Page 239 - Adsorbents fundamentals and applications
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224   π-COMPLEXATION SORBENTS AND APPLICATIONS

                     8.5.1. Removal of Dienes from Olefins
                     Normal α-olefins (NAO) are chemical intermediates used for making a variety of
                     products. The largest uses for NAOs are in the production of alcohols (via oxo
                     chemistry), as co-monomers for polyethylene production, and in the synthesis of
                     poly (α-olefins) for synthetic lubricants. Also, oligomerization of n-butenes to
                     more valuable octenes is an effective way of upgrading their value. A variety
                     of catalysts are used for these reactions. The most common metal-based catalyst
                     involves nickel, which is subject to poisoning by very low levels of 1,3-butadiene
                     (C 4 H 6 ). The selective butadiene hydrotreating process is one option to clean up
                     unwanted butadiene in a mixed-C 4 stream (Meyers, 1986). Removal of dienes
                     is also required for the production of higher α-olefins. Distillation is also being
                     used for these purification processes.
                       Sorbents based on π-complexation for olefin purification have been devel-
                     oped recently in the author’s laboratory (Padin et al., 1999; Jayaraman et al.,
                     2001; Padin et al., 2001; Takahashi et al., 2001a and 2001b). AgY and Cu(I)Y
                     are the best sorbents. Although only vapor phase isotherms are reported in the
                     literature cited above, these sorbents have been demonstrated successfully for
                     the liquid-phase feeds in the field. Diene impurities below 1 ppm can be readily
                     achieved. The isotherms are shown in Figures 8.12 and 8.13, for 1,3-butadiene
                     and 1-butene.
                       For purification, the undesired component or impurity is present at a low con-
                     centration or partial pressure. It is important that a significant amount of the


                             4
                                 Cu-Y(450 × 12, CO/He)         Cu-Y(450 × 1, He)


                                 Cu-Y(450 × 1, He)
                           Amount adsorbed (mmol/g)  2  Cu-Y(300 × 1, He)  Ag-Y(300 × 1, He)
                             3

                                  Ag-Y(300 × 1, He)


                                   Cu-Y(450 × 12, CO/He)
                                                    Butadiene on Cu-Y after 450°C × 12 hr in CO/He
                             1
                                                    Butadiene on Cu-Y after 450°C × 1hr in He
                                                    Butadiene on Cu-Y after 300°C × 1hr in He
                                                    Butadiene on Ag-Y after 300°C × 1hr in He
                                                    Butene on Cu-Y after 450°C × 12 hr in CO/He
                                                    Butene on Cu-Y after 450°C × 1hr in He
                                                    Butene on Ag-Y after 300°C × 1hr in He
                             0
                             1.E−05    1.E−04   1.E−03    1.E−02    1.E−01    1.E+00
                                                Partial pressure (atm)
                                                               ◦
                     Figure 8.12. Pure-component equilibrium isotherms at 120 C for 1,3-butadiene and 1-butene
                     on Cu-Y and Ag-Y. Samples were prepared by reduction of Cu(II)Y by either CO or
                     auto-reduction (in He) (Takahashi et al., 2001a, with permission). Lines are fitted isotherms
                     with various models.
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