• Title/Summary/Keyword: TN system

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Estimation of Water Pollution Load Based on Watershed Unit in Bocheong Seream (보청천에 대한 유역단위의 오염부하량 산정)

  • Shin, Geun-Su;Kim, Hung-Soo;Kim, Gun-Hyung
    • Proceedings of the Korea Water Resources Association Conference
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    • 2007.05a
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    • pp.961-965
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    • 2007
  • 현재 오염총량관리제를 시 군 단위의 기초자치 단체별로 시행하고 있는데 실제로 오염물질의 전달은 행정구역단위가 아닌 유역내에서 이루어지진다. 따라서 본 연구에서는 기초자치 단체별이 아닌 유역단위로 오염부하량과 삭감량을 산정함으로써 유역 단위의 오염총량관리제 계획 수립을 위한 토대를 제공하고자 한다. 본 연구에서는 보청천 유역을 대상으로 유역의 오염부하량을 산정하고자 하였다. 이를 위하여 지리정보시스템(GIS)인 WMS(Watershed Management System)와 ArcView를 이용하여 유역의 지형인자들을 추출하고, 각 소하천의 토지이용도와 생활계, 축산계, 양식계, 토지계를 바탕으로 원단위를 적용하여 발생부하량을 산정하였다. 그리고 각 소하천별 발생부하량 산정 결과를 토대로 각 수질관측점을 기준으로 하여 배출부하량을 산정하였으며, 배출부하량의 산정결과를 이용하여 유달부하량을 산정하였다. 이를 위해서 필요한 수질 데이터는 QUAL2E 모형을 이용하여 모의 하였으며, 수리 및 수질 매개변수를 추정하고 모형의 보정 및 검증을 수행하였다. 그 결과 유달부하량은 BOD는 2013.16kg/일, TN은 1091.34kg/일, TP은 235.16kg/일이 도출되었다. 따라서 장래에 수질이 악화될 경우를 고려하여 수질 항목별 오염량이 2배, 3배로 증가한다고 가정하였다. 오염량이 2배 증가하였을 경우, 오염부하량을 산정한 결과 보청천3 지점에서 BOD는 184.68kg/일이 삭감되어야 하고, 오염량이 3배 증가하였을 경우 BOD는 1775.69kg/일이 삭감되어야 한다는 결과를 도출할 수 있었다. 본 연구와 같이 유역단위로 오염부하량을 산정할 경우, 오염원을 줄이는데 효율적일 것으로 생각되며, 향후 오염총량관리제를 위해 유역단위의 오염부하량 산정을 고려하면 좋을 것으로 사료된다.는 지배적인 요인으로 남게 될 것이다. 본 연구에서는 현재 진행중인 승기천 오염하천 정화사업이 종료되는 시점을 기준으로 남동유수지에 대해 승기천과 연계한 유수지의 환경개선 방법을 제안하였다. 준설을 통해 유수지의 근본적인 오염원을 제거하고 남동유수지 유입부에 인공습지와 수처리설비를 설치하여 유수지의 수질을 개선하고 개선된 수질이 3급수로 유지하도록 하였으며, 설치된 인공습지에는 철새도래지를 조성하여 유수지 유입수인 철새가 날아드는 하천인 승기천의 테마와 연계하도록 하였다. 인공습지 주변으로 식생호안을 설치하고 유수지 주변에는 산책로를 설치하여 지역주민들의 친환경 수변공간으로 활용하도록 하였다. 1유수지와 연결된 2유수지는 BTL사업을 통해 주변공단으로부터의 오폐수를 원천적으로 차단하도록 하였으며 2유수지를 매립하여 지하는 강우시 유출수 저류가 가능한 화물차주차장으로 활용하고 지상은 녹지공간으로 조성하여 공단근로자 및 지역주민을 위한 휴식공간으로 활용될 수 있도록 제안하였다. 본 연구는 남동유수지 환경 개선 사업 실행을 위한 정책 연구로 연구결과를 인천시가 적극 수용하기로 결정함에 따라 인천시의 환경 현안 문제인 남동유수지의 수질개선을 통해 시민의 휴식 및 여가선용 공간으로 활용하기 위한 사업의 기초자료로 활용되며 이미 설계검토가 시작되었다. 본 연구결과는 유수지 및 저수지의 환경개선 사업의 선두적인 성공사례로 국내 타 지역의 유사한 사업에 있어 벤치마킹을 할 수 있는 훌륭한 사례가 될 것이다.요 생산이 증가하자 군신의 변별(辨別)과 사치를 이유로 강력하게 규제하여 백자의 확대와 발전에 걸림돌이 되었다. 둘째, 동기(銅器)의 대체품으로 자기를 만들어 충당해야할 강제성 당위성 상실로 인한 자기수요 감소를 초래하였을 것으로 사료된다. 셋째, 경기도 광주에서 백자관요가 운영되었으므로 지방인 상주

