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9.28                       CHAPTER NINE


         tank  when  DE concentration  is determined  before supplementary  DE is  added  for use in
         mixing a  new batch  of slurry.
           For  DE  concentrations  of 4%  or less,  case-hardened  centrifugal  pumps  may  be  used
         for  slurry  transfer.  Abrasion-resistant  chemical feed metering  pumps  are  also  acceptable
         for  these  concentrations.  Thicker  slurries  must  be  conveyed  with  either  peristaltic-type
         pumps or rubber-lined centrifugal pumps. To minimize breakdown of DE material, pipeline
         velocities should  be  limited to  no  more  than  8  ft/s  (2.4  m/s),  but  must  be  maintained  at
         over 3  ft/s  (0.9  m/s)  to  prevent  settling.

         Waste Disposal.  Because it is predominantly inert, waste DE slurry may be easily treated
         by  thickening  with  polymers  and  dewatering  on  belt  filters.  DE  slurry  may  also  be  set-
         tled  and  concentrated  in  lagoons.
           At large  installations,  DE  may  be  recovered from  wastes  for reuse  as  body  feed, but
         it should never be used  for precoat.  Virgin DE should be used for precoat to provide a fi-
         nal barrier for any  pathogens  that  may pass  through  the upper  levels of the cake. DE re-
         covery saves costs  of DE purchases  and  reduces  the costs  of waste  disposal.
           In the recovery process,  separation  of the  lighter source  water  solids  from the  denser
         DE  is  accomplished  by  pumping  wastes  through  a  series  of vertical hydrocyclones.  The
         heavier DE material gravitates to the bottom discharge to exit into a collector tank,  while
         most of the source water  solids and the finer fraction of the DE remain  in the center core
         of the  unit.  The  finer  material  is  then  removed hydraulically  from  the  top  of each  unit.
         Because  of  the  erosive  nature  of  DE  slurry,  it  is  necessary  to  use  hydrocyclones  con-
         structed  of ceramic  material  and  pumps  designed  for abrasion  resistance.
           A  typical  recovery system  with  connections  to the filtration  process  is  shown  in Fig-
         ure 9. t 8.  Recovery rates  generally range  between 85%  and 90%.  Because of the possible
         carryover of some bacteria,  viruses,  and  cysts  that  have  been  separated  in  precoat filtra-
         tion,  it is advisable to disinfect the recovered material before use as body  feed.  One sim-
         ple  method  of disinfection is the  application  of a  heavy dose of potassium  permanganate
         to the material  before it is reused.  Where  Cryptosporidium cysts  may exist, ozonation or
         UV  may be the only suitable  methods  of disinfection.
         System  Controls.  Most  pressure  filter  systems  are  provided  with  automatic  operating
         systems  similar to  those  for rapid  sand  filters.  Vacuum  filter systems  may  also be  auto-



                                Tails  9
           Filter Waste
                                                           i   Wash Water
                                                   i       i









                                       First Stage   Second Stage   Third  Stage
             Filter Waste   Waste Slurry                         Recovered  DE
                Pit       Feed Tank
         FIGURE 9.18  Schematic of a diatomaceous earth recovery system.
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