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CHAPTER TWELVE
        12.14




                                                Strong
                          i    Strong
                               Acid             Base
                                                               Salt
                    Salt
                               Cation           Anion



                                                           L
             FIGURE 12.1  Strong base dealkalizer.

           Although the sulfate has a higher affinity for the resin during the exhaustion cycle, the
         sulfate/chloride  affinity relationship is affected by the concentration and is reversed at the
        regenerant concentrations. Approximately 5 lb of salt per cubic foot of resin, applied  at
        4% to 6% concentration, is sufficient to fully regenerate  the resin bed to the chloride form.
         Higher dose levels offer very little gain.
           Since the bicarbonate ion is the  least strongly held of the common ions by the resin,
         the operating capacity depends on the total  concentration of ions. The operating capacity
         for most gel type II anion exchange resins can be estimated at 12,500 gr/ft 3 resin. Through-
         put capacities  are calculated based on all the anions in the inlet water including chlorides
         as being exchanged.  First, calculate the  sum in milligrams per liter of all  the  anions as
         their calcium carbonate equivalents, and divide that by  17.1 to convert the concentration
         to grains per gallon. Bicarbonates will be reduced  by about 80% to 90% throughout  most
         of the service cycle, and the treated  water pH  will be about 5. When alkalinity leakage
         reaches  30%, the service cycle is terminated. The operating capacity can be increased  to
         about 15,000 gr/ft 3 and the effluent pH increased to above 7, by adding about 0.25 lb of
         sodium hydroxide to each 5 lb of salt used for regeneration.

        pH Effects of Dealkalization.   The pH of ordinary tap water is determined by the equi-
         librium between carbon dioxide, bicarbonate, and carbonate between pH values of 5.0 and
         10.6. In the  absence of hydroxides,  the  removal of the bicarbonate and carbonates  auto-
         matically reduces the pH of tap water to 5.0, which is the pH of carbon dioxide in water.
         This is what  happens when salt  is used alone as the  regenerant. Carbon dioxide  is only
         slightly ionized, so it is not removed by the resin.  This scenario is changed by adding a
         small amount of caustic to the regenerant salt, usually 0.25  lb of NaOH to each 5.0 lb of
         salt. This places  a very small amount of hydroxide on the resin. Its main effect  is that it
         converts the nonregenerated bicarbonate left on the  resin to carbonates.  The carbonates
         on the resin will combine with  carbon dioxide to form bicarbonates, which are held by
         the resin. By this mechanism, CO2 is removed and the pH is shifted  back to 7.0. The ef-
         fluent is free of bicarbonates and carbon dioxide.

         Dealkalization  with  Weak Acid Resins Regenerated with Acid.   Weakly acidic  resins
         operated  in the hydrogen form are, by their nature, unable to react  with cations except  in
         the presence of a neutralizing agent such as alkalinity. They exchange hydrogen for cations
         but are  only effective in removing hardness and other divalent ions that  are  associated
         with alkalinity. Therefore,  weakly acid resins are able to work effectively as dealkalizers,
         but only on certain waters.  Because  they  are  weakly acidic,  they  have extremely high
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