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For the classification and safe handling and use of the chemicals, special standardized testing proce-dures have been developed and are used world-wide. Safety experts must be able to fully rely on the precise execution of the respective laboratory tests and assessments. In this context interlaboratory tests (round robin tests, interlaboratory comparisons / intercomparisons) are a crucial element of a laboratory's quality system. Participation in interlaboratory tests is explicitly recommended by the standard ISO/IEC 17025.
The present document reports on the results of the interlaboratory test 2010/2011 on the test method DIN EN 15188:2007 “Determination of the spontaneous ignition behaviour of dust accumulations” [1] which was organized by the Center for Quality Assurance for Testing of Dangerous Goods and Haz-ardous Substances.
The test method DIN EN 15188:2007 is applied to characterize the self-ignition behaviour of combus-tible dusts. The experimental basis for describing the self-ignition behaviour of a given dust is the de-termination of the self-ignition temperatures (TSI) of differently-sized volumes of the dust sample by isoperibolic hot storage experiments (storage at constant oven temperatures) in commercially availa-ble ovens. The results thus measured reflect the dependence of self-ignition temperatures upon dust volume [1].
Several internal investigations and interlaboratory comparisons in the past have shown significant differences between the lab-specific results of hot storage tests.
Figure 2-1 shows the Pseudo-Arrhenius plot of hot storage tests of eight different laboratories (Round Robin Test 2002, BAM). The dust under this investigation was Lycopodium powder (spores). The par-ticipants of this interlaboratory test used different laboratory ovens (size, ventilation) as well as differ-ent sample baskets (shape, mesh size, single- and double-walled).
Figure 2-1 shows clearly that this test failed to produce reasonable reproducibility of the TSI between the different laboratories. As possible reasons for the deviations have been identified lab-specific dif-ferences, e.g.:
- oven ventilation (enforced, natural convection),
- oven size,
- sample baskets,
- radiation effects,
- measuring precision (temperature difference between tests with ignition and no ignition),
- minimum sample size.
To reduce the differences between the labs it was necessary to ameliorate the testing method and to improve the execution of the method by the lab. From there, the installation of an inner chamber into the laboratory oven was suggested as experimental set-up in EN 15188:2007 to provide more repro-ducible test conditions. The aappropriateness of this set-up has not been verified yet.
The current interlaboratory test 2010-2011 focuses on the use of a special mesh wire screen and spe-cial volumes of the sample baskets (cubes) to normalise/harmonise the test conditions in the different labs. In preparation for the interlaboratory test a joint program between Syngenta and BAM has been initiated in 2009. As a result of these investigations a modified set-up ( chapter 3) has been identi-fied to be probably more appropriate than the suggested set-up in DIN EN-15188:2007.
Due to the time-consuming test procedure and to optimize the workflow for the laboratories this in-terlaboratory test should be performed stepwise as a multi-level test ( chapter 5.4) on one typical test sample.
Mechanically stable structures with interconnected hierarchical porosity combine the benefits of both small
and large pores, such as high surface area, pore volume, and good mass transport capabilities. Hence, lightweight micro-/meso-/macroporous monoliths are prepared from ordered mesoporous silica COK-12 by means of spark plasma sintering (SPS, S-sintering) and compared to conventionally (C-) sintered monoliths. A multi-scale model is developed to fit the small angle X-ray scattering data and obtain information on the hexagonal lattice parameters, pore sizes from the macro to the micro range, as well as the dimensions of the silica population. For both sintering techniques, the overall mesoporosity, hexagonal pore ordering, and amorphous character are preserved. The monoliths' porosity (77–49%), mesopore size (6.2–5.2 nm), pore volume (0.50–0.22 g cm-3
), and specific surface area (451–180 m2 g-1) decrease with increasing processing temperature and pressure. While the difference in porosity is enhanced, the
structural parameters between the C-and S-sintered monoliths are largely converging at 900 C, except for the mesopore size and lattice parameter, whose dimensions are more extensively preserved in the
S-sintered monoliths, however, coming along with larger deviations from the theoretical lattice. Their higher mechanical properties (biaxial strength up to 49 MPa, 724 MPa HV 9.807 N) at comparable porosities and ability to withstand ultrasonic treatment and dead-end filtration up to 7 bar allow S-sintered monoliths to reach a high permeance (2634 L m-2 h-1 bar-1), permeability (1.25 x 10^-14 m2), and ability to reduce the chemical oxygen demand by 90% during filtration of a surfactant-stabilized oil in water emulsion, while indicating reasonable resistance towards fouling.
