Page 603 - Bird R.B. Transport phenomena
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§19.1  The Equations of Continuity for  a Multicomponent Mixture  583


                 rate  of removal  of mass  of                                       (19.1-3)
                 a  across  face  at x  +  Ax
                 rate  of production of  mass  of  r &x Ay  Az                       (19.1-4)
                                                   a
                 a  by  chemical reactions
                 The  combined  mass  flux  n  includes  both  the  molecular  flux  and  the  convective  flux.
                                        ax
                 There  are  also  addition  and  removal  terms  in  the  у  and  z  directions.  When  the  entire
                 mass  balance is written down  and divided  by  Ax  Ay  Az, one obtains, after  letting the size
                 of  the volume  element decrease  to zero,


                                                                                     (19.1-5)
                               dt
                 This  is  the equation of continuity for species  a  in a multicomponent reacting mixture. It de-
                 scribes  the change  in mass  concentration of  species  a  with  time at a fixed  point in  space
                 by  the  diffusion  and  convection  of  a,  as  well  as  by  chemical  reactions  that produce  or
                 consume a. The quantities n ,  n ,  n  are the Cartesian components of the mass flux  vec-
                                         ax  ay  az
                 tor n a  = p v  given  in Eq. (D) of Table 17.8-1.
                         a a
                     Equation  19.1-5 may be rewritten  in vector notation as
                                                            =  1, 2, 3,              (19.1-6)

                 Alternatively  we  can use  Eq. (S) of Table  17.8-1 to write


                                     -(V-p v) -  (V • U +  r  a  =  1, 2, ,..., N    (19.1-7) 1
                                                                      3
                                dt         e             a
                               rate of  net rate of  net rate of  rate of
                               increase addition  addition  production
                               of mass  of mass of  of mass of  of mass of
                               of A per A per unit  A per unit  A per unit
                               unit  volume by  volume by  volume by
                               volume  convection  diffusion  reaction
                 Addition  of  all  N equations in either Eq. 19.1-6 or 7 gives

                                                                                     (19.1-8)

                 which  is the equation of continuity for  the mixture.  This equation is identical to the equation
                 of continuity for  a pure  fluid  given  in Eq. 3.1-4. In obtaining  Eq. 19.1-8 we  had  to use Eq.
                 (J) of Table  17.8-1 and also the fact that the law  of conservation  of  total mass gives X r  =
                                                                                       a a
                 0. Finally we  note that Eq. 19.1-8 becomes
                                                  (V • v)  = 0                       (19.1-9)

                 for  a  fluid mixture  of constant mass density p.
                     In the preceding  discussion  we  used  mass  units. However,  a corresponding  deriva-
                 tion  is  also  possible  in  molar  units.  The  equation  of  continuity  for  species  a  in  molar
                 quantities  is

                                      ?  =  -(V-N )       a  = 1,2,3   N             (19.1-10)
                                     dt         a



                      J. Crank, The Mathematics  of Diffusion,  2nd edition, Oxford  University  Press  (1975).
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