• 한국분말야금학회:학술대회논문집
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• 한국분말야금학회 1998년도 춘계학술대회 및 발표대회 강연 및 발표논문 초록집
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• pp.10-10
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• 1998

• 콘크리트학회지
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• 제19권6호
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• pp.39-45
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• 2007

• 한국자기학회:학술대회 개요집
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• 한국자기학회 2002년도 춘계연구발표회 논문개요집
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• pp.148-149
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• 2002

No Abstract, See Full Text

• 대한기계학회논문집
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• 제15권2호
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• pp.618-629
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• 1991

The purpose of this experiment is to understand the distribution of coal particles inside CWM droplet which is believed to be a very important factor controlling the flame stability. CWM slurry is atomized by an air assisted twin fluid nozzle. An experimental rig is designed and fabricated. The mean size of coal particle distribution in CWM slurry, atomizing air pressure, coal particle loading in slurry and sampling position inside spray are main experimental variables. The atomized CWM droplets are sampled on the thin white layer of magnesium oxide by the emergency sampling shutter. The sampled coal particles on magnesium oxide layers are collected into test tubes and dispersed completely by Ultra-Sonicator. The size distribution of coal particles inside droplets are measured by Coulter Counter. The presence of coal particle inside the impressions of droplets on magnesium oxide layer are investigated by photo technique. There are quite many droplets which do not have any coal particles. Those are just water droplets, not CWM droplets. The population ratio of droplets without coal particles to toal number of droplets is strongly affected by the mean size of coal particle distribution in slurry and this ration becomes bigger number as the mean size of coal particles be larger. The size distribution of coal particles inside CWM droplets is not even and depends on the size of droplet. Experimental results show that the larger CWM droplets has droplets has bigger mean value of particle size distribution. This trend becomes more evident as the atomizing air pressure is raised and the mean size of coal particles in CWM slurry is bigger. That is, the distribution of coal particles inside CWM dropolets is very much affected by the atomizing air pressure and the mean size of pulverized coal particles in CWM slurry.

• 한국지반신소재학회논문집
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• 제5권2호
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• pp.17-22
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• 2006

비위생매립지(非衛生埋立地)의 설치는 매립지 주변의 지반오염에 심각한 영향을 미친다. 동전기정화기법(動電氣淨化技法, Eelectrokinetic Remediation Technology)은 주로 무기오염물질에 의해 오염된 저투수성(低透水性)지반의 정화에, 투수성반응벽체(透水性反應壁體, Permeable Reactive Barrier)는 주로 지하수 내의 유기오염물질의 분해 등에 각각 효과적이다. 본 연구에서는 동전기정화기법과 투수성반응벽체의 장점을 복합적으로 비위생매립지 주변의 오염현장에 적용하여 정화효과를 조사하였다. 환경오염원이자 폐기물인 제강슬래그를 재활용한 오토마이징슬래그(Atomizing Slag)를 투수성반응벽체의 반응물질로 이용하였다. 현장적용 실험결과, 동전기정화기법과 투수성반응벽체의 장점을 복합적으로 적용한 EK & PRB System(EPS)이 원위치(原位置, In-Situ) 정화효율을 높여줌을 알 수 있었다.

• 한국진공학회:학술대회논문집
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• 한국진공학회 2009년도 제36회 동계학술대회 초록집
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• pp.120.1-120.1
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• 2009

• 한국정밀공학회:학술대회논문집
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• 한국정밀공학회 2011년도 춘계학술대회 논문집
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• pp.1281-1282
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• 2011

• 대한전기학회:학술대회논문집
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• 대한전기학회 2004년도 하계학술대회 논문집 C
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• pp.1900-1902
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• 2004

The degradation systems of non degradable waste water consist of the arc plasma torch, power supply, a feeder of liquid waste and reactors. Output of stable plasma torch, suitable air flux, microscopic atomizing state of waste water and long reaction section must be to degrade waste water more efficiently. In this paper, we are designed the stable power system, the microscopic atomizing state of waste water and the efficient reactors to satisfy various conditions. Non degradable wast water used in this work was $Na_2$EDTA of 1.0 mol. The concentration of $CO_2$ and EDTA was analyzed using GC (Gas Chromatography) and HPLC (High Performance Liquid Chromatography). In the result show that $CO_2$ concentration was about 96% and EDTA was degraded approximately 96%.

• 청정기술
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• 제9권4호
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• pp.163-168
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• 2003

회전형 도장기기의 핵심 부품인 공기 터빈 및 무화 디스크 설계를 위한 기본 설계개념 및 방법을 제시하였고, 이를 이용하여 도장기기를 설계, 제작하였다. 제작된 도장기기의 회전수 및 유량의 측정 결과는 전산유체역 학적 해와 잘 일치하였다. 또한 공기 터빈 및 디스크 설계 사양에 따라 도장기기의 회전수가 현저히 변화됨을 알 수 있었고, 공기 터빈의 유로 기울기 $20^{\circ}$, 노즐 수 2개일 때의 도장기기 성능이 가장 우수하였다.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2001년도 춘계학술대회논문집D
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• pp.528-533
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• 2001

An experimental study is carried out to investigate the effects of air and water mass flow rates on cooling characteristics of mist impinging jet on a flat plate. Experiments are conducted with air mass flow rates from 0.0 to 3.0 g/s, and water mass flow rates from 5.0 to 20.0 g/s. An air-atomizing nozzle is used for the purpose of controlling air and water mass flow rates. In this study, a new test section is designed to obtain local heat transfer coefficient distributions. Heat transfer characteristics of the mist impinging jet are explained with the aid of flow visualization. Surface temperature and heat transfer coefficient distributions become more uniform as air mass flow rate increases, and that the increases in water flow rate mainly enhance cooling performance. Air mass flow rate weakly influences averaged heat transfer coefficient when water mass flow rate is low, but averaged heat transfer coefficient increases remarkably as air mass flow rate in case of high water mass flow rate.