Page 227 - Principles of Catalyst Development
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216                                                      CHAPTER  8
            model components have given a better understanding of this effect, as shown
            with data in Table 8.9. (246)  Initially most of the product comes from  hydro-
            genolysis. A small amount of poison decreases hydrogenolysis but not  acid
            cracking,  as  measured  by  the  concentration  of C 1  hydrocarbons.  Finally,
            all  hydrogenolysis  is  suppressed  but  with  some  loss  of activity.  Yields  of
            isomers,  however, increase,  as  seen in  Figure 8.17.
                In spite of these improvements, deactivation in catalytic reforming was
           severe and regeneration was required every few days. This was accomplished
            with extra "swing" reactors or moving bed designs, both expensive to build
           and  operate.  Another  solution  was  to  increase  pressure  from  about  15  to
           35 atm.  Higher hydrogen  pressure  reduces  hydrogenolysis and accelerates
            hydrogenation of the carbon. Processes then ran three to six months before
            regeneration.  However, aromatic yield from the dehydrogenation of naph-
           thenes and cyclization of n-paraffins decreased and octane number suffered.
                A  breakthrough  came  with  the  discovery  of  bimetallic  reforming
           catalystsY 1)  When  platinum  is  combined  with  rhenium,  the  stability
           improvement  is  dramatic.  Rhenium  appears  to  inhibit  both  coking  and
           sintering, so that deactivation during use and the frequency of regeneration
           is decreased. Use of iridium was a further advance, giving not only prolonged
           life  of over ten  years  but  higher  activity.  Comparisons  are  shown  in  Fig.
           8.23.  Not only was operation easier but plant configuration  was simplified
           with large savings in  capital cost.  Problems exist with bimetallics, however:
           which  tend  to  segregate  during  regeneration,  requiring  more  complicated
           treatment.  But that seems a  small  price  to  pay.

                    TABLE  8.9.  H 2S  Poisoning  of  Ni-LiY  Effect  on  Product
                       Distribution  n-C 6  Hydrogenolysis and  Isomerization"

                                             Moles  of product
                                       Fraction of Ni  poisoned  with  H 2S
                    Product         0     0.05   0.10    0.15   0.20
                    -------
                     C,           56.5    32.8
                     C 2
                     C,           0.89    2.10   0.64    0.25   0.20
                      iC.         (LOS    0.23
                      /lC.         1.63   2.69
                     ie,          0.24    0.53
                     /lC,         2.33    3.43
                     2MP          0.62    1.66   3.43    2.42   1.01
                     3MP          0.32    1.42   0.84    0.66   0.49
                     /le"         85.5   91.2   95.4    96.7

                    u  Reference  246.
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