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AERATION AND AIR STRIPPING               5.5

        Diffuser Aerators.   The most common type of equipment for diffusion aeration  consists
         of rectangular  concrete  tanks  in  which  perforated  pipes,  porous  diffuser tubes  or plates,
         or other impingement devices are inserted.  Compressed  air is injected through the system
         to produce  fine bubbles,  which,  on rising through the water, produce turbulence resulting
         in effective water-air mixing.
           This  type  of aeration  technique  is often  adapted  to  existing  storage  tanks  and  basins.
         If porous  tubes  or  perforated  pipes  are  used,  they  may  be  suspended  at  about  one-half
        tank  depth  to  reduce  compression  head.  Porous  plates  are  usually  located on  the bottom
        of the tank.  Static tube aerators  are also used  in a variety of applications  and provide ad-
        equate  aeration  when  properly  designed.
           A  relatively new type of diffused aeration equipment is the low-profile system,  which
        is a multistage,  diffused bubble  air stripping device. The device differs from conventional
        systems  in  that  it operates  with  a  water  depth  of about  18  to  36  in.  (46  to  92  cm)  com-
        pared  with  10 ft (3 m) or greater for conventional installations.  Shallow water depth  per-
        mits  the  use  of regenerative  or  centrifugal  blowers  instead  of compressors  and  reduces
        overall height of the device to less than  4  to  5  ft.
           In this system, water flows by gravity through  a  series of completely mixed staged re-
        actors.  Individual modules are designed and fabricated to include three, four,  six, or eight
        stages,  depending  on the level of treatment  required.  Each  stage  is  separated  by  a  baffle
        wall and  includes  separate  diffuser heads.  Air is blown into each  stage,  creating  a  turbu-
        lent mixture of diffused bubbles  and water to provide efficient mass transfer.  A  schematic
        of a  typical  device of this  type  is  shown  in Figure 5.3.
           Individual  modules  are  designed  to  treat  water  at  flow rates  ranging  from  1 to  1,000
        gpm  (0.06  to  63  L/s).  Modules  used  in parallel can treat  water  at higher flow rates.  This
        system  also  removes  carbon  dioxide,  VOCs,  gasoline  components,  hydrogen  sulfide,
        methane,  and radon from contaminated groundwater and is particularly applicable to small
        water  systems  with  low  flow rates.  Two  drawings  of low-profile  systems  are  shown  in
        Figure 5.4.








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        FIGURE 5.3  Schematic of a flow-through low-profile aeration system. (Courtesy of Lowry Aeration
        Systems.)
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