• 상하수도학회지
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• 제34권1호
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• pp.35-43
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• 2020

Turbidity has various effects on the water quality and ecosystem of a river. High turbidity during floods increases the operation cost of a drinking water supply system. Thus, the management of turbidity is essential for providing safe water to the public. There have been various efforts to estimate turbidity in river systems for proper management and early warning of high turbidity in the water supply process. Advanced data analysis technology using machine learning has been increasingly used in water quality management processes. Artificial neural networks(ANNs) is one of the first algorithms applied, where the overfitting of a model to observed data and vanishing gradient in the backpropagation process limit the wide application of ANNs in practice. In recent years, deep learning, which overcomes the limitations of ANNs, has been applied in water quality management. LSTM(Long-Short Term Memory) is one of novel deep learning algorithms that is widely used in the analysis of time series data. In this study, LSTM is used for the prediction of high turbidity(>30 NTU) in a river from the relationship of turbidity to discharge, which enables early warning of high turbidity in a drinking water supply system. The model showed 0.98, 0.99, 0.98 and 0.99 for precision, recall, F1-score and accuracy respectively, for the prediction of high turbidity in a river with 2 hour frequency data. The sensitivity of the model to the observation intervals of data is also compared with time periods of 2 hour, 8 hour, 1 day and 2 days. The model shows higher precision with shorter observation intervals, which underscores the importance of collecting high frequency data for better management of water resources in the future.

• 한국유체기계학회 논문집
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• 제10권6호
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• pp.50-56
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• 2007

In this study, we have performed some experimental works on the effects of variation of low, middle and high turbidity for understanding of optical characteristics which is very important factor for the turbidity measurement. The various output frequencies were obtained by the experimental apparatus which consist of detectors, a light source, a frequency counter and so on. From the result of analysis of these frequencies, Firstly, The difference of signal value for each degrees of low turbidity was the smallest of three scopes around the Nephelometric position. Second, the characteristics of each degrees of middle turbidity was proved that signal values of all degrees were larger those of low turbidity but the difference of each signal value of the forward direction was smaller than that of the backward direction. Third, the characteristics of each degrees of high turbidity was proved that though similar to the characteristics of middle turbidity, each signal value of all degrees was larger and the difference of each signal value of all degrees was smaller than those of low and middle turbidity

• 대한환경공학회지
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• 제34권9호
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• pp.644-650
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• 2012

본 연구에서는 고탁도 원수의 효율적인 처리를 위해 수평류식 핀 부착 경사판(HFIP)을 설치하여 그에 따른 적용성을 평가하는데 목적을 두었다. 실험결과는 저탁도 원수 유입의 경우 HFIP 적용 후에 0.34 NTU의 방류수질과 90.45%의 제거효율을 나타냈다. 고탁도 원수의 경우에는 0.75 NTU의 방류수질과 97.27%의 제거효율을 나타냈다. 방류수질 안정성 측면에서는 HFIP 적용 후 0.12 NTU(저탁도 원수), 0.75 NTU(고탁도 원수)의 표준편차를 보였으며, 설치 전과 비교하여 방류수질 변동 폭이 상당히 개선된 것으로 나타났다. 이러한 결과는 HFIP 설치로 인해 수류 속도 분포의 안정화와 침강효율이 증가하였기 때문인 것으로 판단된다.

• 상하수도학회지
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• 제24권5호
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• pp.581-593
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• 2010

The objectives of this study were to investigate the effects of raw water pH and basicity of coagulants on turbidity removal with several raw waters having different level of turbidity, alkalinity and pH. Raw waters were sampled from M, S and B water treatment plants(WTP) located at Miryang, Nakdong, Han river, respectively. Six coagulants which have different levels of basicity and aluminum contents were used for this evaluation. High basicity of the coagulant helped to properly control coagulation processes for treating turbid and low alkali raw water. It was difficult for operators to determine optimum coagulant dose for high basicity coagulants, since residual turbidity tended to decrease continuously as coagulant dose increased. Turbidity removal efficiencies with high basicity coagulants(E and F) were higher than the other coagulants at ambient pH for the M WTP. Turbidity removal efficiencies, however, at adjusted pH 7.0 showed similar among six coagulants. Residual turbidity kept low at excess dosages with high basicity coagulants. Optimum coagulant dosages at adjusted pH 7.0 showed higher than those at ambient pH in M WTP. On the contrary in B WTP, optimum coagulant dosage at ambient pH were higher than that at adjusted pH 7.0.

• 해양환경안전학회지
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• 제24권7호
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• pp.916-922
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• 2018

는 열교 환기를 세척할 때 최근 신재생에너지의무화제도(RPS: Renewable Portfolio Standard)대상 신재생에너지 항목에 발전소 온배수가 신재생에너지공급인증서(REC:Renewable Energy Certificate)의 수열에너지(가중치 1.5)로 추가되어 온배수 열원에 대한 가치가 높아졌다. 본 연구에서는 고탁도지역 온배수의 직접적인 활용을 위한 방안으로 히트펌프시스템 내 탁도저감장치를 도입하여 열교환기에 가해지는 오염물질의 저감 효과를 확인해보기 위해 한 달 동안 실증테스트를 실시하였다. 실험결과 탁도 저감효과가 80 % 이상으로 고탁도 지역의 온배수 활용을 위한 방안으로 탁도저감장치의 적용가능성을 확인 할 수 있었다. 또한 탁도저감시스템에 따른 열교환기의 오염도 저감 효과를 검증하기 위해 30일간 운전한 열교환기를 해체하여 분석해본 결과 탁도저감시스템을 거친 열교환기보다 그렇지 않은 열교환기의 오염정도가 높은 것을 확인하였다. 열교환기에 유입된 오염물질(스케일)을 분석해본 결과 주로 $SiO_2$, $Na(Si_3Al)O_8$, $CaCO_3$, NaCl 성분의 광물이 검출되었는데 이는 높은 탁도로 인해 해양퇴적토가 열교환기에 유입된 것으로 분석되었다. 그 외에도 소량이지만 $TiO_2$, MnO, $Cr_2O_3$가 검출되었다. 이는 열교환기를 세척할 때 열교환기 재료로부터 기인한 중금속이 소량 용출된 것으로 판단된다.

• 대한원격탐사학회지
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• 제38권6_1호
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• pp.1285-1300
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• 2022

탁도는 부유물질에 의한 빛의 산란 또는 흡수로 인한 수체의 흐림을 나타내는 수치로 수질 관리 분야에서 중요 지표로 활용되고 있다. 탁도는 소규모의 하천에서 변동성이 심할 수 있으며, 이는 국가하천의 수질에 직접적으로 영향을 준다. 따라서 고해상도의 탁도 공간정보 산출은 매우 중요하다. 이 연구에서는 Korea Multi-Purpose Satellite-3 및 -3A (KOMPSAT-3/3A) 영상으로부터 한강 수계 하천의 고해상도 탁도 매핑을 위한 eXtreme Gradient Boosting (XGBoost) 알고리즘 기반의 탁도 산출 모델을 개발하였다. 이를 위해 총 24장의 KOMPSAT-3/3A 영상과 150장의 Landsat-8 영상으로부터 계산된 대기 상단(Top Of Atmosphere, TOA) 반사율을 활용하였으며, Landsat-8 TOA 반사율은 KOMPSAT-3/3A의 관측 파장 대역에 적합하도록 교차검보정을 수행하였다. 국가수질자동관측망에서 측정된 탁도를 탁도 산출 모델의 참조자료로 사용하였고, 입력 변수로는 탁도가 실측된 위치에서의 TOA 분광반사율과 탁도 분석에 널리 이용되어 온 분광지수인 정규식생지수, 정규수분지수, 정규탁도지수, 그리고 Moderate Resolution Imaging Spectroradiometer (MODIS)의 대기 산출물(에어로졸 광학 두께, 수증기량, 오존)을 사용하였다. 또한 고탁도와 저탁도에 대한 KOMPSAT-3/3A TOA 분광반사율을 분석하여 탁도를 설명할 수 있는 새로운 정규탁도지수(new normalized difference turbidity index, nNDTI)를 제안하였고, 이를 탁도 산출 모델에 입력 변수로 추가하였다. XGBoost 기반 탁도 산출 모델은 현장관측 탁도와 비교하여 2.70 NTU의 평균 제곱근 오차(root mean square error, RMSE) 및 14.70%의 정규화된 RMSE(normalized RMSE)를 가지는 탁도를 예측하여 우수한 성능을 보였으며, 이 연구에서 새롭게 제안한 nNDTI가 탁도 산출에 있어 가장 중요한 변수로 사용되었다. 개발된 탁도 산출 모델을 KOMPSAT-3/3A 영상에 적용하여 하천 탁도를 고해상도로 매핑하였으며, 탁도의 시공간적 변동에 대한 분석이 가능하였다. 이 연구를 통하여 고해상도의 정확한 탁도 공간정보 산출에 KOMPSAT-3/3A 영상이 매우 유용함을 확인할 수 있었다.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2004년도 총회 및 춘계학술발표회
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• pp.451-454
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• 2004

The study aims to assess the quality of bank filtrate in relation to streamflow and physico-chemical properties of the stream. Turbidity, pH, temperature and dissolved oxygen (DO) of Nakdong River and riverbank filtrate were statistically analyzed. The physico-chemical properties of riverbank filtrate were measured from irregularly different seven pumping wells every day. Autocorrelation analyses were conducted to the qualities of stream water and bank filtrated water. Temperature, pH and DO of streamflow shows strong linearity and long memory effect, indicating the effect of seasonal air temperature and rainy season. Temperature of riverbank filtrate shows weak linearity and weak memory, indicating differently from the trend of stream temperature. Turbidity of steramflow shows strong linearity and long memory effect, while turbidity of riverbank filtrate indicates weak linearity and weak memory. Cross-correlation analysis shows low relation between turbidity, pH, temperature and DO of riverbank filtrate and those of streamflow. Turbidity of streamflow was largely affected by the streamflow rate, showing a similar trend with autocorrelation function of streamflow rate. The turbidity of riverbank filtrate has a lag time of 25 hours. This indicates that turbidity of streamflow in a dry season has very low effect on the turbidity of riverbank filtrate, and a high turbidity of the stream in a rainy season has a fairly low effect on the turbidity of riverbank filtrate.

• 상하수도학회지
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• 제20권1호
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• pp.71-78
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• 2006

The removal of protozoa in the coagulation process was evaluated under the different pH and turbidity using the jar test after the addition of polyaluminium chloride (PAC) as a coagulant. Two well-known protozoa of Cryptosporidium parvum and Giardia lamblia were tested at the same time with turbidity, the critical water quality parameter of the water treatment process. Both protozoa were removed about 1log (and up to 2log) at the optimum injection of PAC. The source water turbidity and pH affected the removal of protozoa and turbidity. At neutral and alkaline pH, 1.3-1.7log removal of protozoa for low turbid water with 5NTU, and 1.6-2.3log removal for high turbid water with 30NTU were achieved. However, at acidic pH, maximum 0.8-1.0log and 1.1-1.2log were removed for low and high turbid water, respectively, at the optimum PAC injection of 15mg/L. The relation of protozoa and turbidity removals were expressed as the 1st order equation (significantly positive relation) in the most of the tested conditions. In addition, the relation of protozoan removals with residual turbidity were also expressed the 1st order equation (significantly negative relation), although the significance of the equations were reduced at acidic pH. Therefore, residual turbidity could be a good index of efficient protozoan removal in the coagulation process, probably except at the low pH condition.

• 상하수도학회지
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• 제21권3호
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• pp.359-366
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• 2007

Slow sand filtrations have been widely used for water treatment in small communities, however their capacity is often limited by high turbidity in the raw water. For this reason, several pre-treatment facilities were required for a slow sand filter. Turbidity removal from the highly turbid raw water was investigated in roughing filters as a pre-treatment process. The roughing filters followed by rapid mixing tank were operated in the form of a contact filtration. In several jar tests, the predetermined optimum aluminium sulfate (alum) doses for turbid water of 30 and 120NTU were 30 and 50mg/L, respectively. At the optimum alum dose, physically optimum parameters including G value of $220sec^{-1}$ and rapid mixing time of 3 minutes were applied to the contact filtration system. Without addition of alum, the filtrate turbidity from the roughing filters, packed respectively with different media such as sand, porous diatomite ball and gravel, was in the range of 5~30NTU at filtration velocities of 30 and 50m/day. However, the application of a contact filtration to roughing filters showed stably lower filtrate turbidity below 1.0NTU at filtration velocity of 30 m/day. Although the filtration velocity increased to 50m/day, filtrate turbidity was still below 1.0NTU in both single and double layer roughing filters. At influent turbidity of 120NTU, the filtrate turbidity was over 5 NTU in the triple layer roughing filter, which shortened the filter run time. The flocs larger than $10{\mu}m$, formed in the rapid mixing tank, were almost captured through the roughing filter bed, while the almost flocs smaller than $10{\mu}m$ remained in filtrate.

• 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.