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PIPES CONVEYING FLUID: NONLINEAR AND CHAOTIC DYNAMICS          28 1

              The derivative in this expression may be obtained from (5.4),
                               - = [ $ (1 + E) - ax, $1       /( + 42,
                                                      aw a2u
                               a0
                               8x0
                                                                 1
              thus yielding the curvature (5.5) for pipes whose centreline may be extensible.
                On  the  other hand, for  cantilevered pipes  whose centreline is  assumed inextensible,
              expressions (5.3) and (5.4) still hold, except that  E  = 0. In this case, s = XO, and hence
              ae/axo becomes

                                                                                   (5.7)

              Application of the inextensibility condition (5.1) leads to the following expression of  the
              curvature:




              Alternatively, the curvature may also be defined as a vector:





              where n is the normal unit vector which is always perpendicular to the tangent direction
              of  the pipe and r = (x, z) is the position vector along the pipe. Hence,

                                                                2
                                                       2  +($).
                                    K=lZl=/($)
              If  the  inextensibility  condition  is  applied  to  the  expression  above,  one  obtains  again
              equation (5.8).
                Note that  for a curve defined by  ~(x) (Eulerian description) rather than ~(s), one has
              the familiar expression of  curvature [e.g. Timoshenko (1955)],





              Care  must  be  taken  as  to  which  expression  of  K  is  used,  depending  on  the  physical
              problem.


              5.2.2  Hamilton's principle and energy expressions
              A  Hamiltonian derivation of  the  equations of  motion is  given  here. It  is  based  on the
              same statement of Hamilton's  principle as in Section 3.3.3, namely

                                                                                   (5.10)

                                                                       %
              where 2 is the Lagrangian of  the system (2 =  + % - y - q, and Vp being the
              kinetic and potential energies associated with the pipe, and ?$ and @l$ the corresponding
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