Die sichere Lagerung und der Transport von Flüssigwasserstoff (LH2) verlangen nach verlässlichen Abschätzungen möglicher Risiken durch Feuer oder Explosion. Aufgrund des breiten Explosionsbereichs (4 Vol.-% - 74 Vol.-%) reagiert Wasserstoff sehr schnell und produziert hohe Flammentemperaturen. Da Wasserstoffflammen ruß- bzw. farblos sind, ist Wärmestrahlung im Fernfeld kein Risikofaktor. Allerdings stellen die hohe lokale Wärmestrahlung und die nicht sichtbaren Flammen eine Gefahr für Menschen und Infrastruktur in der Nähe dar. Es ist daher notwendig die Gefahren von LH2-Feuern sorgfältig zu bewerten.
Einerseits sind experimentelle Untersuchungen verschiedener Szenarien teuer, andererseits können sie teilweise auch praktisch nicht durchführbar sein. Numerische Simulationen dieser Szenarien können ein Ausweg aus diesem Problem sein. In der vorliegenden Arbeit wird ein solcher Ansatz genutzt, um große Brandszenarien mit LH2 mittels CFD (Computational Fluid Dynamics) zu modellieren und so die notwendigen Sicherheitsabstände abzuschätzen. Der Fokus liegt dabei auf der Simulation von Jet- und Pool-Feuerszenarien mit einem kommerziellen CFD-Code (Ansys CFX). Die benötigten geometrischen Modelle werden für Jet- und Pool-Feuer erstellt und mit den nötigen Randbedingungen implementiert. Wichtige Submodelle für chemische Reaktionen (Einschritt- und detaillierte Modelle), Verbrennung (Eddy-Dissipation- und Flamelet-Modell) und Strahlung (Discrete-Transfer-Modell) werden genutzt. Die maximal simulierten Flammentemperaturen liegen bei ~2100 K für Jet-Feuer und ~2300 K für Pool-Feuer. Um Aussagen zu thermischen Sicherheitsabständen zu treffen, wurden die Spezifischen Ausstrahlungen (SEP) ermittelt und anschließend entsprechende Positionsfaktoren gewählt, um verlässliche Sicherheitsabstände zu berechnen. Je nach Bedarf können CFD-Modelle sowohl für qualitative als auch für quantitative Risikobewertungen von LH2-Großbränden genutzt werden.
CFD (Computational Fluid Dynamics) simulations have been carried out to investigate the behavior of turbulent, subsonic jet fires of the peroxy-fuel Di-tert-butyl peroxide (DTBP) using the SAS-SST turbulence model, the discrete transfer radiation model, the eddy dissipation combustion model and the Magnussen soot model. Safety relevant parameters, such as flame length, temperature and thermal radiation are predicted to give recommendations on safety distances.
For the classification, safe handling and use of the chemicals, special standardized testing procedures have been developed and are used worldwide. Safety experts must be able to fully rely on the precise execution of the respective laboratory tests and assessments. In this context, interlaboratory tests are a crucial element of a laboratory's quality system. Participation in interlaboratory tests is explicitly recommended by the standard ISO/IEC 17025.
The present document reports the results of the interlaboratory test 2015-2016, which was performed on the test method DIN EN 15188:2007 “Determination of the spontaneous ignition behaviour of dust accumulations”. It was organized by BAM in the frame of the co-operation project CEQAT-DGHS Centre for Quality Assurance for Testing of Dangerous Goods and Hazardous Substances.
The test method DIN EN 15188:2007 is applied to characterize the self-ignition behaviour of combustible dusts. The experimental basis for describing the self-ignition behaviour of a given dust is the determination of the self-ignition temperatures (TSI) of differently-sized volumes of the dust sample by isoperibolic hot storage experiments (storage at constant oven temperatures) in commercially available ovens. The results measured this way reflect the dependence of the self-ignition temperatures on the volume of a dust accumulation.
The interlaboratory test 2015-2016 on the method DIN EN 15188:2007 is the latest in a systematic stepwise built up series of method validation interlaboratory tests and internal laboratory investigations. The aim of this interlaboratory test was to determine measurement uncertainties of the modified method DIN EN 15188 for different substances, covering a sufficiently wide range of self-ignition behaviours in the scope of the DIN EN 15188 of the four basket test to extrapolate to storage volumes up to 1000 m³ and the single basket test for a basket volume of 1000 cm³.
