Page 203 - Principles of Catalyst Development
P. 203

192                                                      CHAPTER  8
            plugging,  channeling,  pressure  drop  increase,  and  irregular  bed  perform-
            ance.  This  in  turn  leads  to  hot spots,  with  associated  thermal  and  coking
            effects.  Thus  particle  failure  initiates  more  serious  deactivation  by  other
            mechanisms.
                Loss of mechanical strength is  unlikely, unless assisted by thermal and
            chemical effects. For example, an increase in the pressure of steam reforming
            units  produced  a  gradual  loss  of  volatile  silicates.  Since  pellets  were
            cemented  together  with  calcium  silicate  type  binders,  silicate  loss  led  to
            weakening of the catalyst  rings.  The corrective action was  a  change in  the
            method of preparation and formulation. (49)  Another example is  found with
            alumina-based  pellets.  Sulfate impurities that are not removed during pre-
            paration  react  with  aluminum  under  regeneration  conditions  to  form
            aluminum sulfate, weakening the pellet. This also occurs when heavy metals
            deposit during residual oil desulfurization. (36) Regeneration in air at elevated
            temperatures  produces  vanadium  oxides  which  act  as  a  flux  to  change
            particle  binding.  Particle  failure  is  usually  obvious,  but  the  contributing
            factors  may  not be.

            8.3.2.  Fouling
                In this sense, fouling means deposition of reactor debris on the particles.
            Scale,  rust,  and  other  corrosion  products  are  all  possibilities,  in  addition
            to  chemical  components  from  up-stream  units.  Particles  removed  from
            reactors  often  have  red-brown  iron  oxide  crusts  on  the  outside.  Calcium
            compounds are also found. The most severe cases occur in  processing coal
            and coal-derived liquids, which contain large amounts of inorganic mineral
            matter.
                At  best,  these  materials  clog  the  outside  of particles,  plugging  pores
            and blocking active surfaces. At the worst, particles are cemented together,
            resulting  in  loss of void space within the  reactor and complicating catalyst
            removal.  Once again, the analytical  procedures discussed in  Chapter 7 are
           helpful  to  indicate  the  presence  of this  type  of deactivation.  There  is  no
           cure, the  catalyst can only be  replaced,  and care exercised to  avoid  future
           contamination by  the  use  of screens and guards.

           8.3.3.  Component Volatization

                Elevated  temperatures can  result in  loss  of active components or pro-
           moters through vaporization. Loss of activity and promoter function follows,
           with  added  complications  from  corrosive  deposition  on  downsteam  plant
           equipment.  Events of this type are easily detected in  laboratory operations,
           so we must assume that, in process use, they are only found with unexpected
           upsets  or on a  long-term  basis.
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