TY - CONF A1 - Habib, Abdel Karim A1 - Schalau, Bernd A1 - Schmidt, Dirk ED - Pierucci, S. ED - Klemes, J.J. ED - De Rademaeker, E. ED - Fabiano, B. ED - Buratti, S.S. T1 - Comparing different methods for calculating the gas dispersion N2 - When handling flammable and/or toxic liquids or gases, the gas dispersion following a release of substance is a scenario to be considered in the risk assessment to determine the lower flammability distance (LFD) and toxicity thresholds. In this work a comparison of different gas dispersion tools of varying complexity ranging from a simple Gaussian model over a boundary layer model (BLM) and a Lagrangian model to CFD (in this case ANSYS CFX v14) is presented. The BLM covers the special case of liquid releases with formation of a pool. It does not only solve the gas dispersion but also calculates the evaporating mass flow out of the pool. The simulation values are compared to each other and to experimental data resulting mainly from our own open air experiments covering the near field and carried out on the Test Site Technical Safety of BAM (BAM-TTS) for different release types (pool evaporation, gas release) and topologies. Other validation data were taken from literature and cover large scale experiments in the range of several 100 m. T2 - 14th International symposium on loss prevention and safety promotion in the process industries CY - Florence, Italy DA - 12.05.2013 KW - Gas dispersion KW - Simulation PY - 2013 SN - 978-88-95608-22-8 SN - 1974-9791 N1 - Serientitel: Chemical engineering transactions – Series title: Chemical engineering transactions IS - 31 SP - 1 EP - 6 PB - AIDIC, Associazione Italiana di Ingegneria Chimica CY - Milano AN - OPUS4-29587 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim T1 - Simulation und experimentelle Untersuchungen der Schwergasausbreitung T2 - 13. BAM/PTB-Kolloquium CY - Braunschweig, Germany DA - 2013-06-18 PY - 2013 AN - OPUS4-29773 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim T1 - VDI-Richtlinie 3783 Blatt 2, Ausbreitung von schweren Gasen T2 - LUP-Inhouse-Seminar 2014 im Regierungspräsidium Darmstadt CY - Wiesbaden, Germany DA - 2014-03-27 PY - 2014 AN - OPUS4-30467 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim T1 - Lachenverdampfung - Lachenverdunstung T2 - LUP-Inhouse-Seminar 2014 im Regierungspräsidium Darmstadt CY - Wiesbaden, Germany DA - 2014-03-27 PY - 2014 AN - OPUS4-30466 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim T1 - Bestimmung des Massenstroms T2 - LUP-Inhouse-Seminar 2014 im Regierungspräsidium Darmstadt CY - Wiesbaden, Germany DA - 2014-03-27 PY - 2014 AN - OPUS4-30465 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Habib, Abdel Karim A1 - Schalau, Bernd A1 - Schmidt, Dirk T1 - Comparing tools of varying complexity for calculating the gas dispersion N2 - When handling flammable and/or toxic liquids or gases, the gas dispersion following a release of substance is a scenario to be considered in the risk assessment to determine the lower flammability distance (LFD) and toxicity thresholds. In this work a comparison of different gas dispersion tools of varying complexity ranging from a simple Gaussian model over a boundary layer model (BLM) and a Lagrangian model to CFD (in this case ANSYS CFX v14) is presented. The BLM covers the special case of liquid releases with formation of a pool. It does not only solve the gas dispersion but also calculates the evaporating mass flow out of the pool. The simulation values are compared to each other and to experimental data resulting mainly from our own open air experiments covering the near field and carried out on the Test Site Technical Safety of BAM (BAM-TTS) for different release types (pool evaporation, gas release) and topologies. Other validation data were taken from literature and cover large scale experiments in the range of several 100 m. KW - Gas dispersion KW - Modeling KW - CFD KW - Hazard assessment KW - Gauss KW - Lagrange PY - 2014 DO - https://doi.org/10.1016/j.psep.2014.02.014 SN - 0957-5820 SN - 1744-3598 SP - 1 EP - 6(?) PB - Elsevier CY - Amsterdam AN - OPUS4-30529 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim T1 - Beurteilung verschiedener Ansätze zur Modellierung einer Lachenverdunstung im Rahmen von Störfallauswirkungsbetrachtungen T2 - DECHEMA Arbeitskreis "Auswirkung von Stoff- und Energiefreisetzungen" CY - Frankfurt am Main, Germany DA - 2010-10-01 PY - 2010 AN - OPUS4-22111 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - GEN A1 - Habib, Abdel Karim A1 - Schalau, Bernd T1 - Erforderliche Komplexität bei der Modellierung einer Lachenverdunstung im Rahmen von Störfallauswirkungsbetrachtungen T2 - 10. Fachtagung Anlagen-, Arbeits- und Umweltsicherheit CY - Köthen, Deutschland DA - 2010-11-04 KW - Verdunstung KW - Empirische Modelle KW - Experimentelle Daten KW - Anlagensicherheit KW - Umweltschutz KW - Sicherheitstechnik KW - Explosionsschutz PY - 2010 SN - 978-3-89746-119-2 IS - M-01 / Paper 8338 SP - 1 EP - 21 CY - Frankfurt/M. AN - OPUS4-22349 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim T1 - Erforderliche Komplexität bei der Modellierung einer Lachenverdunstung im Rahmen von Störfallauswirkungsbetrachtungen T2 - 10. Fachtagung Anlagen-, Arbeits- und Umweltschutz CY - Köthen, Germany DA - 2010-11-04 PY - 2010 AN - OPUS4-22321 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim T1 - Calculation of the gas dispersion out of an evaporating pool T2 - 8th European congress of chemical engineering CY - Berlin, Germany DA - 2011-09-25 PY - 2011 AN - OPUS4-24427 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim T1 - Gasausbreitung bei Stofffreisetzung aus einer Lache T2 - ProcessNet Jahrestagung 2007 CY - Aachen, Germany DA - 2007-10-16 PY - 2007 AN - OPUS4-16045 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Schalau, Bernd A1 - Habib, Abdel Karim T1 - Praktische Beispiele und Erfahrungen zu Störfallauswirkungsbetrachtungen T2 - 17. Fachgespräch Anlagensicherheit 2008 CY - Bad Dürkheim, Germany DA - 2008-05-06 PY - 2008 AN - OPUS4-17403 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim T1 - Instationäre Berechnung der Lachenverdunstung und -verdampfung mittels eines Grenzschichtverfahrens T2 - 9. Fachtagung "Anlagen-, Arbeits- und Umweltsicherheit" CY - Köthen, Germany DA - 2008-11-06 PY - 2008 AN - OPUS4-18224 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim A1 - Schalau, Bernd A1 - Acikalin, Hatice Aydan A1 - Steinbach, J. T1 - Instationäre Berechnung der Lachenverdunstung mittels eines Grenzschichtverfahrens T2 - ProcessNet Arbeitsauschuss "Sicherheitsgerechtes Auslegen von Chemieanlagen" und "Auswirkungen von Stoff- und Energiefreisetzungen" CY - Frankfurt am Main, Germany DA - 2008-11-19 PY - 2008 AN - OPUS4-18354 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - GEN A1 - Schmidt, Dirk A1 - Schalau, Bernd A1 - Acikalin, Hatice Aydan A1 - Habib, Abdel Karim T1 - Vergleich von Methoden zur Quantifizierung von Risiken verfahrenstechnischer Anlagen T2 - 8. Fachtagung "Anlagen-, Arbeits- und Umweltsicherheit" CY - Köthen, Deutschland DA - 2006-11-09 KW - Risiko KW - QRA KW - Purple Book KW - ARAMIS KW - LOPA KW - Fehlerbaum KW - Gefährdungsermittlung KW - Auswirkungsbetrachtungen KW - Häufigkeiten KW - Datenbank PY - 2006 SN - 3-936415-48-X SP - 1 EP - 14(?) PB - VDI, Hallescher Bezirksverein CY - Halle AN - OPUS4-12745 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim T1 - Berechnung der Lachenverdunstung mit einem Grenzschichtverfahren T2 - ProcessNet-Arbeitsausschuss "Auswirkungen von Stoff- und Energiefreisetzungen" CY - Frankfurt am Main, Germany DA - 2007-03-15 PY - 2007 AN - OPUS4-14601 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Kluge, Martin A1 - Habib, Abdel Karim A1 - van Wingerden, Kees ED - Beyer, Michael ED - Lucassen, Arnas T1 - Large-scale tests to investigate the consequences of exposing cryogenic storage vessels containing liquid hydrogen to a fire load N2 - Large Scale Experiments have been performed to determine whether a storage vessel containing liquid hydrogen (LH2) and caught in a fire engulfing the vessel can result in a BLEVE (Boiling Liquid Expanding Vapour Explosion) and if so its consequences. The tests were performed at the Test Site Technical Safety of the Bundesanstalt für Materialforschung und –prüfung (BAM) in Germany at the Hydrogen Test Area (H2TA) within a research cooperation between BAM and Gexcon as part of the SH2IFT program. Three tests were performed using double-walled vacuum insulated vessels of 1 m3 volume. The cylindrical Vessels differed in orientation (horizontal or vertical) and the insulation material used (perlite or multi-layer insulation (MLI)). The degree of filling of the vessels was approximately 35-40 % in each of the tests performed. The fire load was provided by a propane fed burner-system positioned under the storage vessel and designed to give a homogeneous fire load. The conditions in the vessel (temperatures and pressure) as well as external effects (heat radiation, blast waves, flame ball development and fragmentation) were measured. All vessels were equipped with K-type thermocouples at several locations at the inner and outer vessel shell. The pressure inside the inner vessel and in the space between the inner and outer vessels (vacuum pressure) was measured. Bolometers were used to measure the heat radiation generated by both the propane fire and that generated by a possible fireball/BLEVE. To