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Dust Explosions: An Overview  12 1



              SELECTING APPROPRIATE MEANS FOR PREVENTING
              AND MITIGATING DUST EXPLOSIONS

              1.5.1
              BASK PHILOSOPHY, COST ESTIMATION, AND RISK ANALYSIS

              1.5.1 .I
              The Optimal Solution, or Striking the Balance

              The extensive menu of means of preventing and mitigating dust explosions, summarized
              in Table 1.9, is discussed in Section 1.4.
                Noha (1989) emphasized that the concepts of “primary” and “secondary” means of
              protection against dust explosions, used in the Federal Republic of Germany in the past,
              can be misleading, by indicating that mitigation is of secondary importance as compared
              to prevention. The rational approach is to seek an optimal combination of means of both
              categories for each specific application. In doing so, Noha suggested the need to break
              down the problem and evaluate specifically

              @  The efficacy of the protective means.
              @  The technical feasibility.
              @  The environmental acceptability.
              @  The financial acceptability.
              Figure 1.138 illustrates the situation.







                                                      Figure 1 .I 38  The appropriate set of means for
                                                      preventing and mitigating dust explosions  de-
                                                      pends on type of dust, type of process, and the
                                                      boundary  conditions in  terms of plant  layout,
                                                      type of building(s1,  environmental  constraints,
                                                      financial constraints, and so forth.
                One pitfall related to assessing the efficacy of the protective means is the selection of
              the dust sample on which the assessment is to be based. Noha (1989) mentioned as an
              example a comparatively coarse polypropylene powder to which 4%of fine calcium
              stearate had been added to increase flowability. Such additives have large specific sur-
              face areas and correspondingly low minimum ignition energies. But, as long as they are
              homogeneously mixed with the polypropylene, the small fraction of additive has little
              influence on the ignitability and explosibility of the polypropylene powder as a whole.
              However, if segregation OCCLU-s,the fine, reactive additive may accumulate in certain areas
              of the process, for example, in a filter. This can create a much more hazardous situation
              than would have been anticipated on the basis of the properties of the polypropylene
              powder. Ilnsuch cases, it may be wise to base the assessmentof the efficacy ofthe protective
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