Refine
Year of publication
- 2012 (50) (remove)
Document Type
- Conference Proceeding (11)
- Other (11)
- Article (reviewed) (9)
- Article (unreviewed) (9)
- Contribution to a Periodical (6)
- Part of a Book (3)
- Report (1)
Conference Type
- Konferenzartikel (10)
- Konferenz-Poster (1)
Is part of the Bibliography
- yes (50) (remove)
Keywords
- Adsorption (3)
- Dünnschichtchromatographie (2)
- Metallorganisches Netzwerk (2)
- Abweichungen IFRS zu HGB (1)
- Ammoniumverbindungen (1)
- Batterie (1)
- Bauteil (1)
- Belastung (1)
- Beschränkung (1)
- Biene (1)
Institute
Open Access
- Closed Access (50) (remove)
Multi-phase management is crucial for performance and durability of electrochemical cells such as batteries and fuel cells. In this paper we present a generic framework for describing the two-dimensional spatiotemporal evolution of gaseous, liquid and solid phases, as well as their interdependence with interfacial (electro-)chemistry and microstructure in a continuum description. The modeling domain consists of up to seven layers (current collectors, channels, electrodes, separator/membrane), each of which can consist of an arbitrary number of bulk phases (gas, liquid, solid) and connecting interfaces (two-phase or multi-phase boundaries). Bulk and interfacial chemistry is described using global or elementary kinetic reactions. Multi-phase management is coupled to chemistry and to mass and charge transport within bulk phases. The functionality and flexibility of this framework is demonstrated using four application areas in the context of post-lithium-ion batteries and fuel cells, that is, lithium-sulfur (Li-S) cells, lithium-oxygen (Li-O) cells, solid oxide fuel cells (SOFC) and polymer electrolyte membrane fuel cells (PEFC). The results are compared to models available in literature and properties of the generic framework are discussed.
An isomorphous series of 10 microporous copper-based metal–organic frameworks (MOFs) with the general formulas ∞3[{Cu3(μ3-OH)(X)}4{Cu2(H2O)2}3(H-R-trz-ia)12] (R = H, CH3, Ph; X2– = SO42–, SeO42–, 2 NO32– (1–8)) and ∞3[{Cu3(μ3-OH)(X)}8{Cu2(H2O)2}6(H-3py-trz-ia)24Cu6]X3 (R = 3py; X2– = SO42–, SeO42– (9, 10)) is presented together with the closely related compounds ∞3[Cu6(μ4-O)(μ3-OH)2(H-Metrz-ia)4][Cu(H2O)6](NO3)2·10H2O (11) and ∞3[Cu2(H-3py-trz-ia)2(H2O)3] (12Cu), which are obtained under similar reaction conditions. The porosity of the series of cubic MOFs with twf-d topology reaches up to 66%. While the diameters of the spherical pores remain unaffected, adsorption measurements show that the pore volume can be fine-tuned by the substituents of the triazolyl isophthalate ligand and choice of the respective copper salt, that is, copper sulfate, selenate, or nitrate.
The applicability of finite elements for molecular dynamic simulations depends on both the structure’s dimensions and the underlying force field type. Shell and continuum elements describe molecular structures only in an average sense, which is why they are not subject of this paper. In contrast, truss and beam elements are potentially attractive candidates when it comes to accurately reproducing the atomic interactions. However, special considerations are required for force fields that use not only two-body, but also multi-body potentials. For the example of bending and torsion energies it is shown how standard beam element models have to be extended to be equivalent to classical molecular dynamic simulations.
As a basis for the evaluation of hydrogen storage by physisorption, adsorption isotherms of H2 were experimentally determined for several porous materials at 77 K and 298 K at pressures up to 15 MPa. Activated carbons and MOFs were studied as the most promising materials for this purpose. A noble focus was given on how to determine whether a material is feasible for hydrogen storage or not, dealing with an assessment method and the pitfalls and problems of determining the viability. For a quantitative evaluation of the feasibility of sorptive hydrogen storage in a general analysis, it is suggested to compare the stored amount in a theoretical tank filled with adsorbents to the amount of hydrogen stored in the same tank without adsorbents. According to our results, an “ideal” sorbent for hydrogen storage at 77 K is calculated to exhibit a specific surface area of >2580 m2 g−1 and a micropore volume of >1.58 cm3 g−1.
Buildings that are cooled and, if applicable, heated by thermo-active building systems (TABS) in combination with environmental energy have been established in the market during the last years. Many successful and efficient examples prove, that these systems can achieve a good thermal room comfort with a high energy efficiency of the plant system using environmental energy (mainly surface-near geothermal energy). However, operating experience and a systematic evaluation of several building projects demonstrate that there is potential improvement in the design, implementation, and operation of TABS systems. The article presents operating experience and a detailed evaluation of the operation performance of several non-residential buildings with thermo-active building systems with respect to thermal comfort and energy efficiency.
BFH "Umsatzsteuer bei ebay"
(2012)
BGH "Computer-Bild"
(2012)
BGH "Postfachanschrift"
(2012)