• Environmental Engineering Research
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• 제16권4호
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• pp.213-218
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• 2011

The two-stage intermittent aeration activated sludge process (IAP) and dynamic-flow intermittent aeration activated sludge process (DFP) were investigated for the nutrient removal of domestic wastewater. Three sets of IAP and one set of DFP were operated. The fermented settled sludge taken from the primary settling tank was added to two IAP and one DFP as an external electron donor, with one IAP, in which an external carbon source was not added, as a control. All the systems were operated at a sludge retention time of 20 days and a hydraulic retention time of 12 hr. A Higher denitrification rate was observed with the fermented settled sludge for the denitrification compared to the process without the addition of the organic source. The result indicates that the fermented acid from the primary domestic sludge has been proved to be an excellent electron donor for denitrification and biological phosphorus removal with IAP and DFP in treating relatively low C/N ratio(Carbon / Nitrogen ratio) wastewater. Phosphate accumulating organisms have a capability of competing with denitrifiers in the presence of volatile organic acids under anoxic conditions.

• 유기물자원화
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• 제21권3호
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• pp.82-92
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• 2013

생물학적 질소 및 인을 제거하기 위한 경제적인 공법인 간헐 폭기 MBR공법은 내부순환이 없고, 간헐반응조 폭기 시간 조절을 통해서 반응시간을 조절할 수 있는 장점이 있다. 본 연구에서는 신기술로 인증 받은 폭기에너지 절약 공법인 신 간헐폭기-MBR공법, 그리고 간헐반응조 폭기/비포기 주기가 1시간/1시간 및 4시간/4시간인 일반적인 간헐 폭기 MBR공법에 있어서의 처리성을 컴퓨터시뮬레이션을 통해서 평가하였다. 폭기 주기가 1시간/1시간인 간헐폭기 MBR공법의 경우, 폭기 시 최대 용존산소 농도가 0.23mg/L가 되어, 동시 질산화/탈질 반응이 수행되는 것으로 나타나 질소와 인 제거 효율은 각각 57.0%, 55.0%로 가장 높았다. 본 연구는 유입수질이 일정한 경우에 있어서의 시뮬레이션을 수행하였으며, 각 시스템에 있어서의 실 처리장 적용성을 파악하기 위해서는 유입수질 변동에 따른 처리성을 평가할 필요가 있는 것으로 나타났다.

• 한국물환경학회지
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• 제20권1호
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• pp.18-23
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• 2004

In this research, a 2-stage intermittently aerated activated sludge system(IA) and intermittently aerated dynamic flow activated sludge system(DF) were investigated for the removal of nutrients in domestic wastewater. Wastewater was characterized by low C/N( organics/nitrogen) ratio. $COD_{cr}$, $BOD_s$, TKN and TP concentrations of domestic wastewater were 235, 47, 32 and 5.4 mg/L, respectively. Three sets of IA and one set of DF were operated. Three of four systems were added with fermented settled sludge taken from primary settling tank as an external electron donor and the other(IA) for control reactor was operated without addition of electron donor. All systems were operated at same sludge retention time of 20 days and hydraulic retention time of 12hrs. The supplemental electron donor was supplied into the anoxic mode. A higher denitrification rate was observed from the reactors with fermented settled sludge as an electron donor for denitrification compared to that of without addition of organic source. The result of this study indicates that the settled primary sludge, if the fermented at the acid stage, was an excellent electron donor for denitrification. 81 % of TN and 80% of TP were removed from the systems with the supplemental organic source added. However, the control reactor without addition of electron donor showed only 39% of TN and 43% of TP.