Page 133 - Advanced Mine Ventilation
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114                                               Advanced Mine Ventilation

            The number of particles between x 1 and x 2 is given here by:
                                  x
                        Σ n      log σ  ⎡  (      log x g )log x −  2  ⎤
                n=        i       x ∫  exp ⎢             ⎥ −  ⋅  d log x  (8.22)
                 i
                    log σ  g⋅  2π  log σ  ⎢  ⎣  2log σ g  ⎥  ⎦
                                                  2


            For the mass (weight) distribution, weight fraction between x 1 and x 2 is
                                  x      ⎡  (             2  ⎤
                   ρ S Σ  xi ⋅  3  n  log σ        log x  ) log x −
                                         ⎢
              w=      v       i   x ∫  exp −               ⎥  ∙  d log x  (8.23)
                i
                    log σ  1  2π         ⎢     2log σ 1    ⎥
                                                   2
                         g      log σ    ⎣                 ⎦
                1
                      1
         where x and s are the weight mean and standard deviation, respectively.
                g     g
         8.4.3  The RosineRammler Distribution
         Broken coal behaves a bit differently than silica or limestone. The cumulative mass
         frequency of large or fine coal particles is best described as the RosineRammler
         (RR) distribution [11]. It also fits very well for fine particles obtained from cement,
         gypsum, magnetite, quartz, and glass. Herdan [10] recommends its use to
         (a) distributions that deviate significantly from log normal distributions and
         (b) where particle sizing is done by a series of sieves.
            Let us consider the distribution of broken coal obtained by sieves. Calling the quan-
         tity (in percentage) which passes the sieve, that is, the weight percentages of particles
         smaller than the sieve opening, Y, and the quantity retained on the sieve, that is per-
         centage by weight of particles bigger than the sieve opening, R, we obtain by plotting
         either Y or R against the particle size a straight line called the “fineness characteristic
         curve” of the material. Y þ R is always 100%. The weight distribution curve is math-
         ematically expressed as:

                                        n
                            x n 1
                  dGðxÞ               x
                                     k
             dy ¼       ¼ n       e                                     (8.24)
                    dx      k
         where n and k are constants. k decreases with fineness but “n” remains independent of
         fineness and is a characteristic of the material. “n” is also independent of the device
         used for comminution [10].
            Integrating Eq. (8.24) we get:

                        0          n  1
                                x
                                 k
             y ¼ GðxÞ¼  @ 1   e   A                                     (8.25)

         where y is the cumulative mass fraction below size, x.
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