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2. Sewage, while exposed to aeration and mixing, is allowed to <br /> accumulate within the aeration chamber until enough volume is NOTES <br /> present to initiate a batch cycle. <br /> 3. After the mixed liquor has reached a predetermined level, a <br /> portion, or batch, is transferred to the clarifier for a programmed <br /> period of quiescent settling. <br /> 4. Upon completion of the quiescent settling period, the superna- <br /> tant is transferred through a chlorination cycle in the chlorine <br /> contact chamber, then through tertiary filters, and finally the <br /> tertiaried effluent may be dechlorinated and further sterilized by <br /> optional ultraviolet light prior to discharge. <br /> Settled sludge from each stage, and filter backwash, are returned to <br /> the aeration chamber and recycled.If physical pretreatment is incor- <br /> porated, settled sludge and backwash may be returned to the pre- <br /> treatment chamber. <br /> MECHANICAL PRETREATMENT <br /> DISINTEGRATION. If required, influent may be disintegrated by <br /> pretreatment prior to entering the aeration chamber by one of three <br /> methods: <br /> 1. A receiving basket, partially submerged in the mixed liquor in <br /> the aeration chamber. Sewage solids are contained and exposed <br /> to aerated mixed liquor for particle size reduction and mixed- <br /> liquor absorption. <br /> 2. A static fine screen is mounted outside the aeration chamber. <br /> As the raw waste stream flows across the metal grating, foreign <br /> articles are captured and fall into a dropbox.Sewage waste passes <br /> through the screen directly into the aeration chamber. <br /> 3. A comminutor, mounted outside the aeration chamber, reduces <br /> the size of all incoming matter by high-speed cutting.After pass- <br /> ing through the comminutor,waste enters the aeration chamber. <br /> PHYSICAL PRETREATMENT <br /> SEPARATION AND NITRIFICATION INITIATION. (NOTE: The <br /> following may not be required for nitrification where detention peri- <br /> ods of 14 hours or more are anticipated. With reduced solids con- <br /> centration, the normal calculated aeration demand for the batch <br /> process is sufficient for nitrification supplementation. Should exter- <br /> nal nitrification be deemed necessary, the following procedure is <br /> used.) <br /> Prior to entering the treatment plant, raw sewage may be collected <br /> in a baffled buffer tank. The buffer tank is anaerobic and sized for a <br /> detention period which will allow solid/liquid separation, retention <br /> of solids and floatable materials, and promotion of facultative anaer- <br /> obes by degeneration of natural dissolved oxygen levels. <br /> 10 <br />