TY - JOUR A1 - Keim, Vincent A1 - Paredes, Marcelo A1 - Nonn, Aida A1 - Münstermann, Sebastian T1 - FSI-simulation of ductile fracture propagation and arrest in pipelines BT - Comparison with existing data of full-scale burst tests JF - International Journal of Pressure Vessels and Piping N2 - The fracture propagation and arrest control for pipelines transporting rich natural gases and high vapor pressure liquids is based on the Battelle Two-Curve Model (BTCM). Distinct limitations of this model were demonstrated for past and modern steels and gas mixtures. These can be related to the insufficient description of individual physical processes and interactions between the pipe material and transported mixture during the running ductile fracture. In the past, fluid-structure interaction (FSI) models enabled a more sophisticated, coupled analysis of the failure scenario. To quantify their capability of describing the multi-physical processes, the FSI models need to be verified by experimental data from full-scale burst tests (FSBT). Therefore, this paper deals with the simulation of five FSBTs from the literature on API grade X65 pipes with different pipe geometries, mixtures and initial conditions. The FSI is modeled by the coupled Euler-Lagrange (CEL) method. The modified Mohr-Coulomb (MMC) model is implemented in the CEL framework to describe the deformation and ductile fracture in the X65/L450 pipes. 3D Euler equations are used to calculate the mixture decompression with the GERG-2008 equation of state defining the volumetric behavior of a CO2-rich mixture, CH4 and H2. The extended model considers the effect of soil backfill on the pipe deformation and inertia. The numerical predictions agree well with the experimental findings in terms of the crack propagation speed and arrest length underlining the capability of the developed numerical tool. KW - Running ductile fracture KW - Crack arrest KW - Fluid-structure interaction KW - MMC model KW - CO2 decompression KW - Bruchmechanik KW - Fluid-Struktur-Wechselwirkung KW - Pipeline KW - Simulation Y1 - 2020 U6 - https://doi.org/10.1016/j.ijpvp.2020.104067 VL - 182 IS - May PB - Elsevier ER - TY - JOUR A1 - Keim, Vincent A1 - Nonn, Aida A1 - Münstermann, Sebastian T1 - Application of the modified Bai-Wierzbicki model for the prediction of ductile fracture in pipelines JF - International Journal of Pressure Vessels and Piping N2 - The complex mechanical and corrosive loads of modern pipeline systems transporting oil, natural gas and CO2 impose steadily increasing requirements on material properties. The majority of current design standards still limit the application of modern high toughness linepipe steels due to the simple specification of material requirements in terms of energy levels from Charpy impact or Battelle Drop-Weight-Tear (BDWT) tests. In consequence, research activities have been conducted recently aiming at developing modified or novel experimental methods for the characterization of the ductile fracture behavior. To quantify the effects of various parameters on fracture behavior and derive suitable correlations, it is necessary to accompany these activities by numerical simulations with appropriate ductile damage models. In this paper, the MBW model is applied to study the structural behavior of pipelines in ductile fracture regime. Due to its precise incorporation of the underlying load conditions, the damage model is successfully used to simulate the slant fracture behavior in Battelle Drop weight tear test specimens and pipe sections. In comparison to ductile damage models applied in former studies, namely the Gurson-Tvergaard-Needleman and Cohesive Zone model, the presented numerical methodology allows for a more detailed investigation of loading, material and geometry effects on fracture and crack arrest behavior of pipelines. KW - Running ductile fracture KW - Stress state conditions KW - MBW model KW - Pipeline failure KW - Slant fracture Y1 - 2019 U6 - https://doi.org/10.1016/j.ijpvp.2019.02.010 VL - 171 IS - March SP - 104 EP - 116 PB - Elsevier