Page 398 - Chemical Process Equipment - Selection and Design
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12.5.  PARTICLE  SIZE  ENLARGEMENT  361





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                                     Carbon black feed
                                       Rate, Mg/day               26.3a
                                       Bulk density, kg/m3        5 1.3
                                     Pellets produced
                                       Wet basis
                                                    4
                                       Production  rate, kg h   2108.3
                                       Bulk density, kg/m        562.3
                                       Densification ratio        11.0
                                       Dry basis
                                                    !!
                                       Production rate, kg h    1096.3
                                       Bulk density, kg/m        394.1
                                     Binder
                                       Specific gravity           1.05
                                       Injection rate, kg/h     1011.5
                                       Use ratio,  weight of binder to
                                        weight of wet pellets     0.92
                                     power Consurnptionb
                                      Rate, kW                   18.5
                                      Per Mg  of wet pellets, kWh   15.OC
                                     Production quolity
                                      Rotap test (5 min), %       1.4 (avg. of45 samples)
                                      Crushing strength, g       25  (avg. of 73 samples)
                                     :Average  from 5-day test, plus subsequent  production.
                                      Ammeter readings.
                                     'Cold  shell.
                                                           b)

                        Figure 12.W. Pin mixers which operate at high speed for granulation  of  fine and aerated powders.  (a)
                        Pinmixer  for  the  granulation  of  wetted  fine  powders.  (b)  Performance  of  a  pinmixer,  dimensions
                        0.67 rn dia by 2.54 m, for pelleting a furnace oil carbon black  (Capes, 1980).


          holes. The life  of  a die is measured in hours.  Units of  300HP are   equipment is similar to that for spray drying, but the mechanism  is
          made. Some aplplicaticlns are cited in Table 12.17.   simpler in that  no evaporation occurs and as one consequence  the
              The large  tonnage  application  is to the preparation  of  animal   product is less porous and stronger. A sketch of a prilling process is
          feeds but  many  smaller  scale applications  also  are being  made.  A   in Figure  12.16. At one time the chief application was to fertilizers,
          survey of  this literature is made by Sherrington  and Oliver (1981).   but a list of  many other prillable materials is given in Table 12.18.
                                                                 Dimensional  and some operating data for prilling  of  urea and
                                                              ammonium nitrate also are in Table 12.18. Towers as high as 60 m
          PRILLING
                                                              have  been  installed.  Because  of  the  expense of  towers,  prilling  is
          In the process a molten material is disintegrated  into droplets which   not competitive with  other granulation  processes  until capacities of
          are allowed to fall and to solidify in contact with an air stream. The   200-400  tonslday are reached.
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