• 한국농공학회지
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• 제37권E호
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• pp.63-71
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• 1995

Three types of land use were investigated to describe the effect of land use on both surface and ground water quality. Typical land uses of a grazing pasture, Sudan grass field and paddy in Kangwon province were selected and flumes and monitoring wells were installed. Land managements were carefully monitored, water samples were collected periodically and analyzed with respect to nitrate, TP and TKN at a laboratory of Kangwon Provincial Institute of Health and Environment from August, 1993 to May, 1994. Runoff from the pasture was formed mostly with seeping subsurface flow in the lower areas of the pasture. A few overland flows were observed during heavy storms, and when it occurred, runoff increased sharply. For the Sudan grass field, runoff was formed with overland flow. Nitrate concentration in runoff from both land uses seemed not affected by runoff and ranged from 0.241 to 4.137mg'/1. TP and TKN concentrations from the pasture were affected by overland flow. When overland flow occurred, TP and TKN concentrations abruptly increased to 5.726 and 12.841mg/1, respectively, from less than 1.0mg/l. However, these concentrations from the Sudan grass field were quite stable ranging from 0.191 to 0.674mg/l for TP and 0A70 and 1.650mg/l for TKN. Nitrate concentration was significantly affected by land use(Sudan grass field) and the concentration increase reached about 2mg/l per lOOm ground water flow. Nitrate concentration from a well located in the middle of rice fields also was significantly higher than that measured from a well located relatively undisturbed mountain toe area. TP and TKN concentrations in shallow ground water affected by the depth of the monitoring wells. The deeper the monitoring wells, the less TP and TKN concentrations were measured.

• 물과 미래
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• 제28권3호
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• pp.175-186
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• 1995

강원도의 대표적인 토지이용 방법인 방목지와 초지의 유출수 및 지하수의 수질 특성을 구명하기 위한 연구이다. 강원대학교 농장과 목장에 시험유역을 설치하고 Flume과 지하수 관측정을 이용하여 1993년 8월부터 1994년 8월까지 수질을 관측하였다. 수질관측 항목은 NO3-N, TP 및 TKN 이었다. 조립질 토양인 방목지의 유출은 대부분 지하수를 통하여 배출되었으며 호우시만 지표면 유출이 발생하였고 유출량은 급격히 증가하였다. 유출수의 $NO_3$-NO 농도는 0.241~3.962mg/l로 비교적 안정되어 있었다. 평시 유출수의 TP와 TKN 농도는 안정되어 있었으나 호우시는 급격히 증가하였다. 지하수의 $NO_3$-N 농도는 관측정의 깊이에 관계없이 비교적 일정하였으나 TP와 TKN 농도는 깊은 관측정에서 농도가 작았다. 평지에 조성되고 Sudan Grass로 잘 피복된 초지유출수의 수질은 유출량에 관계없이 비교적 일정하였다. 초지 지하수의 $NO_3$-N 농도는 상류에서 하류로 흐를수록 2.2mg/l 정도 증가하였다. 상류부와 하류부의 TP와 TKN 농도는 유의성 있는 차이를 보이지 않았다.

• 한국환경농학회지
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• 제9권2호
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• pp.133-141
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• 1990

