Page 93 - Adsorption Technology & Design, Elsevier (1998)
P. 93

90  Rates of adsorption of gases and vapours by porous media


            4.3.2   Gravimetric measurements
            As  gas  or  vapour  is  adsorbed  by  an  adsorbent  so  its  weight  gradually
            increases until the adsorbent is saturated. Thus if an adsorbate is admitted to
            an adsorbent and  the increase in weight of the  adsorbent is measured as a
            function  of  elapsed  time,  the  uptake  curve  can  be  used  to  measure  the
            diffusion  coefficient  by  matching  the  curve  obtained  with  the  theoretical
            uptake  curve  described  by  equation  (4.22).  Provided  the  experimental
            conditions are such that isothermal conditions are maintained and the total
            quantity of gas adsorbed up to the time when the adsorbent is saturated in
            comparison with the amount of adsorbate remaining in the gas phase is small
            (essentially constant adsorbate concentration), then equation (4.22) may be
            used  to  estimate  the  effective  diffusion  coefficient  for  the  adsorbate
            -adsorbent pair. The gravimetric balance described by Gunn et al. (1974) for
            the  adsorption  of  water  vapour  by  porous  polyurethane  materials  is  a
            suitable description of the construction and operation of the apparatus and
            also the method of curve fitting used to extract the diffusion coefficient from
            the experimental uptake curve. The form of the curve in the example cited
            differs from equation  (4.22) because of the hollow cylindrical shape of the
            sample  used  which  results  in  radial  as  well  as  longitudinal  diffusion
            coefficients  being  a  property  of  the  system.  Commercially  available
            gravimetric balances are also available which are suitable for experiments of
            this type. When interpreting results from gravimetric measurements involv-
            ing crystalline  adsorbents,  the  portion  of  the  uptake  curve  which  is  most
            suitable  for  matching  with  equation  (4.22)  is  when  0.2  <  mt/m~  <  0.5.
            This is because the initial uptake is sensitive to interparticle transport resis-
            tance  while portions  of the  uptake  curve at values of mt/m~  <  0.5  may be
            affected by heat transfer resistances.


            4.3.3   Nuclear magnetic resonance measurements
            Application of nuclear magnetic resonance (NMR) to the study of diffusion
            of  liquids  in  adsorbents  has  evolved  through  the  use  of  the  pulsed  field
            gradient (PFG) method originally developed by Stejskal and Tanner (1965
            and  1968)  who  measured  self-diffusion  coefficients  in  liquids.  In  this
            technique  a sample of the material to be investigated is placed in a pulsed
            magnetic  gradient  field.  Nuclear  spins  of  the  sample  are  then  excited  by
            means  of  a  radio  frequency  pulse.  Reversing  the  magnetic  gradient  field
            pulse  following  a  known  interval  of  time  produces  an  attenuation  of  the
            signal which is a direct measurement of the mean square distance travelled
            by the diffusing species in the time interval between the gradient pulses. The
            diffusion of n-hexane in zeolite crystals has been successfully studied using
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