Page 368 - Dust Explosions in the Process Industries
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Propagation of Flames in Dust Clouds  337


                                      /OUTLET   PORTS I81
                                         [132OPTIONAL1
                                                            \TL+

                                                            DUST FEEDER




                                                                    AIR  lNLEl






                                              INLET PORTS I61

               Figure 4.44  A 0.95 m3 spherical dosed bomb for studying a combustion of turbulent dust clouds
               (From Kauffman et al., 1984a).

                 Kauffman et al. (1984a) studied the development of turbulent dust explosions in the
               0.95 m3sphericalexplosionbomb illustrated in Figure 4.44. The bomb is equipped with
               six inlet ports and eight exhaust ports, both sets being manifolded and arranged sym-
               metrically around the bomb shell. Dust and air feed rates were set to give the desired dust
               concentration and turbulence level. The turbulence level generated by a given airflow
               was measured by a hot-wire anemometer.The turbulence intensity v’, assuming isotropic
               turbulence, was determined from the rms and mean velocities extracted from the hot-
               wire signal in the absence of dust. As pointed out by Semenov (1965), a hot-wire probe
               senses all velocities as positive, and therefore, a positive mean velocity is recorded even
               if the true mean velocity is 0. In agreement with the suggestionby Semenov, Kauffman
               et a]. assumed that v’  = (1/2)1/2x [(rms velocity)’ + (mean ~elocity)~]’”.This essentially
               is a secondaryrms of two different mean velocities, the primary rms and the arithmetic
               mean oE the hot-wire signal.
                 Kauffman et al.were aware of the complicatinginfluence of dust particles on the tur-
               bulence structure of the air, but they were unable to account for this. It was found that
               the turbulence intensity, in the absence of dust, was reasonably uniform throughout the
               1 m3 vessel volume.
                 When a steady-state dust suspension of known concentration had been generated in
               the 0.95 m3 sphere, all inlet and exhaust openings were closed simultaneously and the
               dust cloud ignited at the center. The rise of explosion pressure with time was recorded
               and (dpldt),,,  and P,,,   determined. Figures 4.45 and 4.46 show a set of  results for
               maize starch.
                 The marked increase of  (dP/dt),,,   with turbulence intensity v’  in Figure 4.45 was
               expected and in agreement with the trend in Figures 4.41-4.43. However, as shown in
               Figure 4.46, v’  dso had a distinct influence on P,,.   At the first glance,this conflicts with
               the findings of Eckhoff (1977) and Amyotte and Pegg (1989) in the 1.2 liter Hartmann
               bomb, where there was little influence of the ignition delay on P,,  up to 200 ms delay.
               However, Eckhoff (1976) discussed the effect of initial dispersion air pressure on the
               development of  explosion pressure in the Hartmann bomb. He found a comparatively
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