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LIME–SODA SOFTENING 7-19

                 179.0 mg/L as CaCO  3       20 mg/L as CaCO  3       199 mg/L as CaCO  3  . Lime is purchased
                 and stored as CaO. The amount of 90% pure lime as CaO is
                                     ⎛ 28 meq/mg⎞ ⎛  1 1 ⎞
                                     )
                   (199 mg/L as CaCO 3 ⎜ ⎝  50 meq/mg⎠ 090.  ⎟ ⎠    123 8 or  124 mg/L as CaO
                                                              .
                                                 ⎟ ⎜
                                                  ⎝
                 where the equivalent weight of CaO     28 meq/mg and the equivalent weight of
                 CaCO  3       50 meq/mg.
              d.  The total hardness of the finished water (after recarbonation ) is

                         Ca 2      Initial 200  mg/L as CaCO   164  mg/L as CCaCO removed
                                                       3                  3
                                with bicarbonate
                                 36  mg/L as CaaCO 3
                         Mg 2      35  mg/L as CaCO 3

                 Total hardness    36   35    71 mg/L as CaCO 3
               e.  The changes in the water composition as illustrated by the changes in the bar chart are
                 shown below.

                 Bar chart after removal of CO  2   (in mg/L as CaCO  3  ).
                 0                           200  235

                              Ca 2             Mg 2

                           HCO               SO 2
                              3               4
                 0                      164       240

                Bar chart of the finished water (in mg/L as CaCO  3  ).

                 0             36       35

                       Ca 2        Mg 2
                               SO 2
                                 4
                 0                             76

            Comments:
                1.  Lime neutralization is used because the CO  2   is less than 10 mg/L as CO  2  .

               2.  The finished water is quite soft and consideration should be given to splitting the flow
                 to bypass some of the raw water to blend to a higher residual hardness. This would save
                 capital costs by using smaller tanks and operating costs by reducing chemical usage as
                 well as the amount of sludge that has to be disposed.
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