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PIPES CONVEYING FLUID: LINEAR DYNAMICS I               145

               A successful experiment with a metal pipe was also conducted by Liu & Mote (1974)
             with  their  apparatus,  described  in  Section 3.4.4.  They  used  an  end-nozzle,  so  as  to
             reduce  the  effective  B  and  achieve  flutter  with  the  available  maximum  flow  rate  (see
             Section 3.3.5); ai = A/Aj, the  ratio  of  pipe  flow  area  to  terminal  flow  area,  was  2.42.
             They obtained  good agreement between  the theoretical  and experimental  values of  ucf :
             2.89 and 3.27, respectively, as well as between the theoretical and experimental frequency
             versus flow curves, as shown in Figure 3.52. In the absence of the nozzle, the agreement
             in  frequency  was  less  good,  because  the  pipe  was  less  straight.  However,  this  is  the
             second instance where the pressure drop in the pipe was very large, - 3 - 10 MPa, yet the
             dynamics was essentially unaffected by it.



























             Figure 3.52  Variation  of  the  second- and  third-mode eigenfrequencies  with  increasing  u  for  a
             metal cantilevered pipe conveying fluid. Experimentalltheoretical reference frequencies (at u = 0):
              %e(Q),   = 8.0/8.0Hz for the second mode and 25321.7Hz for the third (Liu & Mote  1974).

               An important theoretical and experimental study, mainly on forced vibrations of vertical
             cantilevered pipes conveying fluid (see Section 4.6), was conducted by Bishop & Fawzy
             (1976). They  also  examined  the  free  vibration  characteristics,  and  a  few  words  about
             that  will be  said here. The experiments were with  surgical quality silicone rubber pipes
             conveying water. The authors studied extensively the static distortion from the stretched-
             straight state that  they  observed  in  their experiments  and its evolution  with  flow. They
             concluded  that  it  was  due  to  lack  of  perfect  straightness  and  residual  internal  stresses
             related to the manufacturing process, and not  an instability (divergence) - in agreement
             with  previous  studies - even  though  some  other  researchers  later  misinterpreted  this
             finding. Their  experimental  data  and  degree  of  agreement  with  theory  were  similar  to
             those  reported  already.  A  typical  set  is  shown  in  Figure 3.53 for  experiments  without
             (aj = A/Aj = 1) and with end-nozzles (a, = 1.5 and 2.49).
               A  simple  but  ingenious  experiment  was  conducted  by  Becker  et al. (1978)  using
             drinking  straws  (of  unspecified  material)  as  pipes  and  air  flow.  The  supported  end
             was  attached  onto  weighing  scales and the  flow-rate was  determined  from  the  reaction
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