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Nanomaterials as Adsorbents  385

        TABLE 10.3  DED Model Parameters for Naphthalene and 1,2-
        Dichlorobenzene Adsorption and Desorption with nC 60 (Cheng
        et al., 2005)
                    a    1st     a    2nd     a    2nd       2
        Sorbate      Log K d (ml/g)  Log K d (ml/g)   Log q max ( g/g)  R
        Naphthalene  3.75!0.01    5.9!0.04     3.91!0.01  0.996
        1,2-DCB      3.48!0.01   5.68!0.08     3.98!0.03  0.977
          a                         1st
          adsorption data used to determine K d from first term in Eq. 6. Desorption
                1st                                2nd   2nd
        data and K d determined from adsorption data used to find K d  and q max by
        fitting the data to Eq. 6.

           4.28!0.04  0.45!0.05                         3.7!0.01
        10       C w     ), and a linear isotherm (K   10    C ) were used
                                                  d
        to fit the data of the C large aggregates, small aggregates, and the nC 60
                            60
        forms, respectively. The data suggest that adsorption of naphthalene to
        nC is similar to other forms of carbon. Desorption of the naphthalene
           60
        from the nC 60  was highly hysterertic. The K value for desorption
                                                    d
        increased by about two orders of magnitude higher than the correspon-
        ding adsorption value. These data were fitted with a two-compartment
        desorption model (Kan et al., 1998) (Figure 10.5 and Table 10.3).
        Adsorption and desorption experiments were also performed with 1,2-
        dichlorobenzene to nC . The adsorption and desorption data were fitted
                            60
        with a linear isotherm (q   10 3.48!0.01  C ) and with the two-compartment
                                           w
        desorption model, respectively (Table 10.2).
          The experimental data show that 1,2-dichlorobenzene and naphtha-
        lene adsorption and desorption with nC 60  are similar. The different
        sizes of the C 60  aggregates affect the adsorption of naphthalene by
        orders of magnitude. The desorption of the environmental contami-
        nants from nC exhibits hysteresis. Kinetic data also showed that des-
                      60
        orption of naphthalene from C   60  aggregates is composed of two
        compartments: a labile compartment, where naphthalene is probably
        adsorbed on the outside surface and can readily be desorbed, and a
        resistant desorption compartment, where naphthalene may be
        entrapped either in the C 60  aggregates or in the surface crevices and
        desorption is hindered.
          There is great potential for the use of inorganic nanoparticles, such
        as TiO , carbon or metallic nanoparticles (see Chapters 5 and 8), for
               2
        the treatment of organic pollutants in water treatment and the
        environment. These nanoparticles have several advantages over the
        current microparticles used, such as high surface areas, higher affin-
        ity and surface reactivity, faster degradation rates, photocatalytic
        abilities, lower cost, and higher efficiency. With more fundamental
        research and development of technological applications, these inor-
        ganic nanoparticles have the ability to be used for environmental
        applications.
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