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Safety risk modeling and major accidents analysis of hydrogen and natural gas releases: A comprehensive risk analysis framework

机译:氢气和天然气释放的安全风险建模和重大事故分析:全面的风险分析框架

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摘要

The potential safety risk of hydrogen production is often the most important element to achieve authority approval and public acceptance. Safe application of hydrogen, especially in a large scale, will require adopting adequate risk control, which requires investment on reliable risk analysis methodology. In the present study, first of all, a reliable and comprehensive safety risk analysis methodology was developed for a hydrogen production plant in an oil refinery, that consists of two qualitative methods: Hazard and Operability (HAZOP) and Preliminary Risk Analysis (PRA), a hybrid method: Event Tree Analysis (ETA) and a quantitative method: Quantitative Risk Assessment (QRA) along with a risk and consequence simulator. A HAZOP study along with the PRA technique was used for determining main hazardous sources and carrying out a qualitative risk analysis. The incident outcomes of the identified high risk scenarios were modeled using the PHAST 6.7 simulator and the frequencies of the initial events and incident outcomes were calculated using risk assessment data directory of International Association Oil & Gas Producers (OGP) and ETA, respectively. Finally, the vulnerability areas of the incident outcomes were determined and the societal risk of hydrogen plant was shown using a 'Frequency vs. Number of fatality' graph, known as 'F-N' curves. The findings show that the maximum vulnerability distance is caused by the vapor cloud explosion (280 m, at 0.01 bar) and the jet fire (275 m, at 4 kW/m(2)), respectively. The societal risk of the plant fell in the As Low As Reasonable Practical (ALARP) and intolerable regions according to the F-N curve of UK HSE (Health, Safety Executive) The reformer were the highest and the heat exchanger was the lowest contributor to the total risk. Therefore, the ALARP principle should be applied to indicate the appropriate ways to reduce risks and, for the intolerable risks, the system must be modified structurally, functionally, or organizationally. Copyright (C) 2015, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
机译:氢生产的潜在安全风险通常是获得当局批准和公众接受的最重要因素。安全使用氢气,尤其是大规模使用氢气,将需要采取适当的风险控制措施,这需要对可靠的风险分析方法进行投资。在本研究中,首先,为炼油厂的氢气生产厂开发了可靠且全面的安全风险分析方法,该方法包括两种定性方法:危害与可操作性(HAZOP)和初步风险分析(PRA),混合方法:事件树分析(ETA)和定量方法:定量风险评估(QRA)以及风险和后果模拟器。 HAZOP研究与PRA技术一起用于确定主要危险源并进行定性风险分析。使用PHAST 6.7模拟器对识别出的高风险情景的事件结果进行建模,并分别使用国际石油和天然气生产商协会(OGP)和ETA的风险评估数据目录来计算初始事件和事件结果的频率。最后,确定了事故结果的脆弱性区域,并使用“频率与死亡人数”图(称为“ F-N”曲线)显示了制氢厂的社会风险。研究结果表明,最大脆弱距离分别是由蒸气云爆炸(280 m,0.01 bar)和喷射火(275 m,4 kW / m(2))引起的。根据英国HSE(健康,安全执行官)的FN曲线,该工厂的社会风险在合理可行的最低限度(ALARP)和难以忍受的区域内下降。重整器最高,热交换器最低,占总风险的百分比。风险。因此,应该使用ALARP原则来指示降低风险的适当方法,并且对于无法忍受的风险,必须在结构,功能或组织上对系统进行修改。 Hydrogen Energy Publications,LLC版权所有(C)2015。由Elsevier Ltd.出版。保留所有权利。

著录项

  • 来源
    《International journal of hydrogen energy》 |2015年第39期|13653-13663|共11页
  • 作者单位

    Hamadan Univ Med Sci, Sch Publ Hlth, Dept Occupat Hlth Engn, Hamadan, Iran|Hamadan Univ Med Sci, Res Ctr Hlth Sci, Hamadan, Iran;

    Hamadan Univ Med Sci, Sch Publ Hlth, Dept Occupat Hlth Engn, Hamadan, Iran|Hamadan Univ Med Sci, Res Ctr Hlth Sci, Hamadan, Iran|Hamadan Univ Med Sci, Student Res Ctr, Hamadan, Iran;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Risk modeling; Risk assessment; QRA; Hydrogen safety; Consequence; HAZOP;

    机译:风险建模;风险评估;QRA;氢安全性;后果;HAZOP;
  • 入库时间 2022-08-18 00:21:41

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