ER - TY - CHAP A1 - Steininger, Peter A1 - Gaderer, Matthias A1 - Dawoud, Belal T1 - Transient performance of a solar selective thermal insulation system T2 - 16th Advanced Building Skins Conference & Expo, 21 – 22/10/2021, Bern, Switzerland N2 - A prototype of a thermal insulation system to offer high selectivity of the solar gain regarding the solar incidence angle (SATIS) was applied to a typical solid brick masonry for existing buildings in Germany. Light conducting elements (LCEs) inclined at 19 ° were incorporated in SATIS, which equals the average solar noon angle in southern Germany during winter. The entire wall construction was experimentally investigated in a differential climatic chamber test bench at four different irradiation angles according to a dynamic test procedure. In addition, a conventional wall construction (CWC) has been measured. At SATIS’ design angle of 19 °, the SATIS wall construction shows a solar gain (SG) of 394.5 Wh/m², while the SG of the CWC amounts to only 25.4 Wh/m². The validated transient model of the SATIS wall construction showed that, at the end of the irradiation period of the dynamic test procedure (8 h), the solar heat penetrates to a depth of 253 mm and 111 mm inside the 385 mm thick brick wall masonry at the irradiation angles of 19 ° and 50 °, respectively. During the same time, the stored solar energy at 50 ° amounts to only 24.4 % of that stored at 19 °. Y1 - 2021 UR - https://www.researchgate.net/publication/355771950_Transient_performance_of_a_solar_selective_thermal_insulation_system PB - Advanced Buidling Skins GmbH ER - TY - JOUR A1 - Schächinger, J. A1 - Brückl, Oliver A1 - Becker, Mark A1 - Lechner, Raphael T1 - Results of the Research Project Optibiosy: Biogas plants as stabilizers of the power system? JF - BWK ENERGIE T2 - Biogasanlagen als Stabilisatoren des Stromsystems? Y1 - 2022 SN - 1436-4883 VL - 74 IS - 11-12 SP - 34 EP - 39 PB - VDI-Verlag CY - Düsseldorf ER - TY - RPRT A1 - Klitsman, Maksym A1 - Staudacher, Lars A1 - Brückl, Oliver A1 - Eller, Johannes A1 - Brey, Ludwig A1 - Eigenstetter, Florian T1 - neos - NetzEntwicklungsOffensive Strom - Schlussbericht BT - Projektlaufzeit: 01.09.2017 – 31.12.2021; gefördert durch Bayerisches Staatsministerium für Wirtschaft, Landesentwicklung und Energie N2 - Im Zuge der Energiewende werden die erneuerbaren Energien zur tragenden Säule unserer Stromversorgung. Bis 2025 sollen bundesweit 40-45 % des Stroms aus erneuerbaren Quellen stammen, bis 2050 sogar 80 %. Dabei wird der erzeugte Strom hauptsächlich aus Wind und Sonne stammen. Im Norden der Bundesrepublik wird Wind die Erzeugung dominieren, während im Süden, insbesondere in Bayern der Strom vornehmlich aus Photovoltaik gewonnen werden wird. Um die Ziele der Energiewende zu erreichen, wird neben den ausreichenden Erzeugungskapazitäten auch eine leistungsfähige Infrastruktur zur Verteilung und Nutzung des erneuerbaren Stroms notwendig sein. Planbarkeit und Sicherung der Versorgungsqualität bei zunehmenden Anteilen von volatiler Erzeugung werden dabei zu einer immer größeren Herausforderung. Das Projekt neos hat im engen Verbund mit den beteiligten Partnern wichtige tagesaktuelle Fragestellungen wissenschaftlich erörtert und untersucht, die sich durch die laufende Transformation des Energiesystems und den rasanten Ausbau der Anlagen zur erneuerbaren Energieerzeugung den Projektpartnern stellen. KW - Intelligentes Stromnetz KW - Energiewende KW - Netzplanung KW - Netzausbau KW - Elektromobilität KW - Spannungsqualität KW - regelbarer Ortsnetztransformator KW - Oberschwingungsbelastung KW - Netzberechnung KW - intelligente Netzbetriebsmittel Y1 - 2022 U6 - http://nbn-resolving.de/urn/resolver.pl?urn:nbn:de:bvb:898-opus4-45248 ER - TY - CHAP A1 - Haumer, Anton A1 - Kral, Christian T1 - The New EDrives Library: A Modular Tool for Engineering of Electric Drives T2 - Proceedings of the 10th International Modelica Conference, March 10-12, 2014, Lund, Sweden N2 - Simulation is an indispensable tool for the engineering of systems containing electric