Page 149 - Adsorption Technology & Design, Elsevier (1998)
P. 149

138  Design procedures


            regenerated to a residual loading of q0 then it would be necessary to replace
            the  right-hand  side  of  equation  (6.2)  by  M  (q-qo).  After  contacting,  the
            equilibrium is given by:
              q  = Kcf                                                  (6.3)

            Simultaneous  solution  of  equations  (6.2)  and  (6.3)  gives  the  mass  of
            adsorbent required to effect the purification:

              M =  ~    -- 1                                             (6.4)


            This equation shows that the mass of adsorbent required can be reduced if an
            adsorbent  with a higher equilibrium  constant  can be found.  Equation  (6.2)
            can be rearranged to give a linear relationship between q and cf:

                  V
              q  -  --~ (co-  cf)                                        (6.5/

            If the adsorbent were not initially free from the impurity at the start of the
            adsorption process then the linear relationship would be:
                  V
              q = -7: (co- cf) + qo                                      (6.6)
                  M

            The  simultaneous  solution  to  equations  (6.3)  and  either  (6.5)  or  (6.6)  can
            be  found  graphically,  as  shown  in  Figure  6.2  (a)  and  (b),  respectively.
            Whether  or  not  an  analytical  solution  can  be  found  in  the  case  of a  non-
            linear  isotherm  depends  on  the  shape  of  the  isotherm.  If  an  analytical
            solution  is  not  possible  then  the  solution  may  be  found  graphically  as
            shown in Figure 6.2 (c).
              Powdered or granular adsorbents  are usually added to a process in slurry
            form  in  such  a  way  as  to  allow  adequate  dispersion  and  mixing.  The
            adsorbent  can  be  removed  as  a  settled  sludge.  When  large  quantities  of
            adsorbent  are  required  consideration  should  be  given  to  using  a  multiple
            batch or cross-flow system. For example, one way of reducing the amount of
            adsorbent required is to carry out the batch processing in two steps, as shown
            in Figure 6.3. Here the total amount of adsorbent is split arbitrarily into two
            parts M1 and M2. The feed is first contacted with a fresh batch of adsorbent
            and the impurity concentration is reduced to Cl. After separation of the fluid
            from the adsorbent in the first stage the fluid is contacted with a further fresh
            batch  of  adsorbent.  In  multibatch  systems  each  subsequent  batch  of
            adsorbent  removes  less  and  less  impurity  as  the  impurity  concentration
            decreases.
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