• KSBB Journal
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• v.23 no.4
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• pp.323-328
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• 2008

This study was accomplished using Anaerobic/Anoxic/Oxic biofilm reactors with fixed media and post-treatment reactor for natural purification with aquatic floating plants. The objectives of this study was to investigate the characteristics of organics, nitrogen and phosphorus removal from sewage with the HRT. The average removal efficiency of SS and $COD_{Cr}$ increases as increasing the hydraulic retention time (HRT) until 12 hr of the HRT, and it was constant over 12 hr of the HRT. The removal efficiency of them was about 93% and 89% respectively over the 12 hr of HRT. The average $BOD_5$ and $COD_{Mn}$ increases as increasing the HRT and the removal efficiency of them was 84.91 % and 76.03% respectively at the 26 hr of HRT. The removal efficiency of T-N and T-P increases as increasing the HRT until 61 hr of the HRT, and it was constant over 61 hr of the HRT. At the HRT of 61 hr, it was 70.20%, 77.86% respectively. It was found that the optimum HRT was 61 hr in case of the nutrients. Before and after experiment, the nitrogen content was similar in leaves of the water hyacinths but the nitrogen content in roots after experiment was 5.5% more than its content before experiment. It was known that the nitrogen was absorbed by the water hyacinths.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.11 no.2
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• pp.675-680
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• 2010

This study was investigated to complement nitrogen removal of low concentration influent municipal sewage. The following are the results of the effect of Internal Recircularion and Step Feed rates on Treatment efficiency at a BOD low concentration influent municipal sewage. Up to 90.0% of BOD, 87.8% of COD, 71.0% of T-N, 75.3% of T-P were removed on average at a low concentration influent. Whereas BOD and T-P were removed without any relations to Step Feed rates, T-N was influenced. Nitrogen removal efficiencies in 80% of Step Feed rates was 65%, which was caused by the lack of Carbon Source for denitrification. Nitrogen removal efficiency in 40% of Step Feed rates was 58%, which means it was not removed but dischared. Consequently, the efficiency was 73%, 80%, and 78% in 70%, 60% and 50% of Step Feed rates, which was concluded as the best range of Step Feed rates. Nitrogen removal efficiency increased under the condition of Internal Recircularion. At over 150% of Internal Recircularion rate, the efficiencies were not affected any more. It is believed that lots of Recircularion caused inflow of DO to anoxic tank. Therefore, the most appropriate Internal Recircularion rate can be concluded as 50~150%.

• Journal of Korean Society of Environmental Engineers
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• v.22 no.12
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• pp.2125-2134
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• 2000

This research was to develope the economical treatment processes of the landfill leachate to meet the legal discharge standards. To achieve this purpose, experiments were conducted in laboratory to choose the optimum process and to obtain the design factors before a pi!ot-scale test. The concept of the process developing in this research was using the reverse osmosis system. The submerged membrane bio-reactor was used to achieve pre-treatment of reverse osmosis system and the concentrate was treated by evaporator with land fill gas as a fuel. The results of the research showed that SS, $BOD_5$, $COD_{cr}$, $NH_4{^+}-N$ and T-N were removed 99.0%, 43.0%, 12.9%, 48.5% and 18.7% respectively in the submerged membrane bio-reactor. The reverse osmosis system could remove $BOD_5$, $COD_{cr}$, $NH_4{^+}-N$ and T-N as an efficiency of97.5%, 97.6%, 79.7% and 85.4% respectively. The evaporator could remove $COD_{cr}$, $NH_4{^+}-N$ and T-N as an efficiency of 90.5%, 50.6% and 63.3% respectively. However the condensed water of the evaporator was not satisfied the legal standard and should be treated in reverse osmosis with the pre-treated leachate.

