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There is no applicable existing standard for the determination of safety characteristics for hybrid mixtures. While developing a new standard in a joint research project in Germany first results from parameter studies led to a standard procedure that can be adopted by laboratories that are already testing dusts in the so called 20L-sphere with as little additional effort as necessary. In fact, one of the main objectives of this research project was to keep modifications and adjustments from the generally accepted dust testing procedures as easy and minimal as possible so as to limit potential deviations from one laboratory to another.
In this first round robin test on hybrid mixtures ever, with methane as gas component and a specific corn starch as dust sample, the practicality of the whole procedure, the scattering of the results and the deviation between the testing apparatuses is investigated. This paper summarizes the experimental procedure adopted and objectives of the first round-robin phase involving three of the four original German companies, plus volunteering laboratories from Australia, Belgium, Czech Republic, France, Poland and P.R. China. The results will have an impact on the new standard and may lead to robust data for later simulation purposes.
The hybrid mixture of combustible dusts and flammable gases/vapours widely exist in various industries, including mining, petrochemical, metallurgical, textile and pharmaceutical. It may pose a higher explosion risk than gas/vapor or dust/mist explosions since the hybrid explosions can still be initiated even though both the gas and the dust concentration are lower than their lower explosion limit (LEL) values. Understanding the explosion threat of hybrid mixtures not only contributes to the inherent safety and sustainability of industrial process design, but promotes the efficiency of loss prevention and mitigation. To date, however, there is no test standard with reliable explosion criteria available to determine the safety parameters of all types of hybrid mixture explosions, nor the flame propagation and quenching mechanism or theoretical explanation behind these parameters. This review presents a state-of-the-art overview of the comprehensive understanding of hybrid mixture explosions mainly in an experimental study level; thereby, the main limitations and challenges to be faced are explored. The discussed main contents include the experimental measurement for the safety parameters of hybrid mixtures (i.e., explosion sensitivity and severity parameters) via typical test apparatuses, explosion regime and criterion of hybrid mixtures, the detailed flame propagation/quenching characteristics behind the explosion severities/sensitivities of hybrid mixtures. This work aims to summarize the essential basics of experimental studies, and to provide the perspectives based on the current research gaps to understand the explosion hazards of hybrid mixtures in-depth.
In this study, 19 experiments were conducted with 25 pouch cells of NMC cathode to investigate thermal runaway and the release of gases from lithium-ion batteries (LIBs). Single cells, double cells, and a four-cell battery stack were forced to undergo thermal runaway inside an air-tight reactor vessel with a volume of 100 dm3 . The study involved two series of tests with two types of ignition sources. In the Series 1 tests, a heating plug was used to initiate thermal runaway in LIBs in the ranges of 80–89% and 90–100% SOC. In the Series 2 tests, a heating plate was used to trigger thermal runaway in LIBs in the ranges of 30–50%, 80–89%, and 90–100% SOC. Thermal runaway started at an onset temperature of 344 ± 5 K and 345 K for the Series 1 tests and from 393 ± 36 K to 487 ± 10 K for the Series 2 tests. Peak reaction temperatures ranged between 642 K and 1184 K, while the maximum pressures observed were between 1.2 bar and 7.28 bar. Thermal runaway induced explosion of the cells and lead to a rate of temperature increase greater than 10 K/s. The amounts of gases released from the LIBs were calculated from pressures and temperatures measured in the reactor.
Then, the gas composition was analyzed using a Fourier transform infrared (FTIR) spectrometer. The highest gaseous production was achieved at a range of 90–100% SOC and higher battery capacities 72 L, 1.8 L/Ah (Series 1, battery stack) and 103 L, 3.2 L/Ah (Series 2, 32 Ah cell)). Among the gases analyzed, the concentration of gaseous emissions such as C2H4 , CH4 , and C2H6 increased at a higher cell capacity in both series of tests. The study results revealed characteristic variations of thermal behavior with respect to the type of ignition source used.
