Page 573 - Dust Explosions in the Process Industries
P. 573

540  Dust Explosions in the Process Industries

              The flow of  compressed dust/air suspension into the explosion chamber induces
              turbulence in the gadair mixture. Therefore, choosing an appropriate ignition delay
               (turbulencelevel) is important.The influenceof the compressed air from the dust reser-
              voir on the final explosible gas concentration should be taken into account.
              Tests are conducted for the range of total fuel concentrationsand combustiblegashom-
              bustible dust ratios required.


            7.18
            TESTS OF DUST CLOUDS AT  INITIAL PRESSURES
            AND TEMPERATURES OTHERTHAN NORMAL
            ATMOSPHERIC CONDITIONS


            Industrial processes are sometimes operated at initial pressures, temperatures, or both
            higher than normal ambient conditions. In such cases, results from tests of ignitability
            and explosibility at normal ambient initial conditions may not be relevant. The general
            trends of the influencesof initial pressure and temperature are outlined in Sections 1.3.7
            and 1.3.8 in Chapter 1.
              Tests to elucidate specific problems are most conveniently conducted in closed bombs
            of the types described in Section 7.14, fitted with adequate provisions for heating and pre-
            pressurization and of sufficient strength. This applies both to ignition sensitivity tests and
            explosibilitytests. The proportional increase of the maximum explosionpressure with ini-
            tial pressure (Section 1.3.8)requiresvery strong bombs if the initial pressure is appreciable.
            Bombs of the type in Figure 7.64 may be used if the gas phase differs from pure air.


            7.1 9
            INFLUENCE OF OXYGEN CONTENT IN THE OXIDIZING
            GAS ON THE IGNITABILITY AND EXPLOSlBlLlTY
            OF DUST CLOUDS


            7.1 9.1
            THE INDUSTRIAL SITUATION

            Full and partial inerting is discussed in Sections 1.3.6 and 1.4.3 in Chapter 1.
              The possibility of dust explosions in process equipment can, in principle, be effectively
            eliminated by substituting the air by a gas that prevents flame propagation in the dust
            cloud. Sincethe use of large quantities of inert gas in a plant can be expensive, it is impor-
            tant to limit the inert gas consumption to the extent possible. For most dusts, it is not nec-
            essary to substitute the entire atmosphere in the actual area by, for example, nitrogen,
            carbon dioxide, or other inert gas to obtain inerting. Hence, it is essential to know the
            critical gas composition for inerting the dust in question. In some cases, it may even be
            of interest to use smaller fractions of  inert gas than required for completing inerting,
            because this reduces both the ignition sensitivityof the dust cloud and the maximum pres-
             sure and rate of pressure rise at constant volume.
   568   569   570   571   572   573   574   575   576   577   578