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8.16                       CHAPTER EIGHT


           Advantages of auxiliary surface wash include proven effectiveness in alleviating dirty
         filter  problems,  improved  cleaning  (when  compared  with  water  wash  alone)  without  a
         great  change  in  system  complexity,  and  possibly  lessened  danger  of gravel  upset  if the
         quantity  of washwater  introduced  through  the  underdrain  is reduced.
           Because  surface wash  systems constitute a possible  connection  between filtered and
         unfiltered water,  backflow prevention devices must be provided  in supply lines.
           Continuous  Backwash.  An  alternative  to  the  automatic  control  of standard  filters  is
         the  use  of continuous  backwashing  filter beds,  which  eliminate  the  need  to  remove the
         beds from service for washing.  Beds are divided into a series of narrow,  contiguous cells,
         each containing its own underdrain  system that allows it to be washed independently from
         remaining cells. Washing is accomplished by means of a traveling hood suspended  above
         the  bed.  As  the  hood  travels  across  the  bed,  each  cell is  isolated,  and  a  small backwash
         pump  draws  clean  water  from  the  filter effluent  and  reverses  the  flow through  that  par-
         ticular cell. Water is removed by a  second washwater  pump  located in the traveling hood
         and  discharged  to waste.
           The  wash  cycle time  is  controlled  by  preset  adjustable  timers  to  permit  optimization
         of the  automatic  operation  feature.  Media  depth  varies  with  each  application but is typi-
         cally  30 to  36  in.  (0.8  to 0.9  m).
           In addition  to  automatic  washing  features,  these filters have the capability of produc-
         ing relatively constant  washwater flow. In a properly sized system, this constant flow can
         eliminate  the  need  to  provide washwater  equalization  facilities and  can  permit direct re-
         cycle  to  the  plant  headworks.  Consult  with  local regulators  as  to  the  feasibility of recy-
         cling washwater.

         Wash Rates.  In the United  States,  wash  rates  are expressed  as volumetric flow per unit
         surface  area  (gpm/ft2).  In Europe,  wash  rates  are  expressed  as  the  equivalent water  rise
         velocity (ft/s,  ft/min,  in./min,  mm/s,  or  m/h).  Wash  rates  are  generally  variable  and  de-
         pend  on washwater  temperature,  filter media characteristics,  and  washing  method.  Water
         viscosity decreases  with increasing temperature.  Consequently,  as washwater temperature
         rises,  drag  forces  on  media  grains  are  reduced,  and  higher  wash  rates  are  required  to
         achieve bed expansion. Each degree Celsius increase in water temperature requires roughly
         a  2%  increase  in wash  rate  to  prevent  a  reduction  in bed  expansion.  Filter wash  systems
         should  be  designed  for the  warmest  washwater  temperature  that  will be encountered.
           Filter media  characteristics  also  affect washing  rate.  Rate requirements  increase  with
         increasing  grain  size  and  density.  Also,  angular  grains  are  more  easily  expanded  than
         round  grains.  In filters  using  more  than  one  type  of filter medium,  sizes  of each  type  of
         medium  must  be  selected  carefully  to  ensure  proper  positioning  after  water  wash.  Rec-
         ommended  size ratios for dual-  and  mixed-media beds  were discussed  previously. Figure
         8.8 displays  the effect of media  size on the water wash  rate required to achieve  10% bed
         expansion  for three  common  filter media.  Figure  8.9  shows  the  effect of water tempera-
         ture  on  the  viscosity  of  water  and  on  the  wash  rate  for  silica  sand  and  anthracite  coal.
         Specific backwash  rate  curves  can  be  provided  by  media  suppliers.  A  minimum rate  of
         15  gpm/ft 2 (37  m/h)  is  recommended,  with  typical  rates  ranging  from  15  to  23  gpm/ft 2
         (37 to 56 m/h). Rates as low as  10 gpm/ft 2 can be utilized for full-depth GAC or anthracite
         filters.
           Characteristic  washing  rates  and  durations  vary  for  each  washing  method  discussed
         previously. The  suitability of a  washing  method  is related  to influent water quality, filter
         media characteristics  and bed configuration,  and underdrain  design.  Consequently, not all
         washing  methods  are applicable in all cases,  and  different methods  may or may not yield
         similar results  in a  particular  case.
           Upflow Water Wash without Auxiliary Scour.  When water wash is used alone, a high-
        rate  wash  is  employed.  Generally  a  wash  rate  of  15  to  23  gpm/ft 2 (37  to  56  m/h)  is  ap-
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