Page 169 - Adsorption Technology & Design, Elsevier (1998)
P. 169

Design procedures  157


            the  differential  heat  and  mass  balance  equations  for  the  individual  com-
            ponents.  The  analysis  becomes  even  more  complex  when  the  rate  of
            adsorption of any individual species is affected by the presence of the others.
            This  could  arise,  for  example,  when  individual  diffusion  coefficients  are
            found to be functions of composition. Clearly the complexity and hence the
            degree  of difficulty  in obtaining  solutions  for  the  MTZ  and  breakthrough
            curve  increase  rapidly  as  the  number  of components  increases.  Very  few
            analytical solutions are available and therefore considerable research effort
            has  been  directed  at  the  simultaneous  numerical  solution  of  the  set  of
            coupled  heat  and  mass balance  equations,  the  set of rate  expressions,  and
            the  set  of equilibrium  expressions,  all being subject  to  a  set  of initial  and
            boundary conditions.
              Consider  the  case  when  the  flow  pattern  can  be  assumed  to  be  axially
            dispersed plug flow. By not making the assumption that the system is dilute,
            the differential fluid phase material balance for each component is given by:

                        +        +     + pp ~---~-]  -~  - =  0         (6.37)
               -DL  OZ 2    OZ      Ot            Ot
            The  particle  phase  mass  balance  which  provides  the  adsorption  rate
            equation for each component may be written in generalized form as follows:

              -----  = f(q~, qj ....  ct, cj...)             '          (6.38)
                0t
            Rather than being a simple algebraic expression, the function fis more likely
            to  represent  a  set  of  diffusion  equations  with  their  associated  boundary
            conditions.  The  continuity  equation  must  also  be  satisfied,  and  so  in  the
            general case the mass balance equations may not all be independent. When
            the process cannot be considered to be isothermal, then energy balances for
            both the element of packed bed (equation (6.39)) and the adsorbent particle
            (equation (6.40)) are also required:


              -            ~       +       Cs    + cf                   (6.39)
                kL-LU                                 0;


                                             (TI-  rw)
               =            (- AHi)  -~   ed
                          t
                 aTsat               Z   (- an~) ,~,~
              c~       Rp3h  (T f-  Ts) =
                       ~                        Ot                     (6.40)
                                       i
            The response to a change in inlet conditions will generate a set of (n-l) mass
            transfer  zones  which  propagate  through  the  column  when  there  are  n
   164   165   166   167   168   169   170   171   172   173   174