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PILLARED CLAYS  263

                            1.0

                                                                 A
                            0.8                                  B
                          Amount adsorbed (mmol/g)  0.6          a
                                                                 b





                            0.4



                            0.2


                            0.0
                             0.0    0.2    0.4   0.6    0.8    1.0
                                             P (atm)
                                ◦
            Figure 9.22. Isotherms at 25 C for propylene on (A) CuCl/TiO 2 -PILC, (B) CuCl/γ -Al 2 O 3 ,and for
            ethylene on (a) CuCl/TiO 2 -PILC, (B) CuCl/γ -Al 2 O 3 (Cheng and Yang, 1995b with permission).


            that the energy in the Langmuir constant follows a uniform distribution function,
            that is, a rectangular distribution with a spread of the energy between E max and
            E min . The factor s is proportional to the spread (E max − E min ). When s = 0, the
            Unilam reverts to the Langmuir isotherm. Empirically, s = 0–14.
              From the results of Cheng and Yang, it is clear that using the PILC support
            results in a higher value for s. This is likely caused by the heterogeneous nature
            of the PILC, because the PILC contains at least two different types of surfaces:
            that on the pillars and that on the clay layers.
              Using Zr-PILC and Al-PILC as the supports for CuCl spreading, Engwall and
            Ma (2002) also showed very steep isotherms (with high s values) for olefins
            and paraffins. Since Zr-PILC and Al-PILC have the smallest pore sizes among
            the PILCs, the amounts of CuCl that were spread without blocking the micro-
            pores were very limited. In the work of Engwall and Ma (2002), less than
            10% wt. CuCl could be spread, which were well below the monolayer spread-
            ing amounts.
              “Acid activation” has long been known as a means for increasing (dramat-
            ically) the catalytic cracking activity of clays (e.g., montmorillonite) (Rupert
            et al., 1987). Upon acid treatment, the surface area of the clay is also increased.
            Typically, sulfuric acid is used in the treatment. The acid attacks and dissolves
            the octahedral layer that is sandwiched between two tetrahedral silica layers in
            the clay. The attack takes place uniformly on the edges of the octahedral layer,
            and eventually removes this layer. Thus, by optimal treatment (i.e., at a proper
            combination of acid concentration, temperature, and time) one can achieve a high
            surface area.
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