• Title/Summary/Keyword: Gas Hazard

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Qualitative Hazard Analysis for LNG Gas Stations Using K-PSR Method (K-PSR을 이용한 LNG 충진소에 대한 정성적 위험성평가)

  • Ko, Jae-Wook;Lee, Jae-Min;Yoo, Jin-Hwan
    • Journal of the Korean Institute of Gas
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    • v.10 no.4 s.33
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    • pp.63-69
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    • 2006
  • With the increased interest in reducing air pollution, supply of natural gas for gas vehicles is increasing. Thus, the number of establishments of LNG and CNG stations is increasing as well. However, due to major gas accidents such as the fire and explosion accident of a Bucheon LPG station in 1998, it is difficult to establish a new station. In this research, we conducted qualitative hazard analysis fer LCNG/LNG multi-station by using the K-PSR method and proposed recommendations for hazard mitigation.

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Hazard Distance from Hydrogen Accidents (수소가스사고의 피해범위)

  • Jo, Young-Do
    • Journal of the Korean Institute of Gas
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    • v.16 no.1
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    • pp.15-21
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    • 2012
  • An analysis was completed of the hazards distance of hydrogen accidents such as jet release, jet fire, and vapor cloud explosion(VCE) of hydrogen gas, and simplified equations have been proposed to predict the hazard distances to set up safety distance by the gas dispersion, fire, and explosion following hydrogen gas release. For a small release rate of hydrogen gas, such as from a pine-hole, the hazard distance from jet dispersion is longer than that from jet fire. The hazard distance is directly proportional to the pressure raised to a half power and to the diameter of hole and up to several tens meters. For a large release rate, such as from full bore rupture of a pipeline or a large hole of storage vessel, the hazard distance from a large jet fire is longer than that from unconfined vapor cloud explosion. The hazard distance from the fire may be up to several hundred meters. Hydrogen filling station in urban area is difficult to compliance with the safety distance criterion, if the accident scenario of large hydrogen gas release is basis for setting up the safety distance, which is minimum separation distance between the station and building. Therefore, the accident of large hydrogen gas release must be prevented by using safety devices and the safety distance may be set based on the small release rate of hydrogen gas. But if there are any possibility of large release, populated building, such as school, hospital etc, should be separated several hundred meters.

Review of Hazard Test of Combustion Gas and Exhaust Temperature of Acrylic Fire Protection Paint (아크릴계 내화도료 연소가스의 유해성 평가와 배기온도에 대한 고찰)

  • Jeon, Soo-Min;Kim, Jae-Jun
    • Fire Science and Engineering
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    • v.31 no.4
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    • pp.1-6
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    • 2017
  • A fire resistance certification needs to be obtained before fire protection paint can be used in Korea. In the case of paint, the tests for certification are fire, gas hazard and bond strength. According to the hazard test standard of combustion gas, 16 mice are sacrificed every test. Therefore, there are ethical problems for the experimenter and legal problems for the laboratory. Accordingly, many alternatives are being assessed, such as combustion gas analysis, but they have not replaced animal testing yet. With gas hazard testing, the exhaust gas temperature can be measured. The property of the initial reaction of a specific fire paint can be characterized by this temperature. The purpose of this study was to consider the improvement point for a gas hazard test through comparative analysis of the exhaust temperature and the time of death of the mice.

Heat Transfer Coefficient, Heat Release and Gas Hazard Tests for Expanded Polystyrene Heat Insulating Materials with Aluminum Foil (알루미늄 호일 부착 발포 폴리스티렌 단열재의 열전도율, 열방출시험 및 가스 유해성 시험)

  • Kong, Ha-Sung
    • Journal of the Korea Safety Management & Science
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    • v.20 no.4
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    • pp.15-19
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    • 2018
  • The purpose of this study is to enhance heat insulation effect and to decrease fire hazard by attaching aluminum foil to expanded polystyrene, which is mainly used for insulating materials, to have fire retardant. The result of the test confirmed that the insulating materials, expanded polystyrene of $10kg/m^3$ and $14kg/m^3$ of density attached aluminum foil on both sides, showed 12%, 14% of improved heat transfer coefficient respectively compared to existing expanded polystyrene of the same density. Besides, they met all the standards for the testing of heat release and gas hazard. On the other hand, the one made of general expanded polystyrene could not meet the standards of the heat release test and the gas hazard test.

A Study on the Thermal Hazard and Explosion with Floating of Sanitary Feed-stuff (위생사료의 열적 위험성 및 부유 중 폭발성에 관한 연구)

  • 김정환;이한철;현성호;허윤행
    • Journal of environmental and Sanitary engineering
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    • v.13 no.2
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    • pp.82-87
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    • 1998
  • The opening temperature of emit heat, caloric value and decomposition hear were investigated by DSC & TGA in order to find the hazard of sanitary feed-stuff, also explosion hazard of dust was observed with electrical ignition after fodder dispersion by compressed air. Then opening temperature of emit heat of supporting gas. $O_{2}$ was much lower than inert gas. Ar. and caloric value increased 20. and the particle size of sanitary feed-stuff were appeared fire or explosion at 50/60 mesh and 60/80 mesh.