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Isolation of Serratia marcescens CK-3 against phytopathogenic fungi and its enzymatic properties (식물(植物) 병원류(病源惟) 사상균(絲狀菌)에 길항력(拮抗力)을 갖는 Serratia marcescens CK-3의 분리(分離) 및 효소적(酵素的) 성질(性質))

  • Kim, Yeong-Yil;Rhee, Young-Hwan;Kim, Kwang-Sik;Park, Hwa-Sung;Chun, Woo-Bock;Lee, Jae-Wha;Kim, Jong-Hyun
    • Applied Biological Chemistry
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    • v.34 no.1
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    • pp.54-60
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    • 1991
  • Serratia marcescens CK-3, decomposing chitin which is a mar component of cell wall in phyitopathogenic fungi, was isolated from the continuous cropping rhizosphere of pepper and cucumber and its enzymatic property was examined. S. marcescens CK-3 was found tn have an tagonistic effects against, Fusarium axysporum and Rhizoctonia solani and to have complex enzyme system such as chitinase, laminarinase, and proteinase. The preferable composition of the medium for production of chitinase was fond and was as follows : colloidal chitin 1.5%, tryptone 0.5%, glucose 1.0%, peptone 0.2%, $MgSO_4{\cdot}7H_2O\;0.1%,\;K_2HPO_4\;0.1%,\;and\;NaCl\;0.1%$(w/v), pH 6.8. The maximum enzyme production was observed after culture of 72 hours at $30^{\circ}C$ using a medium containing the above chemical composition. The optimal pH and temperature for in vitro activity of chitinase from S. marcescens CK-3 were pH 7.5 and $50^{\circ}C$, respectively. The enzyme activity in-creased by metal ions such as$Ag^+$ and $Mn^{++}$.

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Cultural and Physiological Conditions for T-2 Toxin Production by Fusarium sp. (Fusarium 균주의 배양 조건 및 생리적 조건에 따른 T-2 toxin의 생성 조건)

  • 홍성희;양규환
    • Korean Journal of Microbiology
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    • v.36 no.2
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    • pp.91-96
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    • 2000
  • The cultural and physiological conditions for the T-2 toxin [4,15-diacetoxy-8-(3-mety1butyloxy)-12,13- epoxy-trichothec-9-en-3-01, $C_{24}H_{30}O_9$] production by Fusarium spp. were studied. Thin layer chromatography (TLC) assay and the microbiological assay uslng Rhodotomla rubra were used to quantitate tbe T- 2 toxin. Among the four strains of Fusarium spp., F tn'cinctum NRRL 3299 was best for T-2 toxin production. In solid culture, white com grit medium was best for T-2 toxm production. Temperature played a critical role in the production of T-2 toxin. T-2 toxin production was favored by long duration of low-temperature incubation. The growth and toxin production were relatively high on galactose, fructose, glucose, and sucrose media, when each was used as a sole carbon source, and relatively low on sorbitol, glycerol, and lactose media. For nitrogen sources, $NH_4^(+) and NO_3^{-}were used well as a sole nitrogen source, but $NO_2^-$ was not used. Initial pH and speed of shaker also affected the production of T-2 toxin. From temperature shifting experiment, it is clear that T-2 toxin metabolic pathway is regulated by temperature-dependent enzyme depression or enzyme induction system.

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A Study on Phosphorus and Nitrogen Removal with Unit Operation in the Ferrous Nutrient Removal Process (철전기분해장치(FNR)에서 단위공정에 따른 질소와 인의 제거)

