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The MBLabs consortium comprises various organizations that operate testing facilities encompassing a broad spectrum of tests relevant to the construction sector, particularly building envelopes. In the future, additional testing facilities will join the METABUILDING platform to offer their services. These services will be integrated in the MBLabs Open Innovation Test Bed and accessible via the METABUILDING platform. The METABUILDING platform is operated by the METABUILDING association.
In Task 8.5 the Quality Assurance system of the MBLabs OITB is developed. The presentation gives an overview regarding the development of this system after 3 years of project execution.
In order to reduce global warming, the use of hydrogen as a renewable energy source is becoming more important. To enable this transition, unprecedently large amounts of hydrogen need to be safely transported and stored. Since hydrogen is usually stored and transported under pressure, one scenario to be considered is the release of hydrogen from a leakage with subsequent ignition. The resulting jet flame must be characterized with respect to the thermal radiation emitted into the environment to define safety distances. Various models that characterize the resulting flame shape and radiation already exist in the literature, but these are mainly based on empirical data from hydrocarbon jet flames. To verify the applicability of these models to hydrogen, real-scale tests are carried out at the BAM Test Site for Technical Safety (BAM-TTS) with the aim to assess the flame geometry and the emitted thermal radiation. Parameters such as leakage diameter (currently up to 30 mm), pressure (currently up to max. 250 bar) and mass flow (up to max. 0.5 kg/s) are varied. In particular, the focus will be 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 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. Furthermore, stationary outflow tests with hydrocarbons (methane) were also carried out, which are intended to serve as reference tests for checking flame models based on hydrocarbon data. Following from the experimental investigations, modelling parameters such as the Surface Emissive Power (SEP) and the radiant heat fraction for hydrogen and methane will be compared to literature data.
Englische Übersetzung von BAM Forschungsbericht 237! Keramische Werkstoffe haben auf Grund ihrer herausragenden tribologischen Eigenschaften in verschiedenen Bereichen der Produktion Anwendung gefunden und dadurch klassische Werkstoffe verdrängt. Gegenüber Metallen bieten sie bei Mangelschmierung sowohl unter Gleit- als auch grundsätzlich unter Wälzbeanspruchung Schutz vor adhäsivem Versagen. Hohe Herstellungskosten, bedingt bei der Endbearbeitung von Konturen mit verschiedenen und veränderlichen Radien, behindern die breite Marktdurchdringung. Mit der Modellverschleißprüfung - angelehnt an die DIN 50 324 - kann der bearbeitungsbedingte Einfluss auf das tribologische Verhalten unter Wälzreibung untersucht werden.
In this work the influence of shock waves on organic liquids with and without bubbles is investigated. The experiments were performed in a new experimental setup with the help of high speed photography and pressure measurements. The apparatus consisted of a cylindrical autoclave with a bubble generator at its bottom. For the creation of a detonation wave a tube was installed on the top of the autoclave. The following parameters were varied: The distance between neighboring bubbles, the composition of the gaseous mixture inside the bubbles, the initial pressure of the system, the initial bubble size, and the organic liquid (cyclohexane, 2-ethylhexanal, cumene, and methanol). Two different types of bubble explosion were observed. Their main difference is the length of their ignition delay. The bubble explosion type I takes place during the first oscillation after the shock wave impact. Further important results about this type of explosion refer to: - the explosion range in relation to the composition of the gas mixture within the bubble as well as to the initial bubble size. - the direct ignition of a bubble by a shock wave emitted by a nearby bubble explosion. Such a phenomenon is experimentally observed for the first time. - the shock induced ignition of gas bubbles containing an initially non explosive fuel-lean gas mixture. Optical recordings of jet penetration into the bubble prove that shock wave induced enrichment in vapor of the surrounding liquid is an important stage before the ignition. - the observation of bubble explosion type I in all the investigated liquids. - the mechanism of bubble explosion type I. The bubble explosion type II takes place with much longer ignition delay. It was observed under certain conditions only. An explosion mechanism is proposed on the basis of the experimental results. According to this mechanism, even non explosive fuel-rich gaseous bubbles can become explosive due to partial condensation of the fuel. A further group of results refer to cavitation phenomena inside the liquid and to shock induced phenomena on the surface. Additionally, the explosion limits of gaseous cyclohexane in pure oxygen at elevated pressures and temperatures were determined. The safety engineering aspects of the experimental results are discussed.
