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CURVED PIPES CONVEYING FLUID                     417

             In  (ii) and  (iii), the steady forces depend on fluid friction. Accordingly, variants of  the
             theory considering the fluid to be inviscid or viscous are formulated.
               Of  course,  theories  (i)  and  (ii) are  variants  of  then  already  available  theories.  The
              strength of the Misra et al. work lies in deriving both inextensible and extensible theories
             from the same basic trunk, and thus having control over the assumptions and parameter
             differences between them; and hence being able to make meaningful comparisons between
             their predictions. It  should also be  mentioned that  little  cross-comparison between the
             various theories was done theretofore, and even less systematic analysis of  the reasons
             for the differences between their predictions.
               Therefore,  since  theoretical  models  (i)  and  (ii) substantially incorporate  the  salient
             features of  all the aforementioned inextensible and extensible theories, and since, as will
             be  shown, model  (iii) succeeds in  isolating the important physical differences between
             them,  this  work  (Misra  et al.  1988a,b,c) provides  the  backbone  of  the  material  to  be
             presented in this chapter.
               Other work on this topic was undertaken by  Fan & Chen (1987), who studied three-
             dimensionally curved helical pipes (the only such study), and Aithal & Gipson (1990),
             who studied the effect of dissipative forces on stability, both making the inextensibility
              assumption. KO & Bert  (1984,  1986) undertook  a  nonlinear study of  the  system, and
              Steindl & Troger (1994) looked into the  possibility of  chaotic motions of  cantilevered
             curved pipes. More will be said about these studies in the following sections.
               Finally,  a  thorough  study  of  the  equations  of  motion  was  undertaken  by  Dupuis
              & Rousselet (1992), who concluded that  ‘the stressed-by-flow configuration . . . is  the
             only  equilibrium  state  adequate for  the  study of  the  linear  stability of  such pipe-fluid
              systems’ - as Misra et al. had concluded and as we, in due course, shall do here.


              6.2  FORMULATION OF THE PROBLEM

              6.2.1  Kinematics of the system
             The  system under consideration is  shown in  Figure 6.1. It consists of  a curved pipe of
              length L, with a uniform cross-sectional area Ap, mass per unit length m, flexural rigidity
             EZ  and  shear modulus G. The pipe is initially in a plane, having an arbitrary centreline
              shape, i.e. the radius of  curvature is not necessarily constant along its length. It conveys
              a  stream of  fluid, of  mass M per  unit length. The flow is  assumed to be  a plug  flow
              with constant velocity,  U. Furthermore, the pipe is assumed to be fully submerged in  a
              quiescent fluid.
                The kinematics of the pipe is developed by  the same approach as that  used by  Love
              (1927)  for  a  curved  rod.  This  implies  an  assumption that  the  pipe  diameter  is  small
              compared  to  both  the  radius  of  curvature  of  the  centreline  and  the  overall  length  of
              the pipe.
                To describe the kinematics of the system, it is convenient to use two reference frames
              (Figure 6.1) - cf.  Section 3.3.1.  The  Lagrangian  reference  frame  (XO, yo, ZO)  with  its
             origin  PO is  located  on  the  initial,  undeformed centreline  in  such  a  way  that  the  ZO-
              axis is  tangential to  the  undeformed centreline, while  the  axes xo and  yo  are  directed
              along the principal normal and binormal directions.+ At any instant t  during the motion

                +Unusually, vis-&vis  most  of the foregoing, the long axis along which  the fluid flows is here the zo-axis.
             This being an intricate analysis, conversion was not attempted, as it might have introduced unwanted errors.
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