Page 274 - Dust Explosions in the Process Industries
P. 274

246  Dust Explosions in the Process industries


             of the screw and optimizing its speed of rotation. However, to ensure proper dust dis-
             persion, the dust output from the worm conveyor was fed into a swirl chamber driven
             by a controlled airflow. A high level of turbulence shear created within this chamber by
             the colliding whirlingjets produced cluster-free,uniform dust dispersion. For high dust
             concentrations and especially for coal dust, a secondarydust dispersion source in the form
             of a high-speed rotary disk was incorporated within the settling chamber. Thus, a uni-
             form and finely dispersed dust cloud could be produced. This was gently drawn into the
             explosion chamber by a small suction pump.



             3.9.5
             CONCLUSION

             Provided the relatively large amounts of powder required and the relatively complicated
             experimental apparatus can be justified, the open-circuit principle is the most satisfac-
             tory alternativefor dust dispersion.However, as for the transientcloud systems,it is essen-
             tial that the dust dispersion system be designed carefully, to ensure that the degree of
             agglomeration of the particles in the cloud and the cloud turbulence corresponds with
             the state actually wanted. Quite often, it is desirable or even necessary to keep the con-
             sumption of dust or powder at a minimum. In such cases, the transient air blast technique
             may, provided the limitations of the technique are borne in mind, offer the best solution.



             REFERENCES

             Akiyama, T., and Y. Tanijiri.(1989) “Criterion for Re-Entrainment of Particles.” Powder Technology,
               57, pp. 21-26.
             Allen, T. (1981) Particle Size Measurement, 3rd ed. London: Chapman and Hall.
             Alquier, M., J. Gruat, and F. Valentian. (1979) “Influence of Large Eddies on the Suspension of Solid
               Particles.” International Journal of Multiphase Flow, 5, pp. 427-436.
             Arthur, J. R. F., T. Dunstan, and G. G. Enstad. (1985) “Determinationof the Flow Function by Means
               of  a Cubic Plane Strain Tester.” International Journal of Bulk Solids Storage in Silos  1, no. 2,
               pp. 7-10.
             Bachalao, W. D., R. C. Rudoff, and M. J. Houser. (1987) “Particle Response in Turbulent Two-Phase
               Flows.” ASME FED, 55, pp. 109-120.
             Bagnold, R. A. (1960) “The Re-Entrainmentof Settled Dusts.” International Journal ofAir Pollution
               2, pp. 357-363.
             Ballal, D. R.  (1983) “Flame Propagation through Dust Clouds of  Carbon, Coal, Aluminium and
               Magnesiumin an Environmentof Zero Gravity.”Proceedings of  the Royal Society of London A385,
               pp. 21-51.
             Bartknecht,  W.  (1971) “Brenngas- und  Staubexplosionen.”  Forschungsbericht  F45.  Koblenz:
               Bundesinstitut  fur Arbeitsschutz.
             Bauer, G. (1918) “On Dust Explosions.”  2. ges. Schiess.-u. Sprengstofi. 13, pp. 272-273.
             Beer, J. M., J. Chomiak, and L. D. Smoot. (1984) “Fluid Dynamics of Coal Combustion:AReview.”
               Progress in Energy Combustion Science 10, pp. 177-208.
             Boyle, A. R., and F. J. Llewellyn. (1950) “The ElectrostaticIgnitability of Dust Clouds and Powders.”
               Journal of the Society of the Chemical Industry, London 69, pp. 173-181.
             Brown, K. C., and G. J. James. (1962) “Dust Explosions in Factories: A Review of the Literature.”
               Research Report No. 201. Sheffield, UK: Safety in Mines Research Establishment.
   269   270   271   272   273   274   275   276   277   278   279