• 대한환경공학회지
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• 제29권2호
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• pp.176-183
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• 2007

안 등이 보고한 모형 하상여과정의 수평집수관에 대한 여러 가지 측정치를 해석하기 위해 집수관에서의 흐름을 모사하는 수학적 모델을 개발하였다. 집수관 각 부위에서의 여과수 유입율 측정치와 본 연구에서 개발된 모델 예측치를 비교하였으며, 두 값은 잘 부합하였다. 이 모델을 이용하여 수평집수관 내부의 흐름에 대한 저항 즉, 조도계수를 구했고, 여러 실험조건에서 얻은 집수관의 조도 계수를 분석한 결과 집수정 유입유속이 커짐에 따라 조도계수는 증가하지만 정상적인 하상여과의 경우에는 0.012-0.015로 거의 일정함을 알 수 있었다. 또한, 집수관의 직경이 커지면 조도계수는 감소함을 알 수 있었다.

• 한국물환경학회지
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• 제22권2호
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• pp.222-229
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• 2006

The treatment performance and operational parameters of a tertiary wastewater treatment process a biological filtration system were investigated. The biological filtration system consisted of a nitrification filter (Fiter 1) and a polishing filter with anoxic and aerobic parts (Filter 2). SS, T-C-BOD, and T-N in effluent were kept stable at less than 3, 5 mg/L, and 5 mgN/L, respectively, under a HRT in Filter (filter-bed) of 0.37~2.3 h. T-N at the outlet of Filter 2 were about 1~5 mgN/L under the condition of LV of 50~202 m/d. In Filter 2, denitrification was accomplished under LV of 50~168 m/d in a 1 m filter-bed. However, the denitrification capacity reached the maximum when the linear velocity was increased to 202 m/d. Relationship between increase in microorganism and headloss was clearer in Filter 2. As a result, the denitrification rate increased from 1.0~2.3 kgN/($m^3-filter-bed{\cdot}d$) as the headloss increased. The COD removal rate was 6.0~9.6 kgCOD/($m^3-filter-bed{\cdot}d$) when operated with Filters 1 and 2. These results mean that captured bacteria contributed a part of COD consumption and denitrification. The maximum nitrification and denitrification rate was 0.5 and 4 kgN/($m^3-filter-bed{\cdot}d$) in Filter 1 and 2.The ratio of backwashing water to the treated water was about 5~10 %. In Filter 1, wasted sludge in backwashing was only 0.7~5.3 gSS/($m^3$-treated water). In Filter 2, added methanol was converted into sludge and its value was 8.0~24 gSS/($m^3$-treated water). These results proved that this process is both convenient to install as tertiary treatment and cost effective to build and operate.

• 대한환경공학회지
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• 제28권5호
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• pp.558-562
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• 2006

여과공정에서 망간제거특성을 고찰하기 위하여 모래, 망간사 등의 4가지 여재를 사용한 여과실험이 실시되었다. 여과속도는 123 m/d였고, 칼럼당 유입량은 $3.9m^3/d$이었다. 실험기간은 약 1년이었으며, 실험기간 동안 여재별로 이산화망간 부착량, 탁도제거율, 망간제거율, 유기물제거율 등을 고찰하였다. 평균 망간농도 0.208 mg/L의 여과지 유입수(잔류염소 1.0 mg/L)를 사용하여 여과실험한 결과 모래+망간사 칼럼은 98.9%, 망간사칼럼은 99.2%의 망간제거율을 보였다. 기존 모래여과지를 망간제거를 위해 사용할 경우 여층의 전부를 망간사로 교체하지 않고 일부만 교체하여도 망간제거에 충분한 효과가 나타나는 것으로 조사되었다.

