• Proceedings of the KIEE Conference
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• 2015.07a
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• pp.1513-1514
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• 2015

전력설비가 열화, 서지에 의해 절연이 파괴되었을 경우 밀폐기기 경우 폭발, 화재를 일으킴으로써 일반인에게 피해를 입히거나 인근 설비로 파급이 확대될 가능성이 있다. 최근 전력설비는 대용량화 추세인 반면 콤팩트 사이즈를 요구하고 있어 절연문제로 인한 폭발 가능성은 더욱 커지고 있다. 이러한 전력설비의 폭발을 방지하고 피해확대를 줄이기 위해 방압변, 순간압력상승 방지장치 등이 설치되고 있으나, 예방에는 한계가 있다. 이에 최근, 국외를 중심으로 전력기기 특히, 지상설치기기의 안전성 확보를 위해 고속투입 접지스위치(Arc Eliminator)를 개발하여 설치 의무화를 고려하고 있다.

• Proceedings of the Korean Powder Metallurgy Institute Conference
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• 2003.04a
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• pp.34-34
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• 2003

전기설()폭발(Electric Wire Explosion)법은 고밀도 전류를 금속와이어에 인가시키면 저항 발열에 의해서 금속와이어가 빠르게 가열되고, 수$\mu$sec 이내에 초기체적에 비해 2~3배나 팽창한 후 폭발하는 현상을 이용하여 나노분말을 제조하는 방법으로써, 다른 제조방법에 비해 값싼 비용으로 1~50$\mu$sec의 짧은 시간동안 극히 높은 온도($10^4~10^6K$)에 도달하기 때문에, 와이어 전체가 동시에 기화하여 원재료의 조성을 갖는 분말의 합성이 가능하며, 공급되는 에너지와 시간, 챔버의 용적과 압력을 제어함으로써 평균 분말 크기를 조절할 수 있다는 잇점이 있다. 또한, 금속 와이어 주위의 분위기를 조절함으로써 금속나노분말뿐만 아리나 산화물$\cdot$질화물$\cdot$탄화물 분말, 합금 분말, 화학적 화합물이나 복합재료 나노분말들을 만들 수 있어서 여러 산업분야에 대한 응용이 크게 기대되고 있다. 본 연구에서는 전기선()폭발 챔버(Fig. 1) 와 최대 20kV까지 제어 가능한 고출력 펄스 전원장치를 자체 제작하고, 이를 이용하여 은(Ag)나노분말 합성에 대한 실험을 행하였다. 이렇게 제조된 분말은 SEM, XRD, PSA, BET 등을 이용하여 비교분석 하였다.

• Proceedings of the Korean Society of Disaster Information Conference
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• 2022.10a
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• pp.385-386
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• 2022

본 연구는 방폭지역에서 정전기를 측정하는 설비 (EST:Electrostatic Transmitter), 측정 된 정전기를 저감시키는 설비(EES:Electrostatic Elimination System), 방폭지역에서 인체 정전기를 제거시키는 설비(방폭 디지털 제전봉)를 통한 비방폭구역에서 사용되는 정전기 측정장비와의 비교를 통하여 극히 제한적인 Basic Design(온도/압력/속 도/유량)으로 인한 설계나 장치 등 변경 등을 반영하여 방폭지역에대한 근본적인 문제점을 도출 제거할수 있는 방안을 마련했으며 기존 사용되었던 비방폭지역의 정전기 제거 시스템을 보완한 방폭지역의 정전기 화재폭발 예방 기술을 적용하였다.

• Transactions of the Korean Society of Mechanical Engineers A
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• v.20 no.3
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• pp.825-831
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• 1996

Using the two-dimensional hydrocode HI-DYNA2D, a calculation on the explosive selding of dissimilar plates(Steel Titanium) was made for the pressure, temperature, velocity and impact ingles adjacent to the collision point during the welding process. The FEM result indicates that optimal stand-off distance of initially parallel set-up is 3-5mm for various values of the explosive thickness. The calculation shows that when the explosive thickness is around 30mm, the temperature of welding point which is strongly related to the metallic jet formation is 2, 000-3, 500K for the given stand-off distance.