Bei der Erstellung von brandschutztechnischen Nachweisen für Industriebauten werden häufig Ingenieurmethoden des Brandschutzes genutzt. Dazu zählen die Modellierung und Berechnung von Brandszenarien mittels numerischer Strömungsmechanik (computational fluid dynamics, CFD). In dieser Arbeit wurde ein auf numerischer Strömungs- und Strukturmechanik basierendes Verfahren zur brandschutztechnischen Bemessung von Bauteilen am Beispiel einer Industriehalle angewendet. Instationäre Temperaturverläufe aus der Heißgasschicht dienten dabei als Eingangswerte für die Bauteilberechnung. Aus den Ergebnissen wurde die äquivalente Branddauer berechnet, mit der die rechnerisch erforderlichen Feuerwiderstandsdauern der Bauteile bestimmt werden konnte.
Anwendung und Vergleich von Verfahren zur Berechnung der äquivalenten Branddauer im Industriebau
(2013)
Die äquivalente Branddauer tä wird zur Bestimmung der Feuerwiderstandsdauer erftp von Bauteilen in Industriebauten verwendet. Die Berechnung erfolgt bislang auf der Grundlage des normativenAnsatzes nach DIN 18230 (Verfahren I) und gilt im Zusammenhang mit der Muster-Industriebaurichtlinie (M IndBauRL). Im Rahmen von brandschutztechnischen Nachweisen für Industriebauten ist es ebenfalls möglich, die äquivalente Branddauer unter Anwendung numerischer Methoden zu berechnen (Verfahren II). Die Anwendung solcher Ingenieurmethoden des Brandschutzes ermöglichen die Berücksichtigung komplexer Gebäudegeometrien und Ventialtionsbedingungen sowie lokaler Brandwirkungen auf Bauteile infolge inhomogener Brandlastverteilungen.
Am Beispiel einer Industriehalle werden die Verfahren I und II angewendet und die Ergebnisse gegenübergestellt.
Approaches towards a generic methodology for storage of hazardous energy carriers and waste products
(2013)
Energy carriers – either conventional or 'new' ones – have to be provided in large amounts to meet the requirements of permanent availability and reliable supply of electricity. Depending on their state of aggregation, energy carriers are either stored in large masses (if solid or liquid) or at elevated pressures (if gaseous). Both impose the hazard of large-scale fire, in the latter case additionally the danger of explosion or unintended release. Very similar hazards occur for wastes. Solid wastes are present in large masses and only a small part is recycled. Most of the solid wastes are used in energy conversion. The main gaseous waste is CO2. During capturing also the hazard of unintended release exists. In this article, existing approaches for safe storage and fire prevention are discussed and a generic methodology is outlined. This methodology consists of the following steps:
gaining knowledge about the behaviour of the material stored (reactivity, thermal stability, etc.),
assessing the environmental conditions for the storage site (neighbourhood, safety distances, etc.),
assessment of prospective consequences of an incident and
development of individual loss prevention conceptions.
All steps require both experimental testing and theoretical considerations about accident scenarios as integral parts of the methodology.
Gegenstand des Aufsatzes ist die experimentelle Untersuchung der Auswirkungen verschiedener Zündquellen sowie der Systembeschaffenheit auf das Brandverhalten EPS-basierter Wärmedämm-Verbundsysteme (WDVS). Dazu wurden Brände ausgewertet, die mit EPS-basierten WDVS in Verbindung stehen. Ergebnis dieser Auswertung war, dass nicht wie bisher angenommen der Brand in dem Gebäude (z. B. der Wohnungsbrand), sondern vielmehr der Brand außerhalb des Gebäudes, insbesondere der des Abfallbehälters, das häufigste und kritischste Brandszenario für EPS-basierte WDVS darstellt. Daraufhin wurden an der BAM Bundesanstalt für Materialforschung und -prüfung Brandversuche in der Single Burning Item-Prüfeinrichtung (SBI) an nicht intakten EPS-basierten WDVS-Ausschnitten durchgeführt. Mit zunehmender Beschädigungsgröße und -tiefe stieg die vom System freigesetzte Wärmefreisetzungsrate an. Zusätzlich werden Brandversuche eines Sockelbrandszenarios mit einer abfallbehälteräquivalenten Brandlast vorgestellt. Aus den Brandversuchen werden Empfehlungen zur Verbesserung der Systemsicherheit abgeleitet.-------------------------------------------------------------------------------------------------------------------------------------------------
The influence of different ignition sources and conditions of the systems on the fire behaviour of external thermal insulating systems (ETICS) have been investigated experimentally. As a basis of the investigations real cases with EPS based ETICS have been analysed. The analysis showed that the fire in front of the building is the most common and critical fire scenario for these systems. These fires are often caused by waste containers. This result contradicts the former common assumption that the fire inside the building is the most critical fire scenario for ETICS. Intermediate scale experiments in the Single Burning Item (SBI) test apparatus have been performed at BAM with ETICS specimens. The render of the systems was partially damaged. The measured heat release rate of the specimens increased significantly with size and depths of the damages. Additionally results of large scale experiments with a waste container equivalent ignition source are presented and recommendations to enhance fire safety of these systems are given.