measure blast generated by the vessel burst/BLEVEs blast pencils were positioned at up to three locations. Further several cameras were used to monitor the events: normal cameras, infrared (IR)-cameras, high-speed cameras also on board of an UAV. Two of these vessels, a horizontal and a vertical vessel both insulated with perlite withstood the fire loading for 1 hour 20 minutes and 4 hours respectively without catastrophic failure. A horizontal vessel insulated with MLI failed by bursting after 1 hour and 6 minutes resulting in a fireball, fragments, and blast wave. T2 - 14th International Symposium on Hazards, Prevention and Mitigation of Industrial Explosions CY - Braunschweig, Germany DA - 11.07.2022 KW - Prevention KW - Industrial explosions KW - BLEVE KW - LH2 KW - Fire ball KW - Fragments PY - 2022 DO - https://doi.org/10.7795/810.20221124 SP - 168 EP - 181 AN - OPUS4-59440 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - GEN A1 - Habib, Abdel Karim A1 - Schalau, Bernd A1 - Acikalin, Hatice Aydan A1 - Steinbach, J. T1 - Instationäre Berechnung der Lachenverdunstung und -verdampfung mittels eines Grenzschichtverfahrens T2 - 9. Fachtagung "Anlagen-, Arbeits- und Umweltsicherheit" CY - Köthen, Deutschland DA - 2008-11-06 KW - Quantitative Risikoanalyse KW - Störfall-Verordnung PY - 2008 SN - 978-3-89746-099-7 IS - I 02 SP - 1 EP - 13 PB - VDI, Hallescher Bezirksverein CY - Halle AN - OPUS4-18411 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Habib, Abdel Karim A1 - Schalau, Bernd A1 - Acikalin, Hatice Aydan A1 - Steinbach, J. T1 - Transient calculation of the boundary layer flow over spills N2 - In this work, results of numerical simulations and experimental investigations of the mass flow from evaporating liquid pools are presented. Numerical simulations are based on the boundary layer equations combined with an algebraic turbulence model. The experiments were carried out on open air test sites within flat and very rough topographies, at different temperatures with ethanol and cyclohexane as the evaporating liquids. An experimental investigation of the influence of the topography on the evaporation of a liquid pool is conducted. The results of the simulation are validated against experimental data from the open air experiments. Furthermore, a comparison of the simulation results with empirical prediction models has been made. KW - Evaporation KW - Mass transfer KW - Modeling KW - Simulation PY - 2009 DO - https://doi.org/10.1002/ceat.200800527 SN - 0930-7516 SN - 1521-4125 VL - 32 IS - 2 SP - 306 EP - 311 PB - Wiley-VCH Verl. CY - Weinheim AN - OPUS4-18747 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Habib, Abdel Karim A1 - Schalau, Bernd A1 - Zeps, Robert A1 - Frank, S. T1 - Vergleich von Modellen zur Simulation einer Lachenverdunstung N2 - Betreiber, deren Betriebsbereiche den erweiterten Pflichten der Störfall-Verordnung unterliegen, müssen einen Sicherheitsbericht anfertigen, in dem Szenarien möglicher Störfälle beschrieben sind. Im Rahmen dieser Störfallauswirkungsbetrachtungen sind auch oftmals Szenarien zu untersuchen, bei denen Flüssigkeiten freigesetzt werden. Der Verdunstungsmassenstrom aus der Flüssigkeitslache ist der maßgebliche Eingangsparameter für die Gasausbreitungsberechnung mit der die Gefährdungsradien ermittelt werden. Für die Berechnung des Verdunstungsmassenstroms werden meist empirische Modelle eingesetzt. Anhand von experimentellen Daten aus eigenen Freilandversuchen werden die Leistungsfähigkeit sowie die Grenzen des Anwendungsbereichs diverser bekannter Modelle untersucht. KW - Verdunstung KW - Empirische Modelle KW - Experimentelle Daten PY - 2010 SN - 1434-9728 SN - 1436-4948 SN - 0372-2457 SN - 0376-1185 VL - 51 IS - 1/2 SP - 22 EP - 27 PB - Springer-VDI-Verl. CY - Düsseldorf AN - OPUS4-20873 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim T1 - Lachenverdampfung - Lachenverdunstung T2 - LUP-Inhouse-Seminar 2014 im Regierungspräsidium Darmstadt CY - Frankfurt/Main DA - 2014-12-16 PY - 2014 AN - OPUS4-32761 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim T1 - Ermittlung von Massenströmen T2 - LUP-Inhouse-Seminar 2014 im Regierungspräsidium Darmstadt CY - Frankfurt/Main DA - 2014-12-16 PY - 2014 AN - OPUS4-32760 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim T1 - Schwergasausbreitung T2 - LUP-Inhouse-Seminar 2014 im Regierungspräsidium Darmstadt CY - Frankfurt/Main DA - 2014-12-16 PY - 2014 AN - OPUS4-32759 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Kluge, Martin A1 - Habib, Abdel Karim A1 - van Wingerden, Kees T1 - Unterfeuerung von Flüssigwassersttofftanks - Topologie eines kritischen Behälterversagens N2 - In einer Versuchsreihe im Realmaßstab wurden drei Flüssigwasserstofftanks (LH2) unterfeuert. Hierbei sollte unter anderem geklärt werden, ob es, analog zu druckverflüssigten Gasen, zu einem BLEVE (Boiling Liquid Expanding Vapor Cloud Explosion) kommen kann. Die Experimente wurden auf dem Testareal Wasserstoffsicherheit des Testgeländes Technische Sicherheit der Bundesanstalt für Materialforschung und -prüfung (BAM-TTS) im Rahmen einer Forschungskooperation zwischen der BAM und Gexcon, als Teil des SH2IFT-Programms durchgeführt. Es handelte sich um doppelwandige, vakuumisolierte Tanks von 1 m³ Volumen. Die zylindrischen Tanks unterschieden sich durch ihre Ausrichtung (horizontal oder vertikal) und das verwendete Isoliermaterial (Perlit oder Mehrschichtisolierung (MLI). Der Füllgrad der Tanks betrug bei jedem der durchgeführten Tests etwa 35-40 %. Die Brandlast wurde homogen durch ein propangasbetriebenes Brennersystem erzeugt. Gemessen wurden die Bedingungen im Behälter (Temperaturen und Druck) sowie äußere Randbedingungen und Auswirkungen beim Versagen (Wärmestrahlung, Druckwellen, Flammenballentwicklung und Fragmentierung). Mit Bolometern wurde die Wärmestrahlung gemessen, die sowohl durch das Propanfeuer als auch durch einen möglichen Feuerball/BLEVE erzeugt wurde. Zur Messung der durch das Bersten von Behältern/BLEVEs erzeugten Druckwellen wurden sog. Pencil-Probes verwendet. Des Weiteren wurden mehrere Kameras zur Überwachung der Experimente eingesetzt: Normalbildkameras, Infrarot (IR)-Kameras und Hochgeschwindigkeitskameras, sowohl bodengestützt als auch mittels einer Drohne. Zwei der untersuchten Tanks, ein horizontaler und der vertikale, die beide mit Perlit isoliert waren, hielten der Brandbelastung stand, ohne dass es zu einem Behälterversagen kam. Der mit MLI isolierte horizontale Behälter barst nach 1 Stunde und 6 Minuten und erzeugte dabei einen Feuerball, Trümmerflug und eine Druckwelle. Neben der Beschreibung der Auswirkungen eines kritischen Versagens eines LH2-Tanks sind weitere Ziele der Arbeit die Identifizierung kritischer Behälterzustände sowie die Erstellung eines umfassendes Datensatzes der Trümmer des geborstenen Tanks. Die größten Abstände für kritische Abstände ergaben sich durch Fragmentwurf. Hier sollen 3D-Scans für die Verwendung in CAD und FEM Anwendungen bereitgestellt werden. Umfassende Daten zu den Fragmentwurfweiten, -massen und -positionen wurden bereits publiziert. Damit soll die Voraussetzung geschaffen werden, um vorhandene Wurfweitenmodelle, die bisher nur für einschalige Behälter konzipiert wurden auf ihre Eignung für mehrschalige Behälter zu überprüfen oder mögliche Anpassungen anhand der realen Daten vornehmen zu können. Zudem wurde damit begonnen die nicht geborstenen Tanks zu vermessen und zu zerlegen, um u.a. die Perlit-Schüttung auf Beeinträchtigungen durch den Transport und die Unterfeuerung zu untersuchen. T2 - Magdeburg-Köthener Brandschutz- und Sicherheitstagung 2024 CY - Magdeburg, Germany DA - 14.03.2024 KW - LH2 KW - Flüssigwasserstoff KW - Bleve KW - Tank KW - Bersten KW - Unterfeuerung PY - 2024 SN - 978-3-948749-42-2 SP - 117 EP - 126 CY - Magdeburg AN - OPUS4-59711 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim T1 - Hazard Assessment and reality – or - The difference between theory and practice is greater in practice than in theory. N2 - For hazard Assessment purposes we need models to predict what would happen in case of an accident. The challenge in hazard assessment consists not only in choosing the right model, but beforehand to define the correct scenario .If models can be found for the physical effect to be simulated, the validation of these models is the next challenge. Even if experimental data can be found it should always be checked, if these data are correct, even if in general experimental data are considered as “failsafe” or “the absolute truth”. T2 - EPSC Webinar CY - Online Meeting DA - 27.11.2020 KW - Hasard assessment KW - Gas dispersion KW - Modeling KW - Release PY - 2020 AN - OPUS4-52676 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim T1 - Experimental investigation of the consequences of release of liquified hydrogen onto and under water N2 - Large-scale experiments have been performed to investigate the possible consequences of realistic amounts of liquified hydrogen (LH2) encountering water. The tests were performed at the Test Site Technical Safety of the Bundesanstalt für Materialforschung und –prüfung (BAM) in Horstwalde, Germany. The experiments aimed at investigating that upon contact with water, the evaporation rate of LH2 can be that high that physical explosions or even rapid phase transitions (RPTs), could occur. RPTs can generate air and underwater blast pressures which could damage adjacent plant or structures (which has been demonstrated when