Page 79 - Adsorption Technology & Design, Elsevier (1998)
P. 79

76  Rates of adsorption of gases and vapours by porous media


            The  set  of equations  (4.17)  to  (4.21)  inclusive  was  solved  analytically  by
            Ruckenstein et al. (1971) who compared the mass of adsorbate adsorbed at a
            given  time,  mt, with  the  amount  adsorbed  after  an  infinite  lapse  of time,
            moo, (when  the  crystals  were  saturated  with  adsorbate).  They  expressed
            the  ratio mt[m~, as a function of time  t. It should be noted  that, for small
            quantities of adsorbate introduced to the system the adsorption isotherm is
            linear and q  = Kp. The  intercrystalline diffusivity can then be regarded  as
            independent  of  adsorbate  concentration.  The  theoretical  fractional  ap-
            proach to equilibrium was shown to be

                                   __1  (n2tr2Dct  .
                                                ~
                                               I
                  Z
               mt  _1_~  6_~ _
               moo             ,,=l  n 2exp  --   rc   ]               (4.22)
            When  the fractional uptake  is greater  than 70%, only the first term of the
            summation is retained.  When,  on  the  other  hand,  the  fractional  uptake  is
            less than 30%
               mt-6(   Dot ),/5
                  -                                                    (4.23)
               mm      7rre 2
            is a good approximation.
              The  intracrystalline  diffusion  coefficient  Dc was considered  to  be  inde-
            pendent  of adsorbate  concentration  in  the  above  analysis of Ruckenstein
            et al. (1971).  However,  if the  initial  quantity of adsorbate  admitted  to  the
            adsorbent  is  such  that  the  vapour  phase  concentration  does  not  remain
            constant, then account should be taken of the variation of the intracrystal-
            line  diffusivity  with  concentration.  This  dependence  of  diffusivity  on
            concentration  may be derived  by equating the Fickian flux to the  thermo-
            dynamically defined flux, the latter depending on the product of concentra-
            tion and the gradient of chemical potential.  It then follows (Ruthven  1984,
            Yang  1987) that  the  diffusion  coefficient  is  related  to  adsorbed  phase
            concentration by the equation

               Dc = Do d In p/d In q                                    (4.24)
            in  which  Do  is independent  of concentration.  If the  adsorbate-adsorbent
            system obeys a Langmuir relation then
               De = Do/(1 - (q/qm))                                     (4.25)

            The diffusion equation is then written
               Oq  _DoO{   i   r 20q}
                                                                        (4.26)
                Ot  -  P  Or  1-(q/qm))  Or
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