• 한국농공학회논문집
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• 제48권3호
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• pp.97-106
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• 2006

The pollutant concentrations at experimental paddy plots with three (excessive, standard, reduced) different fertilization rates were investigated during 2001-2002 irrigation seasons. Mean concentrations of pollutants in ponded water were not significantly different among three experimental plots, but the T-N concentrations in percolated water significantly depended on fertilization rates. The T-N, T-P and $COD_{Cr}$, concentrations in ponded water during early irrigation season (late May to mid-June) were much higher than those during later irrigation season likely due to fertilization and low uptake by young rice crops. The T-N concentrations decreased but the concentrations of T-P and $COD_{Cr}$, increased three days after tillering fertilization. The removal rates of T-N by paddy plots were $0.13-0.16g/m^2{\cdot}d$ for an excessive fertilization plot, $0.08-0.25g/m^2{\cdot}d$ for a standard fertilization plot, and $0.03-0.34g/m^2{\cdot}d$ for a reduced fertilization plot three days after tillering fertilization. On the other hand, T-P and $COD_{Cr}$, were released three days after tillering fertilization.

• 한국물환경학회지
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• 제22권4호
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• pp.678-686
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• 2006

The feasibility of the high-hydrophilic biofilter was examined for application in rural wastewater treatment in Korea. The intermittent trickling biofiter was developed for wastewater treatment of media and examined instantaneous wetting water and immersional wetting water. Melamin foam absorbed 120 times it's weight in water and maintained wetting status than other materials. These characteristics are improvement for application in rural areas showing large variance of amount of influent. The biofilter process was effective in treating organic pollutants; mean removal efficiencies of $BOD_5$ and TSS were above 80%. The average SS concentrations of effluent was showed below $10mg/L^{-1}$ and meet guidelines in special regions, however, the average concentration of $BOD_5$ was about $20mg/L^{-1}$. The removals of T-N and T-P were relatively less effective and removal efficiencies were below 40%. It might meet the guidelines for T-P because of low levels of influent T-P concentration. However, the T-N concentration were too high and further treatment is required. The effluent concentration of $NH_4-N$ showed a significant reduction rate about 43.8%, but part of $NH_4-N$ was transformed to $NO_2-N$ and $NO_3-N$ inside the biofilter through nitrification process. The effluent concentration of org-P was removed about 78.8% of influent concentration by filtration. Considering stable performance and effective removal of pollutant in wastewater, low maintenance, and cost-effectiveness, the hydrophilic biofilter system was thought to be an effective and feasible alternative for decentralized rural areas.

• 한국토양비료학회지
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• 제44권2호
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• pp.263-270
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• 2011

주암호 상수원 상류지역에 위치한 복내 바이오파크 인공습지의 수생태학적 효율 향상을 위한 관리 방안을 제시하기 위하여 시기별, 계절별 및 오염물질 부하량별 수처리 효율을 평가하였다. 유입원수의 BOD, SS, T-N 및 T-P의 함량은 각각 1.87-4.23, 5.2-24.0, 4.94-15.59 및 $0.10-0.75mg\;L^{-1}$ 범위이었으며, 연평균 처리효율은 BOD, SS, T-N 및 T-P가 각각 26, 43, 62 및 83%로서 BOD 처리효율은 낮았으나 T-N과 T-P 처리효율은 매우 높았다. 계절별 수처리 효율은 전반적으로 동절기에 비하여 하절기에 높았으며 T-P의 처리효율은 계절적인 차이 없이 비교적 일정하게 높은 처리효율을 보였다. 인공습지 구성시스템별 오염물질 부하량에 따른 오염물질 처리량은 BOD는 침강지 > 습지조 > 마이크로폴, T-N과 SS는 습지조 > 침강지 > 마이크로폴 순이었으며 T-P의 경우에는 습지 구성 시스템별 큰 차이 없이 비교적 일정한 처리량을 보였다.