drives. Depending on the design phase and the engineering task different levels of modeling details are required: proof of concept; investigation of energy and power consumption; design of control; etc. The new EDrives library provides three levels of abstraction for inverters: quasi static (neglecting electrical transients); averaging (neglecting switching effects) and switching – for serving different demands. The inverters can feed the machine models of the Modelica Standard Library: Modelica.Magnetic.FundamentalWave and the new Modelica.Magnetic.QuasiStatic.FundamentalWave. The EDrives library copes with arbitrary phase numbers and can be easily extended to develop new control algorithms. In this publication the structure of the library and the implemented control principles are presented. Furthermore; examples comparing the three different levels of abstraction are included. KW - control KW - Electric machines and drives KW - multi phase KW - power electronics KW - quasi static KW - switching KW - thermal behavior KW - transient Y1 - 2014 SN - 978-91-7519-380-9 U6 - https://doi.org/10.3384/ecp14096155 SN - 1650-3686 SN - 1650-3740 SP - 155 EP - 163 PB - Linköping University Electronic Press ER - TY - JOUR A1 - Gragger, Johannes V. A1 - Haumer, Anton A1 - Einhorn, Markus T1 - Averaged Model of a Buck Converter for Efficiency Analysis JF - Engineering Letters N2 - In this work a buck converter model for multidomain simulations is proposed and compared with a state-of-the-art buck converter model. In the proposed model no switching events are calculated. By avoiding the computation of the switching events in power electronic models the processing time of multidomain simulations can be decreased significantly. The proposed model calculates any operation point of the buck converter in continuous inductor current conduction mode (CICM) while considering the conduction losses and switching losses. It is possible to utilize the proposed modeling approach also for other dc-to-dc converter topologies. Laboratory test results for the validation of the proposed model are included. Y1 - 2010 UR - https://www.researchgate.net/profile/Markus-Einhorn/publication/41668038_Averaged_Model_of_a_Buck_Converter_for_Efficiency_Analysis/links/55100b490cf21287416cb105/Averaged-Model-of-a-Buck-Converter-for-Efficiency-Analysis.pdf VL - 18 CY - Hong Kong ER - TY - THES A1 - Heberl, Michael T1 - Power-to-Ammoniak BT - Möglichkeiten zur erneuerbaren Elektrifizierung und Dekarbonisierung der Ammoniakindustrie N2 - Ammoniak ist Grundbaustein für die Herstellung von Düngemitteln und dementsprechend für die Nahrungsmittelindustrie unentbehrlich. Ca. 40-50 % der Weltbevölkerung sind von Nahrungsmitteln abhängig, die mit Hilfe von Ammoniakdüngern hergestellten wurden. Weltweit wurden alleine im Jahr 2015 181 Mt Ammoniak produziert, wodurch die Ammoniakherstellung mit 1,2 % am gesamten Energieverbrauch der Welt beteiligt ist und für 0,93 % der globalen Treibhausgasemissionen zuständig ist. Auch in Zeiten der Energiewende ist diese Grundstoffchemikalie unentbehrlich, ist aber auf einem anderen Wege herzustellen. Ziel dieser Arbeit ist die Darstellung verschiedener Möglichkeiten zur erneuerbaren Elektrifizierung und Dekarbonisierung der Ammoniakindustrie, wodurch der Einsatz von herkömmlichen Energieträgern wie Erdgas, Kohle und Öl negiert werden kann. Ammoniak wird aktuell über das Haber-Bosch-Verfahren aus den Rohstoffen Erdgas, Kohle und Öl gewonnen. Bei diesem Verfahren wird über einen Primär- und Sekundärreformer Wasserstoff und Stickstoff gewonnen. Andere Gasbestandteile werden gefiltert oder umgewandelt, um schädliche Katalysatorgifte (CO, H2S) zu entfernen. Im Reaktor wird an Eisenkatalysatoren aus Wasserstoff und Stickstoff letztendlich Ammoniak hergestellt. Der Energieverbrauch des Haber-Bosch Verfahrens schwankt zwischen 7,8 MWh/t NH3 für eine moderne und sehr effiziente Anlage mit Erdgas und 13,6 MWh/t NH3 für eine alte mit Kohle betriebene Anlage. An Emissionen treten pro hergestellter Tonne Ammoniak je nach Rohstoff 1,6-3,8 t CO2-eq