Page 87 - Adsorption Technology & Design, Elsevier (1998)
P. 87

84  Rates of  adsorption of  gases and vapours by porous media


            uptake of adsorbate by an adsorbent particle when only a small step change
            in adsorbate  concentration is introduced  to the particle periphery includes
            unsteady state balances for both mass and heat transfer. The transient mass
            balance is

               1  a  [r2Dcaql  =  aq
                                                              (equation (4.17))
              r 2  ar  ~   ---~-r]   cOt
            with the average adsorbed phase concentration given by
                       re
              0 =  _.-25   qr 2 dr                             (equation 4.21))
                   rc   0
            The unsteady state heat transfer equation is

                      d o   dT
                        =  ~  + ha (T--  Tg)                            (4.36)
               (-AH)-d~   Cs dt
            in  which  c~  represents  the  heat  capacity  of  the  solid  porous  adsorbent
            particle.  Note  that  equation  (4.36)  is an  ordinary  differential  equation  (as
            opposed  to a partial differential  equation)  because  the temperature within
            the particle  depends  only on the average  adsorbed  phase  concentration  in
            the particle, the temperature being uniform throughout the particle because
            all the heat transfer resistance is external to the particle. At the surface of the
            crystal a linear equilibrium relationship is assumed to exist

                q--qo
                       =l+laq*l    [T--T~     atr-rc                   (4.37)
                                 ]  ~ Tqoo -- qo
               q~ -- qo     ~ ]  a p
            where qo and  To are the initial values of the adsorbed phase concentration
            and  the  temperature,  respectively,  and  qoo  is  the  final  adsorbed  phase
            concentration  after  adsorption  has  ceased.  The  term  (Oq*/aT)p  is  the
            gradient  of  the  equilibrium  isobar  for  the  essentially  constant  partial
            pressure  at which the small step change in concentration occurs. Boundary
            conditions apposite to this problem as it has been posed are
               aq/ar = 0  at r = 0  for all t -> 0            (equation (4.18))

            and
               q=0   att=0   forallr>--0                                (4.38)
            The  solution  to  the  above  set  of equations,  commencing with the restated
            equation (4.18) through to equation (4.38), is given in a paper by Ruthven et
            al.  (1980).  The  principal  features  of  the  uptake  curves  are  illustrated  by
            Figure  4.7.  Two  parameters  ),  (=  har~2/csD~) and  S  (=  AH  (aq*/aT)/c~)
            are  required  to  describe  the  behaviour  of  the  solution.  The  symbol  c~
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