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14.32                    CHAPTER FOURTEEN

         •  For conventionally reinforced  concrete  structures  in  contact  with  carbon,  a  minimum
          concrete cover of 15 to 40  mm (depending  on reinforcement)  should be provided over
          reinforcing  steel.  Carbon  is  extremely  corrosive  and  attacks  reinforcing  steel through
          cracks  in  concrete.
         •  Provide a  washdown  hose  site on the  vessel deck to facilitate cleaning.
         •  Provide  air release  valves on  the backwash  water  supply  piping  to  ensure  that  air has
          been  completely purged.
         •  Provide adsorber-to-waste  connections  (similar to conventional  filter-to-waste) to per-
          mit additional  removal of GAC fines remaining  after backwashing.

         Design of Carbon Storage and Transport Facilities.  Carbon replacement is a major ex-
         pense  associated  with  carbon  adsorption  systems.  Because  slurry  storage  and  transport
         can cause  major  attrition  losses,  facilities must  be  designed  with  care.  Carbon deliveries
         in excess of 9,000  kg (10  tons)  usually justify an eductor/carbon  slurry  transport  system.
         Design guidelines  include the following:
         •  To  minimize carbon-to-carbon  abrasion,  avoid air-assisted  transfer  of carbon.
         •  Transfer all carbon  in a  water  slurry form, designed for a  slurry of approximately  1 to
           3  lb/gal  (0.12  to 0.34  kg/L).
         •  Minimize  the  length  of carbon  slurry  transfer  pipes  through  optimum  arrangement  of
           structures  and  equipment.
         •  Pipelines  delivering carbon  slurry  to  the  tanks  should  discharge  below  the  water  sur-
           face to minimize attrition and overflows from the dewatering  screw. The tank overflow
           pipeline  should  be  screened  or  diverted  to  a  collection  point  where  carbon  can  be
           recovered.
         •  Provide a  metering device to  measure  carbon  slurry  flow rate  in the  piping  system.
         •  Limit velocities in carbon  slurry  transfer lines to  3  to  5  ft/s (0.9  to  1.5  m/s).
         •  Avoid the use of throttling  valves on carbon  slurry  lines and  on potable  water dilution
          lines that  are  ahead  of the  point of carbon  introduction.
         •  Use a minimum diameter of 50-mm type 316 stainless steel pipe for carbon slurry trans-
          fer  lines  and  long  sweep  bends  to  minimize  pipe  erosion  and  improve  hydraulics.
          Mitered bends  should  not be used  for piping carbon  slurry.
         •  Minimize  the  number  of  movements  (valve  changes,  flow  direction  changes,  pump
          starts)  to effect a  complete carbon  transfer.
         •  Limit  the  speed  of recessed  impeller,  rubber-lined,  centrifugal  carbon  transfer  pumps
          to 900  rpm  or less.
         •  Design carbon storage bins to receive the entire wet contents of carbon transferred from
          a  single carbon  vessel,  plus  at least 20%  for expansion.
         •  Install pressure  gauges  with  diaphragm  seals  throughout  the eduction  system to moni-
          tor system  performance.
         •  Use double-seated  valves for in-line shutoff and  isolation throughout,  because the  sys-
          tem  may  see  carbon  flow  in  both  directions.  Double-seated  knife  gate  valves,  plug
          valves, or ball valves fabricated from materials  suitable for carbon contact can be used.
         •  Design the  carbon  slurry  system  to move slurry  through  the  system  continuously  until
          all carbon  has  been  flushed  from piping.  The  process  must  not be  allowed to stop un-
          til  all  carbon  has  been  moved  through  the  piping,  or  else  carbon  will  settle  and  plug
          the lines.  Provide cleanouts  and  flushing  connections  throughout  the piping system.
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