• Proceedings of the Korean Institute of Electrical and Electronic Material Engineers Conference
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• 1998.11a
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• pp.105-108
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• 1998

Pt-WO$_3$-Si$_3$N$_4$-SiO$_2$-Si-Al 캐패시터를 이용한 NO$_2$ 가스 센서를 개발하였다. 표준 실리콘 MNOS구조에 촉매 게이트로 Pt와 가스 흡착층으로 WO$_3$를 이용함으로서 전통적인 세라믹 가스 센서보다 낮은 온도에서 NO$_2$ 가스를 감지할 수 있었다. 은도 변화와 NO$_2$ 가스 농도의 변화에 따라서 디바이스의 NO$_2$ 가스 감도를 조사하였다. Pt-WO$_3$ 계면에서 NO$_2$ 이온농도의 변화에 기초로 한 가스 감지 모델을 제시하였다. 제시된 가스 감지 모델을 계면에서의 가스 반응 속도론에 의하여 분석함으로서 확인하였다.

• 한국신재생에너지학회:학술대회논문집
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• 2007.11a
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• pp.453-456
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• 2007

감압 증류 후 생성되는 중질유의 고도화를 위하여 코킹 공정을 거친 후 정유 부산물로 생성되는 열적으로 매우 안정하고, 높은 발열량을 갖는 반면 황, 바나듐 함량이 높은 석유코크스의 효과적인 이용을 위하여 본 연구에서는 가스화 공정을 적용하였다. 1T/D 용량의 분류층 가스화기를 이용하여 유연탄(drayton coal), 석유코크스, 또는 혼합한 경우의 가스화 성능을 알아보았으며, 각각의 경우에 대하여 비교하여 보았다. 높은 열 안정성을 갖는 석유코크스의 효과적인 가스화를 위하여 반응기 내 체류시간 및 버너 노즐 변경에 따른 가스화 성능 개선을 시도하였으며, 이때의 온도, 산소/원료 공급량 조건에 따른 생성가스 성분 및 탄소전환율, 냉가스효율 변화 특성을 알아보았다. 버너 노즐 구경 변경으로 인한 슬러리의 미립화를 통하여 향상된 탄소전환율 및 냉가스효율을 얻을 수 있었다.

• Journal of Energy Engineering
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• v.6 no.1
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• pp.58-67
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• 1997

In this study numerical computations were performed to predict reacting flow fields of gasification processes of pulverized subbituminous coal in a cylindrical coal gasifier. To check the size effects of particles on flow fields in the gasifier, simulations were performed for five cases with four sizes of particles such as 40 $\mu\textrm{m}$, 60 $\mu\textrm{m}$, 80 $\mu\textrm{m}$ and 100 $\mu\textrm{m}$. Each case has a unique size of particles with one more case that has evenly mixed four sizes of particles. Predictions showed that the gasification which uses coals of the mixed sizes reveals more preferable gas velocity and temperature distributions than that uses coals of a unique size. Predicted gas temperature at the exit of the gasifier ranged 1,400 to 1580$^{\circ}C$, 1,480 to 1,700$^{\circ}C$, 1,600 to 1740$^{\circ}C$, 1630 to 1790$^{\circ}C$ and 1500 to 1680$^{\circ}C$ for particle sizes of 40 $\mu\textrm{m}$, 60 $\mu\textrm{m}$, 80 $\mu\textrm{m}$, 100 $\mu\textrm{m}$ and the evenly mixed four sizes, respectively.

• Journal of the Korean Institute of Gas
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• v.6 no.1 s.17
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• pp.38-45
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• 2002

Hydrates are solid cryctallines resembling ice in appearance, which are consist of a gas molecule surrounded by a cage of water molecules. Because of containning a large amount of methane, hydrates have been considered as a future energy resource. However, the formation of hydrates in the oil and gas industries has been known as a serious problem for a long time. The formation of hydrate in pipeline is common in seasonally cold or sub-sea environments with low temperatures and high pressures. Especially, hydrate plug formation becomes a real menace to flow assurance in inadequately protected transmission lines. This study was carried out for the purpose of understanding mechanism of hydrate plugging and examining formation conditions of hydrate in high pressure gas pipeline. In this study, we measured hydrate equilibrium conditions under the various flowing conditions with the methane. The results were presented both the plugging tendency and the effect of flowing velocity.