  • Kim, Soo Bok;Kim, Young-Gyu
    • Journal of Environmental Health Sciences
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    • v.39 no.1
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    • pp.83-89
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    • 2013
  • Objectives: The purpose of this experiment was to illuminate the relationship between the phosphorus removal rate of unit operation and the phosphorus removal rate of phosphorus volume loading in the Ferrous Nutrient Removal process, which consists of an anoxic basin, oxic basin, and iron precipitation apparatus. Methods: This study was conducted in order to improve the effect of nitrogen and phosphorus removal in domestic wastewater using the FNR (Ferrous Nutrient Removal) process which features an iron precipitation reactor in anoxic and oxic basins. The average concentration of TN and TP was analyzed in a pilot plant ($50m^3/day$). Results: The removal rate of T-N and T-P were 66.5% and 92.8%, respectively. The $NH_3-N$ concentration of effluent was 2.62 mg/l with nitrification in the oxic basin even though the influent was 17.7 mg/l. The $NO_3$-N concentration of effluent was 5.83 mg/l through nitrification in oxic basin even though the influent and anoxic basin were 0.82 mg/l and 1.00 mg/l, respectively. The specific nitrification of the oxic basin ($mg.NH_3$-Nremoved/gMLVSSd) was 16.5 and specific de-nitrification ($mg.NO_3$-Nremoved/gMLVSSd) was 90.8. The T-P removal rate was higher in the oxic basin as T-P of influent was consumed at a rate of 56.3% in the anoxic basin but at 90.3% in the oxic basin. The TP removal rate (mg.TP/g.MLSS.d) ranged from 2.01 to 4.67 (3.06) as the volume loading of T-P was increased, Conclusions: The test results showed that the electrolysis of iron is an effective method of phosphorus removal. Regardless of the temperature and organic matter content of the influent, the quality of phosphorus in the treated water was both relatively stable and high due to the high removal efficiency. Nitrogen removal efficiency was 66.5% because organic matter from the influent serves as a carbon source in the anoxic basin.

Water Quality Modeling of the Ara Canal, Using EFDC-WASP Model in Series (3차원 EFDC-WASP 연계모델을 이용한 경인아라뱃길 수질 예측)

  • Yin, Zhenhao;Seo, Dongil
    • Journal of Korean Society of Environmental Engineers
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    • v.35 no.2
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    • pp.101-108
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    • 2013
  • Ara Canal is the first artificial canal in Korea that connects the Han River and the Yellow Sea. Due to mixture of waters with different salinity and water quality, complicated hydrodynamic and water quality distributions are expected to occur inside the canal. An integrated hydrodynamic and water quality modeling system was developed using the 3 dimensional hydrodynamic model, EFDC (Environmental Fluid Dynamics Code) and the water quality model WASP (Water Quality Analysis and Simulation Program). According to the modeling results, BOD, TN, TP and Chl-a concentrations inside the canal were lower at the West Gate side than the Han River side since influent concentrations of the West Gate side are significantly lower. Chemical stratification due to salinity difference were more evident at the West Gate side as vertical salinity difference were more pronounced in this area. On the other hand, Chl-a concentrations showed more pronounced vertical distribution at the Han River side as Chl-a concentrations were higher in this area. It was notable that Dissolved Oxygen concentrations can be lower than 2 mg/L occasionally in the middle part of the canal. While major factor affecting DO concentrations in the canal are inflows via both gates, the other important factor was found to be BOD decay in the canal due to extended hydraulic residence time. This study can be used to predict hydrodynamic conditions and water quality in the canal during the year and thus can be helpful in the development of gate operation method of the canal.

Network-adaptive H.264 Video Streaming over IEEE 802.11e (IEEE 802.11e에서 네트워크 적응적인 H.264 비디오 스트리밍)

  • Lee, Sun-Hun;Chung, Kwang-Sue
    • Journal of Broadcast Engineering
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    • v.13 no.1
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    • pp.6-16
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    • 2008
  • An instable wireless channel condition causes more packet losses and retransmissions due to interference, fading, station mobility, and so on. Therefore video streaming service over a wireless networks is a challenging task because of the changes in the wireless channel conditions and time-constraints characteristics of the video streaming services. To provide efficient video streaming over a wireless networks, QoS-enhanced MAC protocol, IEEE 802.11e, is standardized recently. Tn this paper, we propose a new network-adaptive H.264 video streaming mechanism in the IEEE 802.11e wireless networks. To improve the quality of video streaming services, video stream has to adapt to the changes in the wireless channel conditions. The wireless channel conditions are estimated by the packet loss probability and informed to the application layer by the cross-layering. According to the wireless channel information, the video streaming application filters out the low-priority data. This adaptation mechanism efficiently uses system resources because it drops the low-priority data in advance. Therefore, our cross-layer design can provide improved video streaming services to the end-user. Through the implementation and performance evaluation, we prove that the proposed mechanism improves the QoS of the video streaming by providing the smoothed playback.

