Page 261 - Dust Explosions in the Process Industries
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Generation of Explosible Dust Clouds  233





















                                                    Figure 3.25  The nozzle for dispersing agglomer-
                                                    ates  of  cohesive  dust  particles  (Yamamoto  and
                                                    Suganuma, 7 984).

               The distribution of effective particle sizes is shifted systematically toward smaller par-
               ticles as the dispersion process in the nozzle gets more effective, that is, as the average
               air velocity through the nozzle increases.
                 The effect is quite dramatic.For an airvelocity in the nozzle of 10.5m/s, the median effcc-
               tive particle size is somewhat larger than  10 pm; whereas for velocities in the range
               100-150  m/s, it is only 1pm. For the primary dust cloud, which was generated in a way
               that would be typical in industry,the median particle size would probably be considerably
               larger than 10pm. It can be observed from Figure 3.26 that, at the highest air velocities in
               the nozzle, the distribution of the sizes of “effective”particles in the secondary dust cloud
               approachedthe size distributionfound in a sedimentationbalance after having dispersedthe
               powder in a liquid in a way that would be expected to produce close to perfect dispersion.
                 Yamamoto and Suganuma arrived at the following empirical relationship for the effi-
               ciency of the nozzle dispersion process:

                                                                                      (3.35)
               xs
               where x, is the effective in-situ median particle diameter determined by the cascade
               impactor for the actual secondary dust cloud, and x,is the ultimate median particle size
               determinedby the sedimentation balance. The parameter h is defined by
               h = 0.44Ap,V/do  [J/m3s]                                               (3.36)

               where Apo is the pressure drop across the dispersing nozzle, V  is the mean air velocity
               through the nozzle, and dois the orifice diameter.
                 It is interesting to compare the results in Figure 3.26 with those of Corn and Stein
               (1965),in Figure 3.18, from particle dislodgement experimentsin a narrow wind tunnel
               of cross section comparable with those of the smallest nozzles in Figure 3.26. The order
               of airvelocities required to dislodgeparticles in the sizerange 1-10 pm in Corn and Stein’s
               experiments is the same as required to break up agglomerates of 1-10 pm in the Yamamoto
               and Suganuma’s nozzle dispersion experiments. This indicates that the adhesive forces
               between particles in an agglomerate,a particle, and a plane substrate are of the same nature
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