Page 231 - Principles of Catalyst Development
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220                                                      CHAPTER  8
                As  mentioned  earlier,  metal  porphorins also  adsorb  on  hydrotreating
            catalysts, especially  when  using  heavier residua  fractions.  The same  prob-
            lems  develop,  i.e.,  excessive  coke  and  run-away  regeneration.  Pore-shape
            control  is  practiced,  as  in  Fig.  S.24,  for  the  same  reasons.  The  larger
            porphorin  molecules  are  excluded  to  the  outer  surface  of  the  particles.
            Ultimately,  metal  buildup  becomes  so  severe  that  the  catalyst  must  be
            replaced.  Extraction methods for removing these deposits are available, but
            as  yet  have not proven economical.  It is  interesting that discarded catalysts
            may  become  a  useful  source  of  nickel  and  vanadium  metal.  The  best
            solutions  appear to  be  external guards  with  cheaper adsorbents, or larger
            hydrotreating beds,  which  allow  for  metal  trapping at the top.

            8.3.8.3.  Dissociative Coking

                Dissociative coking(CX')  occurs  when  carbon monoxide dissociates on
            a  catalytic site,  as  follows:

                                     2CO  ~ C + CO 2                     (S.12)

            This reaction is  found primarily in steam reforming of hydrocarbons, where
            other  coking  possibilities  also  exist.  With  methane  a  dehydrogenation
            reaction

                                                                         (8.13)

            occurs.  Equilibrium  constants  for  these  are  shown  In  Fig.  S.26,  together
            with  the  third  reaction

                                                                         (8.14 )

           Carbon  formation  is  a  major  concern  in  methane  and  naphtha  steam
            reforming, but Fig. 8.26 shows that under reaction conditions only reaction
           (8.13)  is  possible  in  the  temperature  range  commonly  used,  600-750°C.
           Thermodynamics  favors  the  reverse  of  reactions  (S.12)  and  (8.14),  and
           carbon is  removed, but the catalyst must have sufficient activity to counter-
           balance  coke  deposition  via  reaction  (8.13).  As  discussed  earlier,  this  is
           accomplished by promotion with potassium.  Nevetheless, interesting inter-
           actions occur, which may lead to  reactor failure.  Figure 8.27  illustrates the
           case for a catalyst deactivated either by sulfur or carbon deposition. Below
           the equilibrium line, we expect carbon formation. At the inlet of the reactor
           tube, the  temperature dips  as  the  endothermic reaction absorbs  heat.  If it
           drops below the equilibrium  line, then coke forms and  removal rates must
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