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198   Industrial Wastewater Treatment, Recycling, and Reuse


          Principal advantages of Fenton oxidation are the following:
          1. Simple process, can be conducted in either batch or continuous mode
          2. Readily available chemicals for treatment
          3. Completely green, environmentally friendly process
          4. Destroys a very broad range of organic compounds
          5. Can be a pre- or posttreatment step for a biological process
          6. Sludge generated is completely nonhazardous and can be safely
             disposed of.
          The disadvantages of the Fenton process are the following:
          1. Large quantity of sludge generated
          2. Difficulty of hydrogen peroxide management
          3. The problem of identifying optimum dosages for cost-effective
             treatment.
          The Fenton oxidation process can be effectively applied to treat dye wastewa-
          ters. An example is shown in Figure 4.2a, which shows a photograph of the re-
          sults obtained from treating direct dye wastewater with Fenton oxidation.
             The above results are highly significant because the wastewater contains
          solvents such as nitrobenzene and amines that make biological treatment
          difficult. The Fenton process is very successful in COD reduction from around
          5000–6000 ppm COD to <1000 ppm COD value with a reaction time
          of less than an hour. The process is also attractive because it can handle huge
          fluctuations in COD of incoming wastewater and hydraulic load. The cost
                                                         3
          of treatment ranges from about Rs. 300 to Rs. 600 m . The capital cost of


            (a)                           (b)
                                                      H 2 SO 4  H 2 O 2  FeSO 4 Ca(OH) 2
                                            Dye wastewater
                                              3
                                             50m /day
                                                                  Sink basin
                                                          3    3
                                           Fine sieve   25m  25m
                                           & equalizing
                                            tank                     Effluent
                                                          Fenton
                                                 Pumping  reactors
                                                 station       Draining of
                                                               sludge
                                                                Sludge  3
                                                                tank 6m
                                               Supernatant
                                                                Chamber filter
                                                                press; 2 units
                                                         Filtrate
                                                               Dewatered
                                                               sludge
          Figure 4.2 (a) Fenton oxidation of direct dye wastewater. (b) Scheme for treatment of
          textile wastewater using the Fenton process.
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