• 상하수도학회지
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• 제23권5호
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• pp.517-526
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• 2009

This research has been conducted to investigate the characteristics of hydraulic behavior within the PAC contactor, the rectangular shape sedimentation basin without inclined tube and the other one with inclined tube those are parts of demonstration plants(capacity : $2,000m^3/d$) in Korea Institute of Water and Environment. As results of tracer tests, the flow within PAC contactor was evaluated to divided into plug flow and dead space distinctly, and characteristics of dead space was close to that of CSTR(Complete/continuous Stirred Tank Reactor). Also, considering Reynolds number, Froude number, Morill, Modal, NCSTR Inex and plug flow/mixed flow fraction, in the case of the rectangular shape sedimentation basin without inclined tube, the characteristics of flow pattern was close to CSTR. On the other hand, in the case of the basin with inclined tube, the region of CSTR decreased precisely compared with the case of no-tube. Until now we have recognized that the inclined hydraulic structure just reduces the surface loading rate within a sedimentation basin. Actually besides, the inclined structure have an important effect on the hydraulic behavior within the basin.

• 한국산학기술학회논문지
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• 제8권3호
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• pp.627-631
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• 2007

슬러지의 침전성에 영향을 미치는 인자는 F/M비, 유입수의 성분과 조성, 처리수온, 포기조의 pH, 슬러지 일령, 사상성세균의 증식 등으로 알려져 있으며, 유기산의 잔류량이 EPS의 분비에 영향을 미쳐 슬러지의 침강성에 영향을 주게 된다. 바실러스를 이용한 공법에서 생물 반응조는 특히 바실러스 종의 우점화를 위한 포자화의 진행을 이루는데 중요한 것으로 알려져 있으나 이에 대한 기작 설명은 아직 미흡한 실정이다. 바실러스를 이용한 B3 공법과 RABC 공법으로 운전 중인 처리장의 생물반응조는 점감포기를 하고 있으며 침전조에서 포자를 형성한 바실러스가 생물반응조로 반송되면 1.6mg/L로 높아진 DO농도와 유기물질 유입으로 바실러스가 발아를 하고 활성도가 높아지며, 0.5mg/L로 낮아진 DO농도로 인하여 포자를 형성하면 EPS 추출물질 중 Protein의 함량이 109.95mgEPS/gSS에서 131.77 mg EPS/gSS로 증가하고 SVI는 85mL/g에서 96mL/g사이로 양호함에 따라 DO농도가 EPS 추출물질 중 Protein의 생성에 영향을 미치며 Protein의 함량이 침전에 영향을 미치는 것으로 판단된다. 또한 Protein/Carbohydrate 비율에 따라 침강성은 영향을 받는 것으로 나타났다. 특히 RABC 공법에서는 Protein/Carbohydrate의 비가 침전에 영향을 미치는 것으로 나타난 반면, B3 공법에서는 Protein/carbohydrate의 비에 영향을 크게 받지 않는 것으로 나타났다.

• 상하수도학회지
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• 제26권2호
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• pp.177-189
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• 2012

Sediment load deposited in sewers and manholes reduces not only the capacity of pipes but also the efficiency of the whole sewer system. This causes the inundations of the low places and overflows at manholes, Moreover, sulfides and bad odor can occur due to deposited sediment with organic loads in manholes. Movements of sediment load in manholes are complicated depending on manhole size, location, inside structure, sediment load type, and time. Therefore, it is necessary to understand the movements of sediment load in manholes by experiments. In this study, experiments were implemented by a square manhole with straight path to measure deposited sedimentation quantity. The experimental apparatus was consisted of a high water tank, an upstream tank, test pipes, a sediment supplier, a manhole, and a downstream tank to measure the experimental discharge. The quantity of deposited sediment load was measured by different conditions, such as the inflow condition of sediment(continuous and certain period), the amount of inflow sediment, discharge, and the type of sediment. Jumoonjin sand(S=2.63, D50=0.55mm), general sand(GS, S=2.65, D50=1.83mm) and anthracite (S=1.45, D50=0.80mm) were employed for the experiment. The velocities in inflow pipe were 0.45 m/s, 0.67 m/s, and 0.9 m/s. Sediment load movement and sedimentation quantity in manhole were influenced by many factors such as velocity, shear stress, viscosity, amount of sediment, sediment size, and specific gravity. Suggested regression equations can estimated the quantity of deposited sediment in the straight path square manholes. The connoted equations that were evaluated through the experimental study have velocity range from 0.45 to 0.9m/sec. The study results illustrates that appropriation of design velocity ragne between 1.0 and 2.0m/sec could implement to maintain and manage manholes.

