• 한국가스학회지
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• 제16권1호
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• pp.15-21
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• 2012

수소가스의 제트 누출에 의한 확산, 화재, 그리고 폭발에 의한 위험 범위를 분석하고, 안전거리 기준을 설정하기 위한 위험거리를 확산, 화재, 그리고 폭발에 대한 단순한 예측 식들을 제시하였다. 핀홀에 의한 누출과 같은 소량 수소가스 누출속도에 있어서 피해거리는 제트누출 확산에 의한 피해거리가 제트화재에 의한 피해거리보다 크며, 압력의 제곱근에 그리고 누출 홀의 직경에 비례하고 이는 수 십 미터에 이른다. 배관의 완전 파손 또는 저장 탱크의 큰 홀 발생과 같은 대량의 수소가스 누출속도에서는 제트화재의 피해거리가 개방공간의 가스운 폭발에 의한 피해거리보다 크며, 수 백 미터에 이른다. 수소충전소와 건물과의 최소이격거리 즉 안전거리 설정 기준을 대량 수소가스누출 사고시나리오를 기반으로 한다면, 도심지에 수소충전소는 안전거리 기준을 만족시키기 어려울 것이다. 따라서 대량의 수소가스 누출사고를 안전장치들을 통하여 예방하고, 안전거리 기준을 소량의 수소가스누출사고 기준으로 설정 할 수 있다. 그러나 대량누출 가능성이 있는 경우 학교와 병원 등 인구밀집 건물은 수 백 미터의 안전거리를 유지하여야 한다.

• 한국수소및신에너지학회논문집
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• 제32권5호
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• pp.299-307
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• 2021

In order to expand the supply of hydrogen vehicles, the first thing to be done is to build an infrastructure to supply hydrogen. There are fixed and mobile types of hydrogen refueling stations that can supply hydrogen. Mobile hydrogen refueling stations have the advantage of supplying hydrogen to two or three areas, so the introduction of mobile hydrogen refueling stations is considered at the initial stage of hydrogen vehicle dissemination. However, mobile hydrogen refueling stations have greater risks than fixed hydrogen refueling stations due to the hazard associated with movement and intensive installation of facilities in vehicle, so stricter design standards to lower the risk must be applied. Therefore, in this study, basic data for establishing safety standards for mobile hydrogen refueling stations were proposed by suggesting improvements such as the location of emergency shutoff valves, the number of gas detectors etc., using HAZOP analysis.

• Nuclear Engineering and Technology
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• 제47권1호
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• pp.26-32
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• 2015

During the course of a severe accident in a light water nuclear reactor, large amounts of hydrogen can be generated and released into the containment during reactor core degradation. Additional burnable gases [hydrogen ($H_2$) and carbon monoxide (CO)] may be released into the containment in the corium/concrete interaction. This could subsequently raise a combustion hazard. As the Fukushima accidents revealed, hydrogen combustion can cause high pressure spikes that could challenge the reactor buildings and lead to failure of the surrounding buildings. To prevent the gas explosion hazard, most mitigation strategies adopted by European countries are based on the implementation of passive autocatalytic recombiners (PARs). Studies of representative accident sequences indicate that, despite the installation of PARs, it is difficult to prevent at all times and locations, the formation of a combustible mixture that potentially leads to local flame acceleration. Complementary research and development (R&D) projects were recently launched to understand better the phenomena associated with the combustion hazard and to address the issues highlighted after the Fukushima Daiichi events such as explosion hazard in the venting system and the potential flammable mixture migration into spaces beyond the primary containment. The expected results will be used to improve the modeling tools and methodology for hydrogen risk assessment and severe accident management guidelines. The present paper aims to present the methodology adopted by Institut de Radioprotection et de $S{\hat{u}}ret{\acute{e}}$ $Nucl{\acute{e}}aire$ to assess hydrogen risk in nuclear power plants, in particular French nuclear power plants, the open issues, and the ongoing R&D programs related to hydrogen distribution, mitigation, and combustion.

• 한국가스학회지
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• 제9권1호
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• pp.9-15
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• 2005

수소는 온실효과 가스배출을 저감하기 위한 다양한 연소장치에 이용되는 에너지 전달체로 가장 중요한 물질로 인식되고 있다. 그러나 에너지 전달체로 이용되기 위해서는 수소를 이용하는 장치와 관련된 안전의 문제점이 충분히 조사하고 이해되어야 한다. 따라서 누출된 수소가스와 공기의 혼합 가스운의 확산거동과 점화 가능성에 대한 연구가 필요하다. 본 연구에서는 대기 조건에 따라 대기 중에서 수소가스의 확산거동을 부력을 고려하여 살펴보았다. 풍하방향으로 위험범위는 대기안정도 및 풍속이 증가할수록 증가하게 되고, 지면에서 가스농도는 수소가스의 부력 때문에 거의 제로이다. 그러므로 누출된 수소가스 운의 점화 가능성은 낮고, 화재$\cdot$폭발 위험성은 타 연료가스 즉 부탄 및 프로판에 비하여 낮은 것으로 사료된다.

