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6.2 Gravity Settling Chambers                                   155

            collected on the surface of the lower plate. This height H c can be referred to as the
            critical height. Then the fractional efficiency of the chamber for this group of
            particles (d p )is


                                               H c

                                        g d p ¼                          ð6:10Þ
                                                H
              The time for a particle entering the chamber at the critical height, H c , falls down
            through a vertical distance H c while traveling a horizontal distance L,is

                                           L    H c
                                        t ¼  ¼                           ð6:11Þ
                                           U   v TS
              It leads to

                                             v TS L
                                         H c ¼                           ð6:12Þ
                                               U
              Substitute Eq. (6.12) into the efficiency Eq. (6.10) above, and we have

                                               v TS L

                                       g d p ¼                           ð6:13Þ
                                               UH
            where the gas incoming speed can be determined from the flow rate of the air
            passing through the chamber,
                                              Q
                                         U ¼                             ð6:14Þ
                                             WH
            where W is the width of the chamber. The terminal settling speed of a spherical
            particle falling in a gravitational field is

                                               2
                                            q d gC c
                                             p p
                                       v TS ¼                            ð6:15Þ
                                              18 l
              Therefore, the fractional particle separation efficiency can be described as
                                               2
                                            q gd C c LW
                                             p  p
                                    g d p ¼                              ð6:16Þ
                                             18 l  Q
            6.2.2 Turbulent Flow Model

            For turbulent flow model, we assume that the particles and the air are completely
            mixed at any cross section that is normal to the direction of airflow. Consider an
            element with an infinitesimal length dx. The concentration of particles within which
            is assumed to be uniform and the particles settle down at a terminal velocity of v TS .
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