호소(湖沼)의 수질관리 및 예측에 필요한 기초자료로서 농경지로부터의 오염부하량(汚染負荷量)을 제시할 목적으로 1989년 5월 8일부터 9월 30일까지 벼의 생육기간에 정남면 소재 29.3ha의 논에서 질소와 인을 조사 분석한 결과를 요약하면 다음과 같다, 1. 대상지구로 유입된 관개량은 715mm로서 강우량의 영향을 많이 받았다. 침투수량은 318mm로서 관개와 강우로 인한 담수유무(湛水有無)에 따라, 지표유출 수량은 1060mm로서 관개량과 강우량에 따라 월별로 큰 변화를 보였다. 2. 년간 살포된 비료의 양은 질소로서 180kg/ha, 인으로서 46kg/ha이었다. 조사기간동안 관개수에 의한 유입은 TKN이 15kg/ha, TP가 10kg/ha이었는데, 5, 6월에 특히 많은 유입을 보이는 것은 이 시기에 관개량이 많았고 저수지의 준설(浚渫)로인하여 관개수에 질소 및 인이 흡착된 토입자가 포함되어 그 농도가 높았기 때문으로 사료 된다. 3. 지표유출량은 조사기간 동안 TKN이 39kg/ha, TP가 9kg/ha로 나타났다. 침투유출량은 TKN이 7.5kg/ha, TP가 2kg/ha를 보였다. 두 값 모두 5, 6월에 큰 값을 보이는 이유는 관개수에 의한 유입과 시비로 인한 영향으로 판단된다. 4. 하천에서 유하거리(流下距離)에 따른 영양물질 변화는 WS1에서 TKN이 0.31mg/L/km(0.04g/km), TP가 0.01mg/L/km(0.004g/km)의 감소를 보였고 WS2는 TKN이 0.84mg/L/km(0.24g/km), TP가 0.11mg/L/km(0.10g/km)의 감소를 보였다. WS2가 WS1보다 유거연장(流距延長)이 짧지만 더 큰 감소를 나타낸 것은 사행이 더 심하고 하상기복이 커서 유속이 작기 때문인 것으로 사료된다. 5. 농경지로부터 하천이나 호수(湖沼)로 유입되는 오염물질(汚染物質)의 양(量)을 저감하기 위해서는 비료의 사용량을 제한하거나, 배수로(排水路)와 하천에 보 같은 구조물을 설치하여 유속을 줄이므로서 영양물질을 침전시키거나, 영양(營養)물질을 많이 소비하는 식물을 재배하여 자정작용의 기회를 확대시켜야 할 것으로 사료된다.

• 한국환경보건학회지
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• 제22권2호
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• pp.90-95
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• 1996

This study was performed to calculate the degration rate coefficient, operating parameters to meet the effluent standards, and the temperature adjustment coefficients to each parameter of pollution by seasonal variation of concentration and temperature of influent in livestock wastewater treatment by sequencing batch reactor process in field scale. The followings are the conclusions that were derived from this study. 1. In the field, temperature of livestock wastewater in reactor was 20.3$\circ$C in summer and 6.0$\circ$C in winter. The ratio of BOD:TKN: T-P in influent was 100:80:7. BOD loadings in winter and spring were 0.26 and 0.43 kg $BOD/m^3$ day, respectively. Those in summer and fall were 0.25 and 0.13 kg $BOD/m^3$ day, respectively. 2. The degradation rate coefficient for TKN was larger in summer and fall in which temperature was high than that in which temperature was high than that in winter and spring in which concentration was high. On the contrary, the phosphorus uptake rate was larger in winter and spring than that in summer and fall. 3. The hydraulic retention time in winter and spring was longer than that in summer and fall. Especially, in order to meet the standard for TKN of 120 mg/l in winter in which temperature of wastewater was 6.0$\circ$C, as the MLSS concentration was increased from 4, 000 to 7, 000 mg/l, the hydraulic retention time was increased from 212 to 121 hours. But, in order to shorten that less than 121 hours for the economical wastewater treatment, countermeasure to increase temperature of wastewater in the reactor should be considered. 4. the temperature adjustment coefficients for BOD, $COD_{Mn}$, TKN and T-P were 1.0241, 1.0225, 1.0541 and 1.0495, respectively. Namely, the treatment of TKN was most sensitively affected by temperature. For the purpose of the effective removal of nitrogen and phosphorus which are sensitive to temperature, it is necessary to keep the temperature of livestock wastewater more than 20$\circ$C which is the temperature of it in summer.

