Page 421 - Bird R.B. Transport phenomena
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Problems  403

                   themselves  at a reasonably  steady  temperature. Let the temperature in the ground  be  T(y, t),
                   where у  is the depth below  the surface  of  the earth and  t is the time, measured  from  the time
                   of  maximum  temperature  T . Further, let the temperature  far  beneath the surface  be  T^, and
                                          o
                   let the surface  temperature be given by
                                       7X0, t) -  Т  = 0            for  t < 0
                                               ж
                                       T(0, t) -  T x  = (T  -  T )  cos  <ot  for  t >  0  (12C.5-1)
                                                        x
                                                    o
                   Here (o = 2ir/t , in which t  is  the time  for  one full  cycle  of  the oscillating  temperature—
                                           per
                               peT
                   namely, 24 hours. Then it can be shown  that the temperature at any depth is given by


                                                                                      (12С.5-2)

                   This equation is the heat conduction analog  of  Eq. 4D.1-1, which  describes  the response  of the
                   velocity  profiles  near an oscillating  plate. The first  term describes  the "periodic  steady  state"
                   and  the second  the  "transient"  behavior.  Assume  the following  properties  for  the soil: 8  p =
                            3
                   1515 kg/m ,  к = 0.027 W/m  •  K, and C p  = 800 J/kg  •  K.
                   (a)  Assume that the heating  of  the earth's  surface  is  exactly  sinusoidal,  and  find  the ampli-
                   tude  of  the temperature variation  beneath the surface  at a distance y. To do this, use  only the
                   periodic  steady  state  term in  Eq.  12C.5-2. Show  that at a depth  of  10 cm, this amplitude  has
                   the value  of 0.0172.
                   (b)  Discuss  the importance  of  the transient  term in Eq. 12C.5-2. Estimate the size  of  this con-
                   tribution.
                   (c)  Next consider an arbitrary  formal  expression  for  the daily  surface  temperature, given as a
                   Fourier series  of the form

                                           '  '  °°  =  2  (я„ cos ritot  + b  sin ntot)  (12C.5-3)
                                                                   n
                                            -
                                          i 0  1 K  n =0
                   How many terms in this series  are used  to solve part (a)?
             12C.6.  Heat transfer  in  a falling  non-Newtonian  film.  Repeat Problem  12B.4  for  a polymeric  fluid
                   that is reasonably  well described  by the power  law  model  of  Eq. 8.3-3.
             12D.1.  Unsteady-state heating  of  a slab  (Laplace transform method).
                   (a)  Re-solve  the problem  in  Example  12.1-2 by  using  the Laplace  transform,  and  obtain  the
                   result  in Eq. 12.1-31.
                    (b)  Note that the series  in  Eq.  12.1-31  does  not converge  rapidly  at short  times.  By  inverting
                   the  Laplace  transform  in  a  way  different  from  that  in  (a), obtain  a  different  series  that  is
                   rapidly  convergent  for  small  times. 9
                    (c)  Show  how  the first  term  in the series  in  (b) is  related  to the "short  contact time"  solution
                   of Example  12.1-1.
             12D.2.  The Graetz-Nusselt problem  (Table 12D.2).
                    (a)  A  fluid  (Newtonian or generalized  Newtonian) is in laminar flow in a circular  tube  of  ra-
                   dius R. In the inlet region z <  0, the fluid temperature is uniform  at T v  In the region z >  0, the
                   wall  temperature  is  maintained  at  T . Assume  that  all  physical  properties  are  constant  and
                                                 o


                        W.  M. Rohsenow, J. P. Hartnett, and  Y.  I. Cho, eds., Handbook of Heat  Transfer, 3rd  edition,
                       8
                    McGraw-Hill  (1998), p. 2.68.
                       9
                        H. S. Carslaw  and J. C. Jaeger, Conduction of Heat  in Solids, 2nd edition, Oxford  University  Press
                    (1959), pp.  308-310.
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