Page 44 - Fluid Power Engineering
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Hydraulic Oils and Theor etical Backgr ound    21


               Considering the shown fluid element in the radial clearance, and neglect-
               ing the minor losses at the inlet and outlet, and assuming a concentric
               stationary spool, an expression for the leakage flow rate can be deduced
               as follows. In the steady state, the fluid element speed is constant and the
               forces acting on it are in equilibrium. These forces are the pressure forces
               and the friction forces acting on the internal and external surfaces of the
               fluid element.
                                          r DdP
               The pressure force is   F = 2 π                      (2.10)
                                      P
               The friction force is   F = 2 π Ddxτ                  (2.11)
                                      τ
                               r = 05 c −  y  then   du  =−  du     (2.12)
                                   .
                                              dy    dr
                                                     du     du
               For Newtonian fluid, the shear stress is τ =  μ  = − μ  (2.13)

                                                     dy     dr

               Since F =  F  then   du  =−  rdP  or  du =−  rdP  dr  (2.14)
                     P   τ                           μ
                               dr    μ  dx             dx
                   The pressure gradient dP/dx is constant.
                               dP  =  Δ P   where ΔP = P − P        (2.15)
                               dx   L             1   2
                   The velocity distribution in the radial clearance is found by inte-
               grating Eq. (2.14).

                                    rdP
                                 ∫
                              u = −  μ  dx  dr a+=−  2 r 2 μ  dP    (2.16)
                                               a
                                                     dx
                   If the fluid velocity at the boundaries is zero, then
                                   u = 0 for  r =± c/2              (2.17)


                   By substitution from Eqs. (2.15) and (2.17) into Eq. (2.16), the
               following expression for the velocity distribution is obtained:

                                      1 Δ P c ⎛  2  ⎞
                                   u =         −  r 2               (2.18)
                                            ⎜
                                      2μ  L ⎝ 4   ⎟ ⎠
                   The leakage flow rate, Q , is then found as follows:
                                       L
                                L ∫
                               Q =  − c/2  u Ddr =  π Dc L 3  Δ P   (2.19)
                                        π
                                                 μ
                                               12
                                     c/2
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