• KSCE Journal of Civil and Environmental Engineering Research
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• v.6 no.1
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• pp.43-50
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• 1986

A research was performed to examine the applicability of aerobic fixed-biofilm reactors for removal of biodegradable organics in raw waters. Crushed briquette ashes or granite were utilized as media. Experiments were carried out by feeding packed bed reactors with a synthetic raw water prepared by dissolving phenol in tap water with other inorganic nutrients. Results of the research showed that the effluent TBOD concentrations were lower than 6 mg/l when the influent BOD concentrations were kept below 50 mg/l and a detention time of about 2.7 hours was provided. The SBOD concentrations of the treated waters should be less than 5 mg/l since the effluent SS could be removed by conventional water treatment methods such as coagulation and filtration. It was also found that most of the SS in the effluents were humic materials since the effluent SS caused little BOD. This means the biofilm in the reactor was in endogenous respiration phase due to low F/M ratio. According to the results of this study, it is recommended to pretreat any raw water contaminated with biodegradable organics in an aerobic fixed biofilm reactor with a detention time of 2 to 3 hours.

• Journal of Adhesion and Interface
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• v.19 no.3
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• pp.101-105
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• 2018

With the rapidly growing of the population and industrization of cities, the clean and affordable water resources have gained immense interest because of remaining about 780 million people still lack access to it. However, present wastewater treatment systems have been faced with various issues, such as low processing efficiency, high operational costs and the requirement of a large area for manufacturing. It is therefore urgently required to develop an inexpensive and efficient wastewater treatment system. As the one of these efforts, we suggested and successfully demonstrated the wastewater treatment system using and electrochemical method via a dimensionally stable anode (DSA) based on rutile type $RuO_2$. Our system achieved biochemical oxygen demand (BOD), chemical oxygen demand (COD), and total organic carbon (TOC) removal efficiently at the respective rates of 52.0%, 77.8%, and 65.6% from household wastewater. In addition, we were able to remove BOD, COD, total nitrogen (TN), and total phosphorus (TP) from animal husbandry wastewater at rates of 92.9%, 75.6%, 35.1%, and 100%, respectively, thereby achieving dramatic reductions. Considering the excellent removal efficiency and the small size of this device, electrochemical wastewater treatment using a DSA coated in rutile $RuO_2$ presents a promising option for the treatment of both household and animal husbandry wastewater.

• Journal of Wetlands Research
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• v.12 no.2
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• pp.25-33
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• 2010

Three plans(induction of water flow, supply of oxygen into water, control of fish causing resuspension of solids) proposed to improve the pollutant removal efficiency of Sihwa Constructed Wetland(CW) were estimated by considering the their efficiency and application to the wetland. After construction of facility for induction of water flow in lower part(W 122m${\times}$L 103m) of the wetland, the mean removal efficiencies of BOD, SS, TN and TP were in range of 12.8~37.4% and BOD was showing the highest efficiency. This result indicates that water flows is one of very important factors in the pollutant removal of wetland, especially near the outlet of a large scale wetland such as Sihwa CW. Dissolved oxygen(DO) concentrations after operation of two oxygen supply systems such as Air Bubble Diffuser and Surface Aeration System increased 15.5% and 27.2%, respectively. For maintaining effective DO concentration in Sihwa CW, the operation of oxygen supply system may be desirable during midnight to dawn in the location in which DO concentration is not enough, for instance less than 2 mg/L in CW. In experiments of the fish removal from Sihwa CW, the mean turbidity was lower in test site(6.2 NTU) than control site(10.6). The removal efficiency of thurbidity by th fish removal from the wetland was 41.5%. Therefore, a relevant fish management through a periodical monitoring of fish and turbidity is needed.

• Journal of Animal Environmental Science
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• v.16 no.3
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• pp.167-174
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• 2010

This study was performed to evaluate the removal effects of nutritive salts and organic pollutants in experimental aeration reactor for treatment of piggery slurry. In this study, three types of reactors were manufactured and operated. The fibrous media was equipped in one of three reactors. Another reactor was equipped with the siliceous media and the other reactor used as a control was equipped with typical aeration system only. Treatment efficacy of three types of reactors were evaluated according to the pollutants removal rate of the piggery slurry. The results obtained in this study are as follows : 1) In the reactor containing fibrous media, the removal efficiency of BOD, T-N and T-P was 11%, 13.9% and 21.2%, respectively. 2) In the reactor containing siliceous media, the removal efficiency of BOD, T-N and T-P was 6.9%, 25.3% and 47.8%, respectively. 3) In the reactor not containing media, the removal efficiency of BOD. T-N and T-P was 6.1%, 8.1.% and 23.6%, respectively. 4) Sludge accumulation in the reactor equipped with filamentous media was lower than that of other experimental reactors.

