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INTAKE FACILITIES                   4.31


           The choice of chemical treatment to be applied at the intake must be coordinated with
         overall optimization of the  water treatment process,  including  the  control  of disinfection
         by-product  formation.  Historically,  chlorine  has  been  used  as  the  standard  treatment  to
         oxidize taste  and odor compounds  at the intake structure.  However,  current practice is to
         avoid the early use of chlorine in the treatment process  where the level of organics  in the
         source  water  is  highest because  of the  potential  for forming  chlorinated disinfection by-
         products such as trihalomethanes. Chlorine dioxide, potassium permanganate,  and carbon
         are  alternatives to  chlorine that  avoid  or minimize the  formation of chlorinated disinfec-
         tion by-products.


         RACKS AND  SCREENS

         Racks  and  screens  remove  suspended  particulates  from  water,  including  leaves,  debris,
         and other sizable clogging material.  Racks  and  screens  are  essential to providing protec-
         tion for downstream conduits, pumps, and treatment works.  Properly designed intake racks
         and  screens  can also  minimize  the effect on fish.
           Racks  and  screens  can  be  divided  into  two  broad  categories:  coarse  screens  (racks)
         and fine  screens.  A  summary  of characteristics  associated  with each type  is presented  in
         Table 4.14.


         Design Considerations
         Head loss through racks  and screens is an important consideration to be evaluated as part
         of  the  design  process.  Racks  and  screens  should  be  designed  to  minimize  head  loss  by
         providing sufficient flow-through area to keep velocities low. The total area of clear open-
         ings  in  a  screen  typically  ranges  between  150%  and  200%  or  more  of the  area  or  chan-
         nel protected  by  the  screen.  The  maximum head loss  from  clogging  should be limited to
         between 2.5 and 5.0 ft (0.76  and  1.52 m),  and the screen should be designed to withstand
         the  differential  hydraulic  load.  Head  loss  for  mechanically  cleaned  screens  of  all  types
         can be held nearly constant with proper operator attention. Curves and tables for head loss
         through screening  devices  are available from  equipment manufacturers.

                   TABLE 4.14  Rack and Screen Characteristics
                         Type                    Remarks
                   Coarse screens  (racks)
                    Trash racks         Clear opening 34  in. (8-10 cm)
                                        Inclined or vertical
                                        Manually or mechanically cleaned
                                        Clear opening 3,4-3 in. (2-8 cm)
                     Barracks
                                        Inclined or vertical
                                        Manually or mechanically cleaned
                   Fine screens
                     Traveling water screen   0.24~).35 in. (6-9 mm) mesh cloth
                                         1/~_3/~ in. (3-10 mm) most common
                     Basket screen
                     Disk or drum screen   Vertical
                                        Water spray cleaning
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