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          which produces





          where the constants   are determined as the  coefficients of the  Fourier-series rep-
          resentation of     this is left as an exercise. Thus the solution in the boundary
          layer near y = 1 is






          where the    are  known.  This completes, for  our  purposes, the  analysis of this
          boundary-layer problem.



          This example has admirably demonstrated, we submit, how the ideas of singular per-
          turbation theory  (here exhibited by the existence of boundary layers) developed for
          ordinary differential equations, carry over directly to partial differential equations. The
          boundary layers have been required in the y-direction, by virtue of the presence of the
          parameter  but not in the x-direction. Of course, the method of solution has required
          some knowledge of the methods for solving partial differential equations, but that was
          to be expected; otherwise no other complications have arisen in the calculations.
            For our second example, we consider a physically-based problem: heat conduction,
          and so the governing equation will now be parabolic.

          E3.4  Heat transfer to fluid flowing through a pipe
          We consider a circular pipe of radius r  = 1  (we will describe this problem, from the
          outset, in terms of non-dimensional variables),  extending in a straight line in
          the  role played by the  length of the  pipe  will be  discussed  later.  Through the pipe
          flows a fluid, with a known velocity profile represented by u  = u(r),  the
          equation for the temperature,   of the fluid is





          where we have assumed no variation in the angular variable around the pipe. The non-
          dimensional parameter,  is proportional to the thermal conductivity of the fluid.
          We seek a solution of equation (3.53), for   subject to the boundary conditions




          The fluid enters the pipe (at x = 0) with an initial temperature distribution  and
          the temperature of the pipe wall (r =  1) is prescribed along the pipe   i.e. heat
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