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CLARIFICATION                      7.21


           A  more controllable feed design includes using  a  distribution  well inside a  large  feed
         well that  is  about  3%  to  4%  of the  basin  area.  This  distribution  well has  multiple  ports
         hooded  with adjustable biased  gates.  The gates balance  tangential feed discharges  by im-
         posing  about  a  4-in.  (10-cm)  head  loss  through  the  ports.  This  type  of discharge  causes
         the homogenized mass within the large feed well to rotate around the vertical axis at about
         2 ft/s (61  cm/s). The well-distributed, fine-scale turbulence within and below the feed well
         encourages floc aggregation, and the overall slow rotation ensures that flow from the bot-
        tom of the  skirt into the hindered  sludge mass  moving radially across the floor has  equal
         displacement  vectors.
           Density  and  displacement  currents  for circular basins  are  much  the  same  as  for long,
        rectangular basins.  The vector system is influenced by well-flocculated influent mass sink-
        ing to  the  bottom  adjacent  to  the  feed  well area,  typically  in  the  center  one-third  of the
        basin  (about  10%  of the total basin  area).  The vector system  shows displacement radially
        along the bottom  in the blanket  zone  and  upwelling next to the peripheral  wall.  Clarified
        water generally  flows across  the  surface toward  the  effluent.

        Outlet Design.  Clarified water  collection must  be uniform  around  the  perimeter  of the
        basin.  This is accomplished by a circular trough around  the perimeter with V-notch weirs
        or  with  submerged  orifices.  Some  designs  use  a  double-sided  weir  trough  mounted  in-
        board  along at least  15%  of the tank radius.  This has  the advantage  of reducing wall flow
        disturbances  and  drawing  overflow from  a  more  widely  distributed  region  to  offset  the
        effects  of bottom  density  currents  running  up  the  peripheral  wall.  Inboard  weir  troughs
        also  partially  break  up  wind  current  stirring.  Troughs  should  have  small-diameter  holes
        in the bottom to reduce  buoyant  uplift forces when  they are  empty.
           Some designers prefer orifice troughs to overflow weir troughs because less floc breakup
        occurs.  Others point out that the velocity gradient in a weir trough  is no greater than in an
        orifice trough.  Weir  troughs  are  far  easier  to  adjust  for  equal  linear  overflow, but  if not
        properly  adjusted,  they  have  greater  variation  in  flow  than  improperly  adjusted  orifices.
        Submerged orifice troughs reduce passage  of floating trash  to the filters and permit varia-
        tion in basin  water depths  during  operation.  This  capability  is useful for balancing  differ-
        ences in plant  inflow and discharge rates,  such  as  when multiple filter washing  occurs.
           Regulatory  agencies  sometimes  stipulate  that  weir  rates  should  not  exceed  around
        20,000  gpd per linear foot (248,000  L/m)  of weir.  Flood (1961)  found that weir overflow
        rates  several times this value could be used if the weirs were well distributed  over a  sub-
         stantial portion of the surface.  Placing  a double-sided weir trough  1 ft (0.3  m) away from
        the peripheral  wall  satisfies  the regulatory requirements,  but  still draws  overflow from  a
         narrow  band  of surface immediately in the path  of the upwelling peripheral  flow.

         Sludge Removal  Sludge is removed from circular basins using circular collection equip-
         ment powered by a center turntable  drive and plows that move sludge into a center sludge
         hopper.
           Turntable Drives.  The  tried  and  true,  relatively  trouble-free  drive  for  both  bridge-
         supported  and pier-supported circular collectors is the sealed-turntable drive with the gear
         and  pinion  running  in  oil.  Properly  lubricated  and  with  automatic  condensate  overflow,
         these drives operate for years without major repair.  Typical turntable  drives rotate  on re-
         newable bearing  strips,  and the gear is split so that the ball bearings  and  strips  can be re-
         placed without dismantling  the remainder  of the equipment.
           These  drives  are  protected  by  an  indicator  and  overload  circuit breaker  device  actu-
         ated  by  the  thrust  of the  primary  worm  gear  driving  the  pinion  and  turntable  gear.  The
         indicator  senses  the  torque  load  exerted  on  the  collection arms  by  the  sludge  and  turns
         off power if the  load exceeds  a  preset limit.
           Sludge Hopper and Bottom Slopes.  Because  a  circular sludge hopper  surrounding  a
         central pier holds the greatest volume, it is preferable  to the older-style offset hopper de-
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