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A Study for Health Hazard Evaluation of Methylene Chloride Evaporated from the Tear Gas Mixture

  • Park, Seung-Hyun;Chung, Eun-Kyo;Yi, Gwang-Yong;Chung, Kwang-Jae;Shin, Jung-Ah;Lee, In-Seop
    • Safety and Health at Work
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    • v.1 no.1
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    • pp.98-101
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    • 2010
  • This study explored the health hazard of those exposed to methylene chloride by assessing its atmospheric concentration when a tear gas mixture was aerially dispersed. The concentration of methylene chloride ranged from 311.1-980.3 ppm (geometric mean, 555.8 ppm), 30 seconds after the dispersion started. However, the concentration fell rapidly to below 10 ppm after dispersion was completed. The concentration during the dispersion did not surpass the National Institute for Occupational Safety and Health 'immediately dangerous to life or health' value of 2,300 ppm, but did exceed the American Conference of Governmental Industrial Hygienists excursion limit of 250 ppm. Since methylene chloride is highly volatile (vapor pressure, 349 mmHg at $20^{\circ}C$), the post-dispersion atmospheric concentration can rise instantaneously. Moreover, the o-chlorobenzylidenemalononitrile formulation of tear gas (CS gas) is an acute upper respiratory tract irritant. Therefore, tear gas mixtures should be handled with delicate care.

Earthquake hazard and risk assessment of a typical Natural Gas Combined Cycle Power Plant (NGCCPP) control building

  • A. Can Zulfikar;Seyhan Okuyan Akcan;Ali Yesilyurt;Murat Eroz;Tolga Cimili
    • Geomechanics and Engineering
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    • v.35 no.6
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    • pp.581-591
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    • 2023
  • North Anatolian Fault Zone is tectonically active with recent earthquakes (Mw7.6 1999-Kocaeli and Mw7.2 1999-Düzce earthquakes) and it passes through Marmara region, which is highly industrialized, densely populated and economically important part of Turkey. Many power plants, located in Marmara region, are exposed to high seismic hazard. In this study, open source OpenQuake software has been used for the probabilistic earthquake hazard analysis of Marmara region and risk assessment for the specified energy facility. The SHARE project seismic zonation model has been used in the analysis with the regional sources, NGA GMPEs and site model logic trees. The earthquake hazard results have been compared with the former and existing earthquake resistant design regulations in Turkey, TSC 2007 and TBSCD 2018. In the scope of the study, the seismic hazard assessment for a typical natural gas combined cycle power plant located in Marmara region has been achieved. The seismic risk assessment has been accomplished for a typical control building located in the power plant using obtained seismic hazard results. The structural and non-structural fragility functions and a consequence model have been used in the seismic risk assessment. Based on the seismic hazard level with a 2% probability of exceedance in 50 years, considered for especially these type of critical structures, the ratios of structural and non-structural loss to the total building cost were obtained as 8.8% and 45.7%, respectively. The results of the study enable the practical seismic risk assessment of the critical facility located on different regions.

A Study on Selection Method of Hazard Evaluation Technique for Gas Industries (가스 산업 시설의 잠재위험성 평가기법 선정 방법에 관한 연구)

  • Ko J. W.;Kim J. W.
    • Journal of the Korean Institute of Gas
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    • v.8 no.4 s.25
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    • pp.70-76
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    • 2004
  • This research was for the analysis of gas industries and 12 Hazard evaluation techniques for the industries, and present the selection guideline of the techniques using 6 factors affecting them. 4 indexes & consequences of incidents into 8 characteristics. Also, combining the indexes with the selection procedure in flowchart format could reduce improper techniques and present alternatives. Also, it is used as guidelines to get safety improvement plan to gas companies.

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Development of Preliminary Hazard Ranking System for Underground Storage Tanks Using Geographic Information System (GIS) (GIS를 이용한 지하저장탱크의 위해성 예비평가체계 개발)

  • 황상일;이상훈;이동수
    • Journal of the Korean Society of Groundwater Environment
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    • v.4 no.3
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    • pp.122-129
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    • 1997
  • Spills or leaks of hazardous organic. compounds from underground storage tanks (USTs) are common contaminant sources of soil and groundwater. It would aid in managing USTs to assess and rank the potential environmental hazard posed by the USTs. Therefore, a preliminary hazard ranking system of USTs is developed in this study. The system is combined with GIS and consists of five steps: 1) selection of significant factors, 2) determination of the hierarchy of the factors. 3) determination of the weights, 4) calculation of the potential hazard, and 5) hazard assessment. The system is applied to the gas stations in Kwanak-gu, Seoul. The results indicate that the gas stations can be categorized in three groups as highly hazardous, less highly hazardous, and weakly hazardous. Seven gas stations belong to the highly hazardous group. Through the sensitivity analysis, four stations appear to possess high hazard potentials regardless of weights assigned to the factors. It appears that a user can make flexible application of the hazard ranking system with the user's experience and particular purposes. However, the system still needs validations against field survey data.

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