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7-12   WATER AND WASTEWATER ENGINEERING

                            TABLE 7-2
                            Summary of chemical additions to soften water
                                                                 a
                            Step                   Chemical addition          Reason
                            Carbonate hardness
                            1.                     Lime   CO 2                Neutralize H 2 CO 3
                                                                                                       2
                            2.                                                Raise pH; convert  HCO  to CO
                                                   Lime   HCO 3
                                                                                                 3     3
                                                            2
                            3.                     Lime   Mg   to be removed  Raise pH; precipitate Mg(OH) 2
                            4.                     Lime   required excess     Drive reaction
                            Noncarbonate hardness
                                                                                        2
                            5.                     Soda   noncarbonate hardness   Provide   CO 3
                                                   to be removed
                            a
                             The terms “Lime” and “Soda”refer to mg/L of Ca(OH) 2  and Na 2 CO 3  respectively, as CaCO 3  equal to mg/L of ion (or gas
                            in the case of CO 2 ) as CaCO 3 .


                              Removal of CO  2
                             Because CO  2   in the raw water behaves as H  2  CO  3  , its removal is the first step in raising the pH
                            in lime-soda softening. It may be neutralized by the addition of lime, in which case it is not a
                            “process” in the conventional meaning of the word. When the concentration exceeds 10 mg/L as
                            CO  2   (22.7 mg/L as CaCO  3   or 0.45 meq/L), the economics of removal by aeration ( stripping ) are
                            favored over removal by lime neutralization. Air stripping is a separate process. No hardness is
                            removed in this process.


                                                          1. Add lime   CO (to raise pH)
                                                                     2

                                                                      3
                                        Ca 2     Mg 2     2. Add lime   HCO (to raise pH)
                                                          3.  Check is sum of Ca 2   that remains:
                                CO
                                  2                               2               2
                                                            NCH   Mg   120? If yes, remove Ca  that is

                                       HCO   3   C1          NCH with soda ash (Ca 2     HCO ).
                             (a)                                               3
                                                          4.  Consider excess lime
                                        2         2       1. Add lime   CO 2
                                       Ca       Mg
                                                          2. Add lime   HCO
                                CO                                    3
                                  2
                                                          3.  Consider excess lime

                                                                   2
                                       HCO   3   C1         HCO   Ca , therefore, all Ca 2   has been removed.
                                                               3
                             (b)
                                       Ca 2   Mg 2   Na
                                                          1. Add lime   CO 2
                                CO                        2. Add lime   HCO
                                  2                                   3
                                            HCO           3.  Consider excess lime
                                               3
                             (c)
                            FIGURE 7-7
                                             2
                            Dosage schemes when Mg  concentration is less than or equal to 40 mg/L as CaCO 3  and no split
                                                    2                                 2
                            treatment is required. Note that no Mg  is removed and that reactions deal with CO 2  and Ca  only.
                            (Source: Davis and Cornwell, 2008.)
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