Page 172 - Fluid-Structure Interactions Slender Structure and Axial Flow (Volume 1)
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154               SLENDER STRUCTURES AND AXIAL FLOW




















                                                       ‘cf


                                                    I  I
                                                    I  I
                                                    I
                                                    I
                                                    I  I
                                                    I  I
                                                    I  I
                                                    I
                                                    I
                                                    I
                                                    I  I
                                                    I
                                                    I  I
                                                    I
                                                    I     Stable
                                                    I  I
                                                    I  I
                                              1,IL -
                                                    I
                                         0         7                      1
                                       (b)                   1 lL
                    Figure 3.58  (a) Schematic of  a pipe  fixed  at  the  upstream  end  and  with  a  simple support  at
                    & = 1/L; (b) qualitative stability diagram, showing the dimensionless flow velocities u versus 1/L
                    and the definition of lc/L; &d  and urf are the dimensionless critical flow velocities for divergence
                                     and flutter, respectively (Chen & Jendrzejczyk  1985).
                      The domain  of  the problem  9 = [0, 13  is broken  into two,  e1 = [0, &] and  $2  = [0,
                    1 -    with Cs = 1/L, wherein the dimensionless  displacements  of  the pipe  are  ~1  and
                    ~72, respectively. The equations of motion are then given by


                                                                                        (3.1 15)

                    cf. equation (3.1); the dimensionless quantities are the same as before, based on the overall
                    length L. The boundary conditions are
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