Page 73 - Adsorption Technology & Design, Elsevier (1998)
P. 73

70  Rates of adsorption of gases and vapours by porous media


            poor correlation at low Re may well arise because of the inherent assumption
            of a uniform interface boundary condition leading to errors in the evaluation
            of the  thermal  conductivity  Af. From  the  analogy  between  heat  and  mass
            transfer  due  to  Chilton  and  Colburn  (1934)  implying that  the j  factors  for
            heat  (jH)  and mass  (jD) transfer are numerically equal,  another correlation
            frequently used is
              jH = (h/cflt) (Cf~//~f)  0"66  "-  (0.458/e) (Re) ~       (4.8)

            Heat generated by the adsorption of a component in the gas or liquid phase
            by the porous solid has to be transported not only between solid and fluid in
            an operating column, but is subsequently dissipated by transport  from fluid
            to vessel wall and thence to the surrounding environment. A correlation due
            to Leva (1949) may be used to assess the resistance to heat transfer between
            fluid  and  vessel  wall.  A  film  heat  transfer  coefficient  estimated  from  a
            correlation  described  by  McAdams  (1954)  enables  the  evaluation  of heat
            transfer resistance from the vessel wall to the surroundings.


            4.2.2   Diffusion in porous materials
            Adsorption  is  a  surface  phenomenon,  so  that  the  more  surface  that  is
            available  for adsorption  the greater is the capacity of the adsorbent  for the
            adsorbate.  Hence,  as  discussed  in  Chapter  2,  adsorbents  have  maximum
            ability  to  adsorb  when  the  internal  structure  of these  materials  is porous,
            thus allowing access of adsorbate molecules to the largest amount of internal
            surface. The total mass flux due to an adsorbate entering a porous structure
            is the  sum of fluxes due  to gaseous  diffusion  (Maxwellian  and/or  Knudsen
            diffusion, depending on the pore radii), convective diffusion (occasioned by
            the displacement of one molecular species by another), surface diffusion (in
            which  molecules  are  transported  across  a  surface  rather  than  through  the
            gaseous  phase  contained  by  the  pores  of  the  material)  and  viscous  flow
            (usually  negligible  for  physical  adsorption  when  there  is  only  a  small
            pressure gradient along pores).


            Maxwellian and Knudsen diffusive fluxes
            In pores  of diameter  much  greater  than  the  mean  free path  of a molecule,
            diffusion  occurs by a process of molecular collisions in the gas phase within
            the pore (Maxwellian or bulk diffusion) but, if the molecular mean free path
            is  much  greater  than  the  pore  diameter,  diffusion  occurs  by  molecules
            colliding  with  the  pore  walls  (Knudsen  diffusion).  Both  of these  transport
            processes  occur  with  a  decreasing  concentration  gradient  and  may  be
            described  by means of Fick's law of diffusion with an appropriate  diffusion
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