Page 231 - Adsorbents fundamentals and applications
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216   π-COMPLEXATION SORBENTS AND APPLICATIONS

                     8.4. BULK SEPARATIONS BY π-COMPLEXATION
                     Bulk separation/recovery of CO from synthesis gas by π-complexation has already
                     been commercialized worldwide since 1989. π-Complexation is highly promising
                     for other bulk separations such as olefin/paraffin and aromatic/aliphatic separa-
                     tions, either in vapor phase by PSA or in liquid phase by simulated moving bed
                     processes. Before discussing these processes, problems of deactivation or stability
                     of the π-complexation sorbents will be first addressed.

                     8.4.1. Deactivation of π-Complexation Sorbents
                     The deactivation behaviors of various π-complexation sorbents have been stud-
                           +
                     ied. Cu salts such as CuCl and Cu(I) zeolites are oxidized quickly into Cu 2+
                     state upon exposure to ambient air. Moisture is known to accelerate the oxida-
                                   +
                                               +
                     tion process. Ag salts and Ag -zeolites, on the other hand, are quite stable in
                     ambient air with minimized light exposure (Hutson, 2000).
                       Because H 2 and H 2 S are present in synthesis gas, cracked gases, and other
                     gas streams encountered in industry, their effects on the π-complexation sorbents
                     have been studied. The effects of exposure to 0.5 atm H 2 at various temperatures
                     on AgNO 3 /SiO 2 and AgY zeolite were discussed in detail by Jayaraman et al.
                     (2001). Severe deactivation of both sorbents occurred at temperatures above
                        ◦
                     120 C. X-ray photoemission spectroscopy (XPS) studies of the deactivated sam-
                                                            0
                                          +
                     ples showed that the Ag was reduced to Ag . However, these sorbents could
                                                               ◦
                     be rejuvenated by oxidation with oxygen at 350 C when the valence of Ag
                                     +
                     was restored to Ag .The π-complexation ability of the sorbent was tested by
                     adsorption of ethylene, and the deactivation and reoxidation behaviors are shown
                     in Figure 8.7.
                       The behavior of AgY zeolite in H 2 S was studied by Takahashi et al. (2001b).
                                ◦
                     At 25 to 120 C, H 2 S chemisorbed on AgY, while reaction with H 2 S with contin-
                                                    ◦
                     ual weight gain was observed at 180 C. XPS analysis showed the formation of
                     Ag 2 S. However, the adsorption capacities for 1-butene and 1,3-butadiene were
                     only slightly lowered, indicating the π-complexation capability of Ag 2 S.
                       The effects of H 2 and H 2 S on Cu(I)Y were studied by Takahashi et al. (2001a).
                                                             ◦
                     Unlike AgY, exposure to H 2 and H 2 S at 120 C showed no effect on CuY,
                     demonstrating its excellent poison resistance toward H 2 and H 2 S.
                       The deactivation behaviors of the Ag and Cu(I) sorbents are summarized in
                     Table 8.10.

                     8.4.2. CO Separation by π-Complexation
                     Since 1989, CO separation/recovery by PSA using supported CuCl has been
                     commercialized worldwide. PSA separation results are available in the literature
                     (Kansai Coke & Chemicals Co., 1989; Chen et al., 1997; Golden et al., 1998).
                       CO is typically produced along with H 2 as synthesis gas, by steam reform-
                     ing of methane or naphtha. Separation and recovery of CO has been accom-
                     plished by cryogenic processes. CO is used as a raw material for production of
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