Page 116 - Fluid-Structure Interactions Slender Structure and Axial Flow (Volume 1)
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98                 SLENDER STRUCTURES AND AXIAL FLOW

                   at u2/n2 2: 6.2, followed by coupled-mode flutter at point C (u2/n2 2: 7), in this case via
                   a Hamiltonian Hopf bifurcation. The value of  u for restabilization at point I3 corresponds
                   exactly to the point where the nongyroscopic system, or indeed the pipe  systems in (a)
                   and (b), develop divergence in their second mode.
                     In  closing,  the following two  important points  should be  made.  First, the results of
                   Figures 3.9-3.11,  3.14 and 3.15 apply equally to pipes with a downstream end either free
                   to  slide axially or not  [Figure 3.l(a,b)]: since linear theory cannot distinguish between
                   the  two,  the  same  equation  governs  both;  however,  the  foregoing  explanation  of  the
                   existence of coupled-mode flutter applies only to systems with a sliding end. Second, and
                   as  cautioned  at the  outset, the  existence of  coupled-mode flutter has  to be  decided by
                   nonlinear theory (Chapter 5) and by experiments (Section 3.4.4).

                   3.4.2  Pressurization, tensioning and gravity effects

                   If  dissipative and gravity effects are neglected and  dU/dt = 0, equation (3.38) simpli-
                   fies to

                            +
                                                                 a2w
                        a4w
                     EZ - [MU2 + pA(1-  2~6) - TI     a2w  + 2MU - (M + M)-   a2w  = 0,  (3.98)
                                                                     f
                                                      ~
                        ax4                           ax2        axat          at2
                   in which it is recalled that 6 = 0 if there is no axial constraint, so that axial sliding of the
                   downstream end is permitted, and 6 = 1 if  it is prevented. The case of S = 1 is shown in
                   Figure 3.16(a), where pf is the pressure expended in overcoming the frictional pressure
                                                                          -
                                                  u      PO               T
                                         J=
                                 P= P+Pf  +PO
























                    Figure 3.16  (a) A pipe subject to tensioning T and to pressurization p, measured above the atmo-
                    spheric pressure, pa; (b) divergence due to presurization, represented as if the pipe were pressurized
                    by floating pistons; (c) model experiment with bellows, to show pressurization-induced buckling.
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