Page 394 - Modelling in Transport Phenomena A Conceptual Approach
P. 394

374       CHAPTER 9.  STEADY MICROSCOPIC BALANCES  WITH GEN.


            Table 9.1  The physical significance and the order of  magnitude of  the terms in
            Eq.  (9.3-79).
             Term    Physical Significance  Order of  Magnitude
               &T                              (To - Tl)
             k-  dx2     Conduction              B2
             ’
             -        Viscous dissipation       @
               v2
              B2                                 B2

               Before solving J3q.  (9.3-79)) it is convenient to express the governing equation
            and the boundary conditions in dimensionless form.  Introduction of  the dimen-
            sionless quantities
                                                                            (9.3-81)

                                                                            (9.3-82)

            reduces Eqs.  (9.3-79), (9.3-73) and (9.3-74) to

                                                   Br                       (9.3-83)
                                           dc2 -
                                       at  <=O     8=1                      (9.3-84)

                                       at  <=l  8=0                         (9.3-85)
            Integration of Eq. (9.3-83) twice gives
                                           Br
                                     e = - - t2 + cl + c2                   (9.3-86)
                                                    (
                                           2
            Application of  the boundary conditions, Eqs.  (9.3-84) and (9.3-85)) gives the solu-
            tion as
                                                                            (9.3-87)


            Note that when Br  = 0, Le.,  no viscous dissipation, EQ. (9.3-87) reduces to J3q.
            (8.3-10). The variation of e as a function of  ( with Br as a parameter is shown in
            Figure 9.13.
               In engineering calculations, it is more appropriate to express the solution in
            terms of  the Nusselt  number.  Calculation of  the Nusselt number,  on the other
            hand, requires the evaluation of  the bulk temperature defined by
                                                        €3
                                   lwpzTdzdy  1 vz T dx
                                                    -
                               Tb =                 -                        (9.3-88)
                                    1” la dXdY  Jd”  Vz dX
                                            vz
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