Abstract: A method produces an endless belt having a belt body, which includes a first main surface and a second main surface, wherein the first main surface and the second main surface of the belt body are connected to one another via lateral edges, wherein a coating is applied to the first main surface of the belt body being opposite to an inner side of the endless belt in a finished state of the endless belt, wherein the coating forms an outer side of the endless belt in a finished state, wherein at least one base material, into which reinforcing elements are inserted, is applied to the first main surface of the belt body as the coating.

Abstract: A method processes a belt with a belt body that has a first surface and a second surface connected to each other by side surfaces. Each side surface is smaller than each surface. At least one of the surfaces of the belt is coated with a coating having at least one layer. In a step i) the coating is interrupted or left out in a region of the belt to be processed, and a recess, in particular a gap-shaped or hole-shaped recess, interrupting the coating is produced in the region to be processed, which recess is at least partially delimited by opposite sections of the at least one coating. In a step ii) directly thereafter or after further intermediate steps, the recess is at least partially filled up with at least one material of the same type as that of the at least one layer of the coating.

Abstract: A method for producing an endless belt, and an endless belt having a belt body with a first main surface and a second main surface connected to one another via lateral edges, wherein a coating is applied to the first main surface of the belt body being opposite to an inner side of the endless belt in a finished state of the endless belt, wherein the coating forms an outer side of the endless belt, wherein, as coating to the first main surface of the belt body, a matrix is applied which consists of at least one base material, with hard particles, in particular with a hardness measured according to Vickers of more than 500 [HV], preferably with a hardness between 1400 [HV] and 10060 [HV], being embedded into the matrix, wherein the coating is preferably applied directly to the first main surface of the belt body.

Abstract: A membrane assembly for the permeative separation of a fluid from fluid mixtures includes a porous, fluid-permeable, metallic support substrate, a membrane that is disposed on the support substrate and is selectively permeable to the fluid to be separated off, and a connecting part which is formed, at least on the surface, of a fluid-tight, metallic material. The support substrate is cohesively bonded along a peripheral section thereof to the connecting part. A ceramic, fluid-permeable, porous, first intermediate layer is disposed between the support substrate and the membrane. At least one ceramic bonding layer is disposed directly on the connecting part and the material bond and extends at least over the cohesive material bond and an adjoining section of the connecting part. The first intermediate layer ends on the bonding layer and has a greater average pore size than the bonding layer.

Abstract: A power transmission system enables the electrical contacting of a stack with a power line or with an adjacent stack. The stack is made up of a plurality of planar electrochemical modules and is closed off at each of the end faces by a stack-side power transmission plate. The power line to be contacted ends with a line-side power transmission plate. The power transmission system comprises at least one porous, metallic body which is arranged between the stack-side power transmission plate of the stack to be contacted and the line-side power transmission plate of the power line or the stack-side power transmission plate of the adjacent stack and is electrically connected to these power transmission plates. In addition, the porous, metallic body is sealed in a gastight manner by a closed circumferential seal.

Abstract: A membrane tube is provided for the permeative separation of a gas from gas mixtures. The membrane tube has at least two membrane tube sections, each with a porous, gas-permeable, metallic, tubular support substrate, and a membrane which is selectively permeable for the gas to be separated off. The tube also has, applied to the support substrate around the circumference, at least one connecting section which is gastight at least on the surface and by way of which the two adjacent membrane tube sections are joined, and at least one spacer in the region of the connecting section. The spacer projects in the radial direction to above the membrane.

Abstract: A cathode-electrolyte-anode unit for an electrochemical functional device, in particular a high-temperature fuel cell. The unit has a multi-layer solid-state electrolyte arranged between a porous anode and a porous cathode. The solid-state electrolyte is produced by a vapor deposition process and has a sandwich-type structure consisting of at least one first layer with a lower oxygen content, and at least one second layer with a higher oxygen content. The individual layers have substantially the same composition, with the exception of oxygen.

Abstract: A membrane arrangement for the permeative separation of a gas from gas mixtures has a porous, gas-permeable, metallic support substrate, a membrane formed on the support substrate and selectively permeable for the gas to be separated off. A ceramic, gas-permeable, porous, first intermediate layer is formed between the support substrate and the membrane and directly on the support substrate. A gastight, metallic coupling part is joined by a material-to-material bond to the support substrate. The support substrate and the coupling part are separated by a dividing line. The intermediate layer extends towards the coupling part over the gas-permeable surface of the porous support substrate at least to a distance of 2 mm from the dividing line and extends over the gastight surface of the coupling part by not more than 2 mm beyond the dividing line.

Abstract: A membrane assembly for the permeative separation of a fluid from fluid mixtures includes a porous, fluid-permeable, metallic support substrate, a membrane that is disposed on the support substrate and is selectively permeable to the fluid to be separated off, and a connecting part which is formed, at least on the surface, of a fluid-tight, metallic material. The support substrate is cohesively bonded along a peripheral section thereof to the connecting part. A ceramic, fluid-permeable, porous, first intermediate layer is disposed between the support substrate and the membrane. At least one ceramic bonding layer is disposed directly on the connecting part and the material bond and extends at least over the cohesive material bond and an adjoining section of the connecting part. The first intermediate layer ends on the bonding layer and has a greater average pore size than the bonding layer.

Abstract: A cathode-electrolyte-anode unit for an electrochemical functional device, in particular a high-temperature fuel cell. The unit has a multi-layer solid-state electrolyte arranged between a porous anode and a porous cathode. The solid-state electrolyte is produced by a vapor deposition process and has a sandwich-type structure consisting of at least one first layer with a lower oxygen content, and at least one second layer with a higher oxygen content. The individual layers have substantially the same composition, with the exception of oxygen.

Abstract: A plate-shaped, porous, carrier substrate produced by powder metallurgy for a metal-supported electrochemical functional device, includes a marginal region and a central region with a surface configured to receive a layer stack with electrochemically active layers on a cell-facing side of the carrier substrate. A surface section of the marginal region has a melt phase of the carrier substrate material on the cell-facing side of the carrier substrate. At least sections of a region located beneath the surface section having the melt phase have a higher porosity than the surface section disposed above them and having the melt phase.