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168                                     6  Separation of Particles from a Gas

            Table 6.1 Design parameters for a Lapple cyclone
                                     High efficiency  Conventional  High throughput
            Height of inlet, H/D     0.5–0.44       0.5           0.75–0.8
            Width of inlet, W/D      0.2–0.021      0.25          0.375–0.35
            Diameter of gas exit, D e /D  0.4–0.5   0.5           0.75
            Length of vortex finder, S/D  0.5        0.625–0.6     1.5–1.7
            Length of body, L B /D   1.4            1.75          1.7
            Cone length, L C /D      2.5            2             2.5–2
            Diameter of dust outlet  0.375–0.4      0.25–0.4      0.375–0.4


              The residence time of an involute cyclone is estimated by

                    Circumference of the vortex   Number of turns of the air
                 t ¼                                                     ð6:57Þ
                                   Superficial gas speed
            where the number of turns the gas flow makes before turning upward to the vortex
            finder ðN e )is

                                           L B þ 0:5L C
                                      N e ¼                              ð6:58Þ
                                               H
            where L B is the length of cyclone main body, and L C is the length of the cyclone
            lower cone. Then the residence time can be calculated using

                                            2prN e
                                         t ¼                             ð6:59Þ
                                              u 0
              Equation (6.56) then becomes

                                            pN e q

                                                p   2 2
                                   g d p ¼         d v                   ð6:60Þ
                                                    p h
                                            9lWu g
              If the average tangential speeds are approximated as the same, v h   u h     u g ,
            then Eq. (6.60) becomes
                                            p  u g N e q

                                                  p   2
                                    g d p ¼         d p                  ð6:61Þ
                                              9lW
              Instead of using this equation for direct calculation of the particle fractional
            efficiency, Lapple [19] presented a semi-empirical equation by introducing the cut
            size into the analysis. The corresponding cut size is first determined using
            Eq. (6.61) by letting g ¼ 0:5
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