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Dust Explosions: An Overview  67


               I .4.3
               PREVENTING EXPLQSIBLE  DUST CLOUDS


               1.4.3.1
               lnerting by Adding Inert Gas to the Air

              The influence of the oxygen content of a gas on the ignitability and explosibility of dust
              clouds was discussed in Section 1.3.6. For a given dust and type of added inert gas, there
              is a certain limiting oxygen content, below which the dust cloud is unable to propagate a
              self-sustained flame. By keeping the oxygen contentbelow this limit throughoutthe process
              system, dust explosions are excluded.As the oxygen content in the gas is gradually reduced
              from that of air,the ignitability and explosibilityof the dust cloud is also gradually reduced,
              until ultimately flame propagation becomes impossible. Figure 1.72 shows some of the
              results from the experiments by Palmer and Tonkin (1973) in an industrial-scale experi-
              mental facility. Solid lines separate the experiments that yielded no flame propagation at
              all, flamepropagation in part of the tube, and flamepropagated the entire length of the tube.
                 22
               -  20
               $
               0
               J 18
               VI
               4
               W
               z  16
               b-z
               e  14
               z
               3
               5 12
               0
               >-                   A  FLAME PROPAGATION FULL TUBE  LENGTH
               X
               O  10                0  FLAME  PROPAGATION PART TUBE LENGTH
                  ot    I      I    X  NO  FLAME  PROPAGATION I   I
                                               I
                                         I
                                    I
                   10   20    50   100   200   500   1000   2000   5000
                                 DUST  CONCENTRATION[q/d
               Figure 1.72  Concentration range of flammability of clouds of phenol formaldehyde  (15 p is: CO,.
              Experiments are in a vertical tube of diameter 0.25 m and length 5 m. Flame propagated upward (From
              Palmer and Tonkin, 1973).
                 Schofield and Abbott (1988) and Wiemann (1989) have given useful overviews of the
              possibilities and limitations for implementing gas inerting in industrial practice. Five types
              of inert gases are in common use for this purpose:
              Q  Carbon dioxide.
              @  Water vapor.
              0  Flue gases.
              @  Nitrogen.
              Q  Raregases.
                Fischea:(1978) also included halogenated hydrocarbons (halons) in his list of possi-
              ble gases for inerting. However, due to the environmental problems caused by these sub-
               stances, they may no longer be permitted for protecting against explosions and fires.
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