releasing LNG). The tests were performed in a 10 m x 10 x 1.5 m basin filled with water. LH2 releases with mass flows ranging from approximately 0.25 kg/s to approximately 0.8 kg/s were established releasing directly from a trailer carrying LH2. The LH2 was released through a 46 m long flexible double vacuum insulated transfer line (inner diameter 39 mm). The releases occurred from a height of 50 cm above the water surface pointing downwards, 30 cm under the water surface pointing downwards and 30 cm under the water surface pointing along the water surface. The release system allowed for an initial phase to release flashed LH2 into the air before redirecting the flow towards the water surface for liquid release. A thermocouple inserted near the nozzle is used to indicate the presence of LH2 at the nozzle. The nozzle could be moved up and downwards relative to the water surface and also moved into the water. The release system was purged with helium before starting a release. A mouthpiece at the end of the release line as well as a manually operated valve at the trailer were used to vary the release rate. The temperature of the water and the air was measured at multiple locations. The temperature of the air was also measured at H2 concentration probe locations. In addition, the temperature in the filling line was measured (1 at the outlet and 1 further down into the filling line). The pressure in the filling line was also measured at 3 locations, one located directly at the outlet. The release rate was determined based on the weight loss rate of the road tanker. To this end the trailer was placed onto load cells. Special blast pressure sensors were used to measure the shock waves generated by the rapid evaporation or other phenomena both in the water and in the air. At several locations the gas concentration development in time was measured. Heat radiation was measured at 3 distances from the point of release. High speed, Infra-Red (IR) cameras and normal cameras were used to record events and to follow the gas cloud behaviour in time. This includes cameras mounted on a drone and an underwater camera. Two weather stations were used to measure wind speed, wind direction, temperature and humidity during all tests performed. All investigated release configurations resulted in a very chaotic LH2-water mixing zone, causing considerable evaporation and resulting in minor over pressures. The main phenomenon observed was an ignition of the released gas cloud, resulting in significant blast wave overpressures and heat radiation to the surroundings. The ignition occurred in all under-water releases and in about 90 % of the releases above the water surface. The location of the ignition occurred in free air at some distance from the instrumentation and release location. T2 - 14th International Symposium on Hazards, Prevention, and Mitigation of Industrial Explosions (ISHPMIE) CY - Braunschweig, Germany DA - 11.07.2022 KW - Liquid Hydrogen KW - LH2 KW - RPT KW - Rapid Phase Transition KW - Release PY - 2022 AN - OPUS4-55356 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Mazzola, T. A1 - Hanna, S. A1 - Chang, J. A1 - Bradley, S. A1 - Meris, R. A1 - Simpson, S. A1 - Miner, S. A1 - Gant, S. A1 - Weil, J. A1 - Harper, M. A1 - Nikmo, J. A1 - Kukkonen, J. A1 - Lacome, J.-M. A1 - Nibart, M. A1 - Björnham, O. A1 - Khajehnajafi, S. A1 - Habib, Abdel Karim A1 - Armand, P. A1 - Bauer, T. A1 - Fabbri, L. A1 - Spicer, T. A1 - Ek, N. T1 - Results of comparisons of the predictions of 17 dense gas dispersion models with observations from the Jack Rabbit II chlorine field experiment N2 - The Jack Rabbit II (JR II) chlorine field trials in 2015 and 2016 involved nine 5–20 ton releases of pressurized liquefied chlorine from a tank mounted 1 m above a broad flat desert sand surface. A model comparison study was initiated, where 17 widely-used dense-gas dispersion models were run by scientists in seven countries. Predictions were submitted following specified formats, using specified emissions and meteorology inputs. To compare with the model predictions, sets of observations were defined for the arc-maximum 1–3 s averaged concentrations (arc max C) and for cloud widths and heights (to 20 ppm and 200 ppm contours) at distances from 0.2 to 11.0 km from the release. The initial focus is on the three field trials (1, 6, and 7) that have the highest observed concentrations and that have detailed emissions information. It is found that these models are able to satisfactorily simulate (generally within a factor of two) the observed arc max C's and their variation with downwind distance at this flat desert site. At each downwind distance, the scatter in the arc max C predictions covers about 1 ½ orders of magnitude, but the observed arc max C is within the range of the predictions. The median of the cloud width predictions is about 50% larger than the observed value for the three trials. The median of the cloud height predictions is within about 10% of the observed value. For both cloud width and/or height, there are a few models with large (factor of 3 or higher) overpredictions. Of the 17 models, when compared to observations, there is a core group of 5 or 6 with consistently (across all three trials and all distances) less mean error and scatter in their predictions of arc max C and cloud width and height. However, as a group, the 17 models are performing adequately (using the “factor of two” rule of thumb). An important caveat is that, at the JR II desert site, chlorine deposition is minimal. At a site with vegetation and/or organic-rich soil, the effects of removal of chlorine by deposition are expected to be significant. KW - Jack rabbit II KW - Chlorine KW - Field experiment KW - Dense gas dispersion KW - Model evaluation PY - 2021 DO - https://doi.org/10.1016/j.atmosenv.2020.117887 VL - 244 SP - 1 EP - 14 PB - Elsevier B.V. AN - OPUS4-60740 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Bernardy, Christopher A1 - Habib, Abdel Karim A1 - Kluge, Martin A1 - Schalau, Bernd A1 - Kant, Hanjo A1 - Schulze, Marcel A1 - Orchini, Alessandro T1 - Sicherheitstechnische Untersuchungen von Wasserstoff Freistrahlflammen bei Hochdruck im Realmaßstab N2 - Wasserstoff als Energieträger gewinnt zunehmend an Bedeutung. Die Untersuchung von Störfallauswirkungen mit Wasserstoff rückt somit stärker in den Fokus. Da Wasserstoff meist unter Druck gelagert und transportiert wird, ist ein zu betrachtendes Szenario die Freisetzung aus einer Leckage mit anschließender Zündung. Die daraus resultierende Freistrahlflamme (Jet Flame) muss hinsichtlich der in die Umgebung emittierten Wärmestrahlung charakterisiert werden. In der Literatur existieren bereits verschiedene Modelle, welche jedoch vermehrt auf Daten aus Kohlenwasserstoffflammen mit geringem Impuls basieren. Zur Überprüfung dieser Modelle wird im Zuge des BAM internen H2 Jet Flame Projektes die sicherheitstechnische Untersuchung von impulsbehafteten Wasserstoff Freistrahlflammen vorgenommen. Hierfür finden Versuche im Realmaßstab auf dem Testgelände Technische Sicherheit der BAM (BAM-TTS) statt. Gegenstand der Untersuchungen ist die Beurteilung der Auswirkungen von realistischen Freisetzungsszenarien hinsichtlich der Flammengeometrie und der freigesetzten Wärmestrahlung. Dabei werden Parameter wie Freisetzungswinkel, Leckagedurchmesser (z.Zt. 1 mm bis 10 mm), Druck (z.Zt. bis max. 250 bar) und Massenstrom (bis max. 0,5 kg/s) variiert. Zusätzlich können auch Einflüsse wie Art der Zündung, Zündort sowie Zündung mit zeitlichem Verzug untersucht werden. Gewonnene Erkenntnisse werden mit den Ergebnissen bereits vorhandener Modelle verglichen und diese im Bedarfsfall weiterentwickelt. Insbesondere wird der Fokus auf die Modellierung der freigesetzten Wärmestrahlung von Wasserstoffflammen gelegt. Herausforderung dabei stellt die IR-Vermessung und Modellierung von Sichtmodellen der Flammen dar. Die Visualisierung der Flammengeometrie wird mit Hilfe mehrerer Infrarot Kamerasystemen (aus mindestens zwei Blickwinkeln) vorgenommen. Bisherige Messungen, die in der Literatur zu finden sind, basieren meist auf instationären Auströmbedingungen. Der hier verwendete Versuchsaufbau ermöglicht ein stationäres Ausströmen für mehrere Minuten und somit eine direkte Vergleichbarkeit mit den existierenden (stationären) Modellen. Weiterhin ist der Versuchsstand umrüstbar für Vergleichsmessungen mit Kohlenwasserstoffen (Methan etc.) sowie Mischungen aus Wasserstoff und Kohlenwasserstoffen. T2 - Magdeburg-Köthener Brandschutz- und Sicherheitstagung 2024 CY - Magdeburg, Germany DA - 14.03.2024 KW - Wärmestrahlung KW - Wassersoff KW - Freistrahlflamme PY - 2024 SN - 978-3-948749-42-2 SP - 137 EP - 146 CY - Magdeburg AN - OPUS4-59912 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Schalau, Bernd A1 - Habib, Abdel Karim T1 - Lachenverdunstung bei höheren Dampfdrücken N2 - Bei vielen Störfallauswirkungsbetrachtungen, insbesondere im Rahmen des Leitfadens KAS-18, ist die Betrachtung einer Lachenverdunstung bzw. –verdampfung erforderlich. Für die Berechnung des Verdunstungsmassenstroms werden üblicherweise empirische Modelle eingesetzt. Ein grundsätzlicher Unterschiedzwischen den Modellen ist die Berücksichtigung des Dampfdrucks der freigesetzten Flüssigkeit. In einigenModellen wird eine lineare, in anderen eine logarithmische Abhängigkeit angenommen. Dies führt bei Stoffen mit einer Siedetemperatur, die nur geringfügig über der Umgebungstemperatur liegt, oder