• 한국농공학회논문집
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• 제46권5호
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• pp.141-153
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• 2004

Wetland system is widely accepted as one of natural water purification systems around the world for nonpoint sources pollution control. Constructed wetlands have become a popular technology for treating contaminated surface and waste water. In this study, the field experiment to reduce nonpoint source pollution loadings from polluted stream waters using wetland system was performed from June 2002 to March 2004. Four wetlands were used and the size of each one was 0.8ha. Water of Dangjin stream flowing into Seokmun estuarine reservoir was pumped into wetlands. Inflow and hydraulic residence time of the system was 500 $m^3$/day∼1,500 $m^3$/day, 2∼5 days, respectively. After 2 year operation, plant-coverage of the wetlauds was about 70% from bare soil surface at initial stage . Average water quality of the influent was $BOD_5$ 4.17 mg/L, TSS 18.45 mg/L, T-N 4.32 mg/L, and T-P 0.30 mg/L. The average removal rate of $BOD_5$, TSS, T-N and T-P during the study period was 5.6%, 46.6%, 45.7%, and 54.8%, respectively. Organic ($BOD_5$) removal rate was low and the reason might be low influent concentration. Wetland removal rate of T-P was about 10% higher than T-N. Performance of the experimental system was compared with existing data base (NADB), and it was within the range of general system performance. Overall, the wetland system was found to be adequate for treating polluted water stream with stable removal efficiency even during the winter period. Most of the nonpoint source pollutions from watershed are transported by streams or ditches, and they could be controled by constructed wetland system before entering the lake or reservoir.

• Environmental Engineering Research
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• 제10권5호
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• pp.247-256
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• 2005

A combination of the submerged membrane activated-sludge bioreactor(SMABR) equipped with non-woven fabric filter and oyster-zeolite (OZ) packed-bed adsorption column was studied to evaluate the advanced tertiary treatment of nitrogen and phosphorous. The non-woven filter module was submerged in the MBR and aeration was operated intermittently for an optimal wastewater treatment performance. Artificial wastewater with $COD_{Cr}$ of 220 mg/L, total nitrogen (T-N) of 45 mg/L, and total phosphorous (T-P) of 6 mg/L was used in this study. MLSS was maintained about $4,000\;{\sim}\;5,000\;mg/L$ throughout the experiments. The experiments were performed for 100-day with periodic non-woven filter washing. The results showed that $COD_{Cr}$ could be effectively removed in SMABR alone with over 94% removal efficiency. However, T-N and T-P removal efficiency was slightly lower than expected with SMABR alone. The permeate from SMABR was then passed through the OZ column for tertiary nutrients removal. The final effluent analysis confirmed that nutrients could be additionally removed resulting in over 87% and 46% removal efficiencies for T-N and T-P, respectively. The results of this study suggest that the waste oyster-shell can be effectively reclaimed as an adsorbent in advanced tertiary wastewater treatment processes in combination with SMABR equipped with non-woven fabric filter.

• 한국습지학회지
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• 제11권2호
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• pp.9-16
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• 2009

본 연구는 인공습지 유출수를 추가처리하기 위해 다양한 재료를 이용한 추가처리시설의 적용가능성을 분석하였다. 석문담수호 유입부에 설치된 인공습지 중 무식재구, 갈대식재구, 부들식재구의 하단 배수로(폭 0.3m, 수심 0.35 m)에 각각 제강슬래그, 활성탄, 굴폐각을 이용해 1.0 m 길이로 추가처리시설을 설치하였으며, 각 후 처리시설별로 유입유량을 다르게 적용하였다(제강슬래그 63 $m^3$/day; 활성탄 19 $m^3$/day; 굴폐각 81 $m^3$/day). 제강슬래그, 활성탄, 굴폐각의 COD 처리율은 각각 6 %, 24 %, 1 %로 나타났으며, 제거량은 32, 30, 5 g/day로 나타나, 모든 추가처리시설에서 유기물제거에 효과적인 것으로 나타났다. T-N과 T-P의 제거효율은 활성탄에서 24 %와 4 %로 효과적이었으나, 제강슬래그 및 굴폐각에서는 효과가 없는 것으로 나타났다. 이상의 결과로부터 추가처리시설을 상대적으로 영양물질제거에 효과적인 인공습지와 연계하여 운영할 경우 영양물질 및 유기물을 효과적으로 제거할 수 있을 것으로 판단된다.

• 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.

