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                    202                             3. Heterogeneous Processes and Reactor  Analysis


                    ference,
                    specific density dif the particle size is kept within the appropriate re within gion,
                    0.035     d  p    0.1 mm, depending on the density dif to be in the Group  ference,  A particles
                    regime (Type A fluidization). Since the minimum bubbling velocity could not be less than
                    the minimum fluidization v, the ratio is set equal to unity when  elocity  u  bm    u  fm  .
                      In Figure 3.54, it is clear that while approaching the limit of Group B particles (lar ge
                    particle density and particle size),  u  bm  approaches   u  fm  , as expected. On the other hand, the
                    difference between the two velocities is increased constantly for smaller particles and
                    lower particle density, while it is v ery high for   d  p    0.045 mm where   X  0.45  = 1. This could
                    be useful in the case where an expanded region of particulate fluidization is desirable in
                    gas–solid systems.
                      Since in the re gion between   u  fm  and   u  bm  the fluidization is particulate, eq. (3.475) could
                    be used for the determination of bed voidage at minimum bubbling v setting  , elocity  u  s
                    u  bm  . In Figure 3.55,    bm  and     fm  are compared to each other for Group A particles—an air
                    system at 20 °C (      1,     0.4,      1000–3000 kg/m  3  , X  45    0 for   d  p    0.045 mm, and
                                                p
                                   S
                    X  45   1 for   d  p    0.045 mm). From Figure (3.52) and the specific density dif the ference,
                    gion, particle size is kept within the appropriate re within 0.035     d  p    0.23 mm, depend-
                    ference, ing on the density dif to be in the Group A particles re gime.
                      Pavlov’s equation (3.475) is used for voidage determination at minimum b ubbling con-
                    ditions (for   u  s    u  bm  ), and since   d  p    0.5 mm, the Broadhurst–Becker equation (3.466) is
                    used for     . For a wide range of particle sizes, the values of     fm  and     bm  are close to each
                            fm
                    other, within a ratio between 0.95 and 1.1 for all particle densities.  alues of  V    /   fm  ratio
                                                                                   bm

                               9
                                                                        3000 kg/m  3
                               8                                        2000 kg/m  3
                                                                        1000 kg/m  3
                               7

                               6

                               5
                              fm
                              /u
                              bm
                               4
                              u
                               3
                               2

                               1

                               0
                                 0      0.02  0.04  0.06  0.08  0.1              0.12
                                                       d  (mm) p

                    Figure 3.54  Ratio of minimum bubbling velocity to minimum fluidization v . F or d elocity  p  > 0.045
                    mm,  X  45  = 0 and for   d  p  < 0.045 mm,  X  45  =1 is assumed.
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