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Technical Description <br /> There are three basic classifications of the activated sludge process that are defined by the load- <br /> ing range to the microorganisms: high, conventional. and low. The following shows typical <br /> ranges of the MCRT and F:M for each loading range: <br /> MCRT, F:M <br /> Process day lbs BODs/dxyAb MY,VSS <br /> High Rate 3-5 0.4-1.5 <br /> Conventional Rate 5-15 0.2-0.4 <br /> Low Rate 15-30 0.5-0.2 <br /> (Note:lbs/day x 0.01157=g/ko) <br /> In the complete-mix, activated-sludge process, the characteristics of the mixed liquor are similar <br /> throughout the aeration tank. That is, the influent waste is rapidly distributed, and operating char- <br /> acteristics measured in terms of solids, Oxygen Uptake Rate (OUR), MLSS, and soluble BOD <br /> concentration are nearly identical throughout the tank, with a very low level of food available to a <br /> large mass of microorganisms at any given time. This is the principal reason for the Nitro- <br /> Raptor system's ability to handle surges in the organic loading without producing a change in <br /> effluent quality. <br /> Critical design factors are the tank's length-to-width ratio, amount of air introduced, and turbu- <br /> lence throughout the tank. <br /> The system is operated at Water Pollution Control Federation and federal EPA design standards, <br /> which recommend an MLSS of about 3,000 to 6,000 mg/L.The quantity of sludge returning from <br /> - the clarifier is 100% of sludge volume although only 45% is required in order to maintain the <br /> aeration solids. <br /> To ensure that a Dissolved Oxygen (DO) of 1.5 ppm minimum exists at all points, a minimum <br /> oxygen input of 2.0 mg/L is maintained at the effluent end of the aeration chamber. Therefore, <br /> air is supplied at a rate of 0.8 to 11.5 cubic feet/gallon of wastewater with an additional mixing <br /> factor of 1.5 to 2.0 cubic feet per gallon. <br /> For sizing the air delivery system, the cubic-feet-of-air requirement is expressed as cubic feet of <br /> air required per pound of BOD removed from the aeration reactor. The minimum air/organic <br /> loading recommended by most state agencies is 1,000 cubic feet per pound of BoOD wing a re duo- <br /> Raptor system expands this to 1,500 cubic feet per pound of BOD removed, <br /> al <br /> airbase for compensation of higher organic loading than anticipated and to support further proc- <br /> essing of ammonium nitrogen (NH;). Air availability is always maintained at 125% of maximum <br /> demand with the 25% residual over the 1,250 CF/000 gallons, bled off between the blower and <br /> the aeration tank. <br /> Because the total daily air requirement is dependent upon the pounds of BOD applied, the <br /> ing the treatment plant must be known and can be calculated as follows: <br /> pounds of BOD enter <br /> BxFxC =A <br /> where <br /> B = influent BODS mg/L <br /> F = system maximum daily hydraulic flow <br /> - to- <br /> TH Technical Services Group,Inc. <br />