Page 389 - Chemical Process Equipment - Selection and Design
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352  DISINTEGRATION, AGGLOMERATION, AND  SIZE  SEPARATION OF  PARTICULATE  SOLIDS
                surface of  the bed of  particles. The tumbling action then distributes   performance data in addition to those shown with Figure 12.7 are:
                the liquid uniformly through the mass.
                   The disk granulator  of  Figure  12.7 is  a  shallow pan,  inclined
                45-70"  to the horizontal and rotating  at speeds of  10-30rpm.  The   Material   Diameter (mm)  kg/(min)(m2)
                ratio  of  pan  diameter  to  collar  height  is  3-5.  The  variety  of   Iron ore   10-25   11.4
                materials  to  which  this  equipment  is  applied is  indicated  by  the   Cement flour   18
                listing of part (e) with this figure and in Table 12.14. As the rotation   Fertilizer   1.6-3.3   14.3
                proceeds, fresh solids and spray are charged continually. The finer
                particles settle to the bottom, the largest remain at the top and then   The  data  of  Figure  12.7(c)  for  cement  kiln  feed  are  42-
                overflow the collar and constitute the product. Because of  the size   44 kg/(min)(m2).
                stratification, the product of disk granulation is more uniform in size   Pans  also  are  made  with  height  more  nearly  equal  to  the
                than  of  drum granulators which  discharge a mixed product.  Some   diameter. In one such device the material is continually lifted onto




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                   f                                                          1
                  Product                                          Product outlet
                        (a)                                     (b)
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                                                                                     Grinding disks
                                                                                              Product outlet
                                                                                                  (4

                                                                             Feed inlet

                                                                    Product
                                                                    outlet


                                                                                           ._ Grinding
                                                                                           '  stones















                Figure  12.6.  Examples of  mostly less common devices for  size reduction.  (a)  Schematic of  a  gyratory crusher for  very large lumps.  (b)
                Squirrel-cage disintegrator with four cages.  (c) Disc-type attrition mill, rotating at  1200-7000 rpm,  clearances adjustable by  increments of
                0.001 in.  (d) Schematic of colloid mill, clearance adjustable between 0.001 and 0.050 in., peripheral speeds to 10,000 ft/min.  (e) Buhrstone
                attrition mill, used for making flour and grinding paints, printers inks and pharmaceuticals. (f) Roller or spindle mill; the crushed material is
                thrown outwards and removed with an air stream. (g) Majac fluid energy mill making a -200  mesh product; opposed air jets cause high speed
                collisions and disintegration of  the material.
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