• Journal of Navigation and Port Research
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• v.30 no.3 s.109
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• pp.241-245
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• 2006

Displayed result that handle particle contaminant and hydrospace organism included a number of ballast that is happened in ship using automatic back washing filter. Reason that removes first contaminant that is included in number of ballast is that heighten processing effectof after processing processof the filter. Another advantage is to drop off the solids with controlling revolution of drum screen in pretreatment filtration process. The fact that it is easy to attach and detach a several type of screen for getting the expected water quality is another advantage. Filter rotation speed of filtration filter could be expose by 35mmHg more than 60 rpm and filter consecutively filtration pressure is 40.5mmHg in 20 rpm and 40 rpm are 36.6mmHg. Filtration system removal aquatic organism over $70{\mu}min$ ballast water. This study shows that the filtration treatment system has a potential for the treatment of ballast water.

• Proceedings of the Korean Institute of Navigation and Port Research Conference
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• 2005.10a
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• pp.181-185
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• 2005

The treated ballast water from previous treatment contains microorganisms and pathogenic organisms in an filtration treatment system. The advantage of this process can be filtrated to minimize the demage to screen clogging of drum filter with sweeping the solids off rotating the surface of the filter. Another advantage is to drop off the solids with controlling revolution of drum screen in pretreatment filtration process. Also the fact that it is easy to attach and detach a several type of screen for getting the expected water quality is another advantage, too. Filter rotation speed at 20rpmis 40.5cmHg and 40rpm is 36.6cmHg. Filter out impurities from ballast water over 60rpm is 35cmHg. Filtration system removal aquatic organism over $80{\mu}m$ in ballast water. This study shows that the filtration treatment system has a potential for the removal of ballast water.

• Proceedings of the Korea Water Resources Association Conference
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• 2015.05a
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• pp.542-542
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• 2015

비점오염원은 기상조건과 토지이용에 따라 시간에 따른 오염부하량의 변동폭이 크게 발생하며, 강우초기에 오염물질의 농도가 크게 나타난다. MFFn은 강우지속시간에 따라 다양하게 변화하는 오염물질의 부하량과 유출량을 특정시점에서 강우유출율과 오염물질 유출율을 계산할 수 있으며, 강우가 시작될 때 0, 종료될 때 1의 값을 나타내며, 1보다 크면 초기세척이 있음을 나타낸다. 예를 들면 MFF20에서 평균값이 2.5이면 초기우수유출수의 부피 20%에 오염물질 부하량의 부피 50%를 포함하는 것을 의미한다. 본 연구에서는 논에서의 초기세척비율 정량화하기 위해 영산강수계 논지역(이하, 학야지구)과 섬진강수계 논지역(이하, 적성지구) 각 1개유역을 선정하여 2009년부터 2012년까지 수문 및 수질 모니터링을 수행하였다. 유역면적은 학야지구는 13.69 ha 이며, 적성지구는 8.06ha 이다. 두 지역 모두 외부유입이 없으며, 배수로가 구조물화 되어 있어 관측이 용이한 지점이다. 논에서 강우시유출되는 오염물질을 산정하기 위해서 배수로 말단에 압력식 수위계와 자동채수기를 설치하여 일정간격으로 관측하였으며, 수위별 유량관측을 통해 수위-유량관계곡선식을 산정 후 유량으로 환산하였다. 채취된 수질은 수질공정시험법을 통해 BOD, COD, TOC, T-N, T-P, SS를 분석하였으며, 관측된 유량과 수질자료를 이용하여 부하량을 산정하고, MFFn을 이용하여 초기세척비율을 정량화 하였다. BOD COD, TOC, T-N, T-P, SS 의 논 초기세척비율은 n 값이 10% 때 중앙값이 각각 1.3, 1.18, 1.13, 1.2, 1.13, 1.1 였으며, 13%, 11.8%, 11.3%, 12%, 11.3%, 11% 가 유출되는 것으로 나타났으며, n 값이 20%일 때 1.3, 1.1, 1.1, 1.25, 1.2, 1.2 이였으며, 26%, 22%, 22%, 25%, 24%. 24%가 유출되는 것으로 나타났다. n 값이 30%일 때 1.25, 1.0, 1.0, 1.25, 1.13, 1.3 였으며, 37.5%, 30%, 30%, 37.5%, 33.9%, 39%가 유출되는 것으로 나타났다.

