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NO X REMOVAL  367

            forms monomers or dimers on the benzene rings of the surface of the polymer,
            possibly by π-complex bonding with the π-electrons. However, desorption of
            NO requires temperatures near the thermal stability temperatures of the styrenic
                                  ◦
            polymers, that is near 200 C. Polymeric sorbents with higher thermal stabilities
            such as the acrylics types need to be tested for this application.
              The best sorbents for NO x remain to be mixed metal oxides. Huang and Yang
            (2001) investigated a series of Fe-Mn based transition metal oxides for NO adsorp-
                     ◦
            tion at 25 C in the presence of O 2 . Mixed metal-oxide sorbents are prepared
            from metal salts by standard coprecipitation method. The results of NO x uptake
                                                  ◦
            on Fe-Mn based transition metal oxides at 25 C are shown in Figure 10.64. For
            all sorbents, the initial rates are very high. This is related to their high activi-
            ties in NO oxidation to NO 2 by oxygen. Among the mixed oxides, the uptake
            amount of NO x decreased in the sequence of Fe-Mn-Ti, Fe-Mn-Zr > Fe-Mn-Ce,
            Fe-Mn-Ni > Fe-Mn-Co > Fe-Mn-Cu, Fe-Mn (Figure 10.64). Near 44–45 mg/g
            NO x capacities were obtained on the Fe-Mn-Ti and Fe-Mn-Zr oxides, ∼180%
            increase compared with Fe-Mn oxides. It is clear that TiO 2 and ZrO 2 are good
            storage components for NO x . FTIR results showed that nitrates were formed on
            these oxides. Another reason for the enhancement is the increased surface areas
                                                            2
                                  2
            of these oxides, from 54 m /g for Fe-Mn oxides to 183 m /g for these sorbents.
              NO adsorption was also performed in a fixed-bed adsorber. The results are
            shown in Figure 10.65. After 500 ppm NO + 10% O 2 was passed over the sor-
            bents, all NO was adsorbed and the NO x concentrations in the effluents were zero
            during the first few hours. During this period, 100% NO removal was obtained.



                              50


                             NO x  sorption amount (mg/g sorbent)  30
                              40







                              20


                                                       Fe-Mn-Ti
                                                       Fe-Mn-Zr
                              10
                                                       Fe-Mn-Ce
                                                       Fe-Mn-Ni
                                                       Fe-Mn-Co
                                                       Fe-Mn-Cu
                                                       Fe-Mn
                               0
                                0       5      10     15      20
                                            Time (h)
                                                             ◦
            Figure 10.64. NO adsorption on the mixed, equimolar oxides at 25 C. Reaction conditions:
            [NO] = 200 ppm, [O 2 ] = 10%, and balance He (Huang and Yang, 2001, with permission).
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