• 한국물환경학회지
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• 제36권1호
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• pp.55-68
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• 2020

Because of the intensified environmental problems such as climate change and resource depletion, sewage treatment technology focused on energy management has recently attracted attention. The conversion of primary sludge from the primary sedimentation tank and excessive sludge from the secondary sedimentation tank into biogas is the key to energy-positive sewage treatment. In particular, the primary sedimentation tanks recover enriched biodegradable organic matter and anaerobic digestion process produces methane from the organic wastes for energy production. Such technologies for minimizing oxygen demand are leading the innovation regarding sewage treatment plants. However, sewage treatment facilities in Korea lack core technology and operational know-how. Actually, the energy potential of sewage is higher than sewage treatment energy consumption in the sewage treatment, but current processes are not adequately efficient in energy recovery. To improve this, it is possible to apply chemically enhanced primary treatment (CEPT), high-rate activated sludge (HRAS), and anaerobic membrane bioreactor (AnMBR) to the primary sedimentation tank. To maximize the methane production of sewage treatment plants, organic wastes such as food waste and livestock manure can be digested. Additionally, mechanical pretreatment, thermal hydrolysis, and chemical pretreatment would enhance the methane conversion of organic waste. Power generation systems based on internal combustion engines are susceptible to heat source losses, requiring breakthrough energy conversion systems such as fuel cells. To realize the energy positive sewage treatment plant, primary organic matter recovery from sewage, biogas pretreatment, and co-digestion should be optimized in the energy management system based on the knowledge-based operation.

• 한국환경과학회지
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• 제13권6호
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• pp.571-579
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• 2004

There is a need to improve the efficiency of the existing sanitary treatment facilities, because the effluent standard becomes more stricter and septic sludge increased. Thus, operating processes of sanitary treatment system in M city changed with installation of additional facilities. Process modifications were as follows: Dilution water was added to the next process after primary aeration tank. Some secondary sedimentation sludge was recycled to primary aerator so that most of the organics were stabilized in primary aeration tank under automatic control of dissolved oxygen. The line of effluent from dewatering process flowing to the activated sludge tank was changed to the primary aerator. The primary sedimentation sludge line was linked to a thickener. Polymer was added to the activated sludge tank. The effluent of primary aerator and aerobic digester was recycled from the 5th to the 1st sector. As consequencies of above process modifications, the improvement of removal efficiency was achieved as BOD 54%, COD 42%, SS 61%, T-N 39%, and T-P 12%, respectively.

• 한국환경보건학회지
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• 제20권2호
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• pp.28-38
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• 1994

New problems have been recently posed on the abnormal foaming (Scum) in an aeration tank and the sludge flotation in a final sedimentation tank during the activated sludge process. However, the activities of the causing bacteria, Nocardia-amarae in an aeration tank have not been searched out at all. Therefore, in this article the activities of Nocardia-amarae in an aeration tank have been closely examined by means of the changes of (F/M) ratio, SRT and inflowing substrate using continuous type and fed-batch type. Summarized results of experiments are as follows. 1. Regrading continuous culture when synthetic wastewater was used substrate neither the increase in the number of Nocardia-amarae in the aeration tank nor the Occurrence of Scum was observed. 2. In the case of fed-batch culture, Nocardia-amarae in the aeration tank increased due to the partial change in substrate and the effect of SRT was significant. 3. Once the scum was formed and the quantity of added Nocardia-amarae and substrate were not changed, the effect of STR was not significant.

