• 한국지반공학회:학술대회논문집
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• 한국지반공학회 2009년도 세계 도시지반공학 심포지엄
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• pp.1057-1064
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• 2009

Since the global warming causes debris flow damage has increased in Kangwon Area, Sediment control dam have increasingly founded to protect the damage. In spite of the realities design methods are well not established to determine type of the dam, design parameters and maintenance. Through comparison for design methods to sediment control dam in Korea, it raised some points to improve to correspond with realities. In addition, it pointed that some issues for the sediment control dams in Kangwon Area. Those are shown that unclear positions of the dams, unremoval of sediment, occurrence of seepage under the dams and uninstallation of roads to remove sediment. In addition, the countermeasure for the issues are proposed.

• 한국환경보건학회지
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• 제34권3호
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• pp.240-246
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• 2008

The purpose of this study was to gain basic information on the characteristics of $CO_2$ adsorption in relation to $Na_2CO_3$, $K_2CO_3$, $Li_2CO_3$-impregnated activated carbon in a Fixed Bed Reactor. From the results of this study the following conclusions were made: $Na_2CO_3$, $K_2CO_3$, $Li_2CO_3$-impregnated activated carbon had a longer breakthrough time and more enhanced adsorption capacity than activated carbon alone. When tested with isothermal adsorption and tested for $CO_2$ adsorption the amount of $CO_2$ adsorbed varied with temperature, $CO_2$ inlet concentration, gas flow rate, aspect ratio, etc. Based on the results, when Langmuir, Freundlich and Dubinin-Polanyi adsorption isotherms were used for linear regression of isothermal adsorption data, Langmuir adsorption isotherm was the most suitable. And, the optimum condition for $Na_2CO_3$ and $K_2CO_3$ impregnated activated carbon make-up was 1N and $Li_2CO_3$ was 0.1N. It could be concluded that adsorption capacity was decreased with adsorption temperature and increased gas concentration. When the aspect ratio (L/D) was varied 0.5, 1.0 and 2.0, the significant drop of adsorption amount was observed below 1.0 and breakthrough time was shortened with gas flow rate.

• 한국자기학회지
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• 제10권5호
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• pp.210-219
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• 2000

질화철(FeN)막을 이용한 FeN/Co/Cu/Co와 FeN/Co/Cu/Co/Cu/Co/FeN 다층막의 자기저항효과를 조사하였다. 질소유량이 0.4 sccm 이상인 조건에서 제작한 FeN막의 결정구조는 $\alpha$-Fe와 $\varepsilon$-Fe$_3$N상의 혼합상이며 침상구조인 $\varepsilon$-Fe$_3$N상에 의해 유도되는 형상자기이방성 때문에 자기저항효과가 관찰된다. 자기저항효과는 FeN막의 질소 유량과 두께에 따라서 달라지며 이는 FeN막의 $\varepsilon$-Fe$_3$N상에 의해 유도되는 형상자기이방성이 자유층과 고착층에 미치는 범위가 질소유량과 두께에 따라 달라지기 때문이다. 자유층인 Co막의 두께가 70 $\AA$인 조건에서 가장 우수한 자기저항비와 자기저항감도를 나타내며 자기저항비는 질소유량이 0.5 sccm이고 두께가 250 $\AA$인 조건에서 제작된 FeN/Co/Cu/Co/Cu/Co/FeN 다층막에서 3.2 %로 최대값을 나타낸다. 이 다층막의 3개의 자성층은 각기 다른 보자력을 갖고 있으므로 자기저항곡선상에 각각의 보자력 차이에 의한 step을 형성하며 MRAM 등으로 응용시 4개의 신호를 동시에 구현할 수 있을 것으로 기대된다.

• 공업화학
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• 제18권3호
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• pp.239-244
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• 2007

이산화탄소 분리 및 메탄 회수를 동시에 수행하기 위한 배출구가 두 개로 분리된 내부순환식 기포탑 반응기를 이용하여 $CO_2$ 분리용 흡수제인 모노에탄올아민(MEA)의 최적조건을 도출하였다. 5 wt% MEA 수용액에서 이산화탄소의 흡수 및 탈기 반응 시 pH 변화, 공기주입량에 따른 이산화탄소 탈기량 및 메탄 함량변화를 관찰하였다. 또한 액상수위 및 초기 MEA 흡수액 온도변화에 따른 이산화탄소 흡수 및 메탄 회수율을 측정하였다. 최적반응조건은 정상상태에서 액상수위 40 mm, 공기주입량은 1.5 L/min, 흡수액의 온도 $25^{\circ}C$이었다

• 한국응용과학기술학회지
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• 제32권4호
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• pp.712-717
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• 2015

본 연구에서는 이산화탄소와 석탄을 사용하여 합성가스 CO를 생산하는 실험을 수행하였다. CO 합성특성은 KOH 촉매를 사용한 화학적 활성화 방법에 의해 조사되었으며, 제조공정은 $CO_2$ 전환반응에서 석탄과 활성화 촉매 비율, 가스 유량과 반응온도 등과 같은 실험변수들을 분석함으로서 최적화되었다. KOH 촉매를 사용하지 않은 경우, 반응온도 $950^{\circ}C$와 $CO_2$ 유량 300 cc/min에서 65% $CO_2$ 전환율을 얻었으며, 반면에 촉매를 사용한 경우 같은 반응조건에서 98.1%의 전환율을 얻었다. 석탄의 활성화촉매 반응물의 비(석탄 : KOH = 4 : 1)가 다른 반응물 비에 대해 더 좋은 $CO_2$ 전환율과 CO 선택도 보여줌을 알 수 있었다.

