Abstract: A separator plate for an electrochemical system is described. The separator plate may be used with a bipolar plate and for an electrochemical system comprising a plurality of bipolar plates. The separator plate may have a flow field and guiding structures for guiding a medium through the flow field. The guiding structures of the flow field have a mean height h1 determined perpendicularly to the planar surface plane of the plate. The separator plate may also have a contiguous, lowered transition region where medium flowing from a channel into the flow field, or from the flow field into the channel, flows through the transition region, wherein the transition region has a maximum height hmax determined perpendicularly to the planar surface plane of the plate, where applies: hmax?0.95·h1.

Abstract: Electrochemical systems having a first separator plate, a second separator plate, and a membrane electrode unit (MEA) arranged between the separator plates. The MEA has a membrane in order to form an electrochemical cell and an edge portion connected to the membrane and comprising a film material for positioning and/or fastening the membrane between the separator plates. The edge portion has at least one elevation and/or depression for stiffening the edge portion at least in regions.

Abstract: An integrated gas management device (GMD) for a fuel cell has a gas-to-gas humidifier for transferring water from a second gas to a first gas; and a heat exchanger attached to a first end of the humidifier core for cooling the first gas. The GMD may optionally have a thermal isolation plate between the heat exchanger and the first end of the humidifier core. The GMD further has a bypass line to allow the first gas to bypass the humidifier. The first gas may be cathode charge air and the second gas may be cathode exhaust.

Abstract: A separator plate for an electrochemical system is described. The separator plate may have a first individual plate and a second individual plate which is connected to the first individual plate. The first individual plate may have two first channels for leading media, the first channels running next to one another, being shaped in the first individual plate and being separated from one another at least in sections by a web which is formed between the first channels. The second individual plate may have a second channel which is for leading media and is shaped in the second individual plate. The web which is formed between the first channels and the second channel which is shaped in the second individual plate are designed and arranged in a manner such that a projection of the second channel onto the first individual plate perpendicularly to the planar surface plane of the first individual plate crosses the web along a crossing region of the web.

Abstract: A separator plate for an electrochemical system is described. The separator plate may be used with a bipolar plate and for an electrochemical system comprising a plurality of bipolar plates. The separator plate may have a flow field and guiding structures for guiding a medium through the flow field. The guiding structures of the flow field have a mean height h1 determined perpendicularly to the planar surface plane of the plate. The separator plate may also have a contiguous, lowered transition region where medium flowing from a channel into the flow field, or from the flow field into the channel, flows through the transition region, wherein the transition region has a maximum height hmax determined perpendicularly to the planar surface plane of the plate, where applies: hmax?0.95·h1.

Abstract: An electrochemical system has at least one endplate, a terminal bipolar plate as well as a sealing device arranged between the endplate and the terminal bipolar plate. The materials of the terminal bipolar plate and the endplate have different coefficients of thermal expansion and with the sealing device being designed in such a way that during temperature changes, the sealing function is also given by a sliding of the endplate and/or the terminal bipolar plate along the sealing device.

Abstract: An electrochemical system is described having an end plate, a stack cover plate adjacent to the end plate and at least one metallic electrical conductor. The stack cover plate has an electrically conductive contacting plate adjacent to the end plate and an electrically conductive separator plate half facing away from the end plate. The contacting plate and the separator plate half are connected to each other electrically and media-tight. The metallic electrical conductor extends to an outside of the electrochemical system. The metallic electrical conductor and the contacting plate are in one piece or the metallic electrical conductor contacts the contacting plate directly. The contacting plate and the separator plate half are bonded to each other.

Abstract: The application relates to a water transfer compound, preferably for use for the humidification of process gases for fuel cells, comprising:—a water-permeable and essentially gas-impermeable water transfer layer as well as—at least one thermoplastic protection layer which is water- and gas-permeable at least in sections, where—the water transfer layer and the thermoplastic protection layer overlap each other at least in sections and comprise a first and a second overlapping area, where—the water transfer layer in the first overlapping area is accessible for humid gases through the thermoplastic protection layer and the water transfer compound is thermocompressed in the second overlapping area so that the water transfer layer in the second overlapping area is not accessible for humid gases through the compressed thermoplastic protection layer.

Abstract: A separator plate for an electrochemical system is described. The separator plate may have a first individual plate and a second individual plate which is connected to the first individual plate. The first individual plate may have two first channels for leading media, the first channels running next to one another, being shaped in the first individual plate and being separated from one another at least in sections by a web which is formed between the first channels. The second individual plate may have a second channel which is for leading media and is shaped in the second individual plate. The web which is formed between the first channels and the second channel which is shaped in the second individual plate are designed and arranged in a manner such that a projection of the second channel onto the first individual plate perpendicularly to the planar surface plane of the first individual plate crosses the web along a crossing region of the web.

Abstract: An integrated gas management device (GMD) for a fuel cell has a gas-to-gas humidifier for transferring water from a second gas to a first gas; and a heat exchanger attached to a first end of the humidifier core for cooling the first gas. The GMD may optionally have a thermal isolation plate between the heat exchanger and the first end of the humidifier core. The GMD further has a bypass line to allow the first gas to bypass the humidifier. The first gas may be cathode charge air and the second gas may be cathode exhaust.

Abstract: An integrated gas management device (GMD) for a fuel cell comprises a gas-to-gas humidifier for transferring water from a second gas to a first gas; a heat exchanger attached to a first end of the humidifier core for cooling the first gas; and/or a water separator attached to a second end of the humidifier core for removing liquid water from the second gas. The GMD may optionally comprise a thermal isolation plate between the heat exchanger and the first end of the humidifier core. The GMD further comprises a bypass line to allow the first gas to bypass the humidifier. The first gas may comprise cathode charge air and the second gas may comprise cathode exhaust.

Abstract: An electrochemical system has at least one endplate, a terminal bipolar plate as well as a sealing device arranged between the endplate and the terminal bipolar plate. The materials of the terminal bipolar plate and the endplate have different coefficients of thermal expansion and with the sealing device being designed in such a way that during temperature changes, the sealing function is also given by a sliding of the endplate and/or the terminal bipolar plate along the sealing device.

Abstract: An electrochemical system is described having an end plate, a stack cover plate adjacent to the end plate and at least one metallic electrical conductor. The stack cover plate has an electrically conductive contacting plate adjacent to the end plate and an electrically conductive separator plate half facing away from the end plate. The contacting plate and the separator plate half are connected to each other electrically and media-tight. The metallic electrical conductor extends to an outside of the electrochemical system. The metallic electrical conductor and the contacting plate are in one piece or the metallic electrical conductor contacts the contacting plate directly. The contacting plate and the separator plate half are bonded to each other.

Abstract: The application relates to a water transfