Page 471 - Fluid-Structure Interactions Slender Structure and Axial Flow (Volume 1)
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442               SLENDER STRUCTURES AND AXIAL FLOW

                      It  is  of  interest  to  recall  that  for  the  inextensible  case,  10 or  so  elements  lead  to
                    convergence of the results (Section 6.4.1), as opposed to more than 30 elements required
                    for the extensible case. Thus, the extensible analysis is computationally more demanding.
                      The steady-state configurations of  the system are considered next. Typical results are
                    shown in Figure 6.9, both for inviscid and viscous flow. As indicated in the figure caption,
                    the deformations are exaggerated for clarity. The forms in Figure 6.9(a,b) are for inviscid
                    flow  (Z = 0). It  may  be  noted  that  the  stressed  shape  is  symmetric;  this  is  because
                    the  steady (static) fluid force acting on the pipe is  only the centrifugal force, which is
                    symmetric. When the flow velocity increases, this symmetric deformation away from the
                    initial unstressed shape increases gradually. In the case of  viscous flow of  Figure 6.9(c),
                    on the other hand, the stressed shape is not symmetric, since the frictional pressure loss
                    causes the pressure to vary along the pipe.
                      It may be noted that the deformations for both inviscid and viscous flows are fairly small
                    (less than 5%), even for very large flow velocities (up to U = 6n). It is also interesting
                    to note that, beyond a certain U, the stressed configuration changes to another zero-flow
                    mode  shapet  (see the  case  of  U = 4n  for inviscid flow and  U = 3n for viscous flow).













                                                                                       c





















                     Figure 6.9  Static  in-plane  equilibrium  configurations  of  a  clamped-clamped  semi-circular
                     pipe  conveying  fluid,  for  Se = lo4 and  (a) inviscid  fluid,  ti = 2n, 2Sx, 371;  (b) inviscid  fluid,
                     -
                     u = 3.2n, 3.671, 4n; (c) viscous  fluid,  U = 27r, 2Sn, 3n. In  (a),  (b)  and  (c)  the  deformation  is
                              magnified by  a factor of  28, 30 and 25, respectively (Misra et al. 1988b).
                       +Note that for an extensible pipe, in addition to the shapes in Figure 6.7, there is a zero-node modal shape
                     for in-plane motions: the shape associated with the deflection in Figure 6.9 at small U.
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