• Journal of the Korean Institute of Gas
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• v.9 no.2 s.27
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• pp.1-7
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• 2005

The thermochemical parameters for safe handling, storage, transport, operation and process design of flammable substances are explosive limit, flash point, autoignition temperature, minimum oxygen concentration, heat of combustion etc.. Explosive limit and autoignition temperature are the major physical properties used to determine the fire and explosion hazards of the flammable substances. Explosive limit and autoignition temperature of methane fur LNG process safety were investigated. By using the literatures data, the lower and upper explosive limits of methane recommended 4.8 vol$\%$ and 16 vol$\%$, respectively. Also autoignition temperatures of methane with ignition sources recommended $540^{\circ}C$ at the electrically heated cruicible furnace (the whole surface heating) and recommended about $1000^{\circ}C$ in the local hot surface. The new equations for predicting the temperature dependence and the pressure dependence of the lower explosive limits for methane are proposed. The values calculated by the proposed equations were a good agreement with the literature data.

• Journal of the Korean Institute of Gas
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• v.18 no.4
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• pp.21-26
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• 2014

In this study, the explosion characteristic of aluminium powders have been investigated as a function of particle size using by a 20 L dust explosion apparatus (K$\ddot{u}$hner). The tested aluminium particle sizes were the volume mean diameter of 16, 33 and $88{\mu}m$. The lower explosion limit increases gradually with the increasing of dust particle diameter, respectively 40, 60, $125g/m^3$ in mean diameter of 16, 33 and $88{\mu}m$. Also the increase in particle size for each aluminum dusts was found to cause an decrease in explosion pressure and Kst of dust explosion index, and a increase in the lower explosion concentration. Research results may have important implications for aluminum powders utilization and safety operation.

• Journal of the Korean Institute of Gas
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• v.26 no.6
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• pp.65-75
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• 2022

Recently, the possibility of fire and explosion due to hydrogen leakage and the resulting risk are increasing since the operating pressure of the electrolysis increases. This study performed the hazardous area classification in accordance with KS C IEC 60079-10-1 and KGS GC101 in consideration of the general operating conditions of the electrolysis. In addition, in order to achieve a To Non-hazardous, an appropriate ventilation rate was estimated to maintain a concentration of less than 25 % of the lower explosive limit. As a result, it was reviewed that the electrolysis is classified as an hazardous area when only natural ventilation is applied, and a huge amount of ventilation is required to classify it as a non-hazardous area.

• Journal of the Computational Structural Engineering Institute of Korea
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• v.31 no.5
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• pp.235-241
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• 2018

The internal pressure is a critical parameter for designing a pressure vessel. The static pressure that a pressure vessel must withstand is usually determined according to the various codes and standards with simple formula or numerical simulations considering the geometric parameters such as diameter and thickness of a vessel. However, there is no specific codes or technical standards we can use practically for designing of pressure vessels which have to endure the detonation pressure. Detonation pressure is a kind of dynamic pressure which causes an impulsive pressure on the vessel wall in a extremely short time duration. In addition, it is known that the magnitude of reflected pressure at the vessel wall due to the explosion can be over twice the incident pressure. Therefore, if we only consider the reflected pressure, the design of the pressure vessel can be too conservative from the economical point of view. In this study, we suggest a practical method to evaluate the magnitude of maximum allowable pressure that the pressure vessel can withstand against the detonation inside a vessel. As an example to validate the proposed method, we consider the pressure vessel containing hydrogen gas.

• Journal of the Society of Naval Architects of Korea
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• v.55 no.5
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• pp.379-384
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• 2018

This study showed the development process of structural design method of BHB(Blast Hardened Bulkhead) which are applicable in preliminary design stage. In the previous 1st report, the simplified structural scantling equations of BHB were formulated theoretically using the modified plastic hinge method supplemented by considering the membrane effects due to large plastic deformation. And the scantling methodology of plate thickness and section area of stiffeners of the curtain plate type BHB was dealt with. In the present 2nd report, derivation process of the correction factors which can adjust the developed scantling equations considering the uncertainties contained in the design parameters was introduced. Considering the actual BHB structures of 3 warship, the correction factors for the developed scantling equations for curtain plate type BHB were derived. Finally the applicability, validity of them and the strategy of future improvement were considered.

• Proceedings of the Korean Society of Propulsion Engineers Conference
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• 2011.04a
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• pp.457-462
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• 2011

This paper presents a numerical investigation of deflagration to detonation transition (DDT) induced by shock wave and flame interaction in ethylene-air mixtures. Also shows the change of DDT triggering time by wall cooling effect. A model is consisted of the compressible reactive Navier-Stokes equations. And the effect of viscosity, thermal conduction, molecular diffusion, chemical reaction and wall effect are included. Using this model, the generation of hot spot by repeated shock and flame interaction, occurrence of detonation, and wall cooling effect of detonation confining boundaries are studied.