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Adsorption                                                                                       469



            15.2.1.2.4  Thermodynamics                         values, with the latter appearing in the effluent of a GAC
            The effect of temperature on adsorption equilibrium is given  column, i.e., as a chromatographic effect (McGuire and
            by the van’t Hoff equation (Alberty and Silbey, 1992, p. 160),  Suffet, 1980, p. 102).


                             a ¼ C vh e  DH =RT        (15:17)
                                                               15.2.1.3  Freundlich Isotherm
                                                               The Freundlich isotherm is used commonly, i.e., used more
            or, in terms of base 10 exponent,
                                                               frequently than the Langmuir, to describe adsorbate–adsorbent
                                                               equilibrium (see, for example, Snoeyink et al., 1969, Culp
                                      DH =2:3RT
                            a ¼ C vh 10                (15:18)

                                                               et al., 1978, p. 178) and is given,
            where                                                                          1=n
              DH8 is the standard state enthalpy of reaction (kilocalories        X* ¼ KC*                (15:19)
                per mole),
              R is the gas constant (1.98 kcal per mole per degree),  where
              T A is the temperature (K). The temperature symbol is used,  K is the coefficient unique to a particular adsorbate–
                nearly always, in conjunction with units; thus in T (K)  adsorbent equilibrium
                means temperature in Kelvin, which is synonymous  n is the exponent unique to a particular adsorbate–adsorbent
                with absolute temperature. T (8C) means temperature in  equilibrium
                degree Celsius.
              C vh is the constant, dimensionless              The logarithmic form is

              Figure 15.8 shows two experiment plots of a versus 1=T A .                    i
            Figure 15.8a data are for Rhodamine-B dye and Dowex 50           log X* ¼ log K þ  log C*     (15:20)
                                                                                            n
            resin while Figure 15.8b data are for Staphylococcus aureus
            and Mendon silt loam. The point is that the van’t Hoff relation
                                                               As implied by the form of the equations, the experimental data
            is applicable to a wide variety of adsorption phenomenon. The
                                                               are plotted on log–log paper. The slope and the intercept of
            negative slope means that DH8 is positive. In terms of the
                                                               the best-fit straight line give 1=n and K, respectively. The
            Langmuir constant, a, higher temperatures increase the value
                                                               slope, 1=n, is the ‘‘intensity’’ of adsorption while K is an
            of a. For the plots shown, especially Figure 15.8b, the plot
                                                               index of the ‘‘capacity’’ of the adsorbent and is the intercept
            should be considered in terms of the van’t Hoff relation being
                                                               (Adamson, 1967, p. 401; Adamson and Gast, 1997, p. 393).
            applicable, but the DH8 would be interpreted as an empirical
            coefficient (since the gas constant, R, would not apply to
            bacteria).                                         15.2.1.3.1  Plots
              As related to competitive adsorption, the compounds with  Figure 15.9a and b shows Freundlich isotherm plots in terms
            higher net energy of adsorption will displace those with lower  of Equations 15.19 and 15.20, respectively. The plots are for


                    1.0                                         10 14
                            Regression results by software:
                          y = 1.4291e + 05 *e (–3963.3x)  R= 0.96672       37°C         α= C 10 −ΔH °/2.3RT
                                                                                           vh
                                                                                 27°C
                        40°C
                                         α= C 10 −ΔH °/2.3 RT                        20°C
                   α                         vh                 α
                                30°C
                       Adsorbate: Rh-B dye  20°C
                       Adsorbent: Dowex 50 H+                         Adsorbate: Staphylococcus aureus
                       ΔH°/R= 3946 K                  10°C            Adsorbent: Mendon silt loam
                       C =142,900                                      y = 3.5788e+19*e (–3943.8x)  R= 0.97341
                    0.1  vh                                       13
                                                                10
                       0.00320  0.00325  0.00330  0.00335  0.00340  0.00345  0.00350  0.00355  0.00360  0.0031  0.0032  0.0033  0.0034  0.0035  0.0036  0.0037  0.0038

                                                                                        –1
                 (a)                    1/T                    (b)                  1/T (K )
            FIGURE 15.8 Langmuir constant data plotted in terms of van’t Hoff equation, a ¼ C vh e (DH8=RT ) . (a) Dye and resin. (From Hendricks,
            D.W. and Kuratti, L.C., Kinetics Part I—A laboratory investigation of six proposed rate laws using batch reactors, Utah Water Research
            Laboratory, Utah State University, Report PRWG66-1, p. 20, July 1973.) (b) Bacteria and soil. (From Hendricks, D.W. et al., Water, Air, Soil
            Pollut., 12, 226, 1979.)
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