In order to reduce the human footprint of CO2 emissions and limit global warming effects hydrogen combustion is becoming increasingly important. To enable fuel cells and gas turbines to operates this carbon free fuel, unprecedently large amounts of hydrogen need to be produced and safely transported and stored. The investigation of the effects of accidents involving hydrogen is therefore becoming of outmost importance. Since hydrogen is usually stored and transported under pressure, one scenario to be considered is the release of hydrogen from a leakage with subsequent ignition. The resulting jet flame must be characterized with respect to the thermal radiation emitted into the environment to define safety regulations. Various models that characterize the resulting flame shape and radiation already exist in the literature, but these are mainly based on empirical data from hydrocarbon jet flames.[1-4] To verify these models, a H2 Jet Flame project conducted at BAM, is investigating the safety of momentum driven hydrogen jet flames. For this purpose, large-scale tests are carried out at the Test Site Technical Safety (BAM-TTS). The object of the investigations is to assess the effects of real scale release scenarios regarding flame geometry and the thermal radiation emitted. Parameters such as release angle, leakage diameter (currently 1 mm to 10 mm), pressure (currently up to max. 250 bar) and mass flow (up to max. 0.5 kg/s) are varied. In addition, influences such as the type of ignition, ignition location as well as delayed ignition can also be investigated. The gained knowledge will be compared with existing jet flame models, to validate these and identify a possible need for further development. In particular, the focus will be laid on the thermal radiation of hydrogen flames. The challenge here is the visualization and characterization of the flame geometry in an open environment. Visualization is performed using infrared (IR) camera systems from at least two viewing angles. Measurements of the heat radiation of jet flames, which can be found in 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. Furthermore, the tests can be carried out for comparative measurements with hydrocarbons (methane, etc.) as well as mixtures of hydrogen and hydrocarbons.
In order to reduce the human footprint of CO2 emissions and limit global warming effects hydrogen combustion is becoming increasingly important. To enable fuel cells and gas turbines to operates this carbon free fuel, unprecedently large amounts of hydrogen need to be produced and safely transported and stored. The investigation of the effects of accidents involving hydrogen is therefore becoming of outmost importance. Since hydrogen is usually stored and transported under pressure, one scenario to be considered is the release of hydrogen from a leakage with subsequent ignition. The resulting jet flame must be characterized with respect to the thermal radiation emitted into the environment to define safety regulations. Various models that characterize the resulting flame shape and radiation already exist in the literature, but these are mainly based on empirical data from hydrocarbon jet flames.[1-4] To verify these models, a H2 Jet Flame project conducted at BAM, is investigating the safety of momentum driven hydrogen jet flames. For this purpose, large-scale tests are carried out at the Test Site Technical Safety (BAM-TTS). The object of the investigations is to assess the effects of real scale release scenarios regarding flame geometry and the thermal radiation emitted. Parameters such as release angle, leakage diameter (currently 1 mm to 10 mm), pressure (currently up to max. 250 bar) and mass flow (up to max. 0.5 kg/s) are varied. In addition, influences such as the type of ignition, ignition location as well as delayed ignition can also be investigated. The gained knowledge will be compared with existing jet flame models, to validate these and identify a possible need for further development. In particular, the focus will be laid on the thermal radiation of hydrogen flames. The challenge here is the visualization and characterization of the flame geometry in an open environment. Visualization is performed using infrared (IR) camera systems from at least two viewing angles. Measurements of the heat radiation of jet flames, which can be found in 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. Furthermore, the tests can be carried out for comparative measurements with hydrocarbons (methane, etc.) as well as mixtures of hydrogen and hydrocarbons.