• 한국환경과학회지
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• 제14권2호
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• pp.157-165
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• 2005

This study was conducted to determine optimum design parameters in nitrification and denitrfication of chemical fertilizer wastewater using pilot plant, Jet Loop Reactor. The chemical fertilizer wastewater which contains low amounts of organic carbon and has a high nitrogen concentration requires a post-denitrfication system. Organic nitrogen is hydrolyzed above $86\%$, and the concentration of organic nitrogen was influent wastewater 126mg/L and of effluent wastewater 16.4mg/L, respectively. The nitrification above $90\%$ was acquired to TKN volumetric loading below $0.5\;kgTKN/m^3{\cdot}d$, TKN sludge loading below $0.1\;kgTKN/kgVSS{\cdot}d$ and SRT over 8days. The nitrification efficiency was $90\%$ or more and the maximum specific nitrification rate was $184.8\;mgTKN/L{\cdot}hr$. The denitrification rate was above $95\%$ and the concentration of $NO_3-N$ was below 20mg/L. This case was required to $3\;kgCH_3OH/kgNO_3-N$, and the effluent concentration of $NO_3^--N$ was below 20mg/L at $NO_3^--N$ volumetric loading below $0.7\;kgNO_3^--N/m^3{\cdot}d$ and v sludge loading below $0.12\;kgNO_3^-N/kgVSS{\cdot}d$. At this case, the maximum sludge production was $0.83\;kgTS/kgT-N_{re}$ and the specific denitrfication rate was $5.5\;mgNO_3-N/gVSS{\cdot}h$.

• 대한환경공학회지
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• 제28권5호
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• pp.501-510
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• 2006

교대로 간헐적으로 포기되는 2개의 부직포 여과막 생물반응조로 폐수를 처리할 때 반응조의 MLSS 농도와 유입수의 C/N 비가 질소 제거효율에 미치는 영향을 파악하기 위하여 MLSS 농도를 약 5,500 mg/L, 10,000 mg/L 및 15,000 mg/L로 유지하면서 $NH_4Cl$을 첨가하여 유입수의 TCOD/TKN 비를 5, 4, 3 및 2로 감소시켰다. 유입수는 음식물 쓰레기 침출수를 COD농도가 약 300 mg/L되도록 희석시킨 것이었다. 실험 결과, 반응조의 F/M 비는 0.112 g COD/g MLSS-day 이하, COD 제거효율은 95% 이상, 그리고 미생물 성장계수($Y_{obs}$) 값은 평균 0.283 g MLSS/g COD로 나타났다. 질산화 효율은 MLSS 농도가 5,500 mg/L이고 유입수의 TCOD/TKN 비가 2인 경우의 90.5%를 제외하고 모두 96% 이상이었다. 탈질효율은 유입수의 TCOD/TKN 비가 감소할수록 악화되었다. MLSS 농도가 5,500 mg/L인 경우에 비하여 10,000 mg/L인 경우에 탈질효율이 평균 10.7% 더 높아, MLSS 농도가 1,000 mg/L 증가함에 따라 평균 2.66 mg N/L의 율로 탈질율이 증가하였다. 그러나, MLSS 농도가 15,000 mg/L로 유지된 경우에는 5,500 mg/L인 경우에 비하여 탈질효율이 평균 4.6%만 더 높아 MLSS 농도가 1,000 mg/L 증가함에 따라 평균 0.75 mg N/L의 율로 탈질율이 증가하였다. 따라서 MLSS 농도와 내생 탈질율 간에 비례관계가 성립되지 않았다. 알칼리도 소모량은 유입수의 TCOD/TKN 비가 5인 경우에 제거된 T-N 1 mg당 평균 3.36 mg으로서 이론값인 3.57 mg에 가까웠으나 유입수의 TCOD/TKN 비가 감소함에 따라 증가하는 경향을 나타내었다.

• 대한환경공학회지
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• 제27권11호
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• pp.1141-1145
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• 2005

접촉부와 간헐포기부로 구성된 접촉조 결합형 연속회분식반응조를 질소제거를 위해 제안하고 실험적으로 연구하였다. 짧은 체류시간의 접촉반응을 통해 활성슬러지 플록에 유기물질이 생물흡착되지만 불완전 대사가 진행된다는데 근거를 두고 있다. 결과적으로 실하수의 경우 유입 유기물질의 61.2%가 접촉반응 30분 만에 흡착되었다. 유기물질의 비흡착량은 22.3 mg SCOD/g MLVSS였으며, 이는 후속되는 공정에서 탈질효율의 향상에 기여하였다. 연속운전을 통한 전체적인 처리효율은 TCOD/TKN 비가 6이하의 낮은 조건에서도 SCOD 및 T-N 제거율이 각 86%와 60%를 유지하였다.

