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ION EXCHANGE APPLICATIONS IN WATER TREATMENT     12.7


         Each  ion pair has  a unique  selectivity value for each ion exchange resin.  The higher the
         selectivity coefficient, the higher the relative affinity of the ion for the resin. The higher
         the  affinity, the  easier it is to  load the ion,  and  conversely the more  difficult it is to re-
         move  during  regeneration.  The  operating  performance,  capacity,  and  leakage  data  for
         ion  exchange  resins  for  the  common  ions  found  in  water  are  usually  provided  by  the
         resin  supplier.
           In general,  the ion exchange  resin  is used  in  and regenerated  to  an ionic form,  which
         will exchange ions that are  acceptable in the treated  water.  As the untreated  water passes
         through the resin, the undesirable  ion or ions exchange for the unobjectionable ion on the
        resin.  For example,  a  cation  exchange resin  is regenerated  with  sodium  chloride  and  op-
         erated in the sodium cycle. The resin exchanges sodium ions for all the positively charged
        ions  (cations),  including hardness-causing  calcium and magnesium  ions,  and the water is
        thereby  softened.  Likewise,  if an  anion  resin  is  regenerated  with  sodium  chloride,  it op-
        erates  in the  chloride  cycle.  It will exchange  chlorides  for  the  anions,  i.e.,  bicarbonates,
         sulfates,  nitrates,  etc.,  and  the  effluent  water  will have  a  chloride  concentration  equiva-
        lent to the total concentration of the  anions  in the raw  water.
           Although  salt  exchanges  are  common,  so  are  other  ion  exchanges  that  involve acids
        and bases.  In the process  of demineralization,  for example,  the cation resin is operated in
        the hydrogen form and exchanges hydrogen ions. This converts all incoming salts to their
        equivalent acids.  After the  cation  exchange,  the  water  passes  through  a  hydroxide  form
        anion exchanger where  anions  are exchanged for hydroxides,  which converts the acids to
        water molecules. In this process  the net result is that an equivalent amount  of water mol-
        ecules is added  to the water in  exchange  for the  salts  that  are removed.
           The  weakly  acidic  and  weakly  basic  ion  exchange  resins  are  generally  incapable  of
        converting  salts  to  acids  and  bases  and  are  generally  limited in  use  to  neutralization  re-
        actions.  The hydrogen form weakly acidic cation resins  are usually used  to neutralize  al-
        kalinity,  and  weakly  basic resins  are likewise used  to neutralize  acidity.
           Ion exchange is a dynamic equilibrium-driven process,  and regeneration is never 100%
        complete. There is always some, albeit trace, level of the undesirable ionic constituent left
        on the resin and in the product water. The most complete ion exchange reactions are those
        in which  the resulting products  disappear,  such  as by H--  and  OH-  neutralization  which
        drives  the reaction to  completion by the formation  of water  molecules.
           When the equilibrium is favorable, the exchange of ions occurs in a narrow band within
        the resin bed,  and  a large portion of the resin bed  can be used  before  significant leakage
        occurs due to kinetic  slippage.  When  the equilibrium is not favorable, the exchange zone
        ion is bigger and more diffuse. It can be as long as or longer than  (in terms of the amount
        needed  to reach the desired level of purification)  the entire resin bed.  The leakage of the
        undesirable  ion is almost  immediate  and  gradually  increases  throughout  the  service run.
        When  the  exchange  zone  is  larger  than  the  entire  bed,  the  desired  quality  cannot  be
        achieved, even in the initial portion of the  service cycle.


         Resin  Capacity  and  Regeneration
        Ion exchange  resins  have  a  finite capacity.  When  this  capacity  is used  up,  the resins  are
        exhausted  and  leakage  of the  unwanted  ions  increases.  The  exhausted  resin  can  be  re-
        generated  with  a  salt,  acid,  or base  solution  containing  the  ion  whose  "form"  the  resin
        will  be  operated  in.  This  is  passed  through  the  resin  bed  in  sufficient  quantity  and  at  a
        sufficiently high concentration to reverse the exchange, desorb, and replace the previously
        exchanged ions from the resin  with the ions  from the regenerant  solution.  The high con-
        centration  of the regenerant  minimizes  waste  volumes and  changes  the equilibrium rela-
        tionships  to make the regeneration  more  efficient.
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