Page 783 - Fundamentals of Water Treatment Unit Processes : Physical, Chemical, and Biological
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738                            Fundamentals of Water Treatment Unit Processes: Physical, Chemical, and Biological



            TABLE 23.5
            Activated-Sludge Process Variations
                                                              Loading
                                                     Volumetric        F=M Ratio
                                                                3
            Process Name           Notes         (lb BOD=day=1000 ft )  (lb BOD=day=lb VSS)     Sketch
            Conventional   10%–30% return sludge        35              0.2–0.5
                                                                                         PS       Reactor     FS
                                                                                                Return sludge

                                                                                                          Waste

            Tapered aeration  Airflow is reduced along   35              0.2–0.5
                                                                                         PS       Reactor     FS
                            reactor length
                                                                                               Return sludge
                                                                                                          Waste

            Step loading   Waste is injected along reactor  50          0.2–0.5
                            length
                                                                                                Reactor       FS
                                                                                             Return sludge


                                                                                                          Waste

            Contact stabilization  Organisms assimilate and store  70   0.2–0.5
                                                                                               Reactor        FS
                            in reactor and get hungry in
                            re-aeration basin
                                                                                            Re-aeration
                                                                                        Return sludge
                                                                                                          Waste
            Hatfield process  Used for high organic wastes.
                                                                                    PS           Reactor      FS
                           Nutrients added from
                           Anaerobic digester
                                                                                              Re-aeration
                                                                                            Sludge
                                                                                                          Waste
                                                                                               An-D
                                                                                     Primary sludges  Supernatent

            Extended aeration  Sludge not wasted        20              0.2–0.5
                                                                                            Reactor      FS
                                                                                        Return sludge

            Source: Adapted from Stewart, M.J., Activated sludge process variations, The complete spectrum, in Water and Sewage Works, Part I, April 1964; Part II,
                  May 1964; Part III, June 1964.



            and the involvement of many in the field, is an index of the  more stringent. The outcome is usually increasing operating
            importance of operation. As with other unit processes,  costs and at some point a new plant becomes ‘‘cost-effective.’’
            design has a great deal to do with effective operation. Many
            ‘‘tradeoffs’’ can be seen between capital costs and operating  23.2.5.1  Bulking Sludge
            costs ranging from effective operation of the processes to  Bulking sludge is a sludge that settles poorly. The microorgan-
            routing maintenance tasks. If the design lacks being ‘‘operator  isms do not coalesce into a dense floc.Usually,the floc is
            friendly,’’ the capital investment is at risk. Since the 1980s  associated with an excessive growth of filamentous bacteria
            construction of new plants is rare; plants are expanded often to  (van Niekerk et al., 1987). Causes include low dissolved oxygen
            take into account increasing population and industries and are  concentration, nutrient deficiency, high sulfide concentration, and
            called upon to comply with regulations that are increasingly  low organic loading (low food-to-microorganism ratio, F:M).
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