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14.22                    CHAPTER FOURTEEN





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            .~   it~rd a  syste   4~   ~   4    4      •



                                                Sand  -  4  to 6  in
                                                Carbon  -  3  to 8  in
                                                Sand  -  8  to 10 in
                                                Underdrain  system  -  see Figures  14B  &  149
         FIGURE  14.11  Media  arrangement in a  GAC  sandwich slow  sand filter.

           Postfilter adsorbers  typically use GAC with small effective sizes and  large uniformity
         coefficients to  promote  rapid  adsorption  of organic  compounds,  better  stratification,  and
         reduction  of overall carbon  loss.  These  adsorbers  also  can  provide  an  improved barrier
         against  microbial  penetration,  are  more  compatible  with  other  advanced  treatment  pro-
         cesses such  as  ozonation  (or ozone  and  hydrogen  peroxide),  and  use more of the adsorp-
         tive capacity  of the carbon.

         Adsorber  Configurations.   Various  combinations  of the  three  GAC  contactor  configu-
         rations  and  flow patterns  can  be  made.  Some  of the  most  common  contactor  configura-
         tions  are  shown  in  Figure  14.12.  Table  14.5  provides  a  summary  of each  configuration
         described  below.
         Fixed Beds  in  Series.  In  this  configuration,  flow is downward  through  the carbon  bed
         for each  unit  connected  in  series,  with  the  EBCT  divided between  the  number  of adsor-
         bers.  The  first in the  series  receives the highest contaminant  loading  and  is thus the  first
         to be exhausted.  The last in the series receives the lightest contaminant loading and serves
         as a polishing  step.  When  carbon  is removed for reactivation,  the first adsorber in the se-
         ries is removed from  service, with  the next adsorber  in line becoming the  lead unit.  This
         system  can  be  constructed  with  an  extra  adsorber  on  standby  to  become  the  first  adsor-
         ber when the lead adsorber is taken out of service. The configuration can be arranged and
         controlled  so that  the freshest  GAC  is always  the  last  step  in the  series.
           Capital  cost  considerations  usually  limit the  number  of adsorbers  in  series  to four or
         fewer,  because  the  increased  cost  of piping  and  valving counters  the  cost  benefit of re-
         duced carbon usage. Countercurrent flow provides highly efficient usage of the carbon by
         maximizing carbon  exhaustion  in the lead adsorber  before it is removed for reactivation.
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