Austenitic welds and dissimilar welds are extensively used in primary circuit pipes and pressure vessels in nuclear power plants, chemical industries and fossil fuelled power plants because of their high fracture toughness, resistance to corrosion and creep at elevated temperatures. However, cracks may initiate in these weld materials during fabrication process or stress operations in service. Thus, it is very important to evaluate the structural integrity of these materials using highly reliable non- destructive testing (NDT) methods. Ultrasonic non-destructive inspection of austenitic welds and dissimilar weld components is complicated because of anisotropic columnar grain structure leading to beam splitting and beam deflection. Simulation tools play an important role in developing advanced reliable ultrasonic testing (UT) techniques and optimizing experimental parameters for inspection of austenitic welds and dissimilar weld components. The main aim of the thesis is to develop a 3D ray tracing model for quantitative evaluation of ultrasonic wave propagation in an inhomogeneous anisotropic austeniticweld material. Inhomogenity in the anisotropic weld material is represented by discretizing into several homogeneous layers. According to ray tracing model, ultrasonic ray paths are traced during its energy propagation through various discretized layers of the material and at each interface the problem of reflection and transmission is solved. The influence of anisotropy on ultrasonic reflection and transmission behaviour in an anisotropic austenitic weld material are quantitatively analyzed in three dimensions. Theultrasonic beam directivity in columnar grained austenitic steel material is determined three dimensionally using Lamb’s reciprocity theorem. The developed ray tracing model evaluates the transducer excited ultrasonic fields accurately by taking into account the directivity of the transducer, divergence of the ray bundle, density of rays and phase relations as well as transmission coefficients. The ray tracing model is able to determine the ultrasonic wave fields generated by a point source as well as finite dimension array transducers.
The motivation of this study was to pursue effective eco-friendly and economical flame retarded polymer materials. With wide-ranging advantages such as improved fire and physical properties, halogen-free and relatively low cost, layered silicate / epoxy nanocomposite (EP_LS) was targeted for high efficiency of flame retardancy. One main goal of this study was to increase the understanding of the flame retardancy phenomenon in EP_LS by assessing the shielding effect of the protection layer experimentally and quantitatively. Another main goal of this study was to optimize the flame retardancy by the shielding effect in EP_LS.
Generally accepted quality criteria for the comparison of immunoassays are still missing and assay conditions vary greatly between different laboratories. To address this problem, the influence of different parameters on the overall assay performance was assessed, specifically for different enzyme immunoassays (EIAs) for the anthropogenic markers caffeine (CAF) and carbamazepine (CBZ). Special emphasis was dedicated to the parameters temperature, assay format and enzyme-substrate combination. The temperature parameter was systematically studied for all incubation steps of the direct EIA formats employing the photometric horseradish peroxidase (HRP) substrate 3,3’,5,5’- tetramethylbenzidine (TMB) and the fluorometric HRP substrate 3-(4-hydroxyphenyl)propionic acid for both analytes. A temperature decrease only during the competition step led to an increase in assay sensitivity by a factor of 10 to 15 for CBZ and CAF, respectively, independent of the enzyme substrate used. Room temperature experiments yielded the smallest coefficients of variations, minimizing the edge effect. The influence of the assay format on different performance parameters was studied with the determination of CAF in consumer products. In addition to the HRP substrates, the enzyme alkaline phosphate (AP) and its chromogenic substrate para-nitrophenyl phosphate and a fluorescent substrate, 4-methylumbelliferyl phosphate, were employed. Seven quality criteria were defined and validated to compare these immunoassays. The evaluation of the four criteria (sensitivity, measurement range, relative dynamic range and goodness of fit) for the standard curves revealed that the direct format is superior to the indirect format, with the HRP TMB format showing the best performance. Three additional criteria for an applicationdriven analysis of real samples, in this case CAF-containing beverages and cosmetics, confirmed this result in terms of accuracy as well as intra- and inter-plate precision. The enzyme-substrate combination was investigated when several direct CBZ assays were applied to the analysis of water samples; here, three HRP assays and four AP assays were studied, along with luminescence detection. The HRP assays reached better sensitivities and lower quantifiable concentrations compared to the AP assays. Only the HRP assays and the chemiluminescent AP juice assay fulfilled the requirements for the four criteria applied to standard curves; all other AP assays were not considered for application to real samples based on these criteria. The AP juice assay can only be employed for influent samples whereas all HRP assays are applicable to influent and effluent wastewater samples according to intra- and inter-plate precision. Furthermore, the HRP assays alone are suitable for surface water analysis; here, the chromogenic HRP TMB assay yielded the best results, as any type of water sample can be quantified with high precision. Whether these quality criteria, derived here for standard curves as well as their application to real samples, can be transferred to other immunoassay formats for quality assurance remains to be shown.
