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11.2                      CHAPTER ELEVEN


           Total hardness  is usually defined as  simply the sum of magnesium  and  calcium hard-
         ness in milligrams per liter as CaCO3.  Total hardness  can  also be differentiated into car-
         bonate  and  noncarbonate  hardness.  Carbonate  hardness  is  the  portion  of total  hardness
         present in the form of bicarbonate  salts [Ca(HCO3)2 and Mg(HCO3)2]  and carbonate com-
         pounds  (CaCO3  and MgCO3).  Noncarbonate  hardness  is the portion of calcium and mag-
         nesium present as noncarbonate  salts,  such  as calcium sulfate  (CaSO4),  calcium chloride
         (CaC12),  magnesium  sulfate  (MgSO4),  and  magnesium chloride (MgC1).  The  sum of car-
         bonate  and  noncarbonate  hardness  equals total hardness.


         Acceptable  Level of  Hardness
         Sawyer (1994)  classified the  degree  of hardness  as follows:

                              Hardness    mg/L as  CaCO 3

                              Soft            0-75
                              Moderate       75-150
                              Hard          150-300
                              Very hard      300 +


         The  degree of hardness  acceptable  for finished water  varies with the consumer or indus-
         try  served.  In  1968,  the  American Water Works  Association  (AWWA)  established  a wa-
         ter quality goal for total hardness  of 80 to  100 mg/L expressed  as calcium carbonate,  but
         current  AWWA  water quality  goals do  not include hardness.
           Magnesium hardness  of not more than 40 mg/L is also often proposed as a goal to mini-
         mize scaling at elevated temperatures in water heaters. The magnesium concentration present
         before precipitation  of magnesium  salt  is  a  function  of pH  and  temperature  of the fmished
         water. In recent years, many utilities using a softening process have allowed total hardness  in
         finished water to approach  120 to  150  mg/L to reduce chemical costs  and  residuals produc-
         tion and, in some cases, to produce a  less corrosive water by increasing alkalinity.
           Desired hardness  is  often  stated  as  a  policy by a  utility that  softens  water.  If a policy
         exists,  the  designer must  provide a  treatment  plant  design  meeting that policy. If no pol-
         icy exists  but  softening  is desired,  it is up  to the designer  to  arrive at  a  reasonable  hard-
         ness  for design purposes.  At present,  total  hardness  of  120  mg/L or less and  magnesium
         hardness  of 40  mg/L  or  less  appear  to  be  acceptable  design  criteria  for  softening facili-
         ties for most  applications.
           In practice,  total  hardness  produced  and  the  pH  of the  treated  water  may be  adjusted
         during operation by varying chemical feed to meet other treatment  goals, including mod-
         ification  of hardness  goals,  stability  and  corrosivity requirements,  and  turbidity  removal
         under varying source water quality conditions. Treated water pH of different softening fa-
         cilities typically varies  between  8.5  and  10.0,  depending  on  all these  factors.


         Benefits of Softening
         Potential  benefits  of softening  water  at a  central treatment  plant  include  the  following:

         •  Reducing dissolved minerals  and  scale-forming tendencies
         •  Reducing  consumption  of household  cleaning agents
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