Ecotoxicity Assessment for Livestock Waste Water Treated by a Low Impact Development(LID) Pilot Plant (파일럿 규모의 LID공법을 적용한 축산폐수 처리수에 대한 생태독성 평가)

  • Park, Da Kyung;Chang, Soon-Woong;Choi, Hanna
    • Korean Journal of Environmental Biology
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    • v.35 no.4
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    • pp.662-669
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    • 2017
  • This study evaluated the ecotoxicological properties of livestock waste water treated by a LID (Low Impact Development) system, using a mixture of bio-reeds and bio-ceramics as suitable bed media for a subsequent treatment process of a livestock wastewater treatment plant. The relationship between the pollutant reduction rate and the ecotoxicity was analyzed with the effluents from the inlet pilot plant, with vegetated swale and wetlands and the batch type of an infiltration trench. Each pilot plant consisted of a bio process using bio-reeds and bio-ceramics as bed media, as well as a general process using general reeds and a bed as a control group. The results indicated that, after applying the HRT 24 hour LID method, the ecotoxicity was considerably lowered and the batch type pilot plant was shown to be effective for toxicity reduction. The LID method is expected to be effective for water quality management, considering ecotoxicity by not only as a nonpoint source pollution abatement facility but also, as a subsequent treatment process linked with a livestock manure purification facility. It is necessary to take the LID technic optimization study further to apply it as a subsequent process for livestock wastewater treatment.

The test-bed construction and water purification assessment of the eco-convergence type aerated string contacted oxidation system (생태융합형 접촉산화수로 Test-Bed 구축 및 정화효율 평가)

  • Choi, Sunhwa;Lee, Seung-Heon;Jang, Kyusang;Kim, Heungseop
    • Proceedings of the Korea Water Resources Association Conference
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    • 2016.05a
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    • pp.592-592
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    • 2016
  • 국내에는 17,500여개의 농업용 저수지가 전국적으로 분포하고 있다. 국내 농업용 저수지는 대부분이 소규모이며, 연중 수량 변동이 심하고, 유역배율이 작아 태생적으로 수질오염에 취약한 구조로 되어 있다. 특히 농업용 저수지는 도시 근교나 농촌지역에 많이 위치하고 있어 유역 내 축산 농가나 미처리 생활하수에서 유래된 유기물 및 영양염류 유입에 의한 수질오염도가 높다. 저수지에 고농도로 유입되는 유기물, TN, TP를 처리하기 위하여 농어촌연구원과 수생태복원(주)에서는 공동으로 친환경 수처리시설인 생태융합형 접촉산화시스템을 개발하였다. 생태융합 접촉산화수로는 상부 식생과 수로 내의 섬유상 끈상 미생물 접촉재를 이용하여 오염수가 수로를 흐르면서 침전, 여과, 흡착, 산화, 흡수 등 물리학적, 화학적, 생물학적 원리를 이용하여 고농도의 유기물과 질소, 인을 제거하는 물리적, 생물학적 공정을 융복합 기술이다. 본 연구에서는 경기도 시흥시에 소재하고 있는 M 저수지에 현장 Test-bed를 구축하여 수질정화효율을 평가하였다. M 저수지는 유효저수지량이 약 23만톤에 해당하는 소규모 저수지로, 1941년도 준공된 아주 노후화된 저수지로 평균 수심이 2m 이하이고 연중 수질오염도가 높은 저수지이다. 매화저수지 수변에 설치된 생태융합형 접촉산화수로의 전체규모는 길이 8.6m, 폭 2m, 수심 2m에 해당하며, 끈상 미생물 메디아조 3개($2{\times}2{\times}6m^3$), 침전조 1개($2{\times}2{\times}2m^3$)로 구성되어 있다. 기타 부대 장치로는 끈상 메디아조에 산소공급을 위한 Air-mist(마이크로 버블 발생장치), 자동운전계기판, 유입펌프 등이 있다. 생태융합형 접촉산화수로의 처리 공정은 유입수${\rightarrow}$에어미스트${\rightarrow}$고속복합응집장치${\rightarrow}$융복합 산화조(3조)${\rightarrow}$침전조${\rightarrow}$방류로 구성되어 있다. 테스트 베드는 2015년 8월 말경에 구축 완료하였으며, 끈상 미생물 메디아조의 수질정화효율을 평가하기 위하여 9월부터 11월까지 총 7회 걸쳐 유입수와 유출수를 각각 조사하였다. 현장 측정항목인 수온, pH, EC, DO 등은 유입수 및 유출수간 큰 차이가 없었고, COD, SS, Chl-a, TP 등은 수처리시스템 초기 가동시에는 메디아에 미생물 부착율 저조로 유입수 및 유출수 수질농도에 큰 차이가 없었으나, 운영시간의 경과와 함께 메디아의 미생물 충진율이 높아짐에 따라 처리효율이 최대 SS 69.6%, Chl-a 89.3%, TP 89%까지 도달하는 것으로 나타났다. 생태융합 접촉산화수로는 부지 집약적인 컴팩트한 수처리 시설로서 현재 널리 이용되고 있는 인공습지를 대체할 수 있는 경제적인 시설로 판단된다.