Plasma chemical methods are well suited for introducing functional groups to the surface of chemically inert polymers such as polyolefins. However, a broad variety of functional groups is often formed. Unfortunately, for further chemical processing such as grafting of molecules for advanced applications a highly dense and monotype functionalized polyolefin surface is needed. Therefore, the main task was to develop a selective surface functionalization process, which forms preferably one type of functional groups at the surface in high and variable concentration. Amongst the novel plasma methods, the under-water plasma process (UWP) is one of most attractive to solve the problem of monotype functionalization. Such plasma is an efficient source of ions, electrons, UV-radiation, high frequency shock waves, radicals such as hydroxyl radical and reactive neutral molecules such as hydrogen peroxide, hydrogen and oxygen. It was found that underwater plasma and the closely related glow discharge electrolysis are interesting new methods for polymer surface functionalization. An effective modification into the topmost surface chemistry of polymer layer was observed by the collective effect of wet-chemistry, electrochemistry, atmospheric gas discharges, irradiation, and shock waves. Underwater capillary discharge was seen more effective in -OH functionalization and was largely seen as a flow dominated process because of the shock wave turbulences. Using such water-based plasma a fraction of 25-40% of all O-functional groups was produced as OH-groups in comparison to <10% OH produced in the oxygen low- pressure plasma. The exact concentration of the OH functionality was studied by TFAA gas phase derivatization and measuring the respective fluorine concentration by photoelectron spectroscopy (XPS). In contrast to established gas phase glow discharge processes, the water phase absorbs and therefore limits the particle and radiation energy and thus the energy input into the polymer. Extensive oxidation, degradation, cross-linking and radical formation in the polymer is more limited than under gas plasma exposure because of the liquid water environment, which moderates high energetic plasma species. The variety of plasma produced species in the water phase is also much smaller because of the limited reaction possibilities of the plasma with water. The possibility to admix a broad variety of chemical additives makes underwater plasma additionally highly attractive for the chemist. At last, the water removes all low-molecular weight oxidized products formed by plasma-induced polymer degradation. Hydrogen peroxide and the catalyst (Fe-ZSM5) should influence or increase the equilibrium concentration of OH radicals in the underwater process. It was supposed that these radicals play the most important role for OH functionalization of polyolefin surfaces. Hydrogen peroxide was believed to be the most prominent precursor for OH group formation in the UWP. The catalyst should modulate the steady state of OH group formation and recombination, and thus accelerate the functionalization. This was confirmed by an increased oxidation rate. Owing to the detection limit of XPS the C-O bond selectivity was defined as clearly resolvable subpeak within the C1s signal assigned to C-OH, C-O-C and other singly C-O bonded species. This bondamounts 47 C-O bonds/100 O atoms with pure UWP system and enhances to a maximum of the 81 C-O bonds/100 O atoms using the Fe-ZSM5 catalyst system. Therefore, this method exhibits a great progress for a start. However, after TFAA derivatization the fraction of desired OH groups could not be significantly increased. In the continuation acetic acid, acrylic acid, maleic and itaconic acid were used as additive monomers. The chemical selectivity in -COOH bond formation using bi-carboxylic additives was seen inferior. Acetic acid is not a chemically polymerizing monomer but it could polymerize by monomer/molecular fragmentation and recombination to a cross linked layer. The other monomers form preferably water-soluble polymers on a preferred chemical way. Only the fragmented fraction of these monomers could form an insoluble coating by cross linking to substrate. The XPS analysis was used to track the alterations in COO- bond percentage on the PP surface. To identify the -COOH groups on substrate surface unambiguously, which have survived the plasma polymerization process, the gas phase derivatization with trifluoroethanol was performed. A much higher yield in COOH groups was achieved using the glow discharge electrolysis and acrylic acid.