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ION EXCHANGE APPLICATIONS IN WATER TREATMENT    12.23

        2002, the Office of Environmental Health Hazard Assessment (OEHHA) published 6 ppb
        for adults and 2 ppb for children.
           The removal of perchlorate from potable water supplies is somewhat similar to the re-
        moval  of  nitrate.  In  both  cases,  ion  exchange  technology  is  the  best  currently  known
        method.  Perchlorate  is even more  strongly held by ion exchange resins than nitrates are.
        Sulfate  ions are the  only major competitor besides nitrates for  exchange  sites on  strong
        base anion resins. When nitrate removal is also required, nitrate capacity becomes the lim-
        iting operation and posttreatment for perchlorate removal may be required. However, per-
        chlorate is  so strongly held by ion exchange resins that it is difficult to regenerate using
        normal  regeneration  methods  and  traditional  regeneration  chemicals.  Sulfates  are  less
        strongly held by the resin than perchlorates,  but they  are  almost always  present at  con-
        centrations  several  orders  of magnitudes higher  and,  therefore,  significantly reduce  the
        throughput capacity per cycle.
           To control the amount of regenerant waste, a regenerable ion exchange resin must have
        high capacity for the contaminant of interest and be efficiently regenerated. The very high
        affinity of perchlorate  for  strong base  anion exchange  resins  goes  against this.  Type II
        strongly basic  anion exchange  resins and acrylic  strong base  anion exchange  resins can
        be regenerated with lower amounts of brine than can type I strong base anion resins. How-
        ever, the problem remains of disposal of the brine and/or the destruction of the perchlo-
        rate.  As of March  2003, much work is being done to address  this problem of brine reuse
        and perchlorate  destruction from the waste brines.
           Recent developments in ion exchange technology have resulted in resins that are ex-
        tremely deselective of divalent ions.  Such resins  were  first commonly referred  to  as  ni-
        trate  selective,  because they allowed resins to remove nitrates without interference from
        sulfates.  Although perchlorates  are much  more  strongly held than nitrates,  the presence
        of sulfates in the  water  can reduce the  operating capacity of type I, type  I],  and acrylic
        strong base  anion resins.  Further developments in the  field of ion exchange  technology
        have  now resulted in resins with even further reduced  selectivity for  divalent ions  such
        as  sulfate, reducing sulfate interference in perchlorate  removal by orders  of magnitudes
        below the original nitrate selective resins. The result is that today there exist several resin
        types  that  are  able to  treat  over  100,000  bed  volumes before  perchlorate  breakthrough,
        based on typical inlet perchlorate concentrations well below  1 ppm.
           Typical selectivity coefficients for perchlorate compared to chloride have been reported
        in various literature. There are several ways of stating relative affinities between ions and
        ion exchange  resins.  Distribution coefficients,  separation factors,  and  selectivity coeffi-
        cients  are  commonly used.  Each  defines  different mathematical  relationships, but  they
        have in common that  they represent ratio relationships for  a  specified pair of ions. Val-
        ues  above  1 mean the  first ion is preferred,  and less  than  1 that  it isn't. These  relation-
         ships depend strongly on the solution conditions in which they were measured; therefore
        they  should  be  used  only for  relative  comparisons  and  not  as  absolute preference  of  a
        resin for one ion compared  to  another.  Table  12.1  shows  the  selectivity coefficients for
         perchlorate versus chloride.
           With this development comes the potential use of resins on a nonregenerable basis. Be-
         cause  of their high  affinity for perchlorate  compared  to  sulfate,  these resins can be  used
         without being regenerated on a competitive basis when compared against regenerable, less
         expensive resins, including the cost of the regenerant chemicals, the equipment for the re-
         generation, the disposal cost,  and the  treatment cost of the regenerant brines. Because  of
         their high affinity, these resins pass  the leach test for hazardous material so that they can
         be disposed of, in most cases, as ordinary landfill. However, specific tests for the resins in-
         tended for use must be conducted to ensure compliance with local laws at the time the plant
         is being designed to build, as those laws may change from the date of this publication.
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