auf. Neben der Biomassevergasung gibt es mehrere rein elektrische Ansätze zur Ammoniakherstellung. Die unterschiedlichen elektrochemischen Ansätze zur direkten Ammoniaksynthese, wie der Einsatz von Flüssigsalzelektrolyten oder Feststoffelektrolyten, wurden in Abschnitt 3.2 vorgestellt. Einige dieser Technologien zeigen vielversprechende Ansätze, sind jedoch zum aktuellen Zeitpunkt noch zu weit von einem industriellen Einsatz entfernt. Der Einsatz der Wasserelektrolyse in Kombination mit einer Luftzerlegungseinheit ist die derzeit vielversprechendste Methode Ammoniak auf einem strombasierten und dekarbonisierten Wege herzustellen. Bei diesem System wird Wasserstoff im Elektrolyseur und Stickstoff in der Luftzerlegungseinheit hergestellt. Die Ammoniaksynthese findet hierbei in einem Reaktor nach Vorbild des Haber-Bosch-Prozesses statt. Mit diesem System ist ein Energieverbrauch von ca. 10 MWh/t NH3 notwendig. Durch den Einsatz von rein erneuerbar hergestelltem Strom als Energieträger lässt sich mit diesem Technologiezusammenschluss die Ammoniakherstellung komplett Emissionsfrei gestalten. Dadurch können alleine in Deutschland jährlich bis zu 7,8 Mt CO2-eq eingespart werden. Eine zukünftige Umstrukturierung der Ammoniakherstellung und der gesamten chemischen Industrie ist unabdingbar. Diese kann aber nur parallel mit einem Ausbau erneuerbarer Energien umgesetzt werden. Mit der Wasserelektrolyse und der Luftzerlegungseinheit sind die technischen Möglichkeiten für diesen Umbau bereits heute gegeben und brauchen nur noch eingesetzt werden. N2 - Ammonia is a fundamental raw material for the production of fertilizer and essential for the food industry. About 40-50 % of the world population depends on food produced with the assistance of ammonia fertilizers. In 2015 181 Mt ammonia was produced worldwide. The ammonia production is responsible for 1,2 % of the global energy consumption and 0,93 % of the global greenhouse gas emissions. Even in times of the energy transition this base chemical is essential, although it should be produced on a different way. It is therefore the objective of this work to show different possibilities for an electrified and decarbonised ammonia industry powered by renewable energies. As a result the use of conventional energy carriers like gas, coal and oil will be negotiated. Ammonia is produced with the Haber-Bosch process from gas, coal and oil as feedstock. In this process a primary and a secondary reformer is used to produce hydrogen and nitrogen. Other gaseous components are filtered and converted to remove catalyst poisons (CO, H2S). In the reactor iron catalysts are used to produce ammonia out of hydrogen and nitrogen. The energy consumption of the Haber-Bosch process varies between 7,8 MWh/t NH3 for a modern and really efficient gas based plant and 13,6 MWh/t NH3 for an old coal based plant. The production of one ton ammonia causes emissions between 1,6-3,8 t CO2-eq based on the used feedstock. Beside biomass gassing there are several electric technologies to produce ammonia. The different electrochemical technologies to synthesize ammonia on a direct way, like solid state electrolysis or molten salt electrolytes, are shown in section 3.2. Some of these technologies show a good potential, but all of them are far off the use in the industry. The use of an electrolyser in combination with an air separation unit is the most promising way to produce ammonia on an electrified and decarbonised way. In this system hydrogen is produced in the electrolyser and nitrogen in the air separation unit. The ammonia synthesis works in a reactor based on the Haber-Bosch process. Using this system the production of one ton ammonia has an energy consumption of 10 MWh. With the use of renewable energies in this combination of technologies a greenhouse gas emissions free ammonia production is possible. In Germany alone 7,8 t CO2-eq can be saved. A future reorganization of the ammonia industry and the complete chemical industry is indispensable. A parallel expand of renewable energies is necessary to realize