Page 47 - Adsorption Technology & Design, Elsevier (1998)
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44  Fundamentals of adsorption equilibria


            equals the heat of liquefaction. Neither of these assumptions is strictly valid,
            but despite such difficulties, the BET equation has been widely applied as a
            semi-empirical  tool  for  the  investigation  of  the  characteristics  of  porous
            adsorbents.  By appropriate choice of c and qm the equation can be made to
            fit any of the  isotherm  types  II  to V  inclusive.  For  small values  of plp~ the
            BET equation reduces to the Langmuir equation.  A  typical BET plot (with
            volume  v  replacing  q  as  explained  in  Section  3.3.1)  displaying  a  distinct
            intercept  and  slope  from  which  the  surface  area  of the  adsorbent  may  be
            estimated is shown in Figure 3.6.



            3.3.5   Polanyi's Potential Theory
            The Potential Theory as originally conceived by Polanyi is well documented
            in  the  classic  text  by  Brunauer  (1943).  Polanyi  considered  contours  of
            equipotential  energy  above  solid  surfaces  and  ascribed  a  volume  ~bi to  the
            space  between  the  ith equipotential  surface  of energy e  and  the  adsorbent
            surface. The potential  e was assumed to be independent  of temperature  so
            that e = f(~b) is essentially an isotherm equation. The adsorption potential is
            defined  as  the  work  of  compression  of  the  gas  from  a  pressure  p  to  the
            saturation pressure ps. For one mole of a perfect gas of volume v in an open
            thermodynamic system the adsorption potential is therefore
                    P,
              e =   ~  v  dp = RgT ln(ps/p)                            (3.18)
                    P


            assuming that  the  work  of creating  a  liquid  surface  is small  in comparison
            with the magnitude of e. The volume in the adsorption space is

              ~=nVm                                                    (3.19)
            where n is the number of moles adsorbed per unit mass of adsorbent and Vm
            is the molar volume.  By plotting  e  as a function  of ~b a characteristic curve
            ~e)  is obtained which represents, for a given adsorbate-adsorbent  system,
            the extent of adsorption at any relative pressure and temperature below the
            critical temperature  of the gas. The validity of the characteristic curve may
            be  extended  for application  to non-ideal  gases and vapours by substituting
            fugacities, f, for partial pressures.
              Two  different  applications  of the  potential  theory,  one  for  microporous
            solids and the other for adsorbents with larger pores, have been formulated
            and  will  now  be  briefly  considered.  Dubinin  (1960)  related  the  volume  v
            adsorbed  in  micropores  to  the  adsorption  potential.  Earlier,  Dubinin  and
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