Page 220 - Principles of Catalyst Development
P. 220

CATALYST  DEACTIVATION                                           209
               These poisons are removed during regenerative burning but may cause
           problems by producing NO x  in combustion effluents.  It is  better to remove
           them before the process.  Hydrotreating removes  nitrogen,  and this is  stan-
           dard  procedure with  all  catalytic cracking  feedstocks.  This treatment also
           removes sulfur and much of the  heavy metal contamination.


           8.3.7.4.  Beneficial Poisons

                Poisons generally result in harmful effects  such as  loss of activity, yet
           there are circumstances when small  amounts  of poison  are  beneficial.  An
           example  of  this  is  catalytic  reforming  to  boost  the  octane  number  of
           paraffinic  naphthas.  Early  workers  noticed  that a  few  parts per million  of
           sulfur  in  the  feed  increased  reformate  yield  rather  than  decreasing  as
           expected.  This  "promotion" technique has  become standard in  reforming
           technology.  (277) The reason for this is  seen in studies with pure compounds
           on nickel-faujasite catalysts. (246)  Nickel results in more hydrogenolysis than
           platinum.  This  reaction  leads  to  light  gases  and  coke  and  is  undesirable
           over  dual-functional  isomerization.  With  n-hexane  as  the  feed,  the  fresh
           catalyst  showed  poor  selectivity  to  isomerization,  as  shown  in  Fig.  8.17.
           Poisoning  with  hydrogen  sulfide,  however,  showed  a  dramatic  selectivity
           reversal.  Sulfur poisons the most active hydrogenolysis sites preferentially.


                         15

                      Cl
                      ....
                      W
                      a:
                      w
                      >
                      z
                      0   10   ___ n - HEX ANE  HYDROGENOL YSIS
                      ()
                      w
                      Z
                      <l:
                      X
                      w
                      J:
                                             n  - HEXANE  ISOMERIZATION
                      c   5
                      ....
                      z
                      UJ
                      ()
                      a:
                      w
                      c-
                           O           0.1          0.2          0.3
                                 VOLUME  H 2 S  ADSORBED,  cm 3
                Figure 8.17.  Beneficial  poisoning of a  nickel  catalyst with  hydrogen sulfide.(246)
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