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PIPES CONVEYING FLUID: LINEAR DYNAMICS I               79

                 Hence,  utilizing  (3.47), (3.49) and  (3.50) leads  to  the  following  form for the  virtual
               work equation:

                                                                  p(u -  6r)d'V = 0.   (3.51)

               This,  integrated over time from  tl  to  t2,  at which limits 6r = 0 again, gives Hamilton's
               principle for the open system,

                                                                                   (3.52)


                                                                                   (3.53)

               with Z0 = 7;, - K,  being the Lagrangian of the open system.
                 This is next applied to the case of  a cantilevered pipe conveying fluid. For simplicity,
               the case of  no dissipation and a constant flow velocity  U  is considered. Moreover, it is
               presumed that the only forces involved in 6W  are associated with the pressure p, measured
               above the ambient of  the surrounding medium; hence,
                  JH=-  JJ                       + /L,+ye(tl                       (3.54)
                                                           p(u -  Sr)(V - u) . ndY,
                            :fc  (r )+Yl +4 (11   p(6r  *
               where  Yc(t) is the  surface covered by  the pipe  wall,  and Y, and  $(t)  are the inlet and
               exit  open  surfaces  for  the  fluid. Next,  it  is presumed  that  any  virtual  displacement  of
               the  pipe  does  not  induce  a  virtual displacement  of  the  fluid relative  to the  pipe.  Thus,
               virtual displacements of the fluid relative to the pipe are independent of those of the pipe.
               Hence, since the fluid is incompressible, there can be no virtual change in the volume of
               the system, and expression (3.54) simplifies to
                                                         p(u  6r)(V - u) e  n dY.   (3.55)
                    6~  = - //X+$(r,   '(6'   *  n)dY + //x+z(tl
              Now, if the fluid entrance conditions are prescribed and constant, the integrals over   are
              zero.  Furthermore,  the first integral  over Ye(t) is zero since at the outlet  p  = 0. Hence,
              the only part remaining is

                                                                                   (3.56)

               in  obtaining  which  u = r + Ut [Figure 3.8(a)],  (u - V)  n = U  at  $(t)  and  M  = pA
              have  been  utilized, A  being  the  open  (flow) area. Hence,  Hamilton's  principle  for  this
               system becomes




              which is identical to that obtained by Benjamin (1961a).+

                'In  Benjamin's  derivation, as in Figure 3.l(d), RL is  measured  from the  (x, z) = (L, 0) position, whereas
              here rL = Li + RL is measured from the origin; however, as i~ = RL and SrL = SRL, the two expressions are
              fully equivalent.
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