• Journal of Mechanical Science and Technology
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• 제17권10호
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• pp.1507-1519
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• 2003

The two-phase flow patterns for both non-loop and loop type oscillating capillary tube heat pipes (OCHPs) were presented in this study. The detailed flow patterns were recorded by a high-speed digital camera for each experimental condition to understand exactly the operation mechanism of the OCHP. The design and operation conditions of the OCHP such as turn number, working fluid, and heat flux were varied. The experimental results showed that the representative flow pattern in the evaporating section of the OCHP was the oscillation of liquid slugs and vapor plugs based on the generation and growth of bubbles by nucleate boiling. As the oscillation of liquid slugs and vapor plugs was very speedy, the flow pattern changed from the capillary slug flow to a pseudo slug flow near the annular flow. The flow of short vapor-liquid slug-train units was the flow pattern in the adiabatic section. In the condensing section, it was the oscillation of liquid slugs and vapor plugs and the circulation of working fluid. The oscillation flow in the loop type OCHP was more active than that in the non-loop type OCHP due to the circulation of working fluid in the OCHP. When the turn number of the OCHP was increased, the oscillation and circulation of working fluid was more active as well as forming the oscillation wave of long liquid slugs and vapor plugs in the OCHP. The oscillation flow of R-142b as the working fluid was more active than that of ethanol and the high efficiency of the heat transfer performance of R -142b was achieved.

• International Journal of Fluid Machinery and Systems
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• 제2권3호
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• pp.189-196
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• 2009

The effect of inlet and outlet blade angles on a micro regenerative pump head was examined in experiments. The pump head was little increased by changing the blade angles compared with the original pump with the inlet and outlet blade angles of 0 degree. The effect of the axial clearance between the impeller and the casing on the pump head was also examined. The head was increased largely by decreasing the axial clearance. The computation of the internal flow was performed to clarify the cause of the increase of the pump head due to the decrease of the clearance. The local flow rate in the casing decreased as the leakage flow rate through the axial clearance decreased due to the decrease of the clearance. It was found that the larger head in the smaller clearance was just caused by the smaller local flow rate in the casing. In the case of the smaller clearance, the smaller local flow rate caused the smaller circumferential velocity near the front and rear sides of the impeller. This caused the increase of the angular momentum in the casing and the head.

• 대한기계학회논문집
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• 제14권6호
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• pp.1669-1678
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• 1990

본 연구에서는 다중선회연소기의 원리에 기초하여 연료와 산화제의 접촉면적 및 혼합속도를 증가시킴으로써 연소부하의 증대 및 연소효율의 향상효과를 얻을 수 있 는 새로운 연소방식을 개발하기 위한 시도로서 속도차가 있는 동축의 두 공기분류 사 이의 전단층에 기체연료를 분출시켜서 형성되는 난류확산 화염에 관하여 유동장의 성 상이 화염안정한계 및 화염구조에 미치는 영향을 조사하여 실용연소기의 유도장제어 및 고부하연소기설계를 위한 기초자료를 얻는데 목적이 있다.

• 한국가시화정보학회지
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• 제17권3호
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• pp.12-18
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• 2019

Direct numerical simulation of a fully developed turbulent plane Couette-Poiseuille flow with a two-dimensional (2-D) rod-roughened wall is performed to investigate the impacts of the surface roughness. It is shown that the logarithmic region in the mean velocity profile over the rough wall Couette-Poiseuille flow is significantly shortened by the surface roughness compared to that over a turbulent Couette-Poiseuille flow with smooth wall. The Reynolds shear stress over the rough wall Couette-Poiseuille flow is decreased compared to that for a smooth case in the outer layer. These results are attributed to weakened turbulence activity or roll-cell mode over the rough wall Couette-Poiseuille flow near the channel centerline due to suppressed development of u'-structure on the top wall, as documented through spanwise energy spectra of the streamwise velocity fluctuations. Inspection of congregation motion near the bottom wall and time evolution of u'-structure reveal weakened co-supporting cycle for the rough wall case.

• 한국안전학회지
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• 제24권6호
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• pp.27-31
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• 2009

An experimental study on the unsteady effect of the extinction limit was performed in ethene jet diffusion flames. To impose the unsteadiness on jet flames, the amplitude and frequency of a co-flow velocity was varied, and the two inert gases, $N_2$ and $CO_2$, were used to dilute the oxidizer for extinguishing concentration. The experimental results shows that large amplitude of velocity induces a low extinguishing concentration, which implies that flow variation affects the blow out mechanism. Also, the flow oscillation effects under high frequency attenuates the flame extinction. These results means that flow unsteadiness extends the extinction limit and finally minimum extinction concentration by inert gases. When the Stoke's 2nd Problem is introduced to explain the flow unsteadiness on extinction concentration, the solution predicts the effect of amplitude and frequency of velocity well, and hence it is concluded the effect of low frequency velocity excitation was attributed only to flow effect.