Page 204 - Principles of Catalyst Development
P. 204

CATALYST  DEACTIVATION                                          193
                An  example  is  found  in  hydrotreating  with  molybdenum-containing
            catalysts. During regeneration, coke is burned off with air. Although precau-
            tions are taken to avoid reactor hot spots, these sometimes occur. Molybdena
            volatizes above 800°C, so that yellow crystals deposit downstream, and the
            catalyst  particles  turn  white.  Activity  is  irreversibly  lost.  Another  case  is
            found  with  nickel  methanation  catalysts.  If the  catalyst  bed  cools  below
            150°C in the presence of carbon monoxide-containing gas,  nickel carbonyl
            vaporizes  from  the  particle, creating a  very toxic hazard as  well  as  loss  of
            nickel.
                Long-term  volatization  is  also  found  in  steam  reforming  of naphtha.
            Coke  formation  from  heavier  hydrocarbons  is  controlled  with  potassium,
            which promotes carbon-steam reactions. In the presence of steam, however,
            potassium  slowly  forms  KOH  which  volatilizes,  resulting  in  accelerated
            coke formation. The solution is  an ingenious example of the catalyst desig-
            ners  expertise.  Less  than  10%  kalsilite  (K 20, A1 20 3 ,  Si0 2 )  is  included  in
            the catalyst formulation.  In the presence of steam and CO 2 ,  kalsilite slowly
            decomposes to K 2CO) and KOH, always providing enough alkali to remove
            carbon, even though it eventually vaporizes. (49)  Lifetimes of 4-5 years have
           been achieved  with these catalysts.


           8.3.4.  Phase Change
                All components in the catalyst must be maintained in their most active
           state.  Phase  changes  are  thermal  phenomena  and  are  distinguished  from
           compound formation.  High surface area aluminas, for example, change to
           low area phases when heated. Alumina-based catalysts are often regenerated
           by burning the carbon. Over a period of time, the surface area declines and
           activity  drops,  due  to  thermal  sintering  during  regeneration.  This  is  one
           reason  why  the  activity  does  not  return  to  initial  conditions,  as  shown  in
           Fig.  8.2.  This phase change is  controlled by adding silica as  a promoter.
               Segregation of components is  also considered a  phase change.  Highly
           dispersed alloys are notorious in  their tendency to form  nonhomogeneous
           crystallites,  with  more volatile  components diffusing  to  the  surfaces. This
           is found many times with copper-nickel alloys, confusing much of the early
           work in metal catalysts.  (262) There is also evidence that rhenium and iridium
           promoters of platinum in catalytic reforming catalysts undergo some degree
           of segregation upon regeneration. (II)

           8.3.5.  Compound  Formation

               Compounds form  between components and the reactive atmospheres,
           rendering  the  catalyst  less  active.  Elevated  temperatun:s  accelerate  the
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