Page 675 - Bird R.B. Transport phenomena
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Problems  655

                    in which  Cj and c u  are the concentrations of A  in phases  I and  II, and  2), and  2),, are the corre-
                    sponding diffusivities.  The initial and boundary conditions are:
                     I.C.I:                  atf=O,           c, =  cf                 (20D.2-3)
                     I. C. 2:                at t  = 0,      c u  = c° u               (20D.2-4)
                    В.  С 1 :                at z  = 0,      c  = mc                   (20D.2-5)
                                                              u    }
                    B.C. 2:                  atz  = 0,   -%  ^  = -% ^                 (20D.2-6)
                                                                    {
                    В. С  3:                 at z  = -  oo,   C |  = c?                (20D.2-7)
                    В. С  4:                 at z  = + oo,   Cll  = c° n               (20D.2-8)

                    The first boundary  condition at z  = 0 is the statement  of equilibrium at the interface, m being
                    the  "distribution  coefficient"  or "Henry's  law constant."  The second  boundary  condition  is a
                                                                                 +
                    statement  that the molar  flux  calculated at z  = 0~ is the same as that at z = 0 ; that is, there is
                    no loss of A at the liquid-liquid  interface.
                    (a)  Solve the equations  simultaneously  by  Laplace  transform  or other  appropriate  means to
                    obtain:

                                                                                       (20D.2-9)

                                                                                      (20D.2-10)


                    (b)  Obtain the expression  for  the mass transfer  rate at the interface.
              20D.3.  Critical size  of  an  autocatalytic system.  It is desired  to use the result  of  Example  20.1-3 to dis-
                    cuss  the critical size of  a system  in which  an "autocatalytic reaction" is occurring. In such a  sys-
                    tem  the reaction products increase  the rate  of  reaction.  If  the ratio  of  the system  surface  to the
                    system  volume is large, then the reaction products tend to escape from the boundaries  of the sys-
                    tem.  If the surface  to volume ratio is small, however,  the rate of escape may be less than the rate
                    of  creation, and the reaction rate will increase rapidly.  For a system  of a given shape, there will
                    be a critical size for which the rate of production just equals the rate of removal.
                        One example  is that of  nuclear fission.  In a nuclear pile the rate of  fission  depends on the
                    local neutron concentration. If neutrons are produced at a rate that exceeds  the rate of  escape
                    by  diffusion,  the reaction is self-sustaining  and a nuclear explosion  occurs.
                        Similar  behavior  is  also  encountered  in  many  chemical  systems,  although  the  behavior
                    here  is  generally  more  complicated.  An  example  is  the thermal  decomposition  of  acetylene
                    gas, which  is thermodynamically unstable according to the overall reaction.
                                              H - C  =  C - H ^ H  2  + 2C             (20D.3-1)

                    This  reaction appears  to proceed  by  a branched-chain, free-radical  mechanism, in which  the
                    free  radicals behave  qualitatively  as  the neutrons in the preceding paragraph, so that the de-
                    composition is autocatalytic.
                        However,  the free  radicals  are effectively  neutralized  by  contact with  an iron surface,  so
                    that  the  free-radical  concentration is  maintained  near  zero  at  such  a  surface.  Acetylene  gas
                    can  then  be  stored  safely  in  an  iron  pipe  below  a  "critical"  diameter,  which  is  smaller  the
                    higher  the pressure  or temperature  of  the gas.  If the pipe  is  too large,  the formation  of  even
                    one free  radical is likely to cause a rapidly  increasing rate of decomposition, which may  result
                    in a serious  explosion.
                    (a)  Consider a system  enclosed  in a long cylinder  in which the diffusion  and reaction process
                    is described  by
                                                                                         --
                                              %Н(%)«<*                                (20D 3 2)
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