M. Lucas , N. Salaün , G. Atanga , B. Wilkins , S. Martin-Barbaz
{"title":"Experiments and simulations of large scale hydrogen-nitrogen-air gas explosions for nuclear and hydrogen safety applications","authors":"M. Lucas , N. Salaün , G. Atanga , B. Wilkins , S. Martin-Barbaz","doi":"10.1016/j.jlp.2024.105531","DOIUrl":null,"url":null,"abstract":"<div><div>Hydrogen safety is a general concern because of the high reactivity of hydrogen compared to hydrocarbon-based fuels. The strength of knowledge in risk assessments related to the physical phenomena and the ability of models to predict the consequence of accidental releases is a key aspect for the safe implementation of new technologies. Nuclear safety considers the possibility of accidental leakages of hydrogen gas and subsequent explosion events in risk analysis. In many configurations, the considered gaseous streams involve a large fraction of nitrogen gas mixed with hydrogen. This work presents the results of an extensive large scale explosion experimental campaign for hydrogen-nitrogen-air mixtures. The experiments were performed in a 50 m<sup>3</sup> vessel at Gexcon's test site in Bergen, Norway. Covering a nitrogen fraction range from 0 vol% to 80 vol%, equivalence ratio range from 0.8 to 1.3 and exploring four distinct congestion levels, this research provides comprehensive insights into the complex interplay of variables influencing explosion behaviours in such mixtures. The experiments are simulated in the FLACS-CFD software to inform about the current level of conservatism of the predictions for engineering application purposes. The study shows the reduced overpressure with nitrogen added to hydrogen mixtures and supports the use of FLACS-CFD-based risk analysis for hydrogen-nitrogen scenarios.</div></div>","PeriodicalId":16291,"journal":{"name":"Journal of Loss Prevention in The Process Industries","volume":"94 ","pages":"Article 105531"},"PeriodicalIF":3.6000,"publicationDate":"2024-12-11","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Journal of Loss Prevention in The Process Industries","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0950423024002894","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 0
Abstract
Hydrogen safety is a general concern because of the high reactivity of hydrogen compared to hydrocarbon-based fuels. The strength of knowledge in risk assessments related to the physical phenomena and the ability of models to predict the consequence of accidental releases is a key aspect for the safe implementation of new technologies. Nuclear safety considers the possibility of accidental leakages of hydrogen gas and subsequent explosion events in risk analysis. In many configurations, the considered gaseous streams involve a large fraction of nitrogen gas mixed with hydrogen. This work presents the results of an extensive large scale explosion experimental campaign for hydrogen-nitrogen-air mixtures. The experiments were performed in a 50 m3 vessel at Gexcon's test site in Bergen, Norway. Covering a nitrogen fraction range from 0 vol% to 80 vol%, equivalence ratio range from 0.8 to 1.3 and exploring four distinct congestion levels, this research provides comprehensive insights into the complex interplay of variables influencing explosion behaviours in such mixtures. The experiments are simulated in the FLACS-CFD software to inform about the current level of conservatism of the predictions for engineering application purposes. The study shows the reduced overpressure with nitrogen added to hydrogen mixtures and supports the use of FLACS-CFD-based risk analysis for hydrogen-nitrogen scenarios.
期刊介绍:
The broad scope of the journal is process safety. Process safety is defined as the prevention and mitigation of process-related injuries and damage arising from process incidents involving fire, explosion and toxic release. Such undesired events occur in the process industries during the use, storage, manufacture, handling, and transportation of highly hazardous chemicals.