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Eingeladener Vortrag
- nein (84)
Im Vortrag werden die für den Betrieb der Erdgasnetze relevanten Kenngrößen des Explosionsschutzes erläutert. Der Einfluss von Wasserstoffeinspeisung auf diese Kenngrößen wird dargestellt und diskutiert. Die Stoffdaten der Erdgas-Wasserstoff-Gemische sind im Rahmen eines von der BG-ETEM geförderten Vorhabens in der BAM gemessen worden. Basis dieser Messungen waren in Europa harmonisierte Normen.
Zudem sind mit Hilfe von numerischen Methoden berechnete explosionsgefährdete Bereiche von Erdgas-Wasserstoff-Gemischen im Vergleich zum reinen Erdgas betrachtet worden. Der Vortrag gibt weiterhin Hinweise auf Auswirkungen von Wasserstoffzusätzen auf Gaswarngeräte.
Der Beitrag behandelt die sicherheitstechnischen Kenngrößen (STK) für Gase und Gasgemische. Es wird gezeigt, wie STK für den Explosionsschutz experimentell ermittelt und bewertet werden. Insbesondere wird auf die Abhängigkeiten der STK von Druck, Temperatur und Art des Inertgases eingegangen. Anhand von sogenannten Explosionsdiagrammen werden Gasgemische bewertet und Berechnungsverfahren für Explosionsgrenzen, Entzündbarkeit und Oxidationspotential vorgestellt.
Der Beitrag gibt eine Einführung in den Explossionsschutz. Neben den Schnittstellen zu benachbarten Gebieten wie Anlagensicherheit und Arbeitsschutz werden die Arten möglicher Explosionen in der Prozessindustrie und die Prinzipien des Explosionsschutzes erläutert. Einige Störfälle der letzten Jahre werden diskutiert.
One of the fundamental principles of the UN-GHS (Globally Harmonized System of Classification and Labelling of Chemicals) is that all hazards of a chemical should be assigned and communicated. There is no general prioritization of hazards in the sense that certain hazard classes are not applicable if another one has been assigned. In contrast to health and environmental hazards, there are physical or chemical factors which preclude certain combinations of physical hazard classes. So far, there is no common understanding as to which combinations are relevant and which not. For example, should a pyrophoric liquid be classified as flammable liquid in addition, or is this redundant and unnecessary? In the course of the implementation of the GHS by countries or sectors and the actual application by industry all over the world, such questions become more and more important.
This publication systematically discusses all combinations of the UN-GHS physical hazard classes and assesses them with regard to the relevance of possible simultaneous assignment to a chemical. For many of the combinations an unambiguous decision based on theGHS alone is not possible, thus confirming that the question which physical hazard classes might be assigned simultaneously to a chemical is not trivial. As one more milestone on the path to a globally harmonized system for the classification of hazardous chemicals, this should be discussed and ultimately solved on a global basis. It is the hope that this publication might serve as an impetus for such discussions.
For evaluation of explosion scenarios in closed systems involving the mildly flammable refrigerants R1234yf, R1234ze and R32 dependent on the ignition energy, ignitions were carried out in a closed autoclave. A newly developed ignition system was used, which allows generating electric arcs with defined energies in a range between 3 J and 1000 J. The lower explosion limit of R32 decreases with increasing ignition energy. R32-explosions can be more severe than explosions involving highly flammable substances.
However, in case of R1234yf and R1234ze, the ignition energy had to be increased to more than 100 J and more than 500 J to detect explosions in the closed system at all, although flame Propagation phenomena can already be observed if these substances are ignited with much weaker ignition sources in open glass tubes. The explosions were very mild with these substances.
ISO 10156:2010 contains a test method and a calculation method for flammability of gases and gas mixtures for the selection of cylinder valve outlets. The calculation method is used also to classify gas mixtures according to the national and international dangerous goods and dangerous substances regulations, e.g. according to the UN Recommendations on the Transport of Dangerous Goods (UN TDG) and the Globally Harmonized System of Classification and Labelling of Chemicals (UN GHS). The calculation method for gas mixtures requires substance parameters of the single components. These are the coefficients for the fire potential (Tci) and for inerting ability, the so-called nitrogen equivalence (Kk), which have been estimated conservatively by means of flammability data.
