Page 310 - Water and wastewater engineering
P. 310

LIME–SODA SOFTENING 7-27

              0
              2
              4        FeOH              Fe(OH) (s)
                                             2
           log[species]   6
              8
             10
                           Fe(OH) 3           Fe 2
             12
             14
               0    2    4    6    8   10   12   14
                                pH
          FIGURE 7-11
          Solubility diagram for Fe(OH) 2 .

              0
              2
                          MnOH
                                              2
              4                          Mn(OH) (s)
           log[species]   6
              8
             10
                           Mn(OH)
             12                3            Mn 2
             14
               0    2    4    6    8   10   12   14
                                pH
          FIGURE 7-12
          Solubility diagram for Mn(OH) 2 .


            Turbidity
           Although it is generally not of concern for groundwater sources, turbidity removal is a major
          objective in treating surface water. In those cases where the surface water is hard, softening by
          chemical precipitation will concurrently remove turbidity by sweep coagulation.

            Other Contaminants
            Sorg et al. (1977) identified a number of other contaminants that are removed concurrently by
          lime-soda softening or coagulation. These are listed in  Table 7-3 .

          7     -6   PROCESS CONFIGURATIONS AND DESIGN CRITERIA
           The process flow diagrams for three common softening treatment schemes are shown in  Figure 7-13
          on page 7-29 . Many other variations are possible including, for example, the use of blended raw
          water CO  2   to recarbonate and the use of coagulation and flocculation after the precipitation pro-
          cess to reduce the solids load to the filters. In the case of coagulation/flocculation, the high pH of
          the water coming from the precipitation process favors the use of ferric chloride as the coagulant
          because it is less soluble at higher pH than alum (see, for example, Figure 6-9).
   305   306   307   308   309   310   311   312   313   314   315