bei der Freisetzung von heißen Flüssigkeiten zu gravierenden Unterschieden in den berechneten Massenströmen. Ein weiteres Problem ergibt sich bei der Betrachtung einer Lachenverdunstung in einem Lager. Da der mit den empirischen Modellen berechnete Verdunstungsmassenstrom proportional zur Strömungsgeschwindigkeit ist, und in einem Lager diese als gering angenommen werden kann, stellt sich die Frage, ob die Modelle für dieses Szenario anwendbar sind. Durch eigene experimentelle Untersuchungen im Freifeld, in einem Lagerraum und in einer Lagerhalle wurde eine Grundlage für die Beantwortung dieser Fragen geschaffen. PY - 2015 SN - 2191-0073 VL - 5 IS - 9 SP - 22 EP - 27 PB - Springer-VDI-Verl. CY - Düsseldorf AN - OPUS4-34312 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim T1 - Untersuchung der Freistzung von Flüssigwasserstoff auf und unter Wasser N2 - In einer Reihe von Experimenten wurden die möglichen Folgen der Freisetzung von verflüssigtem Wasserstoff (LH2) auf, bzw. unter Wasser untersucht. Die Experimente zielten darauf ab, eine unbeabsichtigte Freisetzung von LH2 (z.B. durch Schlauchabriss) insbesondere bei der Betankung eines Schiffes zu simulieren. Für verflüssigtes Erdgas (LNG) wurden dabei sog. RPT’s (rapid phase transition) nachgewiesen, bei denen die spontane Verdampfung relevante Druckwellen erzeugt. Es kann nicht ausgeschlossen werden, dass RPTs auch im Falle von LH2 möglich sind. Die Versuche wurden auf dem Testareal Wasserstoffsicherheit auf dem Testgelände Technische Sicherheit der Bundesanstalt für Materialforschung und -prüfung (BAM-TTS) in Horstwalde, im Rahmen einer Forschungskooperation zwischen der BAM und Gexcon im Rahmen des SH2IFT-Programms durchgeführt. Die LH2-Freisetzungen erfolgten direkt aus einem LH2-Tanklastwagen über eine lange, flexible, vakuumisolierte Transferleitung. Während die Freisetzung oberhalb und unterhalb der Wasseroberfläche jeweils vertikal orientiert war, wurde bei der Unterwasserfreisetzung zusätzlich eine horizontale Ausströmung, parallel zur Wasseroberfläche realisiert. Zur Bestimmung des Massenstromes, wurde ein Wägesystem unter dem Tankwagen eingesetzt. Spezielle Drucksensoren wurden verwendet, um die durch die Freisetzungsvorgänge erzeugten Stoßwellen sowohl im Wasser als auch in der Luft zu messen. Die Gaskonzentrationen über dem Wasserbecken wurden an verschiedenen Positionen gemessen. Hochgeschwindigkeits-, Infrarot- (IR) und normale Kameras wurden eingesetzt, um die Phänomenologie der Freisetzung aufzuzeichnen und das Verhalten der Gaswolke im Zeitverlauf zu verfolgen. Neben den fest installierten Systemen an Land, kamen auch Unterwasserkameras sowie eine Drohne mit Normal- und IR-Kameras zum Einsatz. Zwei Wetterstationen wurden zur Messung von Windgeschwindigkeit, Windrichtung, Temperatur und Luftfeuchtigkeit während aller durchgeführten Tests eingesetzt. Des Weiteren kamen Bolometer zur Wärmestrahlungsmessung zum Einsatz. Zwar führten die Freisetzung zu einer hochturbulenten LH2/Wasser Mischzone, jedoch zu keinen nennenswerten Überdrücken durch RPT. Im Gegensatz dazu wurde unerwartet, aber reproduzierbar, eine Zündung der Gaswolke in freier Luft in einiger Entfernung von den Instrumenten und dem Ort der Freisetzung beobachtet. Die daraus resultierenden Gaswolkenexplosionen führten zu relevanten Überdrücken und zur Wärmeabstrahlung in die Umgebung. T2 - Magdeburg-Köthener Brandschutz- und Sicherheitstagung 2024 CY - Magdeburg, Germany DA - 14.03.2024 KW - LH2 KW - Flüssigwasserstoff KW - Gaswolkenexplosion KW - Freisetzung KW - RPT PY - 2024 AN - OPUS4-59716 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Tamburini, Federica A1 - Kluge, Martin A1 - Habib, Abdel Karim A1 - Ustolin, Federico A1 - Cozzani, Valerio A1 - Paltrinieri, Nicola T1 - Exploring experimental tests concerning liquid hydrogen releases N2 - In recent years, the adoption of liquid hydrogen (LH2) has increased significantly in industrial and transport applications, driven by its low carbon footprint, thereby aiding the fight against global warming. Additionally, its high volumetric energy density, compared to gaseous or compressed hydrogen, enhances hydrogen storage capabilities. However, safety remains a major concern due to its physical-chemical properties and inherent hazardous characteristics, especially in the event of spillage scenarios. Therefore, to better understand the consequences of LH2 releases onto or into water, large-scale experimental tests were conducted by Bundesanstalt für Materialforschung und -prüfung (BAM) within the Safe Hydrogen Fuel Handling and Use for Efficient Implementation (SH2IFT) project at the Test Site Technical Safety of BAM, comprising 75 single spill events at varied release rates and orientations. While the rapid phase transition (RPT) phenomenon was not observed, selfignition of the hydrogen-air cloud occurred, accompanied by blast wave overpressure and heat radiation, without a discernible ignition source. These findings emphasize the need for further investigation into LH2 safety. Leveraging experimental data for real-world applications provides insights into safe LH2 infrastructure implementation, laying foundational knowledge for addressing safety challenges and advancing LH2 technology. KW - Liquid Hydrogen KW - Rapid phase transition KW - Ignition KW - Safety PY - 2024 UR - https://nbn-resolving.org/urn:nbn:de:kobv:b43-618644 DO - https://doi.org/10.1016/j.psep.2024.11.014 SN - 0957-5820 VL - 192 SP - 1330 EP - 1343 PB - Elsevier CY - Amsterdam AN - OPUS4-61864 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Mazzola, T. A1 - Hanna, S. A1 - Chang, J. A1 - Bradley, S. A1 - Meris, R. A1 - Simpson, S. A1 - Miner, S. A1 - Gant, S. A1 - Weil, J. A1 - Harper, M. A1 - Nikmo, J. A1 - Kukkonen, J. A1 - Lacome, J.-M. A1 - Nibart, M. A1 - Björnham, O. A1 - Khajehnajafi, S. A1 - Habib, Abdel Karim A1 - Armand, P. A1 - Bauer, T. A1 - Fabbri, L. A1 - Spicer, T. A1 - Ek, N. T1 - Results of comparisons of the predictions of 17 dense gas dispersion models with observations from the Jack Rabbit II chlorine field experiment N2 - The Jack Rabbit II (JR II) chlorine field trials in 2015 and 2016 involved nine 5–20 ton releases of pressurized liquefied chlorine from a tank mounted 1 m above a broad flat desert sand surface. A model comparison study was initiated, where 17 widely-used dense-gas dispersion models were run by scientists in seven countries. Predictions were submitted following specified formats, using specified emissions and meteorology inputs. To compare with the model predictions, sets of observations were defined for the arc-maximum 1–3 s averaged concentrations (arc max C) and for cloud widths and heights (to 20 ppm and 200 ppm contours) at distances from 0.2 to 11.0 km from the release. The initial focus is on the three field trials (1, 6, and 7) that have the highest observed concentrations and that have detailed emissions information. It is found that these models are able to satisfactorily simulate (generally within a factor of two) the observed arc max C’s and their variation with downwind distance at this flat desert site. At each downwind distance, the scatter in the arc max C predictions covers about 1 ½ orders of magnitude, but the observed arc max C is within the range of the predictions. The median of the cloud width predictions is about 50% larger than the observed value for the three trials. The median of the cloud height predictions is within about 10% of the observed value. For both cloud width and/or height, there are a few models with large (factor of 3 or higher) overpredictions. Of the 17 models, when compared to observations, there is a core group of 5 or 6 with consistently (across all three trials and all distances) less mean error and scatter in their predictions of arc max C and cloud width and height. However, as a group, the 17 models are performing adequately (using the “factor of two” rule of thumb). An important caveat is that, at the JR II desert site, chlorine deposition is minimal. At a site with vegetation and/or organic-rich soil, the effects of removal of chlorine by deposition are expected to be significant. KW - Jack rabbit II chlorine field experiment KW - Dense gas dispersion KW - Model evaluation PY - 2021 DO - https://doi.org/10.1016/j.atmosenv.2020.117887 VL - 244 SP - 117887 PB - Elsevier Ltd. CY - Amsterdam AN - OPUS4-51845 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Kluge, Martin A1 - Habib, Abdel Karim T1 - Consequences of exposing cryogenic storage vessels containing liquid hydrogen to a fire load N2 - Within a research cooperation between BAM and Gexcon as part of the SH2IFT program, large scale experiments have been performed at the Test Site Technical Safety of the Bundesanstalt für Materialforschung und –prüfung (BAM) to determine the hazards emerging from a vacuum insulated cryogenic storage vessel containing liquified hydrogen (LH2) is caught in a fire engulfing it. T2 - ELVHYS, 2nd Safety Workshop CY - Online meeting DA - 29.11.2023 KW - BLEVE KW - Cryoegenic storage vessel KW - Liquified hydrogen PY - 2023 AN - OPUS4-59021 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim A1 - Kluge, Martin A1 - van Wingerden, Kees ED - Beyer, Michael ED - Lucassen, Arnas T1 - Experimental investigation into the consequences of release of liquified hydrogen onto and under water N2 - Large-scale experiments have been performed to investigate the possible consequences of realistic amounts of