• 한국환경보건학회지
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• 제18권2호
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• pp.67-74
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• 1992

The lab-scale biological A$_{2}$O system was applied from treating piggery wastewater highly polluted organic material which nitrogen and phosphorous are much contained relatively in conversion with other wastewater. The objective of this study was to investigate the effect of variance parameters on the treatability of this system according to operation conditions. An obtained experimental data were analysed by using principal component analysis (PCA) method. The results are summarized as follows: 1. From Varimax rotated factor loading in raw wastewater, variance of factor 1 was 36.8% and cumulative percentage of variance from factor 1 to factor 4 was 81.5% and of these was related to BOD, TKN and BOD loading. 2. In anaerobic process, variance of factor 1 was 33.5% and cumulative percentage of variance from factor I to factor 4 was 81.8% and of these was related to PO$_{4}$-P, BOD, DO and Temperature. 3. In anoxic process, variance of factor 1 was 30.1% and cumulative percentage of variance from factor i to factor 4 was 84.3% and of these was related to pH, DO, TKN and temperature. 4. In aerobic process, variance of factor 1 was 43.8% and cumulative percentage of variance from factor 1 to factor 4 was 81.5% and of these was highly related to DO, PO$_{4}$-P and BOD. 5. It was better to be operated below 0.30 kg/kg$\cdot$day F/M ratio to keep over 90% of BOD and SS, 80% of TKN, and 60% of PO$_{4}$-P in treatment efficiencies. 6. Treatment efficiencies was over 93% of BOD and SS, 81% of TKN and 60% of PO$_{4}$-P at over 20$^{\circ}$C, respectively.

• 한국환경보건학회지
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• 제21권1호
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• pp.86-92
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• 1995

This study was performed to evaluate the effect of temperature on operating parameters for reactor in pig wastewater treatment using sequencing batch reactor method which is one of the biological treatment methods. Study was accomplished by experimental apparatus of bench scale, and the degradation rate coefficient and temperature correction factor were derived. The followings are the conclusions that were derived from this study. 1. In the characteristics of pig wastewater, concentrations of TKN and T-P were very high as 590 mg/l and 40 mg/l, respectively. 2. Removal efficiency of BOD and $COD_{Mn}$ as organic compound indicators were the highest mark as 97% at 25$\circ$C. 3. When temperature was incresed from 10$\circ$C to 25$\circ$C, removal efficiencies of TKN and T-P were proportionally increased. Especially, the former was greatly effected by temperature of reactor. 4. In experiment of bench scale, the degradation rate coefficients were increased as temperature increased, but decreased at the temperature range of 25~35$\circ$C. Temperature adjustment coefficients for $COD_{Mn}$, BOD, TKN and T-P were 1.1460, 1.1356, 1.1140 and 1.0565, respectively.

• 한국물환경학회지
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• 제21권6호
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• pp.664-668
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• 2005

An experimental study for the comparison of nitrogen and phosphorus removal efficiencies between $A^2/O$ and modified Phostrip (M-Phostrip process) were carried out with bench-scale reactors. In case of nitrogen removal efficiencies both of processes showed similar ones when influent organic loadings were high. However, M-phostrip process was more effective than $A^2/O$ at low organic loadings. This is why M-phostrip process consumes the whole mass of influent organics as a carbon sources for denitrification in anoxic reactor but the anoxic reactor of $A^2/O$ process utilizes the residual carbon followed by consumming a part of influent carbon for phosphorus release in anaerobic reactor. $A^2/O$ process required the influent COD/T-P and COD/TKN ratios were more than 56 and 10, respectively, to take place the phosphorus release in anaerobic process and phosphorus uptake in oxic process. However, the luxury uptake of phosphorus in M-phostrip process was not affected by influent COD/T-P and COD/TKN ratios and the adverse effect of nitrate in return sludge introduced to the p-stripper from the 2nd clarifier was not significant due to the configurational advantage of the p-stripper.