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PIPES CONVEYING FLUID: LINEAR DYNAMICS I1              199


              coordinate along a strcamtube off the centreline (and should not be confused with the s
              used in Sections 3.3.1 and 3.3.2). Hence, the sum of  (4.2) and (4.3) gives





              the  intermediate result  is  obtained with  the  aid  of  Figure 4.l(c), while  the  last  step is
              reached through neglect of  second-order terms.
                Since llrll  is small and arel is negligible, the last integral of (4.1) may be approximated
              as follows:




              in  which  it  is  recalled that  w  is  the  vector displacement of  the  pipe  centreline in  the
              y-direction. The  second  term  in  (4.5)  is  obtained  through  the  following  sequence of
              operations: 23 x W; = 23 x Ui(l + Q/Ui) 2: 23 x Ui = 2 [-(a2w/axat)k]  x(U,i) =
              2Ui(a2w/ax at)j = 2Ui(a2w/ax at), where {i, j, k) are unit vectors associated with {t, q, 0.
              Throughout, the small inclination of  the (6, q}-plane vis-&vis  the (x, y}-plane is utilized,
              subject to order-of-magnitude constraints. Hence, combining (4.4) and  (4.5), the rate of
              change of  fluid momentum is

                                                                                   (4.6)

              which yields components per unit length in the x- and y-direction, respectively equal to

                          d Ui                   +2Ui - ui
                                                       a2w
                           dx                          ax at
                    piAiUi  ~    and    piAi               +                       (4.7)
              The second expression may be written in the compact form piAi%’w,  where 9 = [(a/%) +
              u,(a/ax)], and


                           92w = 9[%w] =                                           (4.8)
                                                     ax at
              It is instructive to note that there are no terms involving dAi/dx in (4.7), as there would
              have been if the lateral momentum change had erroneously been evaluated by a simplistic
              application of  the formula [(slat) + u,(a/ax)]{piAi[(aw/at) + Vi(aW/ax)l)!
                Now, the next steps in the derivation of the equation of motion may be taken. Working
              in a similar way as in Section 3.3.2 (cf. Figure 3.6) by considering an element 8c of  the
              pipe [Figure 4.2(a)], force balances in the x- and y-direction and a moment balance yield





                                                                                  (4.9b)

                                                                                  (4.9c)
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