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6.5 Filtration                                                  183


                                                 g 4aL
                                                   sf
                                 g d p ¼ 1   exp                         ð6:98Þ
                                               ð  1   aÞpd f
              The results are shown in Fig. 6.14.

              Up to this point we assumed that filter fibers are oriented normal to the incoming
            air flow. It is clearly not the case in most engineering applications. Fiber orientation
            also affects the filtration efficiency and resistance to the air flow. The overall fil-
            tration efficiency is affected by the three-dimensional randomness of the fiber ori-
            entations too [31]. A filter with fibers randomly arranged in planes perpendicular to
            the approaching air velocity is more efficient than a filter with fibers randomly
            arranged in three dimensions.
              The other assumptions in the preceding analysis of fibrous filtration are that all
            the aerosol particles are spherical and that the adhesion efficiency is 100 %. These
            simplifications do not introduce much of error because the likelihood of an aerosol
            particle adhering to a fibrous filter depends on not only the air flow velocity but also
            the particle–filter interfacial characteristics. Nonspherical particles are more likely
            to be captured than spherical ones. And, functions that correct for imperfect
            adhesion can be empirically derived for particular cases.



            6.5.3 Fibrous Filter Pressure Drop


            The pressure drop across a fiber filter is caused by the combined effect of each fiber
            resisting the flow of air past it. Davies [8]defined a dimensionless filter pressure
            coefficient as

                                               DP
                                      C DP ¼     .                       ð6:99Þ
                                           4lU 0 L d 2
                                                   f
              With a known pressure drop coefficient, the pressure drop can be calculated as

                                               4lU 0 L
                                      DP ¼ C DP  2                      ð6:100Þ
                                                d
                                                 f
              By dimensionless analysis and experimental correlation, Davies [8] obtained
            C DP as a function of solidity in the range of 0.06–0.3 as follows,

                                   C DP ¼ 16a 1:5    1 þ 56a 3          ð6:101Þ

              Combination of Eqs. (6.100) and (6.101) leads to the total pressure drop over a
            bulk filter as
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