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404  Chapter  12  Temperature Distributions with More Than One Independent  Variable

                           that viscous dissipation and axial heat conduction  effects  are negligible. Use the following  di-
                           mensionless variables:




                           Show that the temperature profiles in this system are

                                                          2            3?f)                   (12D.2-2)

                           in which  X/ and  /3 ; are the eigenfunctions  and  eigenvalues  obtained  from  the solution  to  the
                           following  equation:


                                                                  * * * -  0                  ( 1 2 D 2 3 )
                                                                                                 - -
                           with boundary conditions X =  finite at £ = 0 and X = 0 at £ =  1. Show further  that


                                                          A,  =  - ^                          (12D.2-4)


                           (b)  Solve Eq. 12D.2-3 for the Newtonian fluid by obtaining a power series solution for X ;. Cal-
                           culate the lowest eigenvalue by solving an algebraic equation. Check your result against that
                           given in Table 12D.2.
                           (c)  From the work involved in  (b) in computing fi] it can be inferred  that the computation  of
                           the higher  eigenvalues  is quite tedious. For eigenvalues higher  than  the second  or third  the
                                                             10
                           Wenzel-Kramers-Brillouin  (WKB) method  can be used; the higher the eigenvalue, the more
                           accurate the WKB method is. Read about this method, and verify that for the Newtonian fluid
                                                          $  = \{M ~ If                       (12D.2-5)

                           A similar formula  has been derived  for the power law model. 11


                           Table 12D.2  Eigenvalues pj  for the Graetz-Nusselt Problem for Newtonian Fluids"
                                                                              By Stodola and
                           i            By direct calculation* 7  By WKB method'  Vianello method^
                                                                  3.56
                                                3.67
                           1                    3.67              3.56            3.661 е
                           2                   22.30             22.22
                           3                   56.95             56.88
                           4                  107.6             107.55
                           a
                            The (3j here correspond to \k] in W. M. Rohsenow, J. P. Hartnett, and Y. I. Cho, Handbook of
                           Heat  Transfer, McGraw-Hill (New York), Table 5.3 on p. 510.
                           b
                            Values taken from  K. Yamagata,  Memoirs of the Faculty of Engineering, Kyushu  University,
                           Volume  VIII, No. 6, Fukuoka, Japan  (1940).
                           c  Computed from  Eq. 12D.2-5.
                           d  For the particular trial function in part (d) of the problem.



                               10
                                J. Heading, An Introduction  to Phase-Integral Methods,  Wiley, New York  (1962); J. R. Sellars,
                           M. Tribus, and J. S. Klein, Trans. ASME,  78,441-448 (1956).
                               "I.  R. Whiteman and W. B. Drake, Trans. ASME,  80, 728-732  (1958).
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