Page 381 - Bird R.B. Transport phenomena
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Problems  363

                                                                   3
                                                                                2
                    for methane are: a = 2.322 cal/g-mole -K,b  = 38.04 X 1СГ  cal/g-mole • K , and с = -10.97 X
                    10~  cal/g-mole • K .
                                     3
                       6
                                                       2
                    Answers: (a) pT~  exp[-(b/R)T  -  (c/2R)T ] = constant;
                                  ll/R
                           (b) 270 atm
              11B.2.  Viscous heating in laminar tube flow (asymptotic solutions).
                    (a)  Show that for  fully  developed  laminar Newtonian flow in a circular tube  of radius  R, the
                    energy  equation becomes



                    if  the viscous  dissipation  terms are not neglected. Here v zmax  is  the maximum velocity  in the
                    tube. What  restrictions have to be placed on any solutions  of  Eq. 11B.2-1?
                    (b)  For the isothermal wall problem (T = T  at r = R for z > 0 and at z = 0 for all r), find  the as-
                                                       o
                    ymptotic expression  for  T(r) at large  z. Do this by  recognizing  that дТ/dz  will be zero at  large
                    z. Solve  Eq. 11B.2-1 and obtain





                    (с)  For the adiabatic wall problem (q  = 0 at r = R for  all z) an asymptotic expression  for large z
                                                  r
                    may be found  as follows: Omit the heat conduction term in Eq. 11B.2-1, and then average  the
                    remaining terms over  the tube cross  section, by  multiplying  by  rdr and then integrating  from
                    r = 0 to r = R. Then integrate the resulting  equation over z to get
                                                                 2
                                              (T)  -  T, = (4fjiV Z/max /pC R )z       (11B.2-3)
                                                                p
                    in  which  T} is the inlet  temperature at z  = 0. Postulate now that an asymptotic  temperature
                    profile at large z is of the form

                                                               2
                                             T-T }  = {4fjLV Z/max /pC R )z  + fir)
                                                             p
                    Substitute this into Eq. 11B.2-1 and integrate the resulting equation for/(r) to obtain


                                                                R)    2  \R

                    Keep in mind that the solutions in Eqs. 11B.2-2  and 5 are valid solutions only  for  large  z. The
                    complete solution for small z is discussed  in Problem 11D.2.

              11B.3.  Velocity  distribution  in  a nonisothermal  film.  Show  that  Eq.  11.4-20 meets  the  following
                    requirements:
                    (a)  At x  = 5, v z  = 0.
                    (b)  At x  = 0, dvjdx  = 0.
                                                      2
                    (c)  Urn v (x)  = ( g8 2  cos  p/2fjL )[l  -  (x/8) ]
                                  P
                                             0
                            z
              11B.4.  Heat conduction in  a spherical shell  (Fig. 11B.4).  A spherical shell has inner and outer radii
                    JR and R . A hole is made in the shell  at the north pole by  cutting out the conical segment in
                            2
                      1
                    the region 0 <  0 <  6 V  A  similar  hole is made at the south pole by  removing  the portion  (тг  -
                     6^)  <  в ^  77. The surface  9 = 6^  is kept at temperature T = T  and the surface  at в  = тг  -  в  is
                                                                      v                        }
                    held  at  T  =  T .  Find  the  steady-state  temperature distribution,  using  the  heat conduction
                                2
                    equation.
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