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88    ADSORPTION OF VAPORS ON MINERALS AND OTHER SOLIDS

           TABLE 6.1. N 2 Monolayer Capacities, Total Surface Areas, Micropore Volumes by
           t-Plot, and Nonporous Surface Areas of Selected Solids
                                                 Total    Micropore
                                       Q m(N 2)  Surface    Volume   Nonporous
                                                                            2
                                                     2
           Solid                       (mg/g)  Area (m /g)  (mL/g)   Area (m /g)
           Silica (Alfa Aesar Co.)       2.43      8.2      7 ¥ 10 -4    6.9
           Alumina (Alcoa Co.)           2.74      9.3      3 ¥ 10 -4    9.2
           Goethite (Ward’s Nat. Sci.)   0.77      2.7      2 ¥ 10 -4    2.6
           Kaolinite (KGa-2)             6.03     21.0        0         21.1
           Ca-SAz-1 (homoionic)         20.5      71.5     3.0 ¥ 10 -2  17.2
           K-SAz-1 (homoinoic)          27.9      97.1     3.9 ¥ 10 -2  26.4
           Activated carbon (Calgon Co.)  300    986         0.48       110
           Source: Data on kaolinite, Ca-montmorillonite (Ca-SAz-1), and K-montmorillonite (K-SAz-1)
           from Rutherford et al. (1997) and the rest from C. T. Chiou (unpublished research).





                     12
                                   Alumina
                    Vapor Uptake, Q (mg/g)  8 4
                                   Silica













                      0
                      0        0.2       0.4      0.6      0.8       1.0
                                     Relative Pressure, P/P°
           Figure 6.1  N 2-vapor adsorption at 77K on alumina and silica. The solids are identi-
           fied in Table 6.1.


           shapes at higher  P/P°, in reflection of the pore-size distribution and pore
           geometry and thereby of the energetic heterogeneity of the solid (adsorbent).
           The curvature at low P/P° is related to the heat of adsorption for the first-
           layer adsorbate [i.e., the C value in BET the model, Eq. (4.6)], in which the
           energetic heterogeneity is most pronounced. The relatively flat adsorption
           isotherm along with exceptionally high N 2 uptake for activated carbon is
           indicative of a very large quantity of highly energetic fine pores (in molecular
           dimensions) in the solid. Most natural solids tend to display a large range of
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