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SEDIMENTATION 10-19

               For cocurrent settling, the settling time for a particle to move between two parallel plates is
          given by  Equation 10-23 . The time that particles moving with the fluid spend in the plates is
                                                    L p
                                         t p                                         (10-28)
                                               v fc    v s sin

           If  Equation 10-23  is equated to  Equation 10-28 ,  t    p    is equal to the settling time  t.  Those particles with a
          settling velocity  v    s    are removed. Those particles with larger settling velocity are also removed, that is
                                                   v fc  d
                                      v s                                            (10-29)
                                             L p cos       d sin

               For crosscurrent settling, the settling time for a particle to move between two parallel plates is
          also given by  Equation 10-23 . The time that particles moving with the fluid spend in the plates is
                                                    L p
                                              t p                                    (10-30)
                                                    v fc

              If  t    p    is equal to the settling time (equating  Equation 10-23  and  Equation 10-30 ), then the
          particles with settling time  v    s    are removed. Those particles with a larger settling velocity are also
          removed, that is

                                                   v fc  d
                                           v s                                       (10-31)
                                                  L p cos

              Non-Ideal Behavior of Settling Tanks
           Numerous factors affect settling tank performance. These include turbulence, inlet energy dissipa-
          tion, density currents, wind effects, outlet currents, and sludge equipment movement. In general, for
          most water treatment sedimentation basins, performance is primarily a function of turbulence, inlet
          energy dissipation, density currents, and wind effects rather than outlet currents and mechanical
          movement. Therefore, this discussion is focused on these effects.

            Turbulence.   In Camp’s development of a theoretical basis for removal of discretely settling
          particles he assumed a uniform horizontal velocity in the settling zone. This assumption implies
          near laminar flow conditions (Reynolds number  1). This is rarely, if ever, achieved in actual
          settling tanks. However, this important assumption is considered in the design of the tank by
          evaluation of the Reynolds number and the Froude number. These dimensionless ratios are
          described in the next section of this chapter.
              The Reynolds number is important as a measure of turbulence in flows that are influenced by
          viscous effects, such as internal flows and boundary layer flows. The Froude number is important
          in flows that are influenced by gravity, such as free surface flows.

            Inlet Energy Dissipation.  The performance of the sedimentation basin is strongly influenced
          by the effectiveness of energy dissipation at the inlet. Again using Camp’s theory, the flow must
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