Page 179 -
P. 179

7.42                       CHAPTER SEVEN

         Application
         The  fact  that  clarification  results  from  filtration  limits  the  solids  levels  that  can  be  re-
         moved by  contact clarification without  causing  excessive cleaning.  This  process  is most
         effective for source water having low turbidity,  color, iron,  and manganese.  On such wa-
         ters,  it can be  an economical alternative to  more  conventional types  of clarification: It is
         especially applicable to  upgrading  overloaded direct filtration  systems.


         Design Criteria
         Contact  clarifiers  are  rated  on  the  basis  of  surface  loading  rate  and  typically  operate  in
         the range of 8 to  10 gpm/ft 2 (20 to 24 m/h). To maintain effective flocculation, units must
         also be  selected to operate  in the range  of 50%  to  100%  of design  capacity.


         Operation
         Source  water  is  chemically  treated  by  the  addition  of metal  salts  or polymers  in  a  rapid
         mixer, usually of the  static mixer type.  Chemically treated water is then introduced to the
         clarifier in an upflow  or downflow  mode,  depending  on the proprietary  process  selected.
         Clarified water is then  filtered in a  typical  granular  medium  filter.


         Inlet Conditions

         Proprietary  units  are  designed  as  upflow  units.  The  Adsorption  Clarifier uses  a  buoyant
         medium  held  in  place  by  a  screen.  Chemically  treated  source  water  is  introduced  under
         the medium through  a  pipe lateral.  Other types of units  use a  medium  heavier than water
         that  must  be  supported  by  a  media-retaining  support  system  typical  of gravity  filters.  In
         all cases,  source  water  flows up through  the  medium  as  it would  for any  upflow filter.


         Outlet  Conditions
         Clarified water  is collected above  the  medium  in an  effluent trough  similar to backwash
         troughs  in a  filter and  then  flows to the filter through  an  outlet  valve.


         Sludge  Removal
         Because solids are removed by filtration, they must be removed by backwashing  or flush-
         ing.  The  flushing  cycle  is  initiated  after  a  preset  head  loss  has  been  reached  or a  preset
         time has  passed.
           The  cycle  is  started  by  closing  the  effluent  and  influent  valves.  The  medium  is  first
         air-scoured.  Air is necessary  in the adsorption  clarifier to allow buoyant  media to expand
        during  the  flushing  cycle.  Air reduces  the  apparent  density  of the  water,  causing  media
        to  lose  buoyancy  and  opening  pore  spaces  so  that  accumulated  material  can  be  flushed
        out.  Air is also  necessary  with  other types  of media  to assist  water  in  scouring  accumu-
        lated  solids.
   174   175   176   177   178   179   180   181   182   183   184