The precision of the four basket test and the single basket of the modified method DIN EN 15188 can be assessed as acceptable for the four sample materials investigated in the current interlaboratory test 2015-2016. It was possible to derive a functional equation for the measurement uncertainty U depending on the storage volume V. The measurement uncertainty cannot be ignored and must be considered, if TSI results should be used in practice.
Dual-phase membranes for high-temperature carbon dioxide Separation have emerged as promising technology to mitigate anthropogenic greenhouse gases emissions, especially as a pre- and post-combustion separation technique in coal burning power plants. To implement These membranes industrially, the carbon dioxide permeability must be improved. In this study, Ce_(0.8) Sm_(0.2) O_(2-d) (SDC) and Ce_(0.8)Sm_(0.19)Fe_(0.01)O_(2-d) (FSDC) ceramic powders were used to form the skeleton in dual-Phase membranes. The use of MgO as an environmentally friendly pore generator allows control over the membrane porosity and microstructure in order to compare the effect of the membrane’s ceramic phase. The ceramic powders and the resulting membranes were characterized using ICP-OES, HSM, gravimetric analysis, SEM/EDX, and XRD, and the carbon dioxide flux density was quantified using a high-temperature membrane permeation setup. The carbon dioxide permeability slightly increases with the addition of iron in the FSDC membranes compared to the SDC membranes mainly due to the reported scavenging effect of iron with the siliceous impurities, with an additional potential contribution of an increased crystallite size due to viscous flow sintering. The increased permeability of the FSDC system and the proper microstructure control by MgO can be further extended to optimize carbon dioxide permeability in this membrane system.
Polycarboxylate ethers (PCEs) are widely used in construction, but the exact nature of their interaction with cement is still debated. Aiming at a better understanding of the role of tricalcium Aluminate (C3A) in cement hydration, we assessed the potential of optical spectroscopy in combination with a water-soluble fluorescent organic reporter dye (S0586) to monitor the early hydration of C3A in the presence of 26 wt% CaSO4.2H2O (C3A26G-S) with and without PCE. As optical methods, steady-state fluorescence and diffuse reflectance (UV–VisDR) spectroscopy were employed. Phase characterization and particle size distribution were performed with in-situ X-ray diffraction (in-situ XRD) and dynamic light scattering (DLS). Our results show that fluorescence and UV–VisDR spectroscopy can be used to monitor the formation of metastable phases by the disaggregation of the dye S0586 in a cement paste as well as changes in ettringite formation. Addition of PCE slowed down the disaggregation of the dye as reflected by the corresponding changes of the dyes absorption and fluorescence. This prolonged induction period is a well-known side effect of PCEs and agrees with previous reported calorimetric studies and the Inhibition of gypsum dissolution observed by in-situ XRD. This demonstrates that fluorescence and UV–VisDR spectroscopy together with a suitable optical probe can provide deeper insights into the influence of PCE on C3A-gypsum hydration which could be e.g., utilized as screening method for comparing the influences
of different types of PCEs.
Ordered mesoporous silica materials such as COK-12, analogous to the well-known SBA-15, are characterized by high surface areas and unique features such as defined pore sizes in the meso-size range and high pore ordering.
The aim of this work was to prove the washing step and choice of calcination and aging temperature during the COK-12 synthesis as effective tools in tailoring, markedly improving the specific surface area, pore size, and pore volume. By controlling the aging temperature, the pore size was linearly adjusted between 5.7 and 8.1 nm, while preserving the hexagonal ordering of the pores. The synthesized COK-12 powders possess pore volumes and specific surface areas up to 1.23 cm3 g−1 and 860m2 g−1, respectively, which is markedly higher than what has previously been reported about COK-12. The presented results and the environmentally friendly character of the synthesis will make COK-12 more interesting for future adaption to the industrial processes, for example in catalysis, adsorption, or drug delivery.
Tricalcium aluminate (C3A) is found with less than 10% wt. of the total composition; however, during hydration, C3A plays an important role in the early hydration of cement in the presence of gypsum as a set retarder.
The aim of this investigation is to assess the suitability of optical spectroscopy and a dye-based optical probe to monitor early hydration of C3A in the presence of gypsum and hemihydrate. Optical evaluation was performed using steady-state fluorescence and diffuses reflectance spectroscopy (UV-VisDR). Phase characterization during hydration was done with in-situ X-ray diffraction. UV-VisDR with a cyanine dye probe was used to monitor the formation of metastable phases and was employed together with fluorescence spectroscopy, to follow the Aggregation and disaggregation of the dye during hydration. In conclusion, for the first time, a cyanine dye was identified as a feasible and stable probe to monitor C3A hydration changes in the presence of calcium sulfate.