DETERMINATION OF BIOKINETIC COEFFICIENTS FOR ACTIVATED SLUDGE PROCESSES ON MUNICIPAL WASTEWATER

摘要

abstract_textpBiokinetic coefficients and efficiency for three activated sludge processes including conventional, extended aeration, and contact stabilization were determined in pilot-scale for six months in Isfahan south municipal wastewater treatment plant. These systems were operated under two different MLSS concentrations in aeration tank. For each MLSS, five periods were considered in base of flow rate and sludge retention time (SRT). The samples from the influent wastewater, reactor and effluent were collected periodically and experimented by the Standard Methods. The data were analyzed by the Excel and SPSS softwares. The investigation showed that the yield coefficient (Y), decay coefficient (kd), maximum specific growth rate and saturation constant (K(s)) for conventional activated sludge process were in the range of 0.48-0.8 mgVSS/mg sCOD, 0.0189-0.026 1/day, 0.95-0.98 '1/day and 52-71 mg sCOD/L, extended aeration: 0.6174-1.2512 mgVSS/mg sCOD0.0198-0.0309, 1/day 1.96-3.17 1/day and 311.7-508 mg sCOD/L and for contact stabilization: 0.6322-0.713 mgVSS/mg sCOD1 0.0172-0.0387 '/d0.23-1 0.42/d and 13.8-50.8 mg sCOD/L, respectively. In the conventional and contact stabilization processes values of the coefficients were within the range of those reported in the literature. However, in the extended aeration process, values of K(s) and Y in MLSS of 5000mg/L were out of ranges. The sensitivity analysis of changes in the biokinetic coefficients showed direct relationship of kd and Ks with the concentration of the effluent substrate. Whereas mu(max) is inversely related to concentration of the effluent substrate. In addition, regardless of the type of substrate and MESS concentration, the effluent substrate concentration is more sensitive to mu(max) than kd and Ks. The results also showed a COD removal efficiency ranging for conventional process between 83 and 92.5, for extended aeration process between 88 and 93.8, and for contact stabilization process 77 and 92. The effluent COD was simulated using the biokinetic coefficients determined during the study./p/abstract_text