Page 19 - Principles of Catalyst Development
P. 19

CATALYTIC  FUNCTIONS                                              5
            selectively into methane (Nil AI 20 3 ),(4)  paraffinic hydrocarbons (Fe/kiesel-
            guhr),(S)  alcohols,  aldehydes,  and  acids  (Co/Th0 2 ),(6)  or  methanol
            (Cui ZnO).(7) The catalyst becomes a useful tool for manipulating selectivity.
                The last point concerns the question of permanent involvement by the
            catalyst.  Ideally, the catalyst is  unchanged by the  reaction.  In  practice this
            is  not true.  Since it  is  itself a  reacting substance, the  catalyst suffers  from
            irreversible  chemical  and  physical  changes,  which  decrease  its  ability  to
            perform.  Within  the  time  frame  of the  reacting  molecules,  these  changes
            are  small.  But as  the  process  time  continues  and  the  catalyst experiences
            many billions of these  events, deactivation becomes significanL  (8  )
                We have extracted from our definition an appreciation for three catalytic
            functions:  activity,  selectivity, and deactivation.  Which is  the most impor-
            tant? This is  difficult to answer generally since each application has its own
            set of specific needs.
                Certainly, for the reaction to proceed, the catalyst must have chemical
            activity.  Beyond that,  increasing activity can have several  benefits:

                1.  Higher rates  for the same conditions.
                2.  Equivalent rates but with  higher throughputs or smaller reactors.
                3.  Equivalent  rates  at  lower  temperatures  or  pressures  where  equili-
                  brium  yields  increase,  operations  become  easier,  deactivation
                  becomes less,  or selectivity improves.


                Selectivity becomes a factor in the presence of mUltiple reactions. These
            are generally of the types
                                            k
                Parallel:                R~D                               (1.5)


                                            k
                                        R~U

                Or consecutive:


                          k"      k,                   k"      k"
                      R  --+   0  --+   U   and    R  --+  U  --+   0     (1.6 )

                With  catalyst  control,  the  ratio  kDI ku  may  be  increased  to  optimize
           the  desirable  product  D.  Benefits  are  obvious  and  include  greater  yields
           of D and less extensive separation operations. An especially important case
           occurs  when  U  is  a  deactivating  agent  such  as  "coke"  or  carbonaceous
           deposits.
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