liquified hydrogen (LH2) encountering water. The experiments aimed at simulating an accidental release of LH2 during especially the fuelling of a ship. For liquified natural gas (LNG) it has been demonstrated that when spilled onto water the evaporation rate can be that high that physical explosions occur which are referred as rapid phase transitions (RPTs). It cannot be excluded that RPTs are also possible in the case of LH2. The tests were performed in a 10 m x 10 m x 1.5 m basin filled with water, at the Test Site Technical Safety of the Bundesanstalt für Materialforschung und –prüfung (BAM) in Horstwalde, Germany within a research cooperation between BAM and Gexcon as part of the SH2IFT program. LH2 releases were established releasing directly from a trailer carrying LH2 through a long flexible double vacuum insulated transfer line. The releases occurred from a height of 50 cm above and 30 cm under the water surface both pointing downwards and 30 cm under the water surface pointing along the water surface too. The release rate was determined based on the weight loss rate of the road tanker which was placed onto load cells. Special blast pressure sensors were used to measure the shock waves generated by the release processes both in the water and in the air. At several locations the gas concentration was measured. Heat radiation was measured at 3 distances from the point of release. High speed, Infrared (IR) and normal cameras were used to record events and to follow the gas cloud behaviour in time. This includes cameras mounted on a UAV and underwater cameras. Two weather stations were used to measure wind speed, wind direction, temperature and humidity during all tests performed. All investigated release configurations resulted in a very chaotic LH2-water mixing zone, causing considerable evaporation but only minor over pressures. The main phenomenon observed was an ignition of the released gas cloud, resulting in significant blast wave overpressures and heat radiation to the surroundings. The location of the ignition occurred in free air at some distance from the instrumentation and release location. T2 - 14th International Symposium on Hazards, Prevention and Mitigation of Industrial Explosions (ISHPMIE 2022) CY - Braunschweig, Germany DA - 11.07.2022 KW - LH2 KW - RPT KW - Release KW - Gas cloud explosion KW - Heat radiation PY - 2022 SP - 182 EP - 196 AN - OPUS4-59441 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Schalau, Bernd A1 - Bernardy, Christopher A1 - Habib, Abdel Karim T1 - Modellierung von Wasserstoff - Freistrahlflammen N2 - Bei der Freisetzung von Wasserstoff aus Ausbläsern kann nicht ausgeschlossen werden, dass es zu einer Selbstentzündung und der Bildung einer Freistrahlflamme kommt. Als Auswirkungen für die Umgebung sind der Explosionsüberdruck bei der Zündung und die Wärmestrahlung im Rahmen einer Gefährdungsbeurteilung zu betrachten. In der Literatur sind verschiedene Ansätze für die Modellierung einer Wasserstoff-Freistrahlflamme zu finden, wobei viele sich mit der Berechnung der Flammenlänge befassen. Experimentelle Freifeld-Untersuchungen unter Windeinfluss und entsprechende Modellierungen der Wärmestrahlung in der Umgebung einer Wasserstoff-Freistrahlflamme liegen nur wenig vor. In der Bundesanstalt für Materialforschung und -prüfung BAM sind solche Experimente durchgeführt worden und die daraus abgeleitete Modellierung wird im Folgenden vorgestellt. KW - Freistrahlflamme KW - Auswirkungsbetrachtung PY - 2025 SN - 2191-007 VL - 15 IS - 05-06 SP - 16 EP - 24 CY - Düsseldorf AN - OPUS4-63709 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Bernardy, Christopher A1 - Habib, Abdel Karim A1 - Kluge, Martin A1 - Orchini, A. ED - Fabiano, Bruno ED - Cozzani, Valerio T1 - Heat Radiation Emanating from Hydrogen and Methane Jet Fires N2 - Modelling the heat radiation emanating from jet flames for initial hazard assessment purposes is generally done using simple, steady-state, approaches that give a quick estimation useful for impact analysis. Although nowadays CFD can be used to simulate this phenomenon in detail, it is still very demanding in computational power and time, and generally not all required boundary conditions to achieve a reliable result are known. Therefore, even today simpler empirical approaches are still widely used for consequence analysis. Hydrogen is becoming increasingly important as renewable energy carrier resulting in an increasing demand of “hydrogen-approved” models. Since the aforenamed models were mainly developed based on data from hydrocarbon jet flame experiments, it has to be verified if they also apply to hydrogen jet flames. To this purpose, real-scale tests are carried out at the BAM Test Site Technical Safety (BAM-TTS) with the aim to assess the flame geometry and the emitted thermal radiation of hydrogen and methane jet flames. In particular, the focus is laid on the measurement and modelling of the thermal radiation. Existing heat radiation data from the literature are mostly based on unsteady outflow conditions. The experimental setup used here allows for the generation of a steady-state outflow and thus a direct comparability with existing (steady-state) models. From these data, an assessment of the applicability of jet flame models to hydrogen jet flames is carried out accounting for their accuracy in predicting heat radiation and possible needs of further development. T2 - 18th EFCE International Symposium on Loss Prevention and Safety Promotion in the Process Industries CY - Bologna, Italy DA - 08.06.2025 KW - Jet Fire KW - Hydrogen KW - Methane KW - Heat radiation PY - 2025 DO - https://doi.org/10.3303/CET25116065 SN - 2283-9216 VL - 116 SP - 385 EP - 390 PB - AIDIC Servizi S.r.l. CY - Italy AN - OPUS4-63698 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Kluge, Martin A1 - Habib, Abdel Karim ED - Fabiano, Bruno ED - Cozzani, Valerio T1 - Cryogenic LH2 Storage Vessels in a Fire N2 - To investigate the hazards emanating from cryogenic LH2 storage Vessels in a fire, experiments have been performed at the Test Site Technical Safety of the Bundesanstalt für Materialforschung und –prüfung (BAM), Germany. Three double-walled vacuum insulated vessels of 1 m3 volume, filled to approximately 35-40 Vol.% with LH2 were put in a fire. The cylindrical Vessels differed in orientation (horizontal or vertical) and the insulationmaterial used (perlite or multi-layer insulation (MLI)). The fire load was provided by a propane fed burner-system positioned under the storage vessel and designed to give a homogeneous fire load. During the tests the conditions in the vessel (temperatures and pressure) as well as external effects (heat radiation, blast waves, flame ball development and fragmentation) were measured. Two of these vessels, a horizontal and a vertical vessel both insulated with perlite withstood the fire loading for 1 hour 20 minutes and 4 hours respectively without catastrophic failure, but partly showing leakages. The horizontal vessel insulated with MLI failed by bursting after 1 hour and 6 minutes resulting in a fireball, fragments, and blast wave. The test results as well as the detailed examination of the non-destroyed vessels rose some interesting questions which type of insulation might be better to protect a vessel not only during its normal operation but also under fire loading against a heat flux from the surroundings, as well as to the suitability of cryogenic (safety) equipment under fire loading. T2 - 18th EFCE International Symposium on Loss Prevention and Safety Promotion in the Process Industries CY - Bologna, Italy DA - 08.06.2025 KW - LH2 KW - Cryogenic tank KW - Fire engulfment KW - BLEVE PY - 2025 DO - https://doi.org/10.3303/CET25116130 SN - 2283-9216 VL - 116 SP - 775 EP - 780 PB - AIDIC Servizi S.r.l. CY - Italy AN - OPUS4-63697 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim T1 - Heat radiation emanating from hydrogen and methane jet fires N2 - Modelling the heat radiation emanating from jet flames for hazard assessment purposes, is generally done using simple, steady-state approaches that give a quick result and estimation of the consequences to account for. Although nowadays computational fluid dynamics can be used to simulate this phenomenon in detail, it is still very demanding in computational power and time and generally not all required boundary conditions to achieve a reliable result are known. Therefore, even today the simpler approaches as for example the Model of Chamberlain or Johnson (mainly developed for hydrocarbon flames) are still widely used for consequence analysis. Hydrogen is becoming increasingly important as renewable energy carrier resulting in an increasing demand of “hydrogen approved” models. Since the aforenamed jet flame models were mainly developed based on data from hydrocarbon jet flame experiments, it is to be verified, that they also apply to hydrogen jet flames. To this purpose real-scale tests are carried out at the BAM Test Site Technical Safety (BAM-TTS) with the aim to assess the flame geometry and the emitted thermal radiation of hydrogen and methane jet flames. Parameters such as leakage diameter (ranging from 1 mm to 10 mm), pressure (up to max. 250 bar), release orientation (vertical or horizontal) and mass flow (up to max. 0.5 kg/s) are varied. In particular, the focus is laid on the measurement and modelling of the thermal radiation. The challenge here is the characterization of the flame