Page 226 - Principles of Catalyst Development
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CATALYST  DEACTIVATION                                           215

                                                           I      \
                                                           C       C
                                                           \      /
                                               C-CHHH·C      C -- C
                       ~~~~//~f/~~~~-L--~-~
                       /DEHYDROGENATION
                       /// CATALYST  //
                       ////////////,
                       Figure 8.22.  Carbon  formation  on  dehydrogenation catalysts.


           dehydrogenation surface to  fuel  the  reactions  discussed  for acid  catalysts.
           Both types of coke are present but in much lesser amounts than for cracking,
           since  acidities  are  lower  and  hydrogen  from  dehydrogenation  helps  keep
           the catalyst clean. The carbon-forming tendencies of these catalysts correlate
           well with hydrogenolysis activity, as  expected, since C-C bonds rupture in
           the presence of hydrogen. Therein lies the best possibility for control, since
           we have seen many examples ofhydrogenolysis suppression through catalyst
           modification.
               The characteristics of dehydrogenation coking vary with the chemistry
           of the  catalytic process.  Important features  are best considered  with  three
           important  examples:  (1)  catalytic  reforming,  (2)  hydro treating,  and  (3)
           metal  contamination.

                8.3.8.2a.  Catalytic  Reforming.  Catalytic reforming  combines two  car-
           bon-producing  functions:  dehydrogenation  and  acidity.  For  many  years,
           processes that upgraded octane number with hydrodecyclization, isomeriz-
           ation,  and  hydrocracking of straight chain  paraffins  and naphthenes  used
           dispersed platinum on acidified alumina.  Much research has been done on
           carbon formation by these metal crystallites, and a clearer insight is  begin-
           ning  to  emerge.  (282)  Carbon  is  produced  through  hydrogenolysis  at  sites
           that  correlate  well  with  low  index  positions,  such  as  faces,  edges,  and
           corners.  Carbon diffuses  over the surface as  a type of surface carbide and
           through the bulk as  carbon atoms reaching the interface between platinum
           and support. Some of it progresses to acid sites to begin the polymerization
           process leading to pseudographite. Thus the metal "feeds" the coke precur-
           sor  to  acid  sites  and  carbon  forms  in  regions  around  the  crystallites.  In
           extreme cases,  ribbons of graphitic carbon grow,  supponing the  platinum
           crystallite at its tip. Ultimately, these ribbons and patches cover the surface
           and block pores. (283)
               Early  workers  in  catalytic  reforming  discovered  that  a  small  amount
           of sulfur  poisons  hydrogenolysis  sites  and  reduces  coking.  Studies  with
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