Abstract: An electrolysis system for electrochemically breaking down water to form hydrogen and oxygen, having at least one electrolyser for electrochemically breaking down water to form hydrogen and oxygen. The electrolysis system also has a housing device for receiving the electrolyser, wherein the electrolyser is at least partially arranged in the housing device and the housing device is sealed relative to a first fluid surrounding the housing device. In the electrolyser, water is broken down to form hydrogen and oxygen. The hydrogen and the oxygen are directed out of the housing device.

Abstract: An energy management system includes a control unit and an electrolysis system having an alkaline electrolysis unit and a PEM electrolysis unit. The control unit controls the electrolysis units independently of one another in such a way that a performance adjustment of an overall performance of the electrolysis system is particularly dynamic.

Abstract: A hydrogen filling station system generates hydrogen on demand. The hydrogen filling station system includes a PEM electrolyzer for generating hydrogen, a compression device for compressing the hydrogen, and a filling system for filling a vehicle with the compressed hydrogen. The required space for the hydrogen filling station system is reduced and operational safety is increased in that the PEM electrolyzer is directly connected to the compression device and the compression device is directly connected to the filling system, without temporary storage respectively. That is, there is no requirement to intermediately store the compressed hydrogen.

Abstract: Energy storage modules generally include a housing with component parts arranged therein. The component parts are in this case either capacitors, for example double-layer capacitors and/or electrolyte capacitors. According to the invention, a filler is provided in the housing and binds electrolyte liquid occurring in the even of damage or else electrolyte gases. Beds of material with a large specific surface area, such as zeolites or else active carbons, are suitable as fillers. The surfaces are also possibly catalytically coated.

Abstract: The electrolysis occurs as a high-pressure electrolyzer, oxygen being produced on one side and hydrogen on the other side, with corresponding pressure. The gases may optionally be stored without additional compression. The PEM fuel cell process is used in reverse for the process. It is advantageous that excess energy may be used by wind power plants. In the associated device, a high-pressure electrolyzer (1) is present which is operated using environmentally friendly air power. Due to the improved operating point of the high-pressure electrolyzer, improved economy results for the generation process compared to the prior art, in particular for hydrogen as an energy storage.

Abstract: In a method for treating sludge (1), at least two electrodes (2) are provided for generating an electric field. Water present in the biosludge is electrolyzed and OH° radicals (OH°) are generated at least in part.

Abstract: A device (100) for breaking down pollutants in a liquid (F) by oxidative OH radicals has an arrangement of positively and negatively charged electrodes (104a . . . 104n, 105a . . . 105n), wherein at least one of the positively or negatively charged electrodes (104a . . . 104n, 105a . . . 105n) is surrounded by a separator (107) at least in the contact zone between the liquid (F) and the electrode (104a . . . 104n, 105a . . . 105n).

Abstract: A method for producing a hydrophobic coating for condensers to obtain a dropwise condensation, a hydrophobic coating for condensers, a hydrophobically-coated condenser, and a coating agent are provided. A coating agent is applied to a condenser. The coating agent includes a liquid solvent and a coating material. The coating material may be applied by a wet-chemical method.

Abstract: A gas diffusion electrode for a PEM fuel cell includes a metallic catalyst, and an electrocatalyst layer having a polymer A for hydrophobicizing the electrocatalyst layer and a uniform thickness of between 3 to 40 ?m, especially 25 ?m. The polymer A content is less than 10% by weight based on the metallic catalyst content. Methods of producing and of hydrophobicizing the electrode include screen printing a paste onto a carrier and removing the screen-printing medium by heating. The paste includes at least one metallic catalyst with a content of polymer A up to at most 10% by weight, and a screen-printing medium. The electrocatalyst layer of the electrode has a significantly lower content of the catalyst inhibitor TEFLON® because it is not added only to the screen-printing paste but is subsequently applied, with the same surface-specific effect, by dipping the finished electrocatalyst layer in a solution containing TEFLON®.

Abstract: Energy storage modules generally include a housing with component parts arranged therein. The component parts are in this case either capacitors, for example double-layer capacitors and/or electrolyte capacitors. According to the invention, a filler is provided in the housing and binds electrolyte liquid occurring in the even of damage or else electrolyte gases. Beds of material with a large specific surface area, such as zeolites or else active carbons, are suitable as fillers. The surfaces are also possibly catalytically coated.