geometry in an open environment and its impact on the thermal radiation. Existing heat radiation data from the literature are mostly based on unsteady outflow conditions. The experimental setup used here allows for the generation of a steady-state outflow for several minutes and thus a direct comparability with existing (steady-state) models. From these data, an assessment of the applicability of jet flame models to hydrogen jet flames is carried out not only accounting for their accuracy in predicting the heat radiation but also with regard to possible needs of further development of the models. T2 - 18th EFCE International Symposium on Loss Prevention and Safety Promotion in the Process Industries CY - Bologna, Italy DA - 08.06.2025 KW - Jet Fire KW - Hydrogen KW - Methane KW - Heat radiation PY - 2025 AN - OPUS4-63696 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Bradley, Ian A1 - Kluge, Martin A1 - Habib, Abdel Karim A1 - Scarponi, Giordano Emerys T1 - Experimental Study on Thermal Exposure of Pipes to Steady Hydrogen Jet Fire Impingement N2 - Jet fires resulting from the accidental release of pressurized hydrogen represent a critical issue, especially due to their potential to trigger a domino effect. The lack of studies on the characterisation of the conditions experienced by, and response of, structures and process equipment directly engulfed in a hydrogen jet fire is of concern to industry. This work presents a characterisation study of a hydrogen jet fire with respect to the conditions experienced by an engulfed object. The total heat flux, along with its radiative component, was measured for hydrogen mass flow rates ranging from 0.05 to 0.2 kg/s. Heat fluxes exceeding 700 kW/m2 were measured at a location that coincided with the point of jet impact. The maximum radiative fraction measured was 20 % at the back of the tube where the specimen could receive radiation from the majority of the flame plume. It is concluded that conditions within hydrogen jet fires are notably more severe than those in hydrocarbon jet fires (for which a heat flux of 350 kW/m2 is considered high). This suggests that PFP systems should not be automatically assumed to provide protection against hydrogen jet fires without further research or actual test evidence of performance. KW - Hydrogen KW - Jet Fire KW - Fire Protection KW - Pfp PY - 2025 DO - https://doi.org/10.1016/j.psep.2025.108017 SN - 0957-5820 VL - 204 SP - 1 EP - 15 PB - Elsevier Ltd. AN - OPUS4-64479 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Gant, Simon A1 - Chang, Joseph A1 - Hetherington, Rory A1 - Hanna, Steven A1 - Tickle, Gemma A1 - Spicer, Tom A1 - McMasters, Sun A1 - Fox, Shannon A1 - Meris, Ron A1 - Bradley, Scott A1 - Miner, Sean A1 - King, Matthew A1 - Simpson, Steven A1 - Mazzola, Thomas A1 - McGillivray, Alison A1 - Tucker, Harvey A1 - Björnham, Oscar A1 - Carissimo, Bertrand A1 - Fabbri, Luciano A1 - Wood, Maureen A1 - Habib, Abdel Karim A1 - Harper, Mike A1 - Hart, Frank A1 - Vik, Thomas A1 - Helgeland, Anders A1 - Howard, Joel A1 - Mauri, Lorenzo A1 - Mackie, Shona A1 - Mack, Andreas A1 - Lacome, Jean-Marc A1 - Puttick, Stephen A1 - Ibrahim, Adeel A1 - Miller, Derek A1 - Dharmavaram, Seshu A1 - Shen, Amy A1 - Cunningham, Alyssa A1 - Beverly, Desiree A1 - O’Neal, Daniel M. A1 - Verdier, Laurent A1 - Burkhart, Stéphane A1 - Dixon, Chris A1 - Nilsen, Sandra A1 - Bradley, Robert A1 - Skarsvåg, Hans L. A1 - Fyhn, Eirik H. A1 - Aasen, Ailo T1 - Pressure-Liquefied Ammonia Jet Dispersion: Multi-Model Intercomparison Using Desert Tortoise and FLADIS Field Data N2 - This paper presents the findings of an international model inter-comparison exercise that was undertaken in the period 2021-2024 to assess the performance of atmospheric dispersion models for simulating releases of pressure-liquefied ammonia. The exercise used data from ammonia field trials dating from the 1980s and 1990s: the Desert Tortoise and the FLADIS trials. Concentration data from two arcs of sensors in the Desert Tortoise trials and three arcs of sensors in the FLADIS trials were used. Twenty-one independent modelling teams from North America and Europe participated in the exercise and provided in total twenty-seven sets of results from a range of different models, including empirically-based nomograms, integral, Gaussian puff, Lagrangian particle, and Computational Fluid Dynamics (CFD) models. The work is novel in presenting the results from such a large cohort of models, examining specifically the dispersion behaviour of ammonia. This is particularly relevant at the current time, given the growing international interest in using ammonia as a clean energy vector and shipping fuel. The study found that the agreement between model predictions and measurements (as determined by performance measures such as geometric mean bias and geometric variance) varied between different models. At any downwind distance, the range in predicted plume arc-max concentrations spanned a range of up to one or two orders of magnitude about the measurements. Several modelling teams used the same models and, in most cases, their predictions differed. Given appropriate inputs, most models generally predicted concentrations that agreed with the data within commonly-used model acceptance criteria. There was no single class of model that provided superior predictions to others; predictions from several empirically-based nomograms, integral, Gaussian puff, Lagrangian particle, and CFD models were all in close agreement with the data (as defined by the model acceptance criteria). The findings of the exercise are being used to help plan a programme of future ammonia experiments in the USA, called the Jack Rabbit III trials. The results are also useful for assessing the performance of models that may be applied to assess risks at ammonia facilities, and for emergency planning and response. KW - Ammonia KW - Atmospheric dispersion KW - Validation KW - Jack rabbit PY - 2025 UR - https://nbn-resolving.org/urn:nbn:de:kobv:b43-646069 DO - https://doi.org/10.1016/j.aeaoa.2025.100389 SN - 2590-1621 VL - 28 SP - 1 EP - 76 PB - Elsevier Ltd. AN - OPUS4-64606 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Bernardy, Christopher A1 - Habib, Abdel Karim A1 - Kluge, Martin A1 - Schalau, Bernd A1 - Kant, Hanjo A1 - Schulze, Marcel A1 - Orchini, Alessandro T1 - Experimental Investigation of Large-Scale Hydrogen Diffusion Jet Flames N2 - Hydrogen is a promising alternative to natural gas in industrial energy applications to limit global warming. However, wide application of hydrogen requires specific safety considerations taking into account that hydrogen is stored and transported under much higher pressure than natural gas. Thus, one scenario to be considered for hazard assessment is a sudden release of hydrogen from a leakage or safety valve and its subsequent ignition. For hydrocarbon flames, various jet flame models are available. However, hydrogen flames significantly differ from hydrocarbon flames in their combustion behavior, so that the applicability of these models to hydrogen has to be investigated. For that purpose, reals scale tests were carried out at the BAM Test Site Technical Safety. In these tests, the flame geometry and the thermal heat radiation were investigated for a release angle of 90°, for different release pressures (up to 220 bar) and mass flows (up to 0.175 kg/s). Most existing data on thermal radiation are based on unsteady flow conditions and/or still air, whereas the experiments carried out here ensure a constant mass flow under realistic free-field conditions (with wind influence). This allows a better comparability with the stationary jet flame models and assessment of wind influence on model predictions. A number of parameters such as the surface emissive power and the radiant heat fraction were determined. A detailed comparison of the obtained experimental results with literature radiation models was performed. Based on the investigations, empirical equations for modelling jet flames could be derived. T2 - Proceedings of ASME Turbo Expo 2025 Turbomachinery Technical Conference and Exposition CY - Memphis, Tennessee, USA DA - 16.06.2025 KW - Hydrogen release KW - Radiant heat fraction KW - Thermal radiation KW - Jet flame PY - 2025 UR - https://nbn-resolving.org/urn:nbn:de:kobv:b43-643401 DO - https://doi.org/10.1115/1.4070012 SN - 0742-4795 VL - 148 IS - 5 SP - 51008-1 EP - 51008-8 PB - ASME International AN - OPUS4-64340 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Tschirschwitz, Rico A1 - Krentel, Daniel A1 - Kluge, Martin A1 - Askar, Enis A1 - Habib, Abdel Karim A1 - Kohlhoff, Harald A1 - Neumann, Patrick P. A1 - Rudolpf, Michael A1 - Schoppa, André A1 - Storm, Sven-Uwe A1 - Szczepaniak, Mariusz T1 - Propangasbehälter im Feuer: Auswirkungen des Versagens N2 - In einer Großversuchsserie wurden auf dem BAM-TTS 15 11-kg-Propangasflaschen ohne Sicherheitseinrichtung mit drei verschiedenen Methoden (Holz, Benzinpool, Gas) unterfeuert. Der Beitrag beschreibt die dokumentierten Auswirkungen (z. B. Fragmentierung, Überdruck), die Art des Versagens sowie den Behälterzustand zum Zeitpunkt des Versagens. T2 - 13. Fachtagung Anlagen-, Arbeits- und Umweltsicherheit CY - Köthen, Germany DA - 16.11.2017 KW - Behälterversagen KW - Gassicherheit KW - Feuerwehr KW - Propan KW - Auswirkungsbetrachtung PY - 2017 SN - 978-3-96057-032-5 SP - 1 EP - 2 AN - OPUS4-42954 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Tschirschwitz, Rico