• 상하수도학회지
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• 제19권2호
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• pp.135-143
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• 2005

It was evaluated that the effect of turbidity removal by Pore Controllable Fiber Filter(PCF) installed in NS(Naksang) small water treatmant plant(system) using under flow water as raw water in the study. The results of the study are as the followings. Firstly, the removal efficiency of turbidity by PCF without coagulation(in operation mode not using coagulants) was mostly below 20 percent. On the other hand, when operation using proper coagulants, that of turbidity was mostly over 80 percent. Secondly, slow sand filtration after PCF, total turbidity removal efficiency of final treated water was 84.3 percent, and the contribution by PCF was 57.1 percent and that of slow sand filtration was 27.7 percent. Therefore the introduction of PCF as pre-treatment process would be helpful to reduce the loading of high turbidity of slow sand filtration. Thirdly, the results of particle counter measurements showed that when operated PCF with coagulants, fine flocs captured or adsorbed at the pore of PCF were flow out into the effluents from 120 minutes after backwashing because of the increase of headloss of PCF. Therefore the decision of backwashing time should made consideration into the outflow of fine flocs from PCF. Fourth, coagulant dosages on PCF at the same turbidity was largely variable because of the effect of the raw water characteristics and the turbidity increase velocity at rainy days, therefore flexible coagulant dosages should be considered rather than fixed coagulant dosage by the influent jar-test result.

• 한국물환경학회지
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• 제35권5호
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• pp.409-417
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• 2019

In this study, a $480m^3/day$ pilot device was constructed through laboratory experiments based on the Ministry of Environment manual. The purpose of this study was to analyze the characteristics of CSO treatment and backwashing characteristics by applying the pilot device to the field. The purpose of this study was to acquire the basic data necessary for the design and operation management of the real scale filtration type non-point pollution control system. The filtration was conducted while maintaining the linear velocity of 20m/hour. The CSO treatment efficiencies of the pilot devices were 0.4-76.1%(mean 49.0 %), SS 51.4-91.6%(mean 77.8%), COD 22.2-59.4% (mean 38.3%) and TP 14.5-52.6%(mean 38.1%),respectively. The correlation coefficient between SS and the turbidity of influent water was 0.90, higher than that of CSO. To operate the treatment system effectively, the turbidity can be easily measured in real time as the monitoring item is the most appropriate because SS is the main target substance of the non-point source. As a result of analyzing the adsorbent treatment characteristics of PP filter material applied to this pilot device, the average particle diameter range of influent was $4.6-40.1{\mu}m$(mean $21.2{\mu}m$) and the treated water was $0.9-24.5{\mu}m$(mean $6.4{\mu}m$), respectively. Particles of approximately 10m or less are leached out, and so it is necessary to compensate for the raw water containing micro particulate matter.

• 대한환경공학회지
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• 제35권9호
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• pp.681-685
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• 2013

천변여과지에서 표류수 유속이 여재의 폐색에 주는 영향을 파악하기 위하여 파일럿 규모의 실험을 수행하였다. 표류수 유속을 0~40 cm/sec 범위에서 단계적으로 변화시키면서 설비를 운전하여 폐색이 발달하는 현상을 관측하였고, 관측결과를 수치해석코드로 해석하여 폐색계수를 얻었다. 연구결과 이 범위의 표류수 유속에서는 표류수 유속이 폐색발달에 영향을 주지 않는 것으로 나타났고, 폐색은 주로 표층에서 발생함을 알 수 있었다. 여과수 산출율이 $5m^3/m^2-day$에서 $3m^3/m^2-day$까지 감소하는 동안 표층 50 cm에서의 폐색계수는 약 30,000 sec까지 증가하였으며, 이는 전체 여재두께 2.4 m가 가지는 폐색계수의 87%에 해당되었다. 표층 50 cm의 폐색계수에서 표면폐색이 90% 정도를 차지하여 내부폐색은 약 10%에 불과함을 알 수 있었다. 운전지속에 따라 표면폐색은 심화되었지만 내부폐색은 일정함도 알 수 있었다. 또한, 폐색이 진행되어도 여과깊이에 따른 탁도분포는 일정함을 알 수 있었다.

