Page 460 - Bird R.B. Transport phenomena
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440   Chapter  14  Interphase Transport in Nonisothermal Systems

      Flow Around   a Cylinder
                            A cylinder  in  a stationary  fluid  of  infinite  extent  does  not admit  a steady-state  solution.
                            Therefore  the Nusselt  number  for  a cylinder  does  not  have  the  same  form  as  that  for  a
                            sphere. Whitaker recommends  for the mean Nusselt  number 4
                                                                            IIL  \  1 / 4
                                                            1/2
                                                Nu m  =  (0.4 Re  +  0.06  Re2/3  04            (14.4-7)
                                                                        )Pr (  ^ J
                                                        5
                                                                                  j
                            in the range  1.0  <  Re <  1.0  X 10 , 0.67 <  Pr  <  300, and  0.25  < ^/>o  <  5.2. Here, as in
                            Eq. 14.4-6, the values  of viscosity and  thermal conductivity  in Re and  Pr are those at  the
                            approaching  stream  temperature.  Similar  results  are  available  for  banks  of  cylinders,
                            which are used  in certain types  of heat exchangers. 4
                                                5
                                Another  corelation,  based  on  a curve-fit  of McAdams'  compilation  of heat  transfer
                                         6
                            coefficient  data,  and on the low-Re asymptote in Problem  12B.6, is
                                                         2/3
                                   =  (0.376Re 1/2  +  0.057Re )Pr 1/3  0.92  l                  ,1/3
                               Nu m                                              4.18Re
                                                                                                (14.4-8)
                            This correlation has the proper behavior in the limit that Pr  —» <», and  also behaves prop-
                            erly  for  small values  of the Reynolds number.  This result  can be used  for  analyzing  the
                            steady-state  performance  of  hot-wire  anemometers,  which  typically  operate  at  low
                            Reynolds numbers.


       Flow Around  Other  Objects
                            We learn from  the preceding three discussions that, for the flow around  objects  of shapes
                            other  than  those  described  above,  a  fairly  good  guess  for  the  heat  transfer  coefficients
                            can be obtained by using the relation
                                                                           J / 3                (14.4-9)

                            in which  Nu, W/0 is the mean  Nusselt  number  at zero  Reynolds  number.  This  generaliza-
                            tion, which  is shown  in Fig. 14.4-2, is often  useful  in estimating the heat transfer  from  ir-
                            regularly shaped  objects.




                                  2.0

                                  1.5  -  Cylinders  (Eq. 14.4-8)

                                                  Flat plates (Eq. 14.4-2)  _
                                  1.0  -

                                  0.5
                                         \                              Fig. 14.4-2.  Graph comparing the
                                         Spheres (Eq. 14.4-5) and  Eq. 14.4-9  Nusselt numbers for flow around flat
                                        _ j    |    |    |    i         plates, spheres, and cylinders with
                                   0.1        10   100  10 3  10 4  10 5  Eq. 14.4-9.




                                5
                                 W. E. Stewart  (to be published).
                                6
                                 W. H. McAdams, Heat Transmission, 3rd edition, McGraw-Hill, New  York (1954), p. 259.
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