Page 240 - Dust Explosions in the Process Industries
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2 72  Dust Explosions in the Process Industries



























             Figure 3.8  Nominal tensile strength of a fine Sic powder  as  a function of the powder  bed thick-
             ness and bulk density (or porosity  E)  (From Eckhoff et al.,  1978).

























                        - 1000        0         1000        2000        3000
                                         6,  AND  6,  [N/m2]


             Figure 3.9  Combination  of shear test data assuming isostaticconditions in tensiletests (Fromfckhoff
             et al.,  1978).


               This emphasizes the need for improved methods for measuring basic properties of pow-
             ders, as proposed by Arthur et al. (1985).
               An interesting experimentalstudy of the correlationbetween the tensile strength of a
             bulk powder and its dispersibilityin a gas was performed by Yamamoto (1990).
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