Page 122 - Fluid-Structure Interactions Slender Structure and Axial Flow (Volume 1)
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1 04              SLENDER STRUCTURES AND AXIAL FLOW

                   et al. 1985, 1986) pressurization effects were not considered, by making the downstream
                   end of the pipe free to slide axially [6 = 0 in equations (3.37) and (3.38)].
                      Long’s  (1955)  experiments  involved  simply-supported and  clamped-clamped  steel
                   pipes conveying fluid; the downstream end was mounted on rollers. The simply-supported
                   pipe  had  outer  diameter  Do = 25.4mm  (1 in),  wall  thickness  h = 0.94mm  (0.037 in),
                    and span L = 3.048m (120in). Despite the length and hence relatively large flexibility
                   of  this  pipe,  Ucd  = n corresponds to  Ucd  2: 52 m/s  (172ft/s)  - a  high  and  difficult to
                    achieve flow-rate, because of  the pumping requirements implied: a high flow rate  at a
                   high pressure (to overcome the large pressure drop); indeed, beyond the capabilities of
                    Long’s apparatus. By means of strain gauges, Long measured the first-mode frequency and
                    damping, and how they varied with u.+ It should be recalled that %e(Ql) is expected to
                    decrease parabolically with u; also, since 9nt(s21) is approximately constant according to
                    theory, 61  2 2nC1 = 2n9m(Q1)/%e(O1) is expected to increase parabolically. However,
                    for u  < 1, both d[%e(Ql)]/du  and d&/du are small, and for the urnax 2: 0.68 achieved in
                    these experiments the effect, if any, was judged to be within the margin of  experimental
                    error.* Hence, these experiments were largely inconclusive.
                      A  more effective experiment was  conducted by  Dodds & Runyan (1965), also with
                    simply-supported pipes,  as  shown in  Figure 3.21. The pipes  were of  aluminium alloy,
                    with 0, = 25.4mm, h = 1.65 mm, and an effective length L = 3.812m (12.5ft); the fluid
                    was water. In this case, the critical flow velocity, U,,  = 39.5m/s,  was actually attained.
                    Figure 3.22(a) displays the evolution of %e(Q1) with u for two different pipes, and shows

























                                   Differential pressure transducer

                    Figure 3.21  Schematic diagram of the experimental apparatus used by Dodds & Runyan (1965).
                                        All dimensions are in feet;  1 ft = 0.3048 m.

                      +Since various researchers have used different, and in some cases truly curious, schemes of nondimension-
                    alization, wherever possible these have been converted to those used in this book, for the reader’s convenience.
                      *Long also reports on some experimental results by  E. Ergin of Cal Tech, with a pipe  ‘similar to that used
                    here’, which show a clear quasi-parabolic Q1  versus u curve. However, there appears to be some error, at the
                    very least in the nondimensionalization of  u; for, whereas a urnax E 6.0 is shown, which greatly exceeds U,d,
                    the maximum reduction in %e(Q)  is only 3.2%.
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