A1 - Krentel, Daniel A1 - Kluge, Martin A1 - Askar, Enis A1 - Habib, Abdel Karim A1 - Kohlhoff, Harald A1 - Neumann, Patrick P. A1 - Storm, Sven-Uwe A1 - Rudolph, Michael A1 - Schoppa, André A1 - Szczepaniak, Mariusz T1 - Mobile gas cylinders in fire: Consequences in case of failure N2 - Commercial, off-the shelf propane cylinders are subjected to high safety regulations. Furthermore, those cylinders are equipped with safety devices like pressure relief valves (PRV). Despite these regulations and safety measures, a failure of the Container is possible if exposed to an intense fire. The result of this is severe hazard for users, rescue forces and infrastructure. Within the framework of a destructive test series, 15 identical propane cylinders, without pressure relief devices, were exposed to an intensive fire in horizontal Position until failure. Each cylinder was filled with a mass of m =11 kg of liquid propane. Three different fire sources were used (wood, petrol, propane). The experiments revealed the failure of all cylinders in a time period t < 155 s. The failure lead to a fragmentation into several major parts with throwing distances of up to l =262 m. In all trials, the temperature of the cylinder wall (top, side, bottom), of the liquid phase inside and of the surrounding fire (top, side, bottom) was recorded. In addition, the inner cylinder pressure and the induced overpressure of the blast wave after the failure were recorded. Overpressures of up to p=0.27 bar were recorded close to the cylinder (l =5 m). AM tests were documented hy video from several positions (general view, close-up, high-speed 5000 fps). This test series creates the basis for further experimental studies in the field of alternative fuels for vehicles. The aim of this test series is to assess and analyse the consequences of the failure of gas vessels (for LPG, CNG, CGH2) in the aftermath of severe incidents. T2 - 12th International Symposium on Fire Safety Science CY - Lund, Sweden DA - 12.06.2017 KW - Explosion KW - Gas cylinders KW - Consequences PY - 2017 DO - https://doi.org/X0.1016/j.firesaf.2017.05.006 SN - 0379-7112 VL - 91 SP - 989 EP - 996 PB - Elsevier Ltd. AN - OPUS4-43028 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Hussels, Maria-Teresa A1 - Chruscicki, Sebastian A1 - Baer, Wolfram A1 - Wossidlo, Peter A1 - Weltschev, Margit A1 - Schmidt, Dirk A1 - Baensch, Franziska A1 - Bohse, Jürgen A1 - Prager, Jens A1 - Habib, Abdel Karim T1 - AGIFAMOR – Application of distributed acoustic and fibre optic sensors for continuous monitoring of pipes N2 - Pipelines and industrial piping systems are particularly relevant regarding technical safety, availability and maintenance. Large flow rates of hazardous substances imply that even smallest leakages can lead to high environmental impacts. Therefore, and to ensure the availability of infrastructure, an early detection and localization of potentially hazardous degradations to the walls (e.g. cracks, pittings, sedimentation, etc.) of the containments is necessary. However, in many cases it is not feasible to equip pipelines with a large number of point sensors at reasonable expense. The principle of distributed fibre optic sensing relies on one single optical fibre, which simultaneously acts as a spatially continuous sensor as well as the signal transducer. Therefore, extensive structures can be provided with this type of sensor with comparatively low efforts. As a consequence, monitoring oil and gas pipelines using distributed fibre optic sensors is on the upswing. Besides the established methods to measure temperature and strain, distributed acoustic sensing (DAS) has lately received considerable attention as a means to detect and localize third party threats to pipelines (approach of vehicles, digging, mechanical manipulation). The so far not utilized potential of DAS as a means for continuous condition monitoring of pipes by detecting and localizing acoustic signals that point to certain damage scenarios, is currently under investigation in an interdisciplinary research project at BAM (AGIFAMOR, Ageing Infrastructures – Fibre Optic Monitoring of Pipes). In order to qualify distributed acoustic fibre optic sensors for this application area, we especially focus on detecting and identifying the relevant acoustic emissions of interesting degradations as well as on the optimal way of application of the optical fibres to the specimen to achieve an optimal signal transmission of acoustic signals. T2 - 12th Pipeline Technology Conference CY - Berlin, Germany DA - 02.05.2017 KW - Monitoring KW - Pipelines KW - Fibre optic sensing KW - Acoustic emission KW - Accelerometer PY - 2017 SN - 2198-428X VL - 2017 SP - Session 3.2 Leak Detection, 1 EP - 8 PB - EITEP (Euro Institute for Information and Technology Transfer in Environmental Protection) CY - Hannover AN - OPUS4-40186 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Baensch, Franziska A1 - Baer, Wolfram A1 - Wossidlo, Peter A1 - Habib, Abdel Karim T1 - Non-threshold acoustic emission analysis of damage evolution in pipe segments of steel S355J2H under bending load N2 - Four-point bending tests were carried out to analyze the acoustic characteristics of damage development in pipe segments made of steel, grade S355J2H, being 2.5 m long with an outer diameter of 168 mm and 16 mm wall thickness. To induce stable crack growth, the pipe segments were pre-damaged by a 90°circumferential notch in the middle of the pipe length. While the pipe was quasi-statically loaded, microscopic damage and plastic deformation accumulated to form a macroscopic crack that grew through the pipe wall until leakage. For acoustic emission (AE) monitoring, four broadband sensors of type VS 900 M were mounted close to the notch. Continuous AE signal detection was performed by the non-threshold method. Advantages and disadvantages of the non-threshold AE monitoring compared to a commonly employed method analyzing only signals exceeding a predefined threshold are discussed. The results of AE analysis are compared to additional information on the crack growth detected by the direct current potential drop (DCPD) technique. These studies were carried out in the course of the interdisciplinary research project AGIFAMOR, Ageing infrastructures - distributed acoustic monitoring of pipes at BAM. T2 - 33rd European Conference on Acoustic Emission Testing CY - Senlis, France DA - 12.09.2018 KW - Acoustic emissions (AE) KW - Four-point bending test KW - Steel pipe KW - Crack initiation KW - Crack growth PY - 2018 SP - 340 EP - 347 CY - France, Senlis AN - OPUS4-45960 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Tschirschwitz, Rico A1 - Krentel, Daniel A1 - Kluge, Martin A1 - Askar, Enis A1 - Habib, Abdel Karim A1 - Kohlhoff, Harald A1 - Neumann, Patrick P. A1 - Rudolph, Michael A1 - Schoppa, André A1 - Storm, Sven-Uwe A1 - Szczepaniak, Mariusz T1 - Auswirkungen von Behälterversagen bei alternativen PKW-Antrieben - Teil 3: Auswirkungen des Versagens von 11-kg-Propangasbehältern im Feuer N2 - In Deutschland gibt es eine große Anzahl von Kraftfahrzeugen, die mit alternativen Antrieben (z. B. LPG (Liquefied Petroleum Gas), CNG (Compressed Natural Gas)) ausgerüstet sind. In zahlreichen Großversuchsserien untersucht die Bundesanstalt für Materialforschung und -prüfung (BAM) im Rahmen des internen Forschungsprojekts CoFi-ABV (Complex Fires – Auswirkungen von Behälterversagen) die Auswirkungen beim Versagen der Treibstoffbehälter dieser alternativen Antriebe. Ziel dieser Untersuchungen ist eine ganzheitliche Auswirkungsbetrachtung, um die Risiken für Feuerwehren und Rettungskräfte besser abschätzen zu können. Im Vorfeld zu den Versuchen für LPG- und CNG-Tanks wurden in einer weiteren Versuchsserie 15handelsübliche 11-kg-Propangasflaschen ohne Sicherheitseinrichtung unterfeuert. Alle 15 Behälter haben – wie zu erwarten war – versagt. Neben den Zustandsdaten des Behälters zum Versagenszeitpunkt (Temperatur des Behältermantels, Innendruck und -temperatur) wurden die Auswirkungen auf die Umgebung hinsichtlich Druckwirkung und Fragmentierung (Anzahl, Masse, Distanz, Richtung) dokumentiert. KW - Behälterversagen KW - Gassicherheit KW - Feuerwehr KW - Propan KW - Auswirkungsbetrachtung PY - 2017 SN - 2191-0073 VL - 7 IS - 11/12 SP - 25 EP - 32 PB - Springer-VDI-Verlag GmbH & Co. KG CY - Düsseldorf AN - OPUS4-43270 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Tschirschwitz, Rico A1 - Krentel, Daniel A1 - Kluge, Martin A1 - Askar, Enis A1 - Habib, Abdel Karim A1 - Kohlhoff, Harald A1 - Krüger, Simone A1 - Neumann, Patrick P. A1 - Rudolph, Michael A1 - Schoppa, André A1 - Storm, Sven-Uwe A1 - Szczepaniak, Mariusz T1 - Experimental investigation of consequences of LPG vehicle tank failure under fire conditions N2 - In case of a vehicle fire, an installed LPG (liquefied petroleum gas) tank with a malfunctioning safety device poses severe hazards. To investigate the consequences in case of tank failure, we conducted 16 tests with toroidal shaped LPG vehicle tanks. Three tanks were used for a Hydraulic Burst Test under standard conditions. Another three tanks were equipped with a statutory safety device and were subjected to a gasoline pool fire. The safety device prevented tank failure, as intended. To generate a statistically valid dataset on tank failure, ten tanks without safety devices were exposed to a gasoline pool fire. Five tanks were filled to a level of 20 %; the