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Im Vortrag werden zum einen sicherheitstechnische Aspekte bei der Herstellung von Gasgemischen aus geringen Anteilen an Lachgas und brennbaren Gasen diskutiert. Zum anderen werden allgemein Vorgehensweisen und Berechnungsmethoden zur sicherheitstechnischen Beurteilung der Herstellung von Gasgemischen mit brennbaren und oxidierenden Komponenten vorgestellt.
Es werden im Vortrag die verschiedenen Arten der Elektrolyse kurz vorgestellt sowie die Entwicklung der Elektrolysetechnologie. Danach wird ein Überblick über die aktuell wesentlichen sicherheitstechnischen Herausforderungen gegeben. Im zweiten Teil werden die sicherheitstechnische Eigenschaften von Wasserstoff charakterisiert. Im dritten Teil werden wesentliche Gefährdungsszenarien beim Betrieb von Elektrolyseanlagen gezeigt und ein Überblick über Regelwerke und Standards gegeben. Im letzten Teil werden drei reale Unfallszenarien aus der Praxis diskutiert.
In this lecture the safety related properties of hydrogen and hydrogen mixtures and explosion protection measures are shown and compared with other fuel gases. Measures for primary explosion protection (avoiding flammable mixtures), secondary explosion protection (avoiding ignition sources) and constructive explosion protection (mitigating the consequences of explosions) when handling hydrogen and hydrogen mixtures are presented.
The Joint European Summer School JESS 2022 addresses these issues by offering high quality graduate level courses on selected topics of vehicle technology, innovation & business development, safe handling of hydrogen, and modelling. The course content is tailored to the needs of a diverse audience: newcomers to the field, experienced students, and young professionals working at the forefront of fuel cell and hydrogen applications.
This is a digital lecture on Explosion Protection for Hydrogen Applications. It was designed in context with the project "KICstartH2 Accelerating Sustainable Hydrogen Uptake Through Innovation and Education" and integrated in a teaching module of the University of Birmingham. It is divided in five parts: Introduction, Avoiding Explosive Mixtures, Avoiding Ignition Sources, Mitigation of Consequences and Summary & Comparison.
Im Vortrag wird auf die sicherheitstechnische Beurteilung in Hinblick auf den Explosionsschutz bei der Herstellung und Füllung von Gasgemischen mit brennbaren und mit oxidierenden Komponenten eingegangen. Anhand von Beispielen werden u.a. Vorgehensweisen und Berechnungsmethoden beschrieben, anhand derer beurteilt werden kann, ob Gasgemische überhaupt sicher hergestellt werden können und in welcher Reihenfolge die Komponenten zur sicheren Herstellung der Gemische gefüllt werden sollten.
In this presentation the current focus areas of the competence centre H2Safety@BAM are shown. The fields of competence include “Material properties and compatibility”, “Process and plant safety”, “Component testing, component safety and approval” as well as “Sensors, analytics and certified reference Materials. Moreover, the cross-cutting activities regarding “Education and training” and the testing possibilities and planed test facilities at the Test Site for Technical Safety (BAM TTS) are presented.
The introduction of hydrogen as a safe energy carrier needs a robust knowledge base, tools for the design and safety assessment of hydrogen technologies built on it, and an internationally harmonized set of standards and regulations. Many of the innovative technologies imply hydrogen at high pressures and/or cryogenic temperatures, with which private users come into contact for the first time in distributed applications. In order to avoid over-conservative, expensive safety solutions, while at the same time demonstrating the usability and safety of hydrogen applications and maintaining acceptance for the technology, safety research must also keep pace with, or better yet anticipate, trends in technological development. Thus, this overview article describes not only the current state of knowledge and technology regarding hydrogen safety, but also its further development.
In this presentation the results of the Project HySpark are shown. Mechanical impacts are among the important possible ignition sources to be considered in explosion protection. Hydrogen is particularly prone to be ignited by mechanical impacts compared to natural gas. The effectivity of mechanical impacts as ignition source is dependent from different parameters. In this work the effectivity of impacts as an ignition source for hydrogen containing atmospheres was studied experimentally depending on the inhomogeneous material pairing of the impact. Moreover it was studied, how the effectivity of mechanical impacts as ignition source changes when hydrogen is added to natural gas.
In this study, experimental determination and modelling investigations for the explosion regions of 1,3-dioxolane/inert gas/N2O and 1,3-dioxolane/inert gas/air mixtures were carried out and compared. The experimental measurements were carried out at 338 K and atmospheric pressure according to EN1839 method T using the inert gases N2, CO2, He and Ar. The results showed that the ratio of the lower explosion limit in N2O (LELN2O) to the lower explosion limit in air (LELair) is 0.52 and the ratio of the maximum oxygen content in air (MOCair) to the limiting oxidizer fraction in nitrous oxide (LOFN2O) is 0.36 ± 0.02 independent of the inert gas. When comparing the inert gas amount at the apex based on the pure oxidizing component, which is O2 in case of air, N2O-containing mixtures need less inert gas to reach the limiting oxidizer quantity whereas the efficiency of inert gases is in the same order. The coefficients of nitrogen equivalency however were found to differ to some extent. The explosion regions of 1,3-dioxolane/inert gas/oxidizer mixtures were modelled using the calculated adiabatic flame temperature profile (CAFTP) method as well as corrected adiabatic flame temperatures. The results indicate good agreement with experimental data for CO2, N2 and Ar- containing mixtures. The noticeable deviations that occur when He is the inert gas are due to the lacking transport data of that mixture.
