Page 154 - Principles of Catalyst Development
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142                                                      CHAPTER  7
            which  does  not  penetrate  pores  smaller than  1.2 x  10 nm  at atmospheric
                                                             3
            pressure.  For  this  reason  particle  density  is  also  called  mercury  density.
            There  is  a  relationship  between  particle  and  skeletal  densities,  d p  and  d"
            and porosity,  (),  given by


                                                                           (7.1)


            7.3.1.4.  Packing  Density

                Also  called  bulk or bed  density,  the  volume  in  this  case  includes  the
            void space between  particles. This general definition  poses some problems
            since  measured  volumes  differ,  for  example,  for  various  vessels,  packing
            methods,  and agitation.  This  is  overcome by specifying dimensions  of the
            container  used  and  the  method  of  packing.  From  a  practical  viewpoint,
            packing  methods  should  be  the  same  as  those  used  in  the  reactor  filling.
            Packing  density,  dh ,  and  particle  density  are  related  through  the  void
            fraction,  E;  thus  we  have


                                                                          (7.2)


                Values in the example in Table 7.1  show that considerable errors result
           if these  densities  are  confused.  A  good  practice  is  to  always  specify  the
           volume  included, as  in  Table 7.1.


           7.3.2.  Particle Size

                Measurement  of the  particle  size  of macroscopic  pellets,  extrudates,
           and spheres presents no  problems.  Dimensions can be determined directly
           or sample  material  sieved  for  irregular  particles.  Smaller distributions  in
           powders, such as cracking catalysts, require specialized procedures: optical
           and  electrical  imaging,  light  scattering,  light  shadowing,  elutriation,
           sedimentation,  electrical  resistance,  impaction,  and  nozzle  pressure
           drop. L~)().~) ).~)'.1)41  For  cracking  catalysts  and  other  powders  in  the  range
           0.6-160 ftm,  the  preferred  approach  is  to  use  an  electronic  particle  size
           analyzer.  An  electric  current  path  of small  dimensions  is  modulated  by
           individual  particle passage through apertures, producing individual  pulses
           proportional  to  the  particle  volume.  The  sample  is  suspended  in  an  elec-
           trolyte,  dispersed  ultrasonically,  and  forced  through  restricting  apertures.
           Distributions are  found  from  the  number of particle  passing through  pro-
           gressively smaller openings.(2))) Table 7.2  gives  typical  results.
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