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Methane Fermentation of Facultative Pond in Pond System for Ecological Treatment and Recycling of Livestock Wastewater (축산폐수 처리 및 재활용을 위한 조건성연못의 메탄발효)

  • Yang, Hong-Mo
    • Korean Journal of Environmental Agriculture
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    • v.19 no.2
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    • pp.171-176
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    • 2000
  • A wastewater treatment pond system was developed for treatment and recycling of dairy cattle excreta of $5\;m^1$ per day. The wastes were diluted by the water used for clearing stalls. The system was composed of three ponds in series. A submerged gas collector for the recovery of methane was installed at the bottom of secondary pond with water depth of 2.4m. This paper deals mainly with performance of methane fermentation of secondary pond which is faclutative one. The average $BOD_5$, SS, TN, and TP concentrations of influent into secondary pond were 49.1, 53.4, 48.6, and 5.3 mg/l, and those of effluent from it were 27.9, 45.7, 30.8, 3.2 mg/l respectively. Methane fermentation of 2.4-meter-deep secondary pond bottom was well established at $16^{\circ}C$ and gas garnered from the collector at that temperature was 80% methane. Literature on methane fermentation of wastewater treatment ponds shows that methane bacteria grow well around $24^{\circ}C$, the rate of daily accumulation and decomposition of sludge is approximately equal at $19^{\circ}C$, and activities of methanogenic bacteria are ceased below $14^{\circ}C$. The good methane fermentation of the pond bottom around $16^{\circ}C$, about $3^{\circ}C$ lower than $19^{\circ}C$, results from temperature stability, anaerobic condition, and neutral pH of the bottom sludge layer. It is recommended that the depth of pond water could be 2.4m. Gas from the collector during active methane fermentation was almost 83% methane, less than 17% nitrogen. Carbon dioxide was less than 1% of the gas, which indicates that carbon dioxide produced in bottom sludges was dissolved in the overlaying water column. Thus a purified methane can be collected and used as energy source. Sludge accumulation on the pond bottom for a nine month period was 1.3cm and annual sludge depth can be estimated to be 1.7cm. Design of additional pond depth of 0.3m can lead to 15 - 20 year sludge removal.

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The Treatment of Night Soil using Bacillus sp. (Bacillus sp.를 이용한 분뇨처리)

  • 염혜경;이은숙;이병헌;이민규;정일호;김중균
    • Journal of Life Science
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    • v.12 no.6
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    • pp.700-707
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    • 2002
  • To study the characteristics of organic and nutrient removal by Bacillus species at high COD concentration of influent, three lab-scale batch reactors(R1, R2, R3), each of which has different substrate composition, were operated. More than 95% of $NH_4^+$-N and $COD_{cr}$, concentrations were removed under an aerobic condition, and their removal efficiencies were found to be 22.6 and 90.5%(R1), 23.9 and 65.8%(R2), 30.2 and 86.4%(R3), respectively. The removal efficiency of $NH_4^+$-N was high when an enough amount of $NO_3^{-}$-N was supplied, and that of $COD_{cr}$. was low when a high concentration of initial $NO_2^{-}$-N was added. The amount of carbon utilized in denitrification was a little. In all reactors,$NO_3^{-}$-N was removed under an anoxic condition, but in the R3 reactor, 10% of $NO_3^{-}$-N could be removed even undo, an aerobic condition. The removal efficiencies of TN and TP were 41.8 and 49.5%(R1), 40.1 and 35.8%(R2), 47.0 and 57.6%(R3), respectively. Alkalinities destructed under an aerobic condition for each reactor were 4.96, 5.41 and 3.93 mg/L (as $CaCO_3$) per each gram of $NH_4^+$-N oxidized, respectively, while 3.06, 3.17 and 2.60 mg/L (as $CaCO_3$) of alkalinities were produced for each gram of ,$NO_3^{-}$-N reduced to $N_2$. The SOUR were found to be 38.5, 52.7 and 42.0 mg $O_2$/g MLSS/hr, which indicated that Bacillus sp. had a higher cell activity than activated sludge. The OLR and sludge production were estimated to be 0.69 and 0.28(Rl), 0.77 and 0.20(R2), 0.61 kg COD/$m^3$/day and 0.25 kg MLSS/kg COD(R3), respectively. From the N-balance, the highest percentage(40.9%) of nitrogen lost to $N_2$ was obtained in the R3 reactor. From all the results, the possibility of aerobic denitrification Bacillus sp. has been shown and the B3 process seemed to have two advantages: a little amount of carbon was required in denitrification and not much amount of alkalinity was destructed under an aerobic condition.