Page 45 - Fluid-Structure Interactions Slender Structure and Axial Flow (Volume 1)
P. 45

28                 SLENDER STRUCTURES AND AXIAL FLOW

                   The essence of slender-body theory is to take advantage of the linearity of the problem
                 and to express it as the superposition of the following two problems: (i) the axisymmetric
                 flow  past  the  body  of  revolution  with  flow  velocity  V,  cos a, and  (ii) the  cross-flow
                 around  the  body  with  flow  velocity  V,  sin a  (Ward  1955; Karamcheti  1966). Thus,
                 defining $ = $1  + 42  and u,  = u,l  + u,2,  equation (2.80) may be re-written as
                                                          dR     dR
                                               - (U + u,.)- 2 u -,                   (2.8 1 a)
                                                          dx     dx
                                                     dR
                                               = uX2 - - W  sin 8,                   (2.81b)
                                                     dx

                 where
                                       U = V,  cos a,    W = V,  sin a.               (2.82)

                 The solution to (2.81a) is usually obtained by  representing the body through a distribution
                 of singularities (e.g. sources and sinks) along the centreline, while the solution to (2.81b)
                 may be obtained via standard potential-flow analysis (Streeter 1948; Milne-Thomson 1949;
                 Karamcheti 1966).
                   Consider  next  a  very  slender  cylindrical  body  for  which  dR/dx 2: 0, or  exactly  0,
                 except near the extremities [Figure 2.5(b)]. The body is subjected to an oscillatory lateral
                  displacement w(x, r) in  the 8 = in plane. Then, according to  slender-body theory, the
                  flow can be regarded as compounded of  (a) the steady flow around the stretched-straight
                  body,  which  we  shall  ignore  here  [and hence  (2.81a)  also]  since  dR/dx  is  nearly  or
                  exactly zero over most of  the length of  the body, and (b) the flow due to displacements
                  w(x, t) (Lighthill  1960). Hence, only the velocity component related to (2.81b) remains,
                  namely (a$2/ar)lr=R 2: -W.  The lateral velocity of the fluid relative to the moving body
                  is made up of  (i) the component of  U  normal to the inclined body, equal to  -U  sin a,
                  where a = tan-'(aw/ax),  and (ii) the lateral velocity of  the body, awlat, reversed, if  at
                  that instant the body is moving upwards as in the inset of  Figure 2.5(b). Therefore, for
                  sufficiently small a, one may write

                                                          aw     aw
                                                 V(x,r) = - + U--,                    (2.83)
                                                          at     ax
                  on the implicit assumption that, locally, the body shape differs little from that of a long
                  (infinite) cylinder C, of the same cross-section all the way  along. Thus, according to the
                  slender-body approximation, this lateral flow  near any point of  the cylinder is identical
                  with the two-dimensional potential flow that would result from the motion of C,  through
                  fluid at  rest,  with  velocity  V(x, r).  Lighthill (1960) then  goes  on  to  obtain the  rate of
                  change of lateral momentum of the fluid passing over the flexible body,


                                                                                      (2.84)

                  where A(x) is  the slowly varying (or constant) cross-sectional area along the  length of
                  the body. This equation is further discussed in Chapters 8 and 9, where the slender-body
                  approach is used extensively.
   40   41   42   43   44   45   46   47   48   49   50