Page 218 - Principles of Catalyst Development
P. 218

CATALYST  DEACTIVATION                                          207
            Furthermore, the surface can be cleaned with sulfur-free purge gas.  Regen-
            erative  processes for chlorine- and sulfur-poisoned  low  t1emperatures  shift
            catalysis are available, but there is  some doubt as  to desirability.
                In general, the best approach to  poisons of this  type is  to pretreat the
            feed.  This  is  done in three ways:  (1) chemical treating, which  is  expensive
            and  may  introduce other contaminants;  (2)  catalytic processing,  which  is
            effective for poisons with organic origins; and (3) guard chambers. In guard
            chambers, a  cheaper adsorbent  precedes the main reactor.  Sometimes this
            is  a  separate  unit,  such  as  sulfur-removing zinc oxide beds  in  natural  gas
            reforming.  On  other  occasions  it  may  be  part  of the  reactor bed  and  the
            front section is sacrificed as a scavenger, using the same catalyst or a cheaper
            substitute. Some very ingeneous guard applications are found in automobile
            exhaust catalysts, as  discussed  in  previous sections. (255)


            8.3.7.2.  Oxides

                Semiconducting oxide catalysts owe their activity to electron accepting
            or donating surface sites, with specific surface geometry and favoring redox
            reactions.  Any  molecule  which  adsorbs  strongly  const;itutes  a  potential
            poison. Unfortunately, not too much attention has been given to this subject
            in  the  literature.  (256)  For  example,  poisoning  of hydrogenation  or  hydro-
           genolysis activity in supported oxides and sulfides has not been considered
           to any extent. Other types of deactivation take precedence. Other than these
           general  remarks,  very  little information can be added.



            8.3.7.3.  Solid Acids
                Poisoning  of  acid  sites  is  straightforward.  Basic  constituents  are
           required  to  neutralize  acidity.  This  is  found  in  alkali  and  alkaline  earth
           compounds and in  basic organic molecules.  Process  poisoning by  alkaline
           and alkaline earths is rare. These materials are added as deliberate promoters
           to  remove  acidity  but are  not normally encountered in  process  streams  in
           the basic form.  One exception is  Na +  ions,  encountered in  steam used for
           stripping cracking catalysts and other purposes.
                Basic  organics  are  primarily  nitrogen-containing  molecules  that  are
           abundant in petroleum feedstocks. In a typical straight run stock, 25% -35%
           of the nitrogen compounds are basic.  Basic and nonbasic types are shown
           in  Table 8.8.
               The  susceptibility of solid  acids  to these  poisons  correlates  well  with
           the  basicity  of nitrogen  compounds,  as  shown  in  Fig.  8.16.  In  practical
           feeds,  a  wide  range and variation of types  are present.
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