Es werden die Untersuchungsergebnisse für ein geeignetes Zündkriterium zur Bestimmung von Explosionsgrenzen bei nichtatmosphärischen Bedingungen vorgestellt. Dazu wurden für Anfangsdrücke bis 20 bar Zündversuche an den Explosionsgrenzen von CHL/Luft-, CaHg/Luft-, H2/Luft- und NHs/Luft-Gemischen in einem Autoklav mit Sichtscheibe durchgeführt. In der Auswertung wurden visuelle Zündkriterien und ein Druckschwellenkriterium miteinander verglichen. Weiterhin wurden Untersuchungen zum erforderlichen Mindesvolumen des Explosionsgefäßes in Abhängigkeit des Anfangsdrucks durchgeführt. Dazu wurden jeweils Zündversuche mit demselben Gemisch aus CH4 und Luft bei Anfangsdrücken bis 50 bar in Volumina zwischen 0,2 dm3 und 6,0 dm3 durchgeführt.
Nanotechnologie gilt als die Wachstumsbranche der nächsten Jahrzehnte. Nicht zuletzt ist diese Entwicklung den veränderten Eigenschaften der Materialien im Nanometerbereich zuzuschreiben. Das anders geartete Verhalten solcher Stoffe und die daraus ableitbare Unkenntnis über die Interaktion dieser Materialien mit ihrer Umgebung erfordert zur Risikoabschätzung eine intensive Auseinandersetzung mit der Thematik. Aufgrund von Erfahrungen mit Stäuben mit Partikelgrößen im Mikrometerbereich ist bekannt, dass Stoffe mit abnehmender Partikelgröße kritischer einzustufen sind, da ihre Explosionsheftigkeit und Zündempfindlichkeit durch die Zunahme der reaktiven Oberfläche des Staubs zunimmt. Nachfolgend werden Ergebnisse von Versuchen mit nanoskalig hergestellten Metallstäuben präsentiert. Der Fokus dieser Studie lag darauf, möglichst das kritischste Brand- und Explosionsverhalten solcher Stäube zu erfassen.
CFD modeling approach of smoke toxicity and opacity for flaming and non-flaming combustion processes
(2016)
Current engineer’s methods of fire safety design include various approaches to calculate the fire Propagation and smoke spread in buildings by means of computational fluid dynamics (CFD). Because of the increased computational capacity, CFD is commonly used for prediction of time-dependent safety parameters such as critical temperature, smoke layer height, rescue times, distributions of chemical products, and smoke toxicity and visibility. The analysis of smoke components with CFD is particularly complex, because the composition of the fire gases and also the smoke quantities depends on material properties and also on ambient and burning conditions. Oxygen concentrations and the temperature distribution in the compartment affect smoke production and smoke gas toxicity qualitatively and quantitatively. For safety designs,
it can be necessary to take these influences into account. Current smoke models in CFD often use a constant smoke yield that does not vary with different fire conditions. If smoke gas toxicity is considered, a simple approach with the focus on carbon monoxide is often used. On the basis of a large set of experimental data, a numerical smoke model has been developed. The developed numerical smoke model includes optical properties, production, and toxic potential of smoke under different conditions. For the setup of the numerical model, experimental data were used for calculation of chemical components and evaluation of smoke toxicity under different combustion conditions. Therefore, averaged reaction equations were developed from experimental measurements and implemented in ANSYS CFX 14.0.