• Proceedings of KOSOMES biannual meeting
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• 2006.05a
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• pp.79-83
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• 2006

Displayed result that handle particle contaminant and hydrospace organism included in number of ballast that is happened in ship using automatic bade washing filter. Reason that remove first contaminant that is included in number of ballast is that heighten processing effect of after processing process. of the filter. Another advantage is to drop off the solids with controlling revolution of drum screen in pretreatment filtration process. The fact that it is easy to attach and detach a several type of screen for getting the expected water quality is another advantage. Filter rotation speed at 1.0rpm is filter resistance 3.0bar and 3.0rpm is filter resistance 2.8bar. Filter out impurities from ballast water over 6.0rpm is filter resistance 26bar and 10rpm is filter resistance 2.5bar. Filtration system removal aquatic organism over $80{\mu}m$ in ballast water. This study shows that the filtration treatment system has a potential for the treatment of ballast water.

• Journal of Bio-Environment Control
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• v.9 no.1
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• pp.11-19
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• 2000

In recent, multi-sector nutriculture in which each sectors are managed with different compositions and supplying amounts of nutrient solution is being prevalent especially in large-scale greenhouses. This study was carried out to develop an automatic mixing and supplying system of nutrient solution for the multi-sector greenhouse which can control various compositions of nutrient solution and supplying amounts for each sector. The stock solution control device could control discharge of the stock solution with device actuating time. The experimental result showed high correlation between the discharge and the actuating time. The system could make nutrient solution of various compositions and showed possibility of changing compositions of nutrient solution according to changes of growth stages or environments. Undesirable remnant nutrient-solution effect on the next supply was decreased by lowering RC of the previous nutrient solution remaining in the tank and supply pipe through rinse process. To evaluate performance of the developed system, experiments that compare N $O_3$$^{[-10]}$ , and P $O_4$$^{3-}$ concentrations of nutrient solution made in laboratory level with those made by the developed system were conducted. The experimental results showed that the deviations for N $O_3$$^{[-10]}$ , and P $O_4$$^{3-}$ concentrations of nutrient solution composited by the developed system were -2.36％ and -5.15％, respectively.

• Proceedings of the Korean Institute of Navigation and Port Research Conference
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• 2006.06b
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• pp.221-226
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• 2006

This study is about backwash condition and membrane fouling at continuous filtration process in ballast water treatment. Displayed result that handle particle contaminant and hydrospace organism included a number of ballast that is happened in ship using automatic back washing filter. Reason that removes first contaminant that is included in number of ballast is that heighten processing effect of after processing process of the filter. Another advantage is to drop off the solids with controlling revolution of drum screen in pretreatment filtration process. The capacity of pilot plant was $10m^3/h$. The result of the test, Backwash cycle time and duration time and a signification effect on the efficiency of system and backwash Backwash duration time was determined to be fixed in 6 seconds of the system with more than 95% removal rate, It needed 1hour backwash frequency. Filtration system removal aquatic organism over $70{\mu}m$ in ballast water. This study shows that the filtration treatment system has a potential for the treatment of ballast water.

• Journal of Animal Environmental Science
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• v.18 no.2
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• pp.99-110
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• 2012

The purpose of the study is to collect basis data for to establish standard administrative processes of liquid fertilizer treatment. From this survey we could make out the key point of each step through a case of effective liquid manure treatment system in pig house. It is divided into six step; 1. piggery slurry management step, 2. Solid-liquid separation step, 3. liquid fertilizer treatment (aeration) step, 4. liquid fertilizer treatment (microorganism, recirculation and internal return) step, 5. liquid fertilizer treatment (completion) step, 6. land application step. From now on, standardization process of liquid manure treatment technologies need to be develop based on the six steps process.