Page 233 - Dust Explosions in the Process Industries
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Generation of Explosible Dust Clouds  205




















                Figure 3,2  Liquid bridge between two identical spherical particles (From Schubert, 1973).

                Here E is the porosity of the bed, F(E)the mean interparticleforce (dependent on E), and
               x is the particle diameter. Equation (3.8) is derived from equation (3.10) via the rela-
                tionship E x k( E) = 3.1 = x,found experimentally for spherical particles.
                  Schubert’s equation for the tensile strength of  a powder due to interparticle liquid
                bridges is as follows:

                (r  =-Y.1-E-OF,(€,   S, 6, ;)U
                 T                                                                      (3.9)
                     X   E
                Here y is the surfacetension of the liquid. FF(e,S, 6, dx) is the dimensionlessliquid-bridge
                interparticle attraction force, where S is the fraction of the total pore volume between
                the particles that is filled with liquid, and uand 6are as shown in Figure 3.2. Equation
                (3.9) cannot be solved analytically, but Schubert (1973) arrived at a graphical solution.
                  The liquid bridge regime extends up to about S = 0.25 (Schubert’s experiments with
                70 pm limestone particles). This regime is the most relevant one with a view to trans-
                formation of dust deposits into explosible dust clouds. For a powder of specific density
                of  1g/cm3packed to a porosity E of 0.4, S = 0.25 represents a moisture content of  14%
                (neglecting moisture absorbed by the interior of the particles). The transition regime in
                which the liquid partly forrns bridges between particles and partly fills the voids com-
                pletely spans from S=0.25 to S=0.8. When the voids between the particles arejust filled
               with liquid, the tensile strength of the bulk powder is determined solely by the internal
               underpressurecaused by capillary forces. In practice, this is the case for 0.8 < S < 1.0.
                 Figure 3.3 summarizessome of Schubert’s (1973) experimentaland theoreticalresults.
               He found that equation (3.9), using alx =0.05,yielded excellent agreementwith the exper-
               iments in the liquid bridge regime, for which there is a strong increase of o,as S increases
               from 0 to 0.1.
                 For particles of density 1g/cm3packed to a porosity of 0.4, S =0.1 correspondsto a mois-
               ture content of 6.25%. It is therefore to be expected that the influence of the moisture con-
               tent on the dispersibilityof the powder is particularly strong in the range of a few percent
               of  moisture. However, this does not apply if  a significant fraction of  the moisture is
               absorbed by the interior of the particles rather than adhering to the particle surfaces.
                 As S increases and moves into the capillary pressure region, the tensile strength of the
               powder bed increases further. As Figure 3.3 shows, the tensile strength of the powder
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