Abstract: A gas diffusion electrode for a PEM fuel cell includes a metallic catalyst, and an electrocatalyst layer having a polymer A for hydrophobicizing the electrocatalyst layer and a uniform thickness of between 3 to 40 ?m, especially 25 ?m. The polymer A content is less than 10% by weight based on the metallic catalyst content. Methods of producing and of hydrophobicizing the electrode include screen printing a paste onto a carrier and removing the screen-printing medium by heating. The paste includes at least one metallic catalyst with a content of polymer A up to at most 10% by weight, and a screen-printing medium. The electrocatalyst layer of the electrode has a significantly lower content of the catalyst inhibitor TEFLON® because it is not added only to the screen-printing paste but is subsequently applied, with the same surface-specific effect, by dipping the finished electrocatalyst layer in a solution containing TEFLON®.

Abstract: A method and a fuel cell are described in which it is possible to combine the advantages of a precious-metal coating, which, for example, reduces the contact resistance between a pole plate and current collector of a fuel cell, with low production costs. This becomes possible since it has been established that a sufficient and sometimes even improved reduction in the contact resistance of a component to a contact element is achieved even with a minimal precious-metal coating that is not continuous.

Abstract: A screen-printing paste as a starting material for fabricating a gas diffusion electrode through screen-printing includes at least one polymer, at least one metallic catalyst, and a high-boiling solvent. The polymer is a binder including poly(butyl acrylate)-polymethacrylate copolymer, a poly(vinyl alcohol), and a poly(ethylene oxide). The polymer can be two polymers, a first being used for hydrophobicization and present in an amount of between 0 to 10% by weight based on a content of the metallic-catalyst, and a second being a binder. A screen-printing method of fabricating the electrode for a fuel cell includes forming a screen-printing layer having a thickness between 3 and 40 &mgr;m by applying the screen-printing paste to a base. The solvent and the polymer serve as a screen-printing medium. The screen-printing layer is baked to allow only residues of the solvent and the polymer to remain, which do not interfere with using the electrode in a fuel cell.

Abstract: Discharging the reaction water from the novel PEM fuel cells does not require humidification of the reaction gases or an increase in the gas pressure. This is attained in that a hydrophobic layer on the cathode side is used which has a smaller pore size than the layer on the anode side. The reaction water is removed via the anode during the operation of the fuel cell.

Abstract: Cold starting includes the steps of directly converting process gas into thermal energy by a catalytic reaction, and utilizing the thermal energy to heat up the fuel cell stack, wherein the process of heating up the fuel cell stack is carried out separately from the operation of the fuel cell facility. Heating elements form separate components in the fuel cell stack, the element being mounted in a predetermined order in the fuel cell stack.

Abstract: A fuel cell stack includes at least two stacked fuel cell units which are held together by a material which has sealing and fixing properties. A method for assembling a fuel cell stack is also provided.

Abstract: The invention relates to a DMFC in which an evaporation apparatus is connected before the cell. The fuel, which is predominantly a methanol/water mixture with a possible admixture of inert gas, is variable in its composition, whereby the respective methanol/water and, if warranted, inert gas mixture, can be adjusted in load-dependent fashion. Moreover, the invention relates to a method for operating a DMFC apparatus in which the fuel is present in the anode chamber in gaseous form.

Abstract: A membrane electrode assembly for a fuel cell, in particular a PEM fuel cell, has an asymmetric distribution of the expensive precious metal on the membrane. The asymmetric distribution is realized in accordance with the requirements of the particular region. In the production, the electrodes are coated with membrane first of all, rather than the other way round.

Abstract: A fuel cell installation and a method for operating a fuel cell installation with a dynamic power control are provided. The dynamic power control is achieved by additionally connecting at least one subsystem which is kept ready for operation, a starter system and/or a low-voltage unit for nighttime operation and/or an on-board power supply.

Abstract: A method and a fuel cell are described in which it is possible to combine the advantages of a precious-metal coating, which, for example, reduces the contact resistance between a pole plate and current collector of a fuel cell, with low production costs. This becomes possible since it has been established that a sufficient and sometimes even improved reduction in the contact resistance of a component to a contact element is achieved even with a minimal precious-metal coating that is not continuous.