Page 150 - Fluid-Structure Interactions Slender Structure and Axial Flow (Volume 1)
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132               SLENDER STRUCTURES AND AXIAL FLOW


























                                     0.0     0.2     0.4     0.6     0.8     1 .o
                                                          P
                   Figure 3.43  The stability diagram of ucf versus ,9  of the horizontal cantilevered pipe, for progres-
                         sively higher values of  the viscoelastic dissipation constant, a!  (Semler et al. 1998).


                     The question of destabilization by damping according to the Semler et al. (1998) thesis
                   is considered next. It is recalled that, in viscoelastic or hysteretic damping, each general-
                   ized coordinate component, qr, is damped proportionately to A:;  so, the higher the value
                   of  r, the more is the corresponding qr damped. Let us consider the first jump, at PSI. The
                   effect of  (11 # 0 is to damp q3  more than  q1  and  q2, and to  effectively wipe out all the
                   higher components qr > q3. Now, it is evident from Figure 3.40 that, when it comes into
                   play, q3 has a stabilizing effect on the system, as manifested by the increase in ucf at PSI;
                   hence, its diminution by  a! means that the system is effectively destabilized. As a result,
                   this jump, which has been shown to be related to the emergence of  43, can be entirely
                    suppressed, as shown in Figure 3.43! One can similarly see how the other jumps can also
                    be suppressed. Looking again at Figures 3.41 and 3.42 (the dashed lines), it is seen that
                    both the amplitude ratios and phase differences of the qr are significantly affected. Thus,
                    it is  seen that, with damping present, 43/41 and  42/41  increase more gradually with P
                    beyond PSI. Also, some of the  ‘saturation characteristics’ of the phase differences disap-
                    pear (e.g. for 0,  - el), and both 02 - 03  and 0,  - 01  vary more gradually - thus making
                    the discontinuous changes in ucf with  unnecessary.
                      Another, physical way  of  looking at the problem is  to realize that, in  some circum-
                    stances, if  the  fluid pressure acting on  an undamped oscillating body  is completely in
                    phase with its acceleration (out of phase with the displacement), there can be no interac-
                    tion between fluid and solid. However, the introduction of  dissipation in the solid would
                    produce a phase shift in its oscillation, thereby enabling the fluid to do work on the solid
                    or vice versa. In a situation where energy transfer occurs in any case, independently of
                    dissipation, as for the pipe conveying fluid, one can say that the phase shift may either
                    facilitate or hinder energy exchange, thus destabilizing or  stabilizing the  system as the
                    case may be.
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