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356  Dust Explosions in the Process Industries

            He pointed out that the initiating explosion causes events analogous to those observed
            in shock tubes. The initial thin turbulent dust flame entrains deposited dust and devel-
            ops into the more extensive main explosion, which may in turn lead either to detona-
            tionlike phenomena, including strong shock waves, or to oscillating flames, depending
            on various circumstances.
              Bartknecht (1971) used an external dust dispersion system by which he avoided the
            use of a primary explosion for initiating dust entrainmentand flame propagation.He gen-
            erated a dust cloud of the most explosibleconcentration along the whole tube length by
            simultaneously injecting dust from a number of  equally spaced external pressurized
            reservoirs. (This is essentially the same dust dispersion method as specified in the 1 m3
            test approved by the International Standards Organization, 1985.) The dust cloud was
            ignited by a strong chemical ignitor or a pocket of exploding methane/air as soon as it
            had been generated. On the one hand, Bartknecht’s experiments were clean and well
            defined. On the other hand, they differed from conditions often met in mines and other
            industry, where the dust is initially deposited as layers that are dispersed by the air blast
            preceding the flame as the explosion propagates. There may be situations, however,
            where Bartknecht’s dispersion method corresponds to reality, for example, in pneumatic
            transport of explosible dust concentrations.
              Figure 4.64 gives some of Bartknecht’s results from experiments in 0.40 m diameter
            horizontal one-end-openpipes of various lengths.As can be seen, there is close correlation

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                            COAL  METHYL   ORGANIC       ALUMINUM
                                 CELLULOSE  PIGMENT

             Figure 4.64  Dust explosions in 0.40 m diameter,horizontal, one-end-openpipes of various lengths,
             with maximum flame speeds and maximum explosion pressures as  functions of  tube length and K,,
             value of dusts;  * denotes enlarged pipe diameter in  the ignition  zone  at the closed end  (From
             Bartknecht, 1971).
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