• Journal of the Korean Institute of Gas
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• v.27 no.2
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• pp.39-48
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• 2023

This study presents the experimental results to measure the adsorption amount of methane gas by coal according to the conditions of a coalbed methane (CBM) reservoir. Adsorbed gas to coal seam particles was measured under reservoir conditions (normal pressure ~ 1,200 psi pressure range, temperature range15 ~ 45℃) using coal samples obtained from random mines in Kalimantan Island, North Indonesia. The obtained amount of absolute adsorbed gas was applied to triangular with linear interpolation to calculate the maximum amount of adsorbed gas according to temperature and pressure change, at which no experiment was performed. As a result, it was revealed that the amount of adsorbed gas to coal particles increased as the pressure increased and temperature decreased, but the increase of the amount of adsorbed gas decreased at more than an appropriate depth(1,000 ft). In the cleat permeability and cleat porosity for each depth of the coal bed considering the effective stress, the cleat permeability was 28.86 ~ 46.81 md, and the cleat porosity was 0.83 ~ 0.98%. This means that the gas productivity varies significantly with the depth because the reduction of the permeability according to the depth in the coal seam is significant. Therefore, a coalbed depth should be considered essential when designing the spacing of production wells in a coalbed methane reservoir in further study.

• The Proceedings of the Korean Institute of Illuminating and Electrical Installation Engineers
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• v.3 no.3
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• pp.60-67
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• 1989

본 논문에서는 열병합발전소로서 가스터빈을 이용하는 경우, 계통분리를 비롯한 각종고장에 따른 발전기 및 계통의 응답성을 검토하여 가스터빈의 운전방법 및 계통의 안전운전여부를 파악할수 있는 방법에 대하여 검토하였다. 특히 온도제어루프, 가속도제어루프를 비롯한 가스터빈의 제어루프와 Droop 및 등속도 운전과 같은 운전방법을 시뮬레이션에 포함하여 각종 사례연구를 통하여 열병합발전소의 적절한 운전방법을 연구하였다.

• Bulletin of the Society of Naval Architects of Korea
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• v.41 no.2
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• pp.86-93
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• 2004

일반적으로 액화암모니아, LPG, 메탄, 부탄 등을 운송하는 가스운반선은 가스를 비등점 이하의 온도로 낮춰서 액화하여 운송하는 선박으로, 가스의 비등점이 -3$0^{\circ}C$에서 -4$0^{\circ}C$ 내외의 저온이므로 대기압 상태에서는 냉각되어 액화상태 약 -48$^{\circ}C$ 유지로 화물탱크에 저장 운반되어야 하는 여러 가지 제약조건이 따른다. 이러한 가스를 보관하는 탱크는 주로 저온에 강한 니켈강을 쓰게 되며 완벽한 고도의 용접기술을 필요로 하고, 저온상태의 화물 저장 운송을 위해서는 대형 냉동기와 보온설비도 필요하다. (중략)

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1993.11a
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• pp.42-45
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• 1993

내경 0.1 m 의 draft tube 를 갖는 직경 0.3 m, 높이 2.7 m 인 내부순환유동층 가스화반응기에서 호주산 준 역청탄을 공기와 수증기를 사용하여 가스화 하였다. draft tube에 공기를 주입하여 연소반응, annulus 구역에 수증기를 주입하여 가스화하여 연소반응에서 생성된 열을 annulus 에 공급하였다. 반응기온도와 석탄주입량에 따라 H$_2$, CO 및 발열량이 증가하였으나 공기의 유량증가에 따른 H$_2$, CO는 감소하고 $CO_2$ 는 증가하였으며 발열량은 감소하였다.

• Journal of the Korean Vacuum Society
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• v.6 no.4
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• pp.298-307
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• 1997

TDS(Thermal Desorption Spectroscopy)system, for diagnosis of CRT manufacturing process, was designed and constructed. Outgassings and thermal desorptions from the part or materials of CRT can be measured and analysed with this system at various temperatures. The system is consisted of 3 parts, vacuum chamber and pumping system with variable conductance, sample heating stages & their controller, and outgassing measurement devices, like as ion gauge or quadrupole mass spectrometer. The ultimate pressure of the system was under $1{\times}10^{-7}$ Pa. With the variable conductance system, the effective pumping speed of the chamber could be controlled from sub l/s to 100 l/s. The effective pumping speed values were determined by dynamic flow measurement principle. The temperatures and ramp rate of sample were controlled by tungsten heater and PID controller up to 600℃ within ±1℃ difference to setting value. Ion gauge & QMS were calibrated for quantitative measurements. Some examples of TDS measurement data and application on the CRT process analysis were shown.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.14 no.11
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• pp.5317-5322
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• 2013

This study presents a prediction method for heat transfer performance of a gas cooler of $CO_2$ heat pump using ${\epsilon}$-NTU method, and compared the results with the experimental data from the open literature. The heat transfer rate, refrigerant side outlet temperature and water side outlet temperature were calculated by using EES(Engineering Equation Solver)program in multi-tube-in-tube type $CO_2$ heat pump gas cooler. Analysis was performed in two methods : The first method performed without dividing into the test section by applying an analysis of the mean properties(mean analysis). The second method, tube length divided into 50 sections, was applied to the local properties(local analysis). From the present study, a good agreement at the local analysis was obtained between the analytical and experimental results by 0.3~1.1%, 1.31~1.88% and 3.12~5.18% for heat transfer rate, water and refrigerant side outlet temperatures, respectively.