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OXIDATION AND DISINFECTION              10.25

        tem (aqueous  ammonia and anhydrous  ammonia feed systems).  The vapors  above the so-
        lution  in  an  aqueous  ammonia  tank  are  extremely potent.  Therefore provision should  be
        made  for disposing  of the displaced  vapors in the tank in a  safe manner,  such  as  through
        transfer  back to the delivery vehicle when  the  storage  tank  is being refilled. Pressure  re-
        lief valves on these tanks  should pass  through  a  water-type  scrubber  before going to  the
        atmosphere.
           Delivery of aqueous ammonia to the feed point is typically performed with diaphragm
        metering  pumps.  The  ideal  control  system  would  permit  a  feed  rate  proportional  to  the
        product  of  the  flow  and  the  chlorine  residual  such  that  the  appropriate  ammonia-to-
        chlorine ratio for chloramine  formation  can be maintained.
           Aqueous  ammonia  is  often  fed through  stainless  steel end-type  diffusers  with  corpo-
        ration stops for ease of cleaning. If carrier water is used, the water should be softened and
        the  diffuser  should  have  3A6-in.-or-larger  (4.5-mm)  orifices  designed  with  a  significant
        backpressure  such  that  any  scale formation  is knocked  off the diffuser.
           When one is ordering aqueous  ammonia,  debris-free chemical should be specified, be-
        cause  aqueous  ammonia  is  sometimes  delivered with  considerable  debris  present.  Alter-
        natively, facilities may be installed to strain undesirable  debris from the product before it
        is used.


        Ammonium Sulfate Systems
        Solid ammonium  sulfate  is usually  fed into  a  simple mixing tank  using  a  gravity or vol-
        umetric feeder.  Once mixed,  the  solution can be transported  using  the  same methods  de-
        scribed  earlier  for  aqueous  ammonia.  If the  local  water  is  hard,  scaling  problems  may
        occur,  and  softening of this  carrier water  should  be considered.


        Sodium  Hypochlorite Systems

        Sodium hypochlorite is used by many  small and medium-size water systems to feed chlo-
        rine because of the greater ease of handling and much greater safety as compared to chlo-
        rine  gas.  In recent  years,  some larger water  systems  that  are  located  in  metropolitan  ar-
        eas have also changed from chlorine gas to the use of sodium hypochlorite because  of an
        increased  emphasis  on  safety.


        Purchasing Hypochlorite
        Sodium  hypochlorite  (liquid  bleach)  is  formed  by  combining  chlorine  solution  and  so-
        dium hydroxide. In other instances, it is manufactured from chlorine and sodium hydroxide
        that  have  been  separately  shipped  to  the  manufacturing  site.  The  reaction  that  proceeds
        in this  instance  is  as follows:
                  C12 +  H20 ~  HOC1  +  HC1  (gas  chlorine  to chlorine  solution)
                  HOC1 +  HC1  +  2NaOH ~  NaOC1  +  NaC1  +  H20

        A  slight  excess  of  sodium  hydroxide  is  often  added  to  increase  the  stability  of the  so-
        dium hypochlorite product.
           When  the sodium hypochlorite is added to water,  it hydrolyzes  to form hypochlorous
        acid  (HOC1),  the  same  active  ingredient  that  occurs  when  chlorine  gas  is  used.  The
        hypochlorite  reaction  slightly  increases  the  hydroxyl  ions  (pH  increase)  by  the  forma-
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