• Title/Summary/Keyword: 간략화된 ASM No. 2

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Simplification of ASM No. 2 using Anaerobic-Aerobic-Anoxic SBR (혐기-호기-무산소 SBR 반응조를 이용한 ASM No. 2 모델의 간략화에 관한 연구)

  • Kim, Shin Geol;Choi, In Su;Koo, Ja Yong
    • Journal of Korean Society of Water and Wastewater
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    • v.22 no.1
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    • pp.3-14
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    • 2008
  • ASM No. 2(Activated sludge model No. 2) is very useful model to analyze the wastewater treatment which removes nitrogen and phosphorus. But, it is difficult to apply ASM No. 2 to control of wastewater treatment since it has 17 material divisions and 46 parameters. So the purpose of this study was the simplification of ASM No. 2 and the provement of simplification model. Firstly ASM No. 2 was simplified with 5 material division and three phases(Anaerobic, aerobic, anoxic phases). The simplified model was proved by R-square using track study data. As a result of provement, the values of R-square in ${NH_4}^+$ were 0.9815 in ASM No. 2 and 0.9250 in simplified model and in ${NO_3}^-$ were 0.8679 in ASM No. 2 and 0.7914 in simplified model and in ${PO_4}^{3-}$ are 0.9745 in ASM No. 2 and 0.9187 in the simplified model when the ability to express the material variation was compared by R-square. So, the simplified model has enough ability to express the variation of ${NH_4}^+$, ${NO_3}^-$ and ${PO_4}^{3-}$.

Control of $NH_4-N$ in Wastewater Treatment Effluent According to Simplified ASM No. 1 (간략화된 활성슬러지 모델(ASM No. 1)을 이용한 유출수 중 암모니아성 질소의 제어에 관한 연구)

  • Kim, Shin-Geol;Choi, In-Su;Koo, Ja-Yong
    • Journal of Korean Society of Environmental Engineers
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    • v.29 no.5
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    • pp.548-555
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    • 2007
  • The control of wastewater treatment has two merits; one is to regulate water quality of effluent and the other is to reduce the cost of wastewater treatment. The purpose of this study was to control the ammonium nitrogen in effluent that is known to cause eutrophication. The control was based on simplified ASM No. 1 which had 3 component materials and 8 coefficients, and the control method was as following. Firstly the ammonium concentration of inflow was measured and the optimal aeration time in effluent was determined according to simplified ASM No. 1 to be 1.0 mg/L. If ammonium concentration of effluent was not equal to 1.0 mg/L, the influent ammonium was corrected by adaptive control. These processes above were repeatedly performed. The SBR running aerobic-anoxic phase had been controlled for 1 month with this method. As a result, the ammonium concentration of the effluent showed in the range of $0.22\sim3.1$ mg/L with an average concentration of 1.1 mg/L. The adaptive control method used in this study was found very useful to control and predict the effluent concentration of ammonium.

Control of Wastewater Treatment Removing Phosphate Based on ASM No. 2 Simplified Model and Investigation of Luxury Uptake Limitation (ASM No. 2 간략화 모델에 기초한 인산염의 제어 및 인섭취 제한현상에 대한 고찰)

  • Kim, Shin-Geol;Choi, In-Su;Koo, Ja-Yong
    • Journal of Korean Society of Environmental Engineers
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    • v.30 no.2
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    • pp.181-189
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    • 2008
  • Phosphate is the limiting factor leading to the eutrophication in nature and has been usually removed by the luxury uptake of PAOs(Phosphate accumulating organisms). The purpose of this study was the control of wastewater treatment removing phosphorus. The control of wastewater treatment process was performed by optimal and adaptive control. They were performed as followings. Firstly the inflow phosphate concentration was measured and the optimal aeration time was calculated by simplified ASM No. 2 for the phosphate to be 1.0 mg/L in effluent. It was optimal control. But when the phosphate concentration in effluent was not 1.0 mg/L, adaptive control was necessary to coincide the objective of control with real value. Then it was performed as the objective phosphate concentration in effluent was changed according to calculation of errors and it was adaptive control. The wastewater treatment process had been controlled by them for about one month. The range of phosphate concentration in effluent 0.2$\sim$3.2 mg/L and the average of it was 1.0 mg/L. The limitation of luxury uptake occurred two times while wastewater treatment process was running. After the analysis of laboratory tests, we knew the reasons were the shortage of ammonia nitrogen and the excessive aeration.