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Q Search The following information is given for an activated sludge system design: Flowrate Influent BOD Effluent BOD Unit m/d mg/L mg/L Value 10,000 150 SRT Synthesis yield, Y, g VSS/g bCOD Wastewater 1 Wastewater 2 Wastewater 3 Cell debris yield, f, 0.40 0.50 0.30 0.15 0.08 g VSS/g VSS Endogenous decay, b, gVSS/g VsSd mg/L nbVSS Temperature Note: Wastewater 1, 2, or 3 to be selected by instructor 10 Determine (a) the aeration tank oxygen requirements in kg/d, (b) the aeration tank oxygen uptake rate in mg/L h, (c) the aeration tank biomass concentration (mg/L), and (d) the portion of the total oxygen required that is needed for nitrification. Naranja
engineering   Civil-Engineering   
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Sol O) demand biodijhadabe domital n 1.6 r 150 > 240 mg/L bio- ma» phoduetien tt k,.SRToo0o 05150-2 l4 (o.o8k6) 740 53.28 536 ka/d t.ur8 tont oxJgan んCute (OUR Ro OUR io - 142 536 1480 - T6l- 12- 718.88 ^/a- 1000(c) bio mob , bioSRT (536 kalas) (6J) 10000 mg ld 24 h 3 216 .929 kgL 1666.67 , 1929 mg IL

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