Page 327 - Bird R.B. Transport phenomena
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§10.8  Forced Convection  311


                       Forced Convection         Free Convection
                         Heat  Transfer           Heat  Transfer






                                                            (No fan)





                   Heat swept  to right by  forced  Heat transported upward by
                         stream  of air         heated air that rises
                   1. The flow patterns are  1. The flow patterns are
                    determined primarily by  determined by the buoyant
                    some external  force     force on the heated  fluid
                   2 First, the velocity  profiles are  2. The velocity  profiles and
                    found; then they are used to  temperature profiles are
                    find  the temperature  profiles  interdependent
                    (usual procedure for  fluids
                    with constant  physical
                    properties)
                   3. The Nusselt  number depends  3. The Nusselt number depends
                    on the Reynolds and Prandtl  on the Grashof and Prandtl
                    numbers (see Chapter 14)  numbers (see Chapter 14)

                 Fig. 10.8-1.  A comparison  of  forced  and free  convection in non-
                 isothermal  systems.



                 how  this  may  be  done  for  tube  flow  by  using  the shell  balance  method. We  know  that
                 the  velocity  distribution so obtained is v  = 0, v  = 0, and
                                                  r     e
                                                                                     (10.8-1)

                 This parabolic distribution is valid sufficiently  far downstream  from  the inlet that the en-
                 trance length has been  exceeded.
                     In  this problem, heat  is  being  transported  in both the r and  the z directions. There-
                 fore,  for  the energy  balance we  use  a  "washer-shaped"  system,  which  is  formed  by  the
                 intersection  of an annular region  of thickness  Ar with  a slab  of thickness  Az (see Fig. 10.8-
                 2).  In this  problem, we  are dealing  with  a flowing  fluid,  and  therefore  all  terms  in the e
                 vector will be retained. The various  contributions to Eq. 10.1-1  are
                 Total energy  in at r       e \  • lirrkz  = (2тгге,)\ г  Az        (10.8-2)
                                              r r
                 Total energy  out at r  +  Ar  е \ ь,. •  2тг(г  + Ar)Az =          (10.8-3)
                                              г г+
                 Total energy  in at z       e \  •  2тггАг                          (10.8-4)
                                              z z
                 Total energy  out at z  +  Az  ^ZUAZ •  2тггАг                      (10.8-5)
                 Work  done on fluid by  gravity  pv g  •                            (10.8-6)
                                               z z
                 The  last  contribution is  the rate  at  which  work  is  done on the  fluid  within  the ring  by
                 gravity—that  is, the force  per unit volume pg z  times the volume  2тгг  Ar  Az multiplied  by
                 the  downward  velocity  of the  fluid.
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