Page 329 - Bird R.B. Transport phenomena
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§10.8  Forced Convection  313

                 term  containing  the viscosity  is the viscous  heating, which  we shall  neglect  in  this dis-
                 cussion. The last term  in the first  bracket, corresponding  to heat conduction  in the axial
                 direction, will be omitted, since we know from  experience that it is usually small in com-
                 parison  with  the heat  convection  in the axial direction.  Therefore,  the equation  that  we
                 want to solve here is

                                                                                    (10.8-12)

                 This partial differential  equation, when solved, describes the temperature  in the fluid as
                 a function  of r and z. The boundary conditions are

                 B.C. 1:                 atr  =  0,  T = finite                     (10.8-13)
                 B.C. 2:                 at r = R,  kj^  = q 0 (constant)           (10.8-14)

                 B.C.3:                  at z =  0,  T = T,                         (10.8-15)
                 We now put  the problem  statement  into dimensionless  form.  The choice  of  the  dimen-
                 sionless quantities is arbitrary. We choose

                                    0  =           =         =    ?L
                                       T¥7T       ^  i     £  -~    ~T-       dO.8-16,17,18)
                                                                       2
                                        VoR/k        R         PC pv z>maxR /k
                 Generally  one  tries  to  select  dimensionless  quantities  so as  to minimize  the number  of
                 parameters  in the final  problem  formulation.  In this problem  the choice  of £ =  r/R  is a
                 natural one, because  of the appearance  of r/R  in the differential  equation. The choice for
                 the  dimensionless  temperature  is  suggested  by  the  second  and  third  boundary  condi-
                 tions. Having  specified  these  two  dimensionless  variables, the  choice  of  dimensionless
                 axial coordinate follows  naturally.
                     The resulting problem statement, in dimensionless form, is now

                                                       1  д  Ы 8 ,                   (10.8-19)

                 with boundary conditions
                 B.C.  1:                    at f  = 0,  0  = finite                (10.8-20)
                 B.C.  2:                    a t f = l ,  ^  = 1                    (10.8-21)

                 B.C.  3:                    at I = 0,   0  = 0                     (10.8-22)
                 The  partial differential equation in Eq. 10.8-19 has been solved  for these boundary condi-
                      3
                 tions,  but in this section we do not give the complete solution.
                     It is, however, instructive to obtain the asymptotic solution to Eq. 10.8-19 for large  f.
                 After  the fluid is  sufficiently  far  downstream  from  the beginning of  the heated  section,
                 one  expects that the constant  heat flux through the wall  will  result in a rise  of the fluid
                 temperature that is linear in f.  One further  expects that the shape of the temperature pro-
                 files  as a function  of £ will ultimately  not undergo further  change with increasing £ (see
                 Fig. 10.8-3). Hence a solution  of the following  form seems reasonable for large £:

                                                                                    (10.8-23)
                                                       0
                 in which  C o is a constant to be determined  presently.



                     3
                      R. Siegel, E. M. Sparrow, and T. M. Hallman, AppL Sci. Research, A7, 386-392 (1958). See Example
                 12.2-1 for the complete solution and Example 12.2-2 for the asymptotic solution for small £.
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