• Environmental engineer
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• v.18 s.191
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• pp.62-64
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• 2002

• Environmental engineer
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• v.21 s.213
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• pp.82-87
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• 2004

• Environmental engineer
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• v.24 s.247
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• pp.14-19
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• 2007

• Environmental engineer
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• v.22 s.229
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• pp.41-48
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• 2005

• Environmental engineer
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• v.21 s.210
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• pp.68-71
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• 2004

[ $\circ$ ] 본 기술은 기존의 A2O공법과 Sludge Blanket Filtration(SBF)을 단위공법으로 조합한 공정으로서 각 생물반응조의 미생물 농도를 6,000mg/ 이상의 고농도로 운전하여 생물학적 유기물,질소 및 인 제거효율을 극대화하고자 하는 기술 $\circ$ 또한 활성슬러지 반응조로부터 유입된 슬러지를 SBF에서 미세기포를 이용하여 부상시킴으로써 수면에 농축 슬러지층을 형성시키고 이 부

• Journal of Navigation and Port Research
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• v.34 no.5
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• pp.375-381
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• 2010

This study was carried out for advanced treatment development on shipboard sewage. We employed SBR process using Bacillus sp. to remove Organic compounds, Nitrogen and Phosphorus simultaneously. Based on Res. MEPC.159(55) the system was qualified. From the results it was suggested that SBR system might be suitable process for shipboard sewage treatment in terms of pollutant removal efficiency, maintenance and special environmental conditions of ship. More than 90% of COD and BOD were removed. In addition, aover 50% of T-N and T-P were reduced.

• Journal of Korean Society of Water and Wastewater
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• v.34 no.6
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• pp.411-423
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• 2020

To remove phosphorus from the effluent of public wastewater treatment facilities, hundreds of enhanced phosphorus treatment processes have been introduced nationwide. However, these processes have a few problems including excessive maintenance cost and sludge production caused by inappropriate coagulant injection. Therefore, the optimal decision of coagulant dosage and automatic control of coagulant injection are essential. To overcome the drawbacks of conventional phosphorus removal processes, the integrated sedimentation and dissolved air flotation(SeDAF) process has been developed and a demonstration plant(capacity: 100 ㎥/d) has also been installed. In this study, various jar-tests(sedimentation and / or sedimentation·flotation) and multiple regression analyses have been performed. Particularly, we have highlighted the decision-making algorithms of optimal coagulant dosage to improve the applicability of the SeDAF process. As a result, the sedimentation jar-test could be a simple and reliable method for the decision of appropriate coagulant dosage in field condition of the SeDAF process. And, we have found that the SeDAF process can save 30 - 40% of coagulant dosage compared with conventional sedimentation processes to achieve total phosphorus (T-P) concentration below 0.2 mg/L of treated water, and it can also reduce same portion of sludge production.

• Journal of the Korean Society for Environmental Technology
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• v.19 no.6
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• pp.556-562
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• 2018

Due to the enforcement of effluent water regulation the advance sewage treatment system is needed to retrofit and remodelling. In this case the most important issue is the effluent concentrations of TP and there are a lot of system to reduce its concentration. But biological treatment processes have many restrictions to enhance the removal efficiency of TP. In this study the efficient ECO operating condition to improve and retrofit biological sewage wastewater treatment system is as follow; 1) The treatment efficiency of BOD, TN and TP at the current density of $15mA/cm^2$ was higher than the treatment efficiency at $5mA/cm^2$ in the electrodes arranged with Al-SUS(Stainless Steel) regardless of the reaction time, The TP concentration was 0.1 mg/L or less. Especially, when the reaction time was maintained at 10 min, the TP concentration was 0.06 mg/L or less irrespective of the current density. 2) The change of TP concentration is not influenced by the change of current density and rather the concentration of treated water changes according to the reaction time. In the case of electro coagulation reaction, a few seconds to several minutes are required. However, the reaction time of electro coagulation and oxidation was studied to be more than 10 minutes. 3) As a result, it has been studied that the economical current density of the electro coagulation oxidation process for TN and TP treatment of domestic wastewater is $15mA/cm^2$ or less and the reaction time is 10 minutes.

