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LIME SOFTENING                      11.3


         •  Removing radium 226 and 228
         •  Removing heavy metals,  including arsenic
         •  Removing certain organic compounds and reducing total organic carbon (TOC)
         •  Removing silica and fluoride
         •  Removing iron and manganese
         •  Reducing turbidity of  surface  waters  in  conjunction with  the  hardness  precipitation
          process
         The  degree  of removal of constituents usually depends on the  treatment process  used.
         Benefits to the consumer depend on source water quality and user requirements.



         Softening Plants in the United States
        Currently more than 1,000 domestic-use water plants in the United States use lime soft-
        ening processes.  Although water  plants using lime softening are  found in most sections
        of the United States,  the majority of large plants are located in the midwestern states  and
        in Florida. These plants range in size from less than 1 mgd to more than 100 mgd.


        Chemistry of Lime Softening
        Water softening involves a number of complex and dynamic chemical interactions. The
        chemical reactions involved and calculation of chemical feed requirements are discussed
        in detail in AWWA's Water Quality  and Treatment.  The discussion that follows in this
        text simplifies the chemistry involved, highlighting only the predominant reactions.
           Lime, the primary chemical used for water softening, reacts  with carbon dioxide and
        carbonate hardness to precipitate  calcium carbonate and magnesium hydroxide. Quick-
        lime, CaO,  is first slaked  to produce calcium hydroxide:
                                CaO +  H20  =  Ca(OH)2               (11.1)
        Chemical Reactions.  Reactions between calcium hydroxide and carbon dioxide and bi-
        carbonate alkalinity are  shown in Equations (11.2)  and (11.3).  The reactions convert the
        bicarbonate alkalinity present to carbonate alkalinity, which precipitates  as insoluble cal-
        cium carbonate.
                              CO2 +  Ca(OH)2  =  CaCO 3 +  H20       (11.2)
                         Ca(HCO3)2 +  Ca(OH)2  =  2CACO3 +  2H20     (11.3)
           The optimum pH to produce minimum soluble calcium carbonate is about  10.3, de-
        pending on water temperature,  total dissolved solids,  and other factors  affecting the sol-
        ubility of calcium carbonate.  In precipitating the calcium ion, 2 mol of calcium carbon-
        ate is formed for every 1 tool of calcium ion removed from the water, as shown in Equation
        (11.3).
           Magnesium hardness,  present as  magnesium bicarbonate, is  removed in a  stepwise
        fashion, as shown in Equations (11.4)  and (11.5).
                                                                      (11.4)
                     Mg(HCO3)2 +  Ca(OH)2  =  CaCO3 +  MgCO3 +  2H20
                        MgCO3 +  Ca(OH)2  =  CaCO 3 +  Mg(OH) 2       (11.5)
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