• Journal of Environmental Impact Assessment
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• v.28 no.5
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• pp.471-482
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• 2019

Water treatment system filled with Bio-stone Ball (BSB) have been developed for the purification of polluted water in many rivers and lakes. The real-scale plants of BSB water treatment system was constructed for field application test and water purification evaluation in Maewha reservoir. The average water purification efficiencies of BSB watertreatment system shows BOD 70.3% (47.2~97.4%), COD 45.3% (26.1~64.7%), TOC 19.2% (8.5~50.0%), SS 82.8% (73.1~92.7%), Chl-a 80.4% (57.2~91.8%), TN 23.2% (6.4~39.5%), and TP 51.8% (-1.1~80.1%). BSB water treatment system shows very high at 70~80% in the water purification efficiencies of BOD, Chl-a, and SS. The average of pollution loading reduction by installation of BSB treatment system shows 39.2% for COD and 16.8% for TP. The water quality improvement rates (%) of the Maewha reservoir shows TOC 14.5%, COD 14.5%, Chl-a 12.5% and TP 25.1%. The BSB watertreatment system can be applied to many agricultural reservoirs and major rivers to deal with serious water pollution issues.

• Korean Journal of Ecology and Environment
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• v.39 no.4 s.118
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• pp.471-480
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• 2006

The field scale experiment was performed to examine the performance of the constructed wetland for nonpoint source (NPS) pollution loading reduction. Four sets (each set of 0.88 ha) of wetland (0.8 ha) and pond (0.08 ha) systems were used. Water flowing into the Seokmoon estuarine reservoir from the Dangjin stream was pumped into wetland systems. Water depth was maintained at 0.3-0.5 m and hydraulic retention time was managed to about 2-5 days; emergent plants were allowed to grow in the wetland. The wetland effluent concentrations of $BOD_5$, TSS, and T-N were higher in winter than in the growing season excepting the T-P, and effluent $BOD_5$ concentration was higher than influents in winter. Mass retention of T-N and T-P was stable throughout the year, whereas mass retention of $BOD_5$ and TSS was decreased in winter. $BOD_5$, TSS, T-N, and T-P performance of the experi-mental system was compared with the existing database (North American Treatment Wetland Database), and was within the range of general system performance. From the first-order analysis, T-P was virtually not temperature dependent, and $BOD_5$ and TSS were more temperature dependent than T-N. Overall, the wetland system was found to be an adequate alternative for treating polluted stream water with stable removal efficiency and recommended as a NPS control measures.

• Korean Journal of Soil Science and Fertilizer
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• v.44 no.6
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• pp.1089-1094
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• 2011

To treat non-point source pollution in Juam lake, removal efficiencies of pollutants were investigated in Bongsan constructed wetlands (CWs) at different treatment time, stages and wastewater loads. The constructed wetlands consisted of forebay, $1^{st}$ and $2^{nd}$ wetlands. The concentrations of BOD, SS, T-N, and T-P in inflow were $1.87mg\;L^{-1}$, $1.62mg\;L^{-1}$, $11.47mg\;L^{-1}$, and $4.40mg\;L^{-1}$, respectively. The removal rates of BOD, SS, T-N, and T-P in Bongsan CWs were 26, 18, 16 and 9%, respectively. The removal rates of BOD and T-N were higher than those for SS and T-P. The amounts of pollutant removal in Bongsan CWs were higher in the order of forebay > $1^{st}$ wetland > $2^{nd}$ wetland for BOD, forebay > $2^{nd}$ wetland > $1^{st}$ wetland for SS, $1^{st}$ wetland > forebay > $2^{nd}$ wetland for T-N and $2^{nd}$ wetland > forebay > $1^{st}$ wetland for T-P.