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CHEMICALS AND CHEMICAL HANDLING           ] 5. ] 1

           Vent  pipes  should  terminate  outdoors  with  screened  elbows  facing  downward.  Vent
         and  fill  lines  must  be  run  without  traps.  Overflow  lines  may  interconnect  sealed  tanks
         containing the same material, but the lines should not be allowed to terminate in the open
         air  unless  they  are  inside  the  secondary  containment  area.  Such  a  line  would  otherwise
         become  the primary  vent and  permit  a  spill to  occur in  the  event of an overfill. As  with
         any  chemical, but particularly  with liquids,  the  user must  be  certain  that  the quantity  or-
         dered  can be  accommodated  in  storage  at the time of delivery.
           Accidental overflows are best prevented by providing dependable  level indicators  and
         alarms  on all tanks.  To  further  guard  against  overfilling a  storage  tank,  a  high-level au-
         dible alarm  should be provided as part  of the in-plant chemical tank-level indicating  sys-
         tem.  This  alarm  should  be  mounted  outside  at  the  unloading  station  to  alert  the  vehicle
         operator.  The  alarm  can  be  common  to  all  tanks  served  by  the  particular  unloading
         station.
           Several level-sensing systems  are available with local or remote indicating  and  alarm
        capability.  Pneumatic  level sensors  using bubble  pipes are effective and accurate,  but be-
         fore  they  are  used,  first  it  must  be  determined  that  air  bubbles  will  not  deteriorate  the
         chemical whose level is being  measured.
           Types of Storage  Tanks.  Storage tanks  for liquid chemicals are commonly fabricated
        from  steel,  stainless  steel,  fiberglass-reinforced  plastic  (FRP)  [also  referred  to  as  rein-
        forced thermoset plastic (RTP)],  and various forms of polyethylene, such as high-density,
        cross-linked  polyethylene  (HDXLPE).
           For  very corrosive  chemicals,  such  as  ferric  salts,  sodium  hypochlorite,  and  sodium
        hydroxide,  the  nonmetallic  materials  are  normally  most  appropriate.  Polyethylene  tanks
        should be designed in accordance with ASTM D-1998. Whenever possible, nozzles should
        be  constructed  as  integrally  molded  flanged  outlets  (IMFOs)  to  avoid  stress  points  and
        potential leak sites.  Polyethylene is more  appropriate  for  smaller day  tanks.
           The use of FRP for chemical  service began in the mid-1950s.  ANSI Standard  RTP-1,
        Reinforced  Thermoset Plastic  Corrosion Resistant Equipment,  should be the basis  for de-
        sign of FRP  tanks  having  internal  pressures  less  than  15  psi  (103  kPa).  FRP  has  greater
        structural  strength and flexibility for installation of nozzles and other appurtenances  in the
         sidewalls.  A  variety  of polyesters,  vinyl esters,  and  other  materials  are  available for the
        resin  or double  laminate  construction,  depending  on  chemical resistance  requirements.
           The  choice of tank  material  or lining,  in  addition  to  its chemical  resistance,  depends
        on the concentration  of chemical, pressure,  and temperature  conditions,  and  tank  dimen-
         sions.  The  tank  manufacturer  must  be  consulted  about  the  types  of materials  to  use  for
        the proposed  chemical.  Improper material  selections could lead to tank failure.
           Open-top  tanks  can  be  used  for  stable,  nonvolatile liquids,  but  their use  is restricted.
        Buried  tanks  must be  strapped  to  anchor  blocks  with  sufficient mass  to prevent flotation
         when the tank is empty  and must  meet U.S. Environmental  Protection Agency (USEPA)
        leak prevention criteria.  These  criteria mandate  the use of double-walled tanks  with leak
        detection alarms. Buried tanks must also be equipped with manholes, vent lines, and other
        connections.
           The majority of storage tanks  are located in the lower or basement  areas  of buildings,
         where  air is naturally  cooler, or outdoors  if winters  are  not too  severe.  As  a  result,  heat-
         ing and insulation may be required for those tanks  that contain chemicals subject to crys-
        tallization.  Installing  insulation  and  thermostatically  controlled hot-water  or  steam  coils,
        or electric immersion heaters within or around the tank, ensures positive protection against
         slushing  or  freezing.  If the  problem  is  marginal  or  occurs  only  during  severe  seasonal
        weather,  applying  electrical  heating  tape  on  the  tank  exterior  usually  offers  sufficient
        protection.
           Spill  Containment.  Chemical  storage  and  feed  facilities  require  adequate  provision
        for  spill containment  with  consideration  for  worker  safety;  water  quality;  customer  pro-
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