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Technical Description <br /> Nitrogen removal in the Bio-Pure process is considerably greater than that offlowthrough and single- <br /> tank, sequencing-batch reactor systems. The Bio-Pure system achieves an average of 96% total <br /> nitrogen removal. This high nitrogen removal is achieved through simple modifications of the timing <br /> (batching) cycle in the controlling microprocessor. <br /> '— AERATION DETENTION <br /> The Bio-Pure system's superior low-sludge-producing performance is obtained,in part,by combining <br /> the complete-mix hydraulic design with the detention times of the extended-aeration designs. This <br /> combination effectively produces a low RM ratio and a subsequent high MCRT. This promotes the <br /> development of specific, high-process microorganisms. <br /> The growth curve of the cell life cycle is related to the effectiveness of BODS removal within the <br /> treatment process. In all cases, removal of BODS is dependent upon aerator detention time. <br /> Growth and predominance of microorganisms are controlled by a variety of circumstances,including <br /> type offood matter,metabolic rate,and microorganism size.Because a definite type of microorganism <br /> lives best under certain conditions, it is possible to relate treatment efficiency to microorganism type. <br /> This is a determining factor for good batch process detention design. <br /> As the BOD remaining in the batch decreases, ciliated protozoa increase in number. A general guide <br /> as to relative predominance of protozoa and efficiency in the process may be characterized in the <br /> following chronological order: <br /> TYPE PROCESS EFFICIENCY <br /> 1. Sarsodina Plant startup or recovery <br /> 2. Holophytic flagellates High organic overloading <br /> 3. Holozoic flagellates Decreasing organic overloading <br /> 4. Ciliates Lowering efficiency <br /> 5. Stalked ciliates Elevating efficiency <br /> 6. Rotifers High BOD efficiency, rapid oxidation <br /> High rotifer concentration will occur when the BODS removal efficiency is high;therefore,additional <br /> detention capacity is required. The aerator size required to achieve this efficiency is based upon F:M <br /> ratio criteria between 0.1 and 0.5 pound BOD/pound MLVSS. <br /> A second method of determining retention time is a microscopic examination of the stalked ciliates. <br /> Groupings of 3 to 4 stalks indicate a healthy sludge;less or more groupings indicate either too young <br /> or too old a sludge. <br /> The quantity of microorganisms can be represented by the quantity of MLVSS. Ideally, the living or <br /> active microorganisms would simply be counted, but this is not feasible; studies show the MLVSS is <br /> a good approximation of microorganism concentrations in the NILSS. Data obtained are calculated <br /> using a moving seven-day average. <br /> 12 <br /> a. <br />