TY - JOUR A1 - Abdelkhalik, A. A1 - Askar, Enis A1 - Markus, D. A1 - Brandes, E. A1 - Stolz, T. T1 - Explosion regions of acetone and alcohol/inert gas/air mixtures at high temperatures and atmospheric pressure JF - Journal of Loss Prevention in the Process Industries N2 - The explosion regions of 1-propanol, 2-propanol, acetone and 1-butanol in air were measured in the presence of CO2, He, N2 and Ar in accordance with EN1839 method T at high temperatures and at atmospheric pressure. The experimental results show that 1-propanol, 2-propanol and acetone have very similar lower explosion limits (LELs). 1-Butanol shows a slightly wider explosion area near the LEL line. In addition, the explosion regions of all combustible/inert gas/air mixtures were calculated with the method of constant adiabatic flame temperature profiles (CAFTP), using the flame temperature profile along the explosion region boundary curve of each combustible/N2/air mixture as a reference to determine the explosion regions of combustible/inert gas/air mixtures with inert gases other than N2 at different initial temperatures. To calculate the explosion regions for systems containing He, the calculation method was modified to include the very different physical transport properties of He. Moreover, the procedure for calculating the apexes in the ternary explosion diagrams was modified. The calculation results show good agreement with the experimental results. KW - Explosion limits KW - Elevated temperatures KW - Alcohols KW - CAFTP KW - Acetone PY - 2019 DO - https://doi.org/10.1016/j.jlp.2019.103958 SN - 0950-4230 VL - 62 SP - 103958, 1 EP - 8 PB - Elsevier AN - OPUS4-49030 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Abdelkhalik, A. A1 - Askar, Enis A1 - Markus, D. A1 - Stolz, T. A1 - Brandes, E. A1 - Zakel, S. T1 - Explosion regions of 1,3-dioxolane/nitrous oxide and 1,3-dioxolane/air with different inert gases - Experimental data and numerical modelling JF - Journal of Loss Prevention in the Process Industries N2 - In this study, experimental determination and modelling investigations for the explosion regions of 1,3-dioxolane/inert gas/N2O and 1,3-dioxolane/inert gas/air mixtures were carried out and compared. The experimental measurements were carried out at 338 K and atmospheric pressure according to EN1839 method T using the inert gases N2, CO2, He and Ar. The results showed that the ratio of the lower explosion limit in N2O (LELN2O) to the lower explosion limit in air (LELair) is 0.52 and the ratio of the maximum oxygen content in air (MOCair) to the limiting oxidizer fraction in nitrous oxide (LOFN2O) is 0.36 ± 0.02 independent of the inert gas. When comparing the inert gas amount at the apex based on the pure oxidizing component, which is O2 in case of air, N2O-containing mixtures need less inert gas to reach the limiting oxidizer quantity whereas the efficiency of inert gases is in the same order. The coefficients of nitrogen equivalency however were found to differ to some extent. The explosion regions of 1,3-dioxolane/inert gas/oxidizer mixtures were modelled using the calculated adiabatic flame temperature profile (CAFTP) method as well as corrected adiabatic flame temperatures. The results indicate good agreement with experimental data for CO2, N2 and Ar- containing mixtures. The noticeable deviations that occur when He is the inert gas are due to the lacking transport data of that mixture. KW - Explosion limits KW - Flammability KW - CAFTP KW - Adiabatic Flame Temperatures PY - 2021 DO - https://doi.org/10.1016/j.jlp.2021.104496 SN - 0950-4230 VL - 71 SP - 4496 PB - Elsevier Ltd AN - OPUS4-52849 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Askar, Enis A1 - Baumeier, Andreas A1 - Holtappels, Kai A1 - Schröder, Volkmar A1 - Franzen, S. A1 - Büttgen, F. T1 - Explosionskenngrößen von Ethylenoxid und Ethylenoxid/Propylenoxid-Gemischen JF - Chemie - Ingenieur - Technik N2 - In Gasphasen aus Ethylenoxid (EO) und Propylenoxid (PO), die bei technischen Alkoxylierungsreaktionen vorkommen, können auch ohne den Zutritt von Luft Zerfallsreaktionen stattfinden, die explosionsartig mit einer vielfachen Temperatur- und Drucksteigerung verlaufen. Zur Abschätzung der Auswirkungen solcher Explosionen wurden die Explosionsdrücke und die zeitlichen Druckanstiege von reinem EO und EO/PO-Gemischen bei Temperaturen von 100°C bis 200°C und Drücken von 1 - 10 bar in einem 3-dm³-Behälter und punktuell in einem 100-dm³-Behälter experimentell bestimmt. KW - Explosionsdruck KW - Explosionsgrenzen KW - Explosionsschutz KW - Gase KW - Sicherheitstechnik KW - Explosion control KW - Explosion limits KW - Explosion pressure KW - Gases KW - Saftey engineering PY - 2011 DO - https://doi.org/10.1002/cite.201000099 SN - 0009-286X SN - 1522-2640 VL - 83 IS - 3 SP - 365 EP - 370 PB - Wiley-VCH Verl. CY - Weinheim AN - OPUS4-23354 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Holtappels, Kai A1 - Pahl, Robert T1 - Explosions limits of H2S/CO2/air and H2S/N2/air JF - Chemical engineering & technology KW - Explosion limits KW - Hydrogen sulfide KW - Ternery gas system PY - 2005 DO - https://doi.org/10.1002/ceat.200500066 SN - 0930-7516 SN - 1521-4125 VL - 28 IS - 7 SP - 746 EP - 749 PB - Wiley-VCH Verl. CY - Weinheim AN - OPUS4-6922 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Janssen, H. A1 - Bringmann, J.C. A1 - Emonts, B. A1 - Schröder, Volkmar T1 - Safety-related studies on hydrogen production in high-pressure electrolysers JF - International journal of hydrogen energy N2 - At Juelich Research Center the prototype of an alkaline 120-bar electrolyser has been developed and built. Constructive and process-engineering measures must be taken to ensure the safe operation of such facilities. Potential hazards occur due to the high operating pressure in conjunction with the reactivity of the product gases and the electrolyte. First of all, the operating mode and technical features of the Juelich high-pressure electrolyser will be dealt with. Within the framework of a parametric study, the potential for weight reduction of the prototype while observing the rules for pressure vessel design will be shown. The Federal Institute for Materials Research and Testing in Berlin has performed measurements concerning the explosion limits of H2/O2 mixtures at different temperatures and pressures up to 200 bars. At an electrolysis test rig of IWV-3, which can also be operated up to 200 bars, investigations were carried out concerning the gas composition on the H2 and O2 path under different operating conditions. These measurement series were compared to the explosion limits determined and evaluated to derive safety measures required for the operation of high-pressure electrolysers. KW - High-pressure electrolysis KW - Electrolysis KW - Pressure vessel KW - Explosion limits KW - Explosion pressures PY - 2004 DO - https://doi.org/10.1016/j.ijhydene.2003.08.014 SN - 0360-3199 VL - 29 SP - 759 EP - 770 PB - Elsevier CY - Oxford AN - OPUS4-3534 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Molnarne, Maria A1 - Mizsey, P. A1 - Schröder, Volkmar T1 - Flammability of gas mixtures - Part 2: Influence of inert gases JF - Journal of hazardous materials N2 - Ternary systems, which contain flammable gas, inert gas and air, were studied in order to give the user an evaluation of the ISO 10156 calculation method for the flammability of gas mixtures. While in Part 1 of this article the fire potential of flammable gases was the focal point, the influence of inert gases on the flammability of gas mixtures was studied in Part 2. The inerting capacity of an inert gas is expressed by the dimensionless K value, the so-called “coefficient of nitrogen equivalency”. The experimental determination of K values is demonstrated by using explosion diagrams. The objective of this study was to compare the estimated results, given by ISO 10156, with measurements of explosion ranges based on the German standard DIN 51649-1, given by CERN and CHEMSAFE. The comparison shows that ISO 10156, Table 1, supplies conservative K values, which can be regarded as safe in all cases. Nevertheless, in a number of cases ISO underestimates the inerting capacity, so that non-flammable gas mixtures are considered flammable. KW - Gas classification KW - Flammability KW - Explosion limits KW - Inerting KW - Calculation method PY - 2005 DO - https://doi.org/10.1016/j.jhazmat.2005.01.033 SN - 0304-3894 VL - 121 IS - 1-3 SP - 45 EP - 49 PB - Elsevier CY - Amsterdam AN - OPUS4-7448 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Tschirschwitz, Rico A1 - Schröder, Volkmar A1 - Brandes, E. A1 - Krause, U. T1 - Determination of explosion limits - Criterion for ignition under non-atmospheric conditions JF - Journal of Loss Prevention in the Process Industries N2 - Many industrial processes are run at non-atmospheric conditions (elevated temperatures and pressures, other oxidizers than air). To judge whether and if yes to what extent explosive gas(vapor)/air mixtures will occur or may be generated during malfunction it is necessary to know the safety characteristic data at the respective conditions. Safety characteristic data like Explosion limits, are depending on pressure, temperature and the oxidizer. Most of the determination methods are standardized for ambient conditions. In order to obtain determination methods for non-atmospheric conditions, particularly for higher initial pressures, reliable ignition criteria were investigated. Ignition tests at the explosion Limits were carried out for mixtures of methane, propane, n-butane, n-hexane, hydrogen, ammonia and acetone in air at initial pressures up to 20 bar. The tests have been evaluated according to different ignition criteria: visual flame propagation, temperature and pressure rising. It could be shown that flame propagation and occasionally self-sustained combustion for several seconds occurred together with remarkable temperature rise, although the pressure rise was below 3%. The results showed that the combination of a pressure rise criterion of 2% and a temperature rise criterion of 100 K seems to be a suitable ignition criterion for the determination of explosion limits and limiting oxidizer concentration at higher initial pressures and elevated temperatures. The tests were carried out within the framework of a R&D project founded by the German Ministry of Economics and Technology. KW - Explosion limits KW - Ignition criterion KW - Standardization KW - Non-atmospheric conditions PY - 2015 DO - https://doi.org/10.1016/j.jlp.2015.01.012 SN - 0950-4230 VL - 36 SP - 562 EP - 568 PB - Elsevier CY - Amsterdam AN - OPUS4-36954 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER -