Vorwort der Herausgeber

Ohne Zusammenfassung     

Untersuchungen des Zeitstandverhaltens von Schweißverbindungen der Werkstoffe X 20 CrMoV 12 1 und GS-17 CrMoV 5 11

Untersucht wird das Zeitstandverhalten gleichartiger Schweißverbindungen des Werkstoffs X 20 CrMoV 12 1 sowie ungleichartiger Verbindungen zwischen diesem und dem Werkstoff GS-17 CrMoV 5 11. Bei quer entnommenen Kleinproben zeigt sich ein Abfall der Zeitstandfestigkeit gegenüber dem Grundwerkstoff. Große Querproben aus einer ungleichartigen Verbindung weisen eine höhere Zeitstandfestigkeit auf als entsprechende Kleinproben. Zur Klärung der in den Schweißverbindungen auftretenden Spannungs- und Dehnungsumlagerungen wurden inelastische Finite-Elemente-(FE-)Berechnungen durchgeführt. Dabei wurde das Zeitdehnverhalten von Grundwerkstoffen, Schweißgut und thermisch simulierten Gefügen der Wärmeeinflußzone berücksichtigt. Die Anwendung spannungsbezogener Kriterien zur Bestimmung der Anrißdauer der Proben auf die FE-Ergebnisse läßt eine Voraussage des Versagensorts sowie eine sichere Abschätzung der Versagenszeit zu.     

Vapour pressures and saturated-liquid volumes for heavy fossil fuel fractions from a perturbed hard-chain equation of state

A semitheoretical equation of state has been used to correlate residual thermodynamic properties of heavy hydrocarbons. The correlation requires three characteristic molecular parameters obtained from liquid density and vapour pressure data. These parameters are presented for 61 hydrocarbons with molecular weights up to 560 and are correlated with molecular weight and structural features. The correlation is extended to narrow-boiling fractions. Molecular parameters for such fractions are obtained from experimental characterization data (molecular weight, aromaticity, naphthenicity and number of methyl groups per molecule). Calculated vapour pressures and liquid densities are in reasonable agreement with new experimental results obtained from Belridge crude oil.     

Model-based control of cathode pressure and oxygen excess ratio of a PEM fuel cell system

For PEM fuel cells supplied with air, pressure and flow control is a key requirement for an efficient and dynamic operation because fuel cells are in risk of starvation when the partial pressure of oxygen at the cathode falls below a critical level. To avoid oxygen starvation and, at the same time, to allow for a dynamic operation of the fuel cell system, both excess ratio of oxygen and cathode pressure need to be adjusted rapidly.     

Computation of plate columns for NOx absorption by a new stage-to-stage method

A new stage-to-stage method has been developed for the calculation of NX_x absorption columns. Each stage of the absorption column is simulated as a combination of a bubble column reactor (absorption) and an adiabatic plug for reactor (oxidation). The bubble column reactor is modelled as two single stirred tank reactors, one as a gas-phase and one as a liquid-phase reactor, both coupled by mass and heat transfer. In this hydrodynamic model, a dynamic approach is adopted, in which the gas-phase transport of N₂O₄ is the limiting step for the absorption. A gas-phasepseudo-enhancement for factor for N₂O₄ is therefore introduced. The balance equations for a single phase of the bubble column are solved with a Newton-Raphson algorithm. The entire column calculation is divided into a gas and a liquid side. On both sides, the stage-to-stage method is applied in such way that the overall calculation is performed as a loop process. The direction of the loop calculation follows that of the flow: gas-side upwards and liquid-side downwards.     

Interfacial chemistry of cobalt(II) during sol–gel synthesis of cobalt-containing mesoporous materials

Co-MCM-41 and Co-MCM-48 with cobalt amounts from about 3 wt.% to 9 wt.% have been synthesized under various conditions, and the samples were characterized by XRF, XRD and N₂-sorption. EXAFS least-squares curve fitting detected only oxygen and silicon backscattering shells, which verified the incorporation of cobalt into the silica framework both for as-synthesized and calcined samples. XANES profiles showed that the oxidation state of cobalt in the samples is unaltered during synthesis. It has been shown that the cobalt is precipitated as cobalt hydroxide during synthesis, and this hydroxide is in equilibrium with aqueous cobalt ions in the synthesis gel. The precipitated cobalt hydroxide precursors are incorporated into the mesoporous silica framework, while the aqueous cobalt ions remain dissolved in the aqueous phase. The cobalt amount in the final samples is therefore pH dependent. This equilibrium is also important in the formation of the mesoporous structure. Addition of increasing amounts of cobalt salt to a MCM-48 synthesis gel causes a change in the mesoporous structure from cubic Ia3d to hexagonal, which is suggested to be a consequence of the charge density matching process. The increased amounts of the divalent cobalt(II) ions in the gel screen the negatively charged silica precursors, which decreases the total surface charge density of the silica, and thus causes the surfactants to self-assemble into the hexagonal structure.