Page 60 - Partition & Adsorption of Organic Contaminants in Environmental Systems
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ISOSTERIC HEAT OF ADSORPTION    51

              The isosteric-heat data describe how sensitively the molar heat of adsorp-
            tion of a vapor or a solute varies with the amount adsorbed by a solid. To
            determine the isosteric heat of adsorption at a given Q (say, Q A in Figure 4.3),
            one accounts for the variation of P (or C e) with T at a fixed Q using the general
            form of the Clausius–Clapeyron equation:

                                d log  P  D H d      -D H a
                                      =          =                        (4.14)
                                 dT      . 2 303 RT  2  . 2 303 RT  2

            or


                                      d log  P  -D H d
                                             =                            (4.15)
                                      d 1 (  T)  . 2 303 R

            Similarly,

                               d log  C e  D H d     -D H a
                                       =          =                       (4.16)
                                 dT      . 2 303 RT 2  . 2 303 RT  2

            or

                                      d log C e  -D H d
                                             =                            (4.17)
                                      d 1 (  T)  . 2 303 R

            where  DH d is the molar heat of desorption and  DH a  is the molar heat of
            adsorption (DH d =-DH a  ). By repeating the calculations for DH a  at other fixed
                                    on Q can then be determined. For vapor or solute
            Q, the dependence of DH a
                               should have the largest negative value (i.e., the molar
            adsorption, the DH a
            exothermic heat) at the lowest Q and hence the smallest negative value at the
            highest Q. As stated before, if the adsorbed vapor forms a condensed phase
                                   should be more exothermic than the molar heat of
            on the adsorbent, the DH a
            vapor condensation (i.e., -DH evap or -DH sub ). Similarly, if the adsorbed solute
            displaces the solvent to form a separate phase on the adsorbent surface, D H a
            should be more exothermic than the reverse molar heat of solute solution (i.e.,
            -DH sol ). When the adsorption reaches the maximum on an adsorbent, the net
                                              is equal to the heat of adsorbate con-
            adsorption heat is zero and thus DH a
            densation. In systems where the adsorption energy is not high enough to con-
            dense the vapor into a separate phase or to condense the solute by displacing
            the solvent, the adsorption will be weak. In this case, the thermicity of adsorp-
            tion would be small and notably less exothermic than the heat of adsorbate
            condensation. However, as long as a net adsorption occurs, the system will
            nevertheless exhibit an exothermic effect, despite the fact that it may be very
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