BAM checked Tci and Kk values of ISO 10156:1996 using three-component diagrams (Flammable gas-Inert-Air) of the CHEMSAFE® database. The experimental fundamentals and the principles of the calculation method are summarized in this paper. The revised data for Tci and Kk values were adopted in the tables of ISO 10156:2010.
Furthermore, subcategorization of flammable gases has been proposed by a UN working group and shall be implemented in the GHS in the meantime. The subcategorization requires the lower flammability limit (LFL) as an additional indicator. Therefore, a test method and a calculation method for LFL were proposed by BAM and have been implemented in the new draft of ISO/CD 10156:2016.
The calculation method for gas mixtures is based on Le Chatelier’s rule and was extended by using the Kk values for inert components in the mixture. The calculated LFLs of methane-inert gas mixtures were compared with experimental values for different types of inert gases. It could be shown that calculated LFLs are in good agreement with experimental values if the Kk values derived from three-component flammability diagrams are used. Although using the Kk values of ISO 10156:2010 leads to higher deviations, the results are still on the safe side.
In der Präsentation werden die aktuellen Änderungen im Globally Harmonized System (GHS) zur Klassifizierung der Gase bezüglich ihrer physikalisch-chemischen Gefahren gezeigt. Die Anbindung an europäisches und nationales Recht wird erläutert. Bei den Gasen und Gasgemischen wird insbesondere auf die neuen Klassifizierungsverfahren für pyrophore Eigenschaften und auf die neue Unterteilung der entzündbaren Gase eingegangen.
The presentation will discuss the difference between EU and US standards for the determination of explosion (flammability) limits and limiting oxygen concentration. Small differences observed in measured values can be traced back to the different test apparatuses and criteria. The discrepancies can be much greater in the case of limiting oxygen concentration because of the high amount of inert gases and the corresponding low laminar burning velocities. The paper describes some examples and the influence of the chosen criteria on the results. The European and US standards use the criteria of flame propagation in open test vessels and of pressure rise in closed ones. The examples discussed show that flame propagation is still possible at very small pressure rise values, as observed much below the pressure rise criterion of usual standards. However, flame propagation in a process plant can cause an accident or explosion and must be avoided. Therefore, the flame propagation criterion is recommended to be used in chemical safety engineering. The European safety database CHEMSAFE contains expertevaluated safety data for cases where the determination method and criteria are known. Flammability characteristics based on the pressure rise criterion may suffice in certain cases, e.g. for explosion protection in closed vessels without any connecting pipes.
Im Vortrag wird die Klassifizierung von Gasen und Gasgemischen nach CLP-Verordnung bei Anwendung der neuen Fassung der ISO/DIS 10156:2016 gezeigt. Dabei werden sowohl experimentelle Bestimmungsverfahren als auch Berechnungsverfahren für die Entzündbarkeit von Gasgemischen erläutert. Die physikalisch-chemischen Grundlagen der Berechnungsverfahren werden diskutiert.
The safety characteristics of flammable gases and liquids are required when identifying potentially explosive mixtures and taking appropriate actions concerning explosion protection. Examples are given in this review of the safe handling and evaluation of hazards during the processing, storage, transport, and disposal of flammable liquids and gases. The CHEMSAFE database is presented as a reliable source of safety characteristic data, and ist new open-access version is introduced. CHEMSAFE currently contains assessed properties for about 3000 flammable liquids, gases and mixtures. The lack of a broad experimental foundation in the extensive field of non-atmospheric conditions shows the need for further investigation and standardization. This review summarizes experimental evidence and estimation methods for safety characteristic data under non-atmospheric conditions pointing out current limitations. Suggestions for pre-normative research on safety data under nonatmospheric conditions are given.