Page 28 -
P. 28

MASTER PLANNING AND TREATMENT PROCESS  SELECTION   2.9

         TREATMENT  OPTIONS

         As  illustrated  in  Table  2.4,  a  summary  of more  common  drinking  water  treatment  pro-
         cesses,  there  are many  treatment  options  available to the  designer  to  achieve the desired
         water quality results.


         Principal  Process  Alternatives  and  Issues

         Where  pertinent,  detailed unit  process  tests  and  comparisons  should  be conducted  under
         the guidelines of the companion volume to this text,  Water Quality and Treatment, to de-
         termine the more effective options. Bench and pilot-scale treatment operations would also
         be conducted in the water quality and treatment phase  to determine the more critical pro-
         cess design  and  operating  parameters.
           Under the  current  regulations,  some form  of filtration  must  be  provided  for effective
         particulate  solids  removal.  In  general,  filtration  would  be  required  for  all  source  water
         supplies  except  perhaps  for  some  groundwater  sources.  The  particular  type  of filtration
        required would depend upon the particulate solids loading contributed by that in the source
        water in addition to that which may be generated in treatment such as in precipitation (i.e.,
        cold lime softening, manganese dioxide) and coagulation. Filtration types and solids load-
        ing capabilities may be categorized in general terms  as follows:

        •  Direct,  slow  sand,  and  diatomaceous  earth  filtration  may be feasible for waters  low in
          turbidity  (5  ntu  or less)  and  organic matter.  Potential  supply  sources  must  also be  sta-
          ble,  of high  quality,  and  not  subject  to  significant  algal  blooms  or  other  major  water
          quality changes.
        •  Conventional clarification and rapid  sand  filter plants  would be needed  for source  wa-
          ters  higher  in  turbidity  and  organic  matter  content,  and  those  where  higher  coagulant
          dosages  may  be required.
        •  The  limitations  of membrane  filtration  are  more  difficult to  define.  Closed-vessel ap-
          plications  would  more  likely be  limited to  source  waters  of higher  quality.  Immersed
          membranes  can  handle  higher  solids  loading  including  that  generated  in  precipitation
          and  coagulation to improve  solids removal.
           In  considering  conventional  clarification/filtration,  the  type  of  clarification  selected
        would also be influenced by the type of source water solids. Where  suspended  and/or dis-
        solved organic  matter  predominates,  high-rate  clarifiers  including  dissolved air flotation
        could be the more effective and more economic application. Where seasonal algal blooms
        occur,  dissolved-air flotation may be the preferred  alternative.  Plain  settling with greater
        detention  would  be  desired  where  more  profuse,  denser  solids  predominate,  such  as  in
        many  river sources.
           With  few  exceptions,  most  U.S.  public  surface  water  supplies  are  currently  provided
        treatment the preponderance  of which is some form of filtration. For this reason,  a major
        water treatment plant  design effort now and in the future will be devoted to retrofit rather
        than  new  design.  New  designs  for the  most  part  will be  for new  area  development,  ma-
        jor capacity  expansion,  or changing  rules,  such  as  for groundwater.
           Another feature of water treatment plant process  selection and design that must be ob-
        served is potential regulatory conflict. Scrutiny of Tables  2A  and 2.3 will show that there
        are two groups  of rules that currently  apply  or soon will apply  to all public  drinking  wa-
        ter treatment.  These  are the control of microbiological contaminants  and the formation  of
   23   24   25   26   27   28   29   30   31   32   33