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§12.2  Steady Heat Conduction in Laminar, Incompressible Flow  381

                                                                      Fig. 12.1-4o  Variation  of the fluid  tem-
                                                                      perature with time after  a sphere  of ra-
                                                                      dius R at temperature T  is placed in a
                                                                                         ]
                                                                      well-stirred  fluid  initially  at a tempera-
                                                                      ture T . The dimensionless parameter В
                                                                           o
                                                                      is defined  in the text following  Eq.
                                                                      12.1-50.  [H. S. Carslaw  and J. С  Jaeger,
                                                                      Conduction of Heat in Solids, 2nd edi-
                                                                      tion, Oxford  University Press (1959),
                                                                      p.  241.]






                                        0.04  0.08  0.12   0.16  0.20
                                                a s t/R 2


                           It can be  shown  that D(p) has  a  single  root at p  =  0, and  roots at  \fp k  = ib  (with  к =  1, 2,
                                                                                        k
                           3,...,  oo), where the b  are the nonzero roots  of tan b  = 3b /(3  + Bb\).  The Heaviside partial
                                             k
                                                                          k
                                                                      k
                           fractions expansion theorem  may now be used  with
                                                  4
                                               N(0)    1/3     N(p k )     IB               (12.1-59, 60)
                                                                                2
                                              D'(0)   1  + В   D'ty*)  9(1 +  B)  + B b\
                           to get
                                                                    exp  (-b r)
                                                             6B2          k                    (12.1-61)
                                                                             2 2
                                                                =i 9(1 + B) +  B b  k
                           Equation  12.1-61  is  shown  graphically  in  Fig.  12.1-4.  In this  result  the only  place  where  the
                                                                                           2
                           thermal diffusivity  of the solid  a s  appears is  in the dimensionless  time т = a t/R ,  so that the
                                                                                        s
                           temperature rise  of the fluid  can be used  to determine experimentally  the thermal  diffusivity
                           of  the solid. Note that the Laplace transform  technique allows  us  to get the temperature his-
                           tory  of the fluid  without obtaining the temperature profiles  in the solid.
      §12.2  STEADY HEAT CONDUCTION IN LAMINAR,
             INCOMPRESSIBLE FLOW
                           In the preceding discussion  of  heat conduction in solids, we  needed  to use  only  the en-
                           ergy  equation.  For problems  involving  flowing fluids,  however,  all  three  equations  of
                           change  are  needed.  Here we  restrict  the  discussion  to  steady  flow  of  incompressible,
                           Newtonian  fluids  with  constant  fluid  properties,  for  which  the  relevant  equations  of
                           change are:
                           Continuity                     (V  • v)  = О                        (12.2-1)
                           Motion                       p[v  • Vv]  =                          (12.2-2)
                           Energy                     pC (v-VT)  =                             (12.2-3)
                                                        p




                               4
                                A. Erdelyi, W. Magnus, F. Oberhettinger, and F. G. Tricomi, Tables of Integral  Transforms,  Vol.  1,
                           McGraw-Hill, New York  (1954), p. 232, Eq. 20; see also C. R. Wylie and  L. C. Barrett, Advanced Engineering
                           Mathematics,  McGraw-Hill, New York, 6th Edition (1995), §10.9.
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