re-maining five were filled to a level of 100 %. In order to gain information on the heating process, three tem-perature readings at the tank surface, and three nearby flame temperatures were recorded. At distances of l = (7; 9; 11) m to the tank, the overpressure of the shock wave induced by the tank failure and the unsteady tem-peratures were measured. All ten tanks failed within a time of t < 5 min in a BLEVE (boiling liquid expanding vapor explosion). Seven of these resulted directly in a catastrophic failure. The other three resulted in partial failure followed by catastrophic failure. A near field overpressure at a distance of l = 7 m of up to p = 0.27 bar was measured. All ten tests showed massive fragmentation of the tank mantle. In total, 50 fragments were found. These 50 fragments make-up 88.6 % of the original tank mass. Each fragment was georeferenced and weighed. Fragment throwing distances of l > 250 m occurred. For the tanks with a fill level of 20 %, the average number of fragments was twice as high as it was for the tanks that were filled completely. KW - Blast wave KW - BLEVE KW - Consequences KW - Explosion KW - LPG PY - 2018 UR - https://authors.elsevier.com/a/1XnFv_Ld32ewKu DO - https://doi.org/10.1016/j.jlp.2018.09.006 SN - 0950-4230 VL - 56 SP - 278 EP - 288 PB - Elsevier CY - Kidlington - Oxford AN - OPUS4-46238 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Baensch, Franziska A1 - Baer, Wolfram A1 - Wossidlo, Peter A1 - Habib, Abdel Karim T1 - Damage evolution detection in a pipeline segment under bending by means of acoustic emission N2 - A steel pipeline segment of 2.5 m length was subjected to quasi-static four-point bending load in three steps for studying the initial cracking and damage accumulation based on the Acoustic Emission (AE) technique and by the direct current potential drop (DCPD) technique. For the latter, a new post-test analysis method was established. AE is found more sensitive to crack initiation than DCPD. Formation of mesoscopic and macroscopic cracks as well as their closure and the resulting friction generate weighted peak frequencies below 400 kHz, whereas microscopic cracking produces AE with broad band spectra identifiable by weighted peak frequencies above 400 kHz. Critical states alike the maximum load level and the leak opening were accompanied by peak amplitudes above 85 dBAE. This rather fundamental study provides a data base for possibly developing advanced strategies of detection and alarm systems based on acoustic monitoring of pipelines, or at least, steel structures. KW - Crack KW - Accoustic emission KW - Frequency domain KW - Potential drop technique KW - Fracture PY - 2023 UR - https://nbn-resolving.org/urn:nbn:de:kobv:b43-565171 DO - https://doi.org/10.1016/j.ijpvp.2022.104863 SN - 0308-0161 VL - 201 IS - 104863 SP - 1 EP - 9 PB - Elsevier Science CY - Amsterdam AN - OPUS4-56517 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Askar, Enis A1 - Schröder, Volkmar A1 - Tashqin, Temir A1 - Habib, Abdel Karim A1 - Schütz, S. A1 - Seemann, A. T1 - Explosion protection for mixtures of hydrogen and natural gas N2 - Safety characteristics for explosion protection for mixtures of hydrogen and natural gas were studied in laboratory tests. Also calculations on the explosion zones for mixtures of hydrogen and natural gas were conducted. Moreover calculation methods for the safety characteristics of such mixtures were tested aiming to reduce the high effort for the experimental determination of safety characteristics prospectively. Admixture of up to 10 mole% hydrogen to natural gas has very low influence on safety characteristics for explosion protection. With increasing hydrogen fraction the mixtures become mainly more „critical“ considering explosion protection, an substantial influence on explosion protection occurs for hydrogen fractions of more than 25 mole%. T2 - 21st World Hydrogen Energy Conference 2016 (WHEC) CY - Saragossa, Spain DA - 13.06.2016 KW - Power-to-gas KW - Explosion regions KW - Safety of hydrogen KW - Hydrogen energy KW - Explosion groups PY - 2016 SP - 818 EP - 819 AN - OPUS4-37998 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Bernardy, Christopher A1 - Habib, Abdel Karim A1 - zur Nedden, Philipp Maximilian A1 - von Saldern, Jakob Georg Raimund A1 - Beuth, Jan Paul A1 - Orchini, Alessandro T1 - Thermal Radiation Of Inclined Large Scale Hydrogen Jet Flames N2 - In order to assess the thermal radiation emanating from hydrogen jet flames, experiments under real scale conditions were carried out at the Test Site Technical Safety of BAM. Herein, the behavior of inclined hydrogen jet flames was investigated. The aim of the work is to determine the Surface Emissive Power (SEP) and radiant heat fraction of these flames and to provide a reliable dataset for model evaluation purposes. Since the aforementioned values are not directly measurable, the incident heat radiation was measured at defined distances from the flame, as well as the flame’s shape and size. The required values were then derived from these measurements. The hydrogen releases ranged from 0.0125 kg/s to 0.175 kg/s with a 30 mm orifice. The mass flows were held constant during the releases, nevertheless a transient behavior of the flame could be observed since the experiments were carried out under open field conditions, with unsteady wind fields. In the literature, the flame lengths are often determined using visible light imaging, either by injecting coloring substances in the low light emitting hydrogen jet flame or by carrying out the measurements in darkness. In this work the jet flames were visualized using infrared (IR) and OH* imaging. The recorded flame shapes and resulting flame lengths are compared. Results from this showed that the flame lengths determined with OH* and IR recordings differ greatly. A flame length ratio lf OH*/lf IR in the range of 0.47–0.62 can be found. In addition, the SEP differ also in the range of 10 kW/m2–16 kW/m2 (IR) and 40 kW/m2–80 kW/m2 (OH*) for hydrogen jet flames due to differences in the determined flame surface. Conclusions regarding the determined xRAD values for IR and OH* result in approximately the same range of 0.031–0.043. T2 - 11th Iinternational conference on hydrogen safety 2025 CY - Seoul, Republic of Korea DA - 22.09.2025 KW - Hydrogen safety KW - Jet flames KW - Thermal radiation KW - Large scale experiment PY - 2026 UR - https://nbn-resolving.org/urn:nbn:de:kobv:b43-655181 DO - https://doi.org/10.58895/hysafe.27 SN - 2943-5935 VL - 3 IS - 1 SP - 39 EP - 50 PB - Karlsruhe Institute of Technology Library AN - OPUS4-65518 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim A1 - Kluge, Martin T1 - Experimentelle Untersuchungen zu Schäden an Membranabdeckungen im Biogasbereich N2 - Bei Störfallauswirkungsbetrachtungen an Biogasanlagen muss das Versagen der Membranabdeckung des Fermenters untersucht werden. Hierbei sind insbesondere Risse in derselben hinsichtlich des austretenden Massenstromes an Biogas zu bewerten, ebenso wie der durch eine Zündung resultierende Flammenstrahl. Zurzeit existieren für Membranabdeckungen jedoch keine Erkenntnisse zu realistischen Ausflussziffern für die Massenstromberechnung. Im Leitfaden KAS-32 wird für Störfallauswirkungsbetrachtungen für die Berechnung des austretenden Massenstromes eine Ausflussziffer von 1 und eine „Leckfläche" von 0,6 m2 vorgegeben. Die Anwendbarkeit verfügbarer Modelle zur Berechnung des Flammenstrahls ist bisher ebenso ungeklärt. Um diese Fragestellungen zu untersuchen, wurden in der BAM Versuche zur Bestimmung der Ausflussziffer, sowie der Zündung des austretenden Gases an einem 80 m3 Sack zur Speicherung von Biogas durchgeführt, der aus demselben Material besteht wie die in Biogasanlagen verwendeten Membranabdeckungen. T2 - 14. Fachtagung Anlagen-, Arbeits- und Umweltsicherheit CY - Köthen, Germany DA - 07.11.2019 KW - Biogas KW - Ausflussziffer KW - Membranabdeckung PY - 2019 SN - 978-3-89746-220-5 VL - 2019 SP - 142 EP - 152 AN - OPUS4-50857 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Habib, Abdel Karim T1 - Experimentelle Untersuchungen zu Schäden an Folien- und Membranabdeckungen im Biogasbereich N2 - Bei Störfallauswirkungsbetrachtungen an Biogasanlagen muss das Versagen der Folien- oder Membranabdeckung des Fermenters untersucht werden. Hierbei sind insbesondere Risse in derselben hinsichtlich des austretenden Massenstromes an Biogas zu bewerten, ebenso wie der durch eine Zündung resultierende Flammenstrahl. Zurzeit existieren für Folien- oder Membranabdeckungen jedoch keine Erkenntnisse zu realistischen Ausflussziffern für die Massenstromberechnung. Im Leitfaden KAS-32 wird für Störfallauswirkungsbetrachtungen für die Berechnung des austretenden Massenstromes eine Ausflussziffer von 1 und eine „Leckfläche“ von 0,6 m2 vorgegeben. Die Anwendbarkeit verfügbarer Modelle zur Berechnung des Flammenstrahls ist bisher ebenso ungeklärt. Um diese Fragestellungen zu untersuchen, wurden in der BAM Versuche zur Bestimmung der Ausflussziffer, sowie der Zündung des austretenden Gases an einem 80 m3 Sack zur Speicherung von Biogas durchgeführt, der aus demselben Material besteht wie die in Biogasanlagen verwendeten Folien- und Membranabdeckungen. T2 - 14. Fachtagung Anlagen-, Arbeits- und Umweltsicherheit CY - Köthen, Germany DA - 07.11.2019 KW - Biogas KW - Riss KW - Folie KW - Ausflussziffer PY - 2019 AN - OPUS4-50864 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER -