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MIXING, COAGULATION, AND FLOCCULATION         6.13

           Energy  applied  by  air injection may  be varied directly by  adjusting  airflow.  Air mix-
         ing  is  not widely  used,  and  before  it is  incorporated  into  a  design,  an  inspection  should
        be made  to determine  whether  scum and  floatable material  would be a  problem.  Limited
        quantities  of floating  scum  (or  sludge)  may  be  accepted  onto  filters,  but  certain  coagu-
         lants  and  algae may increase  scums.

        Hydraulic Mixing.  Hydraulic  mixing can be achieved by using V-notch weirs, Parshall
        flumes,  orifices,  throttled  valves,  swirl  chambers,  and  simple  turbulence  caused  by  ve-
        locity in  a  pipe,  fitting,  or  conduit.  Hydraulic  mixing  is  a  nonbackmix  method  that  can
        sometimes  be highly efficient. The principal problem is that energy input varies  with the
        flow.  However,  if a  plant  has  relatively constant  flows,  energy  variations  may  not  be  a
        concern.  Seasonal  flow variations  can  sometimes be overcome by  varying the number  of
        plant mixing modules in operation to maintain more or less constant  flows on those mod-
        ules in operation.
           Total head  loss  across  a  throttled  valve used  for  mixing  coagulant  chemicals  should
        not exceed 4  ft  (3.2  m).  If head  loss exceeds this  amount,  coagulants  should  be  added  to
        the flow downstream  of the valve in the zone of decaying energy because  excessive con-
        fined energy  may  shear polymers.
           The energy provided by a weir with an effective fall of 1 ft (30 cm) provides a G valve
        of 1,000  s-1  at 20 ° C.  Such a weir mixer with a downstream baffle develops  G  values as
        a function of flow, as  shown  in Table 6.4.  If the volume V where turbulence  dissipates  is
        assumed  to be  constant,  G  may  vary  significantly; but  if turbulence  volume  is  assumed
        to be proportional  to the flow Q, there  is a  lesser variation in  G.
           Weir  mixers  require  that  coagulant  chemicals  be  fed equally  across  the  length  of the
        weir at multiple points  spaced  at not more than the head  distance of the weir.  Because  of
        maintenance  problems  with  multiple-orifice chemical feed manifolds  and  other practical
        considerations,  weir mixers tend to be used on plants  of less than  approximately  40  mgd
        (151  ML  per day)  capacity.

        Induction Mixing.  Induction  mixing  essentially  serves  as  an  all-in-one chemical  feed,
        mixing,  and  control  system.  Induction  mixing  systems,  which  are  primarily  proprietary
         systems,  have primarily  been  utilized for  gaseous  introduction  of disinfectants  in  waste-
        water treatment  facilities. However, the application of this  process  can be considered for
        metal  coagulants  in  drinking  water.
           Induction  mixers basically employ a  vacuum via a  propeller  system to pull  coagulant
         chemicals into the mixing system and then inject into the water stream.  The chemical re-



              TABLE  6.4  Hydraulic  Weir Mixing

              Flow Q (percent  of maximum)   G relative  (V constant)   G relative (VQ)
                       1.0                   1.0              1.0
                      0.9                    0.92             0.97
                      0.8                    0.83             0.93
                      0.7                    0.74             0.88
                      O.6                    0.65             O.84
                      0.5                    0.47             0.73
                      0.35                   0.42             0.71
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