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418   Industrial Wastewater Treatment, Recycling, and Reuse


          Table 10.6 Experimental Operating Conditions Maintained During the Study
          S. No.  Operating parameter       Unit             Reading

          1       Bioreactor volume         Liters           670
          2       Working volume of the     Liters           550
                    bioreactor
          3       Average feed COD          mg/L             385
          4       HRT in the bioreactor     h                15, 12, 10, 7
          5       Temperature in the          C              37
                    bioreactor
                                                     3
          6       Organic loading rate to   kg COD/m /day    0.62, 0.77, 0.92,
                    bioreactor                                 1.32
          7       MLSS in the bioreactor    mg/L             10,000–11,000
          8       MLVSS in the bioreactor   mg/L             7500–8000




          two to three times. One hundred liters of alkali solution (0.1% NaOH
          +0.2% NaOCl) was prepared in the cleaning tank and recirculated through
                                                 3
          the membrane modules at a flowrate of 10 m /h for 30 min. After stopping
          the recirculation flow, the membranes were allowed to soak in the alkali
          solution for 8 h. The recirculation pump was operated for 5 min after ending
          the soaking cycle and then membrane modules were rinsed with tap water
          two to three times.



          10.4.2.3 Overall Performance Evaluation of AnMBR Under Optimized
          Operating Conditions
          Chemical cleaning of the membranes was carried out before starting the
          performance evaluation study. During the performance evaluation, organic
                                                           3
          loading to the bioreactor was set at 1.155 kg COD/m /day. Depending
          upon the MLVSS in the bioreactor, a calculated quantity of the sludge
          was withdrawn from the bioreactor on a daily basis to keep the MLVSS
          in the range of 7500–8000 mg/L. The bioreactor temperature was constant

          and maintained at 37 C for the complete study. The initial permeate flux
                           2
          was set at 93 L/m /h (LMH). Chemical cleaning of the membrane was
          carried out after 60 days of operation, and the membrane unit was discon-
          nected from the bioreactor for 10 h. Feed flow to the bioreactor was
          stopped during the membrane cleaning operation; however, an equivalent
          amount of substrate dose was provided to the bioreactor for stable opera-
          tion. The partial recycling of permeate flow was continued during this
          phase of study, and the recycling flow was adjusted throughout the study
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