Page 50 - Principles of Catalyst Development
P. 50

36                                                       CHAPTER  2
            during catalyst regeneration.  Furthermore, the phase change occurs slowly
            at  lower  temperatures,  which  for  anticipated  lifetimes  (3+  years)  could
            result  in  significant  changes.  Incorporation  of small  amounts  of Si02  or
            Zr02 into the  'Y-AI20J  (only 1-2%) moves the a-AI 20 J phase transition to
            higher  temperatures. (65)  The  support is  then  adequately  protected  against
            major upset and long term changes.
                Most often, promoters are added to supports in order to inhibit undesir-
            able  activity, such as  coke formation.  Coking originates from  cracking on
            Bronsted  sites  followed  by  acid-catalyzed  polymerization  to  give  (CHx)n
            species that cover surface sites and ultimately block pores.  Removal of the
            coke  by  burning  may  itself lead  to  activity  loss  due  to  sintering.  Acidic
            cracking sites are neutralized by bases, most effectively alkalis. (66) Potassium,
            added as potash during preparation, lowers the coking tendencies of alumina
            supports. Sodium is  used also but appears to facilitate sintering and is  more
            mobile,  often  poisoning the  active component.
                When dual-functional activity is needed, as in catalytic reforming, extra
            acidity is  achieved by adding chloride ions to the surface. (56) Since chlorine
            is  removed during regeneration, it  must be replenished during reactivation
            or chlorine compounds must be added to  the feed  during operation.


                      TABLE 2.5.  Examples of Promoters in  Major Processes

                     Catalyst           Promoter              Function

            AI 20,                  Si0 2 ,  ZrO: , P   Improves  thermal stability
             Support  and  catalyst   K,O          Poisons coking sites
                                    HCI            Increases acidity
                                    MgO            Retards sintering of active component
           Si0 2·AI 20,             PI             I ncreases  CO oxidation
             Cracking catalyst and  matrix
           Zeolites                 Rare earth ions   Increases acidity and thermal stability
             Cracking catalyst      Pd             Increases  hydrogenation
           PI/ AI 20,               Re             Decreases  hydrogenolysis  and  sin·
             Catalytic reforming                     tering
           MoO,/AI 20,              Ni,Co          Increases  hydrogenolysis  of C-S  and
             Hydrotreating                           C-N
                                    P,B            Increases  MoO, dispersion
           Ni/ceramic supports      K              I ncreases  carbon removal
             steam reforming
           Cu-ZnO-AI 20,            ZnO            Decreases Cu sintering
           Low temperature shift
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