• 대한환경공학회지
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• 제39권8호
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• pp.478-488
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• 2017

도로변 등에 여과형 강우유출수 처리시설이 많이 이용되고 있으나, 유지관리의 최소화, 성능의 검증 및 최적 조건의 수립이 선행되어야 한다. 본 연구에서는 강도가 우수하고 성형이 용이한 세라믹 여재를 사용하고, 하단 지지부와 상단의 여과조로 이루어진 상향류식 여과 시스템을 구성하고, SS 제거능과 역세척 조건을 검토하여, 최적 운전 조건을 설정하였다. 여과 선속도 20-40 m/h 조건에서 운전하였을 때, 총 고형물 부하 $30kg/m^2$에 이르는 조건에서도 최대 수두 손실 상승이 3 cm 내외이었으며, SS 처리 효율이 96% 이상으로, 안정적인 운전이 가능하였다. 운전 중의 손실수두와 여재층 공극률은 급수 모델에 의해 모사가 가능하였다. 특히, 하단 지지부에서 일정 입도 이상의 SS가 상당량 제거되어, 여과조에 부하를 감소시킬 수 있음을 확인하였다. 최적의 역세척 조건을 설정하기 위하여 공기 및 수세척의 시간과 유량, 그리고 정체수 배출 공정의 유무에 따른 영향을 확인하였으며, 실험한 모든 조건에서 만족할 만한 손실수두의 회복을 달성할 수 있었다. 다만, 역세척 직후 SS의 배출을 최소화하기 위해서는 공기세척과 수세척 공정 사이에 정체수 배출 공정의 도입이 효과적인 것으로 파악되었다. 본 연구에서 설정한 역세척 조건을 적용하였을 때, SS 부하 $400-450kg/m^2$의 여재층이 성공적으로 세척될 수 있어, 장기운전이 충분히 가능할 것으로 판단된다.

• 펄프종이기술
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• 제32권3호
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• pp.1-9
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• 2000

The MDDA (Modified Dynamic Drainage Analyzer) was developed to evaluate the drainage characteristics on paper machine. The initial forming vacuum velocity was decreased with the increase of stock consistency and there were no significant effects of the applied vac-uum. On the other hand the initial forming drainage velocity was rapidly decreased with the increase of stock consistency above the 0.35 bar of applied vacuum. The final drainage time and wet web permeability showed similar trends under 0.075% consistency but increased rapidly at the higher consistencies. SFR(Specific Filtration Resistance) and drainage obtained for different vacuum level applied and deposited weights measured by using MDDA showed the linear relationship.

• Nuclear Engineering and Technology
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• 제53권12호
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• pp.3979-3989
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• 2021

Several parametric effects on the magnetic collection have been evaluated considering dimension, strength of external magnetic field, injected velocity and particle concentration in the working fluid. Besides, accidental environments, expected in the containment of nuclear power plants, have also been addressed for the capture efficiency. The capture efficiency is especially enhanced with magnetic particle size and magnetic field strength through increased magnetic force; the non-magnetic coating thickness and fluid velocity hinder the magnetic collection. Based on the assessment, the magnetic withdrawal system can effectively capture magnetic particles even under accidental environments. Withdrawal of multifunctional magnetic particles or filtering of magnetic impurities can be effectively realized through the system.

• 한국환경과학회지
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• 제32권9호
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• pp.659-669
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• 2023

The purpose of this study is to predict the pressure drop due to the installation of venturi under diverse operating conditions such as dust concentration, pulse interval and pressure, and filtration velocity using algebraic-linear regression model and use it as an economic data and efficient operating condition for a pulse air jet bag filter. A pilot scale bag filter with a filter a filter size(Ø140 × 850ℓ, 12) was used, and the filters used in the experiment were the polyester filters most commonly used in real industrial sites. The SAS 9.4 program (SAS Institute, USA) was used to predict and to determine the effects of inlet concentration (C_i), pulse interval (P_i) and pressure (P_p), filtration velocity (V_f), presence or absence of venturi, etc. The results are shown below. The variation in pressure drop with or without venturi installation was 38.8 mmAq when venturi is installed and 47.6 mmAq when venturi is not installed, indicating a difference in pressure drop of 8.8 mmAq depending on venturi installation. It is estimated that the efficiency can be improved by about 18.5% if the venturi is installed.