• 한국수소및신에너지학회논문집
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• 제28권2호
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• pp.166-173
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• 2017

For commercialization of hydrogen refuelling station (HRS), we need to reduce the clearance distance for jet fire in the real entities in the HRS. Thus, we revisited the current regulations of clearance distance for jet fire in the law. The law in korea has been set up by replica of japan, not by our own scientific basis. Recently, sandia lab developed Hydrogen Risk Assessment Model (HyRAM) tools and we simulated a series of circumstances such as 10 to 850 bar with several leak hole sizes. In 850 bar with 10 mm diameter hole leak cases, it shows $4,981kW/m^2$ at 12 m separation from leak source and $1,774kW/m^2$ at 17 m separation from leak source. In 850 bar with 1 mm diameter leak hole, it shows $0.102kW/m^2$ at 12 m separation and $0.044kW/m^2$ at 17 m separation. Current law may be acceptable with 1 mm hole size with 850 bar.

• 한국수소및신에너지학회논문집
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• 제31권1호
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• pp.65-72
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• 2020

In this study, the purpose is to identify the risks of the facilities of packaged hydrogen stations. As a risk identification method, failure mode & effect analysis (FMEA), a qualitative risk assessment, was used to analyze failure mode and effects of component of each facility. The analysis criteria were used to derive the risk priority number (RPN) using the 5-point method according to severity, incidence, and detectability. The study analyzed a total of 141 components of 23 types that can be identified on the design of the packaged hydrogen filling station. As a result, 683 types of failures and their causes and effects were identified. and the RPN was number of a total of 1,485. Of these, 10 failure types with a RPN value of 40 or more were deemed necessary. In addition, a list of failure types with a severity score of 5 was identified and analyzed.

• 한국수소및신에너지학회논문집
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• 제35권4호
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• pp.460-467
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• 2024

As the hydrogen economy receives attention, much research has been conducted on water electrolysis that can produce green hydrogen. After investigating the various risk factors that exist in the alkaline water electrolysis process through hazard and operability study and job safety analysis, which are risk assessments, measures to ensure safety were prepared and made into a manual. Possible risks that could occur during various emergency stop situations and operations were identified, and leakage of potassium hydroxide (KOH) and hydrogen used as electrolyte appeared to be the main risk. If you utilize a risk assessment for the relevant equipment when writing a manual, you will be able to prepare work procedures that substantially reduce risk factors.

• 한국수소및신에너지학회논문집
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• 제31권5호
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• pp.459-466
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• 2020

As the hydrogen industry grows, expansion of infrastructure for hydrogen supply is required, but the safety of hydrogen facilities is concerned due to the recent accidents at the Gangneung hydrogen tank and the Norwegian hydrogen fueling station. In this study, the damage range and impact analysis on the on-site hydrogen fueling station was conducted using Hy-KoRAM. This is a domestically developed program that adds functions based on HyRAM. Through this risk assessment, it was evaluated whether the on-site hydrogen fueling station meets international standards and suggested ways to improve safety.

• 한국수소및신에너지학회논문집
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• 제34권4호
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• pp.381-387
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• 2023

The risk assessment (safety assessment) must be performed to verify the risks during operation and installation of the hydrogen system and to ensure safe design and operation. Among them, hazard and operability study (HAZOP), a qualitative risk assessment, is most often used to discover risk factors and secure safety. However, in HAZOP performance, there is a difference in the level of evaluation results depending on the level and experience of the evaluator, and there is a high possibility that subjective results will be derived. This study aims to develop a risk factor library that can list and provide information on potential risk factors in order to solve these problems when performing HAZOP, reduce risk factors that are omitted or overlooked.

• 한국수소및신에너지학회논문집
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• 제30권1호
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• pp.29-34
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• 2019

Safety of hydrogen handling facilities is needed as supply of hydrogen cars has been expanded recently. In this study, the adequacy of safety regulations of hydrogen handling facilities and the risk of damage with hydrogen leakage were studied. The range of explosion hazard location of the hydrogen filling plant was investigated using the computational fluid dynamics (CFD) method, Explosive hazardous area is influenced by leakage type, hole size and sectional area. When the conditions of KS standard are applied, range explosive hazardous area is expanded 7.05 m, maximum. It is about 7 times larger than exceptional standard of hydrogen station. Meanwhile, distance from leakage point to 25% LEL of hydrogen is investigated 1.6 m. Considering the shape of charging hose, regulation of hydrogen station is appropriate.