Page 91 - Adsorption Technology & Design, Elsevier (1998)
P. 91

88  Rates of adsorption of gases and vapours by porous media


            (such as helium) across one face of the adsorbent material fabricated into a
            cylindrical shape and sealed within the cell. A steady stream of pure inert gas
            is allowed  to  pass  through  the  detector  volume  at  the  obverse  face  of the
            pellet  where  a  thermistor  detects  the  response  signal  arising  from  the  gas
            diffusing  through  the  pellet  from  the  original  input  pulse.  Gaskets  ensure
            that  no  gas  passes  through  to  the  detector  volume  except  by  diffusion
            through the pellet.  An unsteady state material balance for the adsorbate  in
            the direction z yields
                  c3c     t3q     c32c
               8p  ~   + pp   = D~
                          t3t     ~Z 2                                 (4.40)
            where  ep  and  pp  are  the  porosity  and  density  of  the  adsorbent  pellet,
            respectively.  The  net  rate  of  adsorption  may  be  represented  by  the
            difference in rates of adsorption and desorption


               aq  = ka (c-q/K)                                         (4.41)
               at
            where  k~ is the  adsorption  rate  constant  and  K  the  adsorption  equilibrium
            constant. At the face of the pellet there is a pulse input of adsorbate which is
            represented by
               z = 0   c = m t~ (t)                                     (4.42)
            where m is the magnitude of the concentration pulse and d; (t) is the Dirac delta
            function. Within the detector perfect mixing is assumed, so if the cross-sectional
            area of pellet is S and its volume is V the diffusive flux at the obverse face is

              z = L,  De (OC/aZ)z=L =-  (V/S) (OCL/Ot)                  (4.43)
            The initial condition, when the pulse is admitted to the pellet face, is
               t=0    c=0   foraUz>-0                                   (4.44)
            It is unnecessary to solve the above set of equations in the form c (t) because
            the  first  absolute  moment  of  the  experimentally  measured  response  curve
            (see Figure 4.10)  can be related,  by means of Laplace  transformation,  to the
            parameters D~, ep, K  and  V/SL. If a number of adsorbent pellets of differing
            length are each subjected to the same magnitude of concentration impulse then
            a plot of the first absolute moment (corrected for dead volume and the finite
            time of injection) against V/SL yields a straight line of slope 1/D~ and intercept
            -  ep/2, the latter quantity also being determined independently by pyknometry.
            For details of the technique of moments analysis the reader should consult a
            text  such  as  Wen  and  Fan  (1975).  Figure  4.10  illustrates  the  type  of  input
            concentration pulse often used for this method and the corresponding output
   86   87   88   89   90   91   92   93   94   95   96