• 한국토양비료학회지
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• 제44권3호
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• pp.434-441
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• 2011

축산농가에서 소규모로 발생하는 고농도의 질소와 인을 함유한 축산폐수의 처리효율을 극대화시키기 위해 수생식물여과조-활성슬러지조-인공습지로 구성된 축산폐수처리 시스템에서 축산폐수 재주입 비율별 및 주입방법별 수처리 효율을 조사하였다. 축산폐수의 재주입 비율별에 따른 처리효율을 조사한 결과 COD, SS, T-N 및 T-P 처리효율은 30% < 70% ${\leq}$ 100%의 순으로 재주입 비율이 증가함에 따라 오염물질의 처리효율이 점점 증가하는 경향이었다. 또한, 주입방법에 따른 COD, SS, T-N 및 T-P의 처리효율을 조사한 결과 1차 및 2차 처리조까지는 연속적 주입이 간헐적 주입에 비해 약간 높은 처리효율을 보였으나, 3차 처리조 부터는 비슷한 처리효율을 보였으며, 방류수 중COD, SS, T-N 및 T-P의 처리효율은 연속주입방법이 각각 99.5, 99.8, 99.0 및 99.8%로 간헐주입에 비해 약간 높았다. 이들 결과를 미루어 볼 때, 본 현장 인공습지 축산 폐수처리장에서 은 적합한 축산폐수의 재주입 비율과 주입방법을 선정한다면 질소 및 인 처리효율을 향상 시킬 수 있을 것으로 판단된다.

• 한국양식학회지
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• 제16권4호
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• pp.252-256
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• 2003

양식장에서 생성되는 어류의 노폐물이나 미섭취되고 남은 사료분은 고농도의 질소와 인을 함유하고 있으나 미처리된 상태로 처리하고 있어 그에 따른 처리방안이 요구된다. 본 연구에서는 기존의 처리공정의 대용으로 생태공학적 처리로서 경제적으로 질소와 인 제거를 위해 실내재배조에 물상추를 적용하였다. 앙식장 배출수 처리를 위한 생물여과상의 처리효율을 향상시키기 위하여 물상추 여과조를 설치하여 다양한 조건하에 시도되었다. 실험 재료인 수초는 물상추를 재배하였고, 6개의 수조(62${\times}$60${\times}$86cm)에 재배조 용량이 80 L가 되도록 채우고 수리학적 체류시간(hydraulic retention time; HRT)을 1, 2, 4, 8일로 하여 운영하였다. HRT 8일인 경우 1차 배출수를 대상으로 하였을 경우 BOD, T-N, T-P의 제거율은 92.8, 79.0 및 93.6%로 각각 나타났다.

• 상하수도학회지
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• 제20권4호
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• pp.519-526
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• 2006

In this study, the major operating factors in SND(simultaneous nitrification and denitrification) using bioreactor packed with submerged cilia media and granular sulfur such as variation of nitrification rate, organic matter removal efficiency and denitrification efficiency in different DO concentration were mainly evaluated. Synthetic wastewater and actual sewage were used as influent wastewater. Experiment with synthetic wastewater as influent wastewater was divided into three phases with the adjustment of DO concentration. As the results, nitrification efficiency and T-N removal efficiency in the Phase 3(DO 1.0~2.0 mg/L) were 99% and 52.3%, which is significantly greater than those in other two phases. Also, loading rate and denitrification efficiency of SCPGS(Submerged Cilia media Packed with Granular Sulfur) were calculated as $0.44kg\;NO_3^--N/m^3-day$ and 50%, respectively. On the other hand, nitrification rate was decreased from 99% to 64% according to the DO concentration with the variation from 3.0~3.5 mg/L(phase1) to 0.4~0.6mg/L(phase2). Although the nitrification rate was decreased in 64% according to the variation of the DO concentration, T-N removal rate was rapidly increased to 49% by increasing of the denitrification efficiency. Experiment with actual sewage as influent wastewater was carried out to evaluate efficiency of SCPGS in real operation condition of full-scale sewage water treatment plant. At the time, T-N removal rate in this experiment and full-scale wastewater treatment plants were given by 43% and 20%, respectively. The above results indicate that SCPGS can be used as an advanced treatment process for economical efficiency considered.