Page 445 - Industrial Wastewater Treatment, Recycling and Reuse
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416   Industrial Wastewater Treatment, Recycling, and Reuse


          Table 10.4 Constituents of Synthetic Wastewater and Their Concentrations
          Constituents                                   gm/L

          Dextrose monohydrate                           0.5
          Urea                                           0.021
          Di-ammonium phosphate                          0.0106
          Sodium chloride (NaCl)                         0.3
          Magnesium chloride (MgCl 2 )                   0.15
          Calcium chloride (CaCl 2 )                     0.04
          Manganese sulfate (MnSO 4 )                    0.005
          Ferrous sulfate (FeSO 4 )                      0.005
          Sodium carbonate (Na 2 CO 3 )                  0.15



          Table 10.5 Average Characteristics of the Synthetic Wastewater (Feed)
          Parameter                 Unit                   Reading
          COD                       mg/L                   385
                                    mg/L                   247
          BOD 5
          TOC                       mg/L                   140
          TSS                       mg/L                   23
          pH                        –                      6.9


             The average characteristics of the synthetic wastewater are shown in
          Table 10.5.

          10.4.2 Experimental Methodology and Operating Conditions
          The initial seeding of the bioreactor was carried out by inoculating 200 L of
          anaerobic sludge collected from Pimpri Chinchwad Municipal Corpora-
          tion’s sewage treatment plant, Pimpri–Chinchwad Link Road, Pimpri,
          Pune. The reactor was fed with synthetic wastewater (COD: 500 mg/L)
          while inoculating. The TSS concentration in the bioreactor immediately
          after inoculation was 12,500, which reduced later and stabilized in the range
          of 10,000-11,000 mg/L. A synthetic feed solution having a COD of about
          500 mg/L was prepared in the feed tank on daily basis. It was observed that
          the organic content of the feed was naturally degrading with time and gen-
          erally more than 25% organic load was getting degraded in one day. To min-
          imize the degradation effects, fresh feed was prepared in the feed tank every
          day. The complete study was carried out in two phases. During the first
          phase of 120 days of experimentation, optimization of the OLR to the bio-
          reactor was carried out. In the second phase of 80 days of operation, overall
          performance evaluation at optimized operating conditions was undertaken.
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