)dxdz, which is shaded. Either
                                analysis gives the same product of velocity and area. Hence the total flows
                                qi inwards through the lower boundary of the geometric space and q 2
                                outwards through the upper boundary area, are respectively







                                Continuity with an incompressible fluid requires that the total inward flow
                                across the boundaries equals the total outward flow, or





                                For the case of a compressible fluid (gas bearings), mass flows instead of
                                volume flows wound be equated. A relationship between density and
                                pressure must be introduced. With substitution from eqns (5.3) and (5.4)
                                into eqn (5.5), selective differentiation, and elimination of the product dx dz,
                                the result is














                                With rearrangement








                                The last two terms are nearly always zero since there is rarely a change in
                                the surface velocities U and W, which represents the stretch-film case. The
                                stretch-film case can occur when there is a lubricating film separating a wire
                                from the die through which it is being drawn. Reduction in the diameter of
                                the wire gives an increase in its surface velocity during its passage through
                                the die.
                                  This basic equation of hydrodynamic lubrication was developed for a less
                                general case in 1886 by Osborne Reynolds. As usual, the eqn (5.7) and its
                                reduced forms in any coordinate system shall be referred to as the Reynolds
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