Page 311 - Water and wastewater engineering
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7-28   WATER AND WASTEWATER ENGINEERING

                            TABLE 7-3
                            Effectiveness of lime softening and coagulation in removing inorganic contaminants
                            Contaminant         Method                             Removal, %
                            Arsenic
                             As 3               Oxidation to As 5   required           90
                             As 5               Ferric sulfate coagulation, pH 6–8     90
                                                Alum coagulation, pH 6–7               90
                                                Lime softening, pH 11                  90
                            Barium              Lime softening, pH 10–11               90
                            Cadmium a           Ferric sulfate coagulation, pH   8     90
                                                Lime softening, pH   8.5               95
                            Chromium a
                             Cr 3               Ferric sulfate coagulation, pH 6–9     95
                                                Alum coagulation, pH 7–9               90
                                                Lime softening, pH   10                95
                                6
                             Cr                 Ferrous sulfate coagulation, pH 6.5–9   95
                                                (pH may have to be adjusted after
                                                coagulation to allow reduction
                                                    3
                                                to Cr )
                            Fluoride            Lime-soda softening, pH 11–12          55
                            Lead a              Ferric sulfate coagulation, pH 6–9     95
                                                Alum coagulation, pH 6–9               95
                                                Lime softening, pH 7–8.5               95
                                  a
                            Mercury             Ferric sulfate coagulation, pH 7–8     60
                                   a   4
                            Selenium  (Se  )    Ferric sulfate coagulation, pH 6–7    70–80
                                a
                            Silver              Ferric sulfate coagulation, pH 7–9    70–80
                                                Alum coagulation, pH 6–8              70–80
                                                Lime softening, pH 7–9                70–80
                            a
                             No full scale evidence.
                            (Source: Benefield et al., 1982; Sorg et al., 1977)

                                Conventional Softening Basins
                             These basins are similar to conventional basins used for coagulation and flocculation. Rapid
                            mixing either with paddle mixers or vertical turbines is followed with paddle mixers or vertical
                            turbines for the reaction basin (also called the flocculation basin because of its analogy to the
                            coagulation/flocculation process). When conventional basins are used, a portion of the precipitate
                            is recycled to the head end of the process. Recycling accelerates the precipitation reactions, and
                            the process more closely approaches true solubility limits when mixed with the previously formed
                            precipitate crystals (Horsley et al., 2005).
                                Because they are similar to coagulation/flocculation systems, the design criteria are specified
                            in a similar fashion. Flash mixing is generally provided by radial flow impellers though older
                            plants may be using paddle wheels. The flash mixing velocity gradient ( G ) should be in the range
                                        1
                            300 to 700  s      and the minimum mixing time should be 10 to 30 s. With cold water found in
                            most groundwater, rapid mixing for as long as 5 to 10 minutes may be required for dissolution
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