Page 63 - Adsorption Technology & Design, Elsevier (1998)
P. 63

60  Fundamentals  of  adsorption  equilibria


            where  (~is Xis) is the product of mole fraction Xis and the activity coefficient
            ~'is of component i in the adsorbed phase solution.
              Substitution  of ]-/is (T~/~i)  into  equation  (3.45)  for  a  component  i in  the
            vacancy solution thus yields

              ~is(T~ ~)  -  ~0 s(T)  +  RgT In (~tisXis) +  ~/~i       (3.47)

            Equilibrium  between  the  two  vacancy  solutions  in  the  gas  and  adsorbed
            phases demands that pig -  lais and so, from equations (3.43) and (3.47),
              fiyiP/(Ti~xis)-  exp  {(/l~ - ll~   exp  (rrAi/RgT)      (3.48)

            Equation  (3.48) relates the mole fraction yi of component i in the gas phase
            to the mole fraction xis in the adsorbed phase. The latter is based on the total
            number of moles of the adsorbed vacancy solution. To interpret experimen-
            tal data an expression is required relating the experimentally measured mole
            fraction  of  component  i  in  the  adsorbed  phase,  x~,  to  the  corresponding
            vacancy solution  quantity xi. For  components  i  =  1, 2 the  equation  is x~s -
            XieO where  0  is  the  ratio  of  the  total  number  of moles  nTs in  the  vacancy
            solution to the total number of moles nre adsorbed as measured experiment-
            ally. The mole fraction of vacancies in the vacancy solution is then Xvs =  (1 -
            0). Substitution of xis in equation (3.48) gives
                   =     e0
              r      (Tisxi  ) exp {(p~176    exp (rrfi~i/RgT)         (3.49)
            All of the terms on the right-hand side of equation  (3.49) may be obtained
            from pure component adsorption data. As the equation is valid for the whole
            range  of  concentrations,  it  is  therefore  also  applicable  at  infinite  dilution
            when r  7i, ~'is and xie are unity and the spreading pressure is zero. For such
            conditions

              exp {(/l~ -  I~~   -  P/O                                (3.50)

            and  so may be  found  from single-component  data  at  low coverages where
            the  isotherm  is linear.  The  partial  molal  area A  may  also be  computed  by
            means  of  the  integrated  form  of  the  Gibbs  adsorption  isotherm  given  by
            equation  (3.28).  Fugacity  and  activity  coefficients,  however,  are  found  by
            somewhat tedious fitting of experimental data to an idealized isotherm such
            as that of Langmuir. Multiplication  of the Langmuir equation by a function
            containing  one  or  more  parameters,  only  found  by  regression,  then
            correlates  equation  (3.49) with single-component  data  and, after a number
            of iterations, gives values for r  and 7i. The VSM theory, although based on
            fundamental principles, is thus semi-empirical.
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