Page 412 - Bird R.B. Transport phenomena
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394  Chapter 12  Temperature Distributions with More Than One Independent Variable

                                                           Fig. 12.4-3.  Forced-convection heat transfer  from a
                                                           sphere in creeping flow. The shaded region  shows
                                                           the thermal boundary layer  (defined  by П  <  0.99
                                                                                             т
                                                           or у  <  1.55 ) for  Pe = RePr «  200.
                                                                    T
                                             Separation  point
                                                 (6 = 0)
                                                =  r-R



                                           Stagnation  point
                                               (б»  =  77")
                             t  t t t t t t f t
                            Fluid  approaching  with velocity  v x
                                 and temperature T^


                            also  the region  where  most  of  the heat transfer  occurs. The result  for  Q is  good  within  about
                            5% for  RePr >  100; this limits its use primarily  to fluids with  Pr >  100, since creeping flow is
                            obtained only at Re of the order of 1 or less. 12
                               Results  of  the same  form  as  Eq.  12.4-34  are  obtained  for  creeping flow  in other  geome-
                            tries, including packed  beds. 813
                               It  should  be  emphasized  that the asymptotic  solutions  are  particularly  important: they
                            are relatively  easy  to obtain, and for  many applications they are sufficiently  accurate. We will
                            see in Chapter 14 that some of the standard heat transfer  correlations are based  on asymptotic
                            solutions  of the type discussed  here.



                            QUESTIONS FOR DISCUSSION
                         1.  How does Eq. 12.1-2 have to be modified  if  there is a heat source within the solid?
                         2.  Show  how  Eq.  12.1-10 is  obtained  from  Eq.  12.1-8.  What  is  the  viscous  flow  analog  of  this
                            equation?
                         3.  What  kinds  of  heat conduction problems  can be solved  by  Laplace transform  and which can-
                            not?
                         4.  In Example  12.1-3 the heat flux and the temperature both satisfy  the "heat conduction equa-
                            tion." Is this always true?
                         5.  Draw a carefully  labeled  sketch  of the results  in Eqs. 12.1-38 and 40 showing  what is meant by
                            the statement that the "temperature oscillations  lag behind the heat flux oscillations by  тг/4."
                         6.  Verify  that Eq. 12.1-40  satisfies the boundary conditions. Does it have to satisfy  an initial con-
                            dition?  If so, what is it?
                         7.  In Ex. 12.2-1, would  the method of separation of variables  work  if applied  directly  to the func-
                            tion 0(& 0  rather than to 0 rf(£  f)?
                         8o  In Example  12.2-2, how  does the wall temperature  depend  on the downstream  coordinate  z?
                         9.  By means  of a carefully  labeled  diagram,  show  what  is meant  by the two cases A <  1 and  A  ^
                            1 in §12.4. Which  case applies  to dilute  polyatomic  gases?  Organic  liquids?  Molten  metals?
                        10.  Summarize  the situations  in which  the four  mathematical  methods  in §12.1 are  applicable.



                               12
                                 A review of analyses for a wide range of Pe =  RePr is given by S. K. Friedlander, AIChE Journal, 7,
                            347-348 (1961).
                               13
                                 J. P. S0rensen and W. E. Stewart, Chem. Eng. Sci., 29, 833-837 (1974).
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