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SEDIMENTATION 10-27

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           Recommended values for the settling zone design are  R  < 20,000 and  Fr  > 10    (Kawamura,
          2000). A large Reynolds number indicates a high degree of turbulence. A low Froude number
          indicates that water flow is not dominated by horizontal flow, and backmixing may occur. Like
          all design criteria, these values are based on experience. While the desired Reynolds number is
          relatively easy to achieve by modifying the tank shape, the recommended Froude number is very
          sensitive to the shape of the tank and is difficult to achieve while maintaining other design crite-
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          ria when the flow rates are under 40,000 m  /d.
              The Reynolds number may be reduced and the Froude number increased by the placement of
          baffles parallel to the direction of flow. The baffles must be placed above the sludge collection
          equipment and should be about 3 m apart (MWH, 2005).
              GLUMRB (2003) recommends a minimum of four hours detention time or an overflow rate
          not to exceed 1.2 m/h. This appears to be a carryover from the time when basins were manually
          cleaned and were designed with depths of 5 m or more to store large volumes of sludge between
          cleaning. Thus, more than half the volume could be filled with sludge before cleaning was re-
          quired, and real detention times could vary from four hours when the tank was clean to less than
          two hours just before cleaning. Modern designs do not provide for this large of a storage zone,
          and detention times of 1.5 to 2.0 h have proven to provide excellent treatment (Willis, 2005).

            Outlet Zone.  The outlet zone is composed of launders running parallel to the length of the
          tank. The weirs should cover at least one-third, and preferably up to one-half, the basin length. As
          shown in  Figure 10-17 , they are spaced evenly across the width of the tank. If baffles are used, a
          launder is placed midway between the baffles. Long weirs have three advantages: (1) a gradual
          reduction of flow velocity toward the end of the tank, (2) minimization of wave action from wind,
          and (3) collection of clarified water located in the middle of the tank when a density flow occurs.
                The water level in the tank is controlled by the end wall or overflow weirs. V-notch weirs
          are attached to the launders and broad-crested weirs are attached to the end wall. Submerged




























            FIGURE 10-17
           Launders in horizontal-flow rectangular sedimentation tanks.
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