• 한국지반공학회논문집
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• 제16권4호
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• pp.149-156
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• 2000

해성점토를 이용하여 준설매립한 부지의 장기적인 침하거동을 규명하기 위하여 실린더와 대형토조를 이용하여 침강.자중압밀시험을 수행하였으며, 준설매립단지에 자동무선계측시스템을 설치하여 매립부지의 층별침하량과 간극수압의 변화를 계측하였다. 이를 이용하여 준설매립 공정에 따른 매립지층의 침하거동을 분석하고 유한변형률 압밀이론을 이용한 수치해석 결과와 비교하였다. 침하거동 분석결과, 불연속 준설매립공정으로 인하여 매립지층의 분리 현상이 발생하였고 지층별 침하거동이 상이하게 나타났다.

• 웰빙융합연구
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• 제6권3호
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• pp.19-23
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• 2023

Purpose: High concentrations of nitrogen exist in food wastewater, and when nitrogen is not properly treated and discharged, it can cause eutrophication in the aquatic ecosystem. Research design, data and methodology: In order to remove nitrogen using sodium hypochlorite, the BNCR tank was designed and installed in the step behind the biological treatment tank, and the data of pH, TOC, and T-N were collected after about a month of demonstration. Results: As a result of operating the BNCR tank, total nitrogen decreased by about 83% on average. The total nitrogen in the second sedimentation tank before going through the BNCR tank must be removed and finally discharged after nitrogen is removed above the legal standard of 60 mg/L. Conclusions: If BNCR tank is added to the process currently applied to nitrogen removal and operated, ammonia nitrogen can be removed more efficiently. However, the disadvantage is that nitric acid nitrogen and nitric acid nitrogen cannot be removed. If these disadvantages are supplemented and optimized in the future, it will be helpful for workplaces that are having difficulty removing nitrogen.

• 한국수산과학회지
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• 제34권1호
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• pp.70-76
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• 2001

우리나라의 실정에 적합하고 실용적인 순환 여과식 양식 시스템을 개발하여 package 형태로 개발하기 위하여 $2.5 m^3$ 규모의double drain 형태의 사육조와 침강성 고형물질을 제거하기 위한 침전조, 부유성 고형물의 제거를 위한 floating bead filter, 용존고 형물을 제거하기 위한 포말 분리기와 암모니아성 질소를 제거하기 위한 회전 원판 반응기를 조합한 순환 여과식 양식 시스템을 설계하고 제작하였다. 본 시스템에 평균 어체중 392.8g의 나일 틸라피아 173마리를 수용하여 일간 보충수를 사육조 용적의 $10\%$를 사용하여 14일간 어류사육을 실시한 걸과 사육조의 수질을 보충수와 거의 동일한 수질로 유지할 수 있었으며 사료계수 1.4, 일간 성장률 0.64를 얻을 수 있었다.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2000년도 춘계학술발표대회
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• pp.125-128
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• 2000

본 연구에서는 순환식 돈분 폐수 처리 시스템에서의 미생물 분포에 따른 폐수 처리 효과를 모델링하기 위해 신경회로망과 PCA를 이용하는 새로운 방법을 제안하였다. PCA 분석 결과를 바탕으로 신경회로망의 최적 입력 조건을 찾고, 실측 데이터를 이용하여, 폐수 처리 시스템의 각 탱크를 별도로 학습함으로써 비교적 적은 수의 데이터에도 불구하고 정확한 모델링 결과를 얻었다. 제안한 시스템은 폐수 처리 시스템의 효과적인모니터링 시스템으로 사용할 수 있으며, 향후 실제 돈분 처리 시스템에서 원하는 기준의 방류수를 얻기 위한 최적의 입력조건 (미생물밀도 등)을 결정하는데 있어서 에뮬레이터로 사용될 수 있을 것으로 기대된다.