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DISINFECTION AND FLUORIDATION 13-9

              Chlorine dioxide and ozone can oxidize a number of organic constituents without producing
          THMs or HAAs. However, chlorine dioxide itself and the chlorite ion are toxic. Approximately
          70 percent of the chlorine dioxide consumed by oxidation reactions is converted to chlorite under
          conditions typical in water treatment (Singer, 1992). In addition, if bromide is present, ozonation


          will form the hypobromite ion (OBr    ) which, in turn, forms, hypobromous acid that will react
          with NOM to form brominated byproducts.
                There are no known disinfection byproducts that result from UV radiation (Haas, 1999).
            Chemical Disinfectant Kinetics
           Although more complex models are available, it is often assumed that decay of chlorine, com-
          bined chlorine, and chlorine dioxide can be modeled as a first order or pseudo-first order reac-
          tion, that is:

                                             dC
                                                    kC
                                                     d
                                              dt                                     (13-17)

           where  C       disinfectant concentration, mg/L
                                                   1
                   k    d        first order decay rate constant, time
                   t       time, complementary units to  k    d
           Example pseudo-first order decay rate constants are shown in  Table 13-3 .


            TABLE 13-3
            Pseudo-first order decay rate constants

          Compound     k d                    Condition               Source
                                                                b
                               4  1
          Ozone a      1.5   10  s            Ground water low DOC ;   Acero & von Gunten, 2001
                                              high alkalinity
                               3  1
          Ozone a      2.5   10  s            Surface water high DOC;   Acero & von Gunten, 2001
                                              low alkalinity
          Ozone a      0.108 to 0.128 min  1  Ozone contact chamber   Rakness, 2005
                             3  1
          AOP c        1.4     s              Ground water low DOC;   Acero & von Gunten, 2001
                                              high alkalinity
                                 s
          AOP          5.8   10  3  1         Surface water high DOC;   Acero & von Gunten, 2001
                                              low alkalinity
                                                             d
          Chloramine   0.01 to 0.02 d  1      Surface water TOC  1 to   Wilczak et al., 2003
                                              2 mg/L
          Chlorine     0.0011 to 0.0101 min  1  Surface water TOC 2.3 to   Sung et al., 2001
                                              3.8 mg/L
          Chlorine     0.71 to 11.09 d  1     Distrib. sys. pipe      Clark et al., 1993
          Chlorine     0.36 to 1.0 d  1       Distrib. sys. storage tank  Rossman et al., 1995
            a
              Note that these authors presented these as first order approximations.
          b
          DOC   dissolved organic carbon.
            c
              AOP     advanced oxidation processes. These are combinations of disinfectants to produce hydroxyl radicals. Most
          noteworthy of the AOP processes is ozone plus hydrogen peroxide.
          d
          TOC   total organic carbon.
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