this approach. With electrolysers and air separation units the technical possibilities for this reconstruction are already given. All that remains is the implementation of them. KW - Ammoniaksynthese KW - Haber-Bosch KW - Emissionen KW - Erneuerbare Energien Y1 - 2021 U6 - http://nbn-resolving.de/urn/resolver.pl?urn:nbn:de:bvb:898-opus4-22167 ER - TY - JOUR A1 - Gärtner, Sebastian A1 - Marx-Schubach, Thomas A1 - Gaderer, Matthias A1 - Schmitz, Gerhard A1 - Sterner, Michael T1 - Techno-Economic Analysis of Carbon Dioxide Separation for an Innovative Energy Concept towards Low-Emission Glass Melting JF - energies N2 - The currently still high fossil energy demand is forcing the glass industry to search for innovative approaches for the reduction in CO2 emissions and the integration of renewable energy sources. In this paper, a novel power-to-methane concept is presented and discussed for this purpose. A special focus is on methods for the required CO2 capture from typical flue gases in the glass industry, which have hardly been explored to date. To close this research gap, process simulation models are developed to investigate post-combustion CO2 capture by absorption processes, followed by a techno-economic evaluation. Due to reduced flue gas volume, the designed CO2 capture plant is found to be much smaller (40 m3 absorber column volume) than absorption-based CO2 separation processes for power plants (12,560 m3 absorber column volume). As there are many options for waste heat utilization in the glass industry, the waste heat required for CO2 desorption can be generated in a particularly efficient and cost-effective way. The resulting CO2 separation costs range between 41 and 42 EUR/t CO2, depending on waste heat utilization for desorption. These costs are below the values of 50–65 EUR/t CO2 for comparable industrial applications. Despite these promising economic results, there are still some technical restrictions in terms of solvent degradation due to the high oxygen content in flue gas compositions. The results of this study point towards parametric studies for approaching these issues, such as the use of secondary and tertiary amines as solvents, or the optimization of operating conditions such as stripper pressure for further cost reductions potential. KW - economic evaluation KW - CO2-separation KW - glass industry KW - oxyfuel KW - methanation KW - power-to-gas Y1 - 2023 U6 - http://nbn-resolving.de/urn/resolver.pl?urn:nbn:de:bvb:898-opus4-53627 N1 - Corresponding author: Sebastian Gärtner VL - 16 IS - 5 SP - 1 EP - 25 PB - MDPI CY - Basel ER - TY - JOUR A1 - Freni, Angelo A1 - Frazzica, Andrea A1 - Dawoud, Belal A1 - Chmielewski, Stefanie A1 - Calabrese, Luigi A1 - Bonaccorsi, Lucio Maria T1 - Adsorbent coatings for heat pumping applications: Verification of hydrothermal and mechanical stabilities JF - Applied Thermal Engineering N2 - This paper presents novel experimental methods for verification of both hydrothermal and mechanical stabilities of adsorbent coatings. Experiments have been carried out on zeolite-based coatings over aluminum substrates, prepared by a dip-coating technique developed at CNR-ITAE. Hydrothermal aging of several adsorbent coatings is ongoing. Adsorption and structural stability of some samples under test was successfully verified after 35000 aging cycles by isobars measurement and XRD analysis. Mechanical properties of coatings have been evaluated by applying different typologies of static and dynamic mechanical stresses. Results obtained have been compared with those achieved by subjecting adsorbent coatings prepared by Mitsubishi Plastic Incorporation (MPI) to the same characterization protocol. The comparison between the two types of coating returned that MPI coatings posses similar thermal stability and better mechanical strength than CNR-ITAE coatings. KW - Adsorbent coating KW - Adsorption heat pump KW - Hydrothermal stability KW - Mechanical stability Y1 - 2013 U6 - https://doi.org/10.1016/j.applthermaleng.2011.07.010 VL - 50 IS - 2 SP - 1658 EP - 1663 PB - Elsevier ER -