• Proceedings of the Korea Water Resources Association Conference
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• 2012.05a
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• pp.478-478
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• 2012

국내의 하수도 보급률은 90%에 달하고 있으며, 하수의 고도처리와 처리기술이 향상된 신기술개발 등으로 수질개선 효과가 크게 개선되어 있고, 전국 각지에 활발하게 하수처리장의 건설이 추진 중에 있지만, 다양한 오염원의 증가와 함께 환경기준은 점차적으로 강화되고 있어 기존 하수처리장은 강화되고 있는 환경기준을 만족시키기 어려운 실정으로 새로운 처리법의 도입이 절실히 요구되고 있는 실정이다. 시설이 노후화된 하수종말처리장의 경우에는 경제적인 부담감을 이유로 기존 공법 개선을 통한 수질기준을 만족하기 위하여 노력하고 있으며, 특히, 방류수 수질 중에서 총질소(T-N)와 총인(T-P)의 기준을 평상시와 겨울철(12월 1일부터 3월 31일까지)로 구분하여 적용하여 왔지만, 2012년부터는 이를 동일하게 적용함으로써 겨울철 생물학적 처리 공정에서의 효율저하로 인한 기준치 만족이 어려운 상황이다. 본 연구에서는 인천의 하수처리장을 대상으로 동절기 수온의 저하에 따른 생물학적 공정을 개선시키기 위하여 운전조건을 변경하여 수질개선 증대 방안을 도출하고자 하였으며, 생물학적 공정인 MLE공법으로 동절기 외부 온도의 영향을 받는 조건을 갖는 사업소를 대상으로 실내 실험장치를 구성하여 조건을 변화하면서 개선 효과를 검토하였다. 생물반응조의 공정위치 변화, 미생물농도 그리고 체류시간변화 등의 실험조건으로 하수 처리 효율을 분석하였으며, 운전 중 외부반송 유량, 내부반송 유량 등의 운전인자는 일정하게 유지하였고, 동절기 온도인 $10^{\circ}C$로 유지하여 실험을 진행하였다. 실험 결과 대상 하수처리장의 생물학적 공정의 개선방향은 공정 배열을 변화하였을 때, 현재의 공정 배열 조건인 무산소조 1개, 호기조 4개의 공정보다 호기조 1개, 무산소조 1개, 호기조 3개로 수정하는 경우 현재 공정보다 질소는 7%, 유기물은 9.2% 처리효율이 개선되는 것으로 분석되었다. 미생물 농도 변화를 주어 수질 개선 효과를 검토한 결과 하수처리장 설계농도인 3,500ppm의 경우보다 미생물 농도를 5,970ppm으로 증가시킨 경우 17.4% 처리효율의 개선효과를 보여 질소 제거를 위해 미생물의 농도를 증가시키는 것이 바람직한 것으로 판단하였다. 또한, 체류시간(HRT)을 변화한 경우에는 현재 체류시간(HRT)인 8시간 보다 10시간으로 증가시켰을 경우 유기물은 3.2%, 질소는 2.6%의 처리효율이 개선되는 것으로 분석되었다.

• Journal of Korean Society of Environmental Engineers
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• v.36 no.2
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• pp.96-102
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• 2014

To meet the reinforced discharge standards, effect of coagulant PAC (Poly aluminium chloride, 10.4% as $Al_2O_3$) on phosphorous removal in advanced wastewater treatment process (a modified $A^2$/O). 15 mg/L of PAC determined by jar-test was added to influent of settling basin in a modified $A^2$/O consists of anaerobic, anoxic, and oxic chamber which contains Bio-clod and porous polyurethane media. Performance of PAC was tested by supernatant after settling. The removal efficiencies of BOD, COD, TP (total phosphorus) and SP (soluble phosphorus) on biological process with PAC were 96.1%, 88.8%, 97.0% and 98.6%, compared with those on biological process without PAC were 95.4%, 72.4%, 71.6% and 59.5% respectively. 18.4% of TP and 39.1% of SP removal efficiency was increased, although increase of BOD and COD removal rate was not significant. Only PAC addition to influent of settling basin in $A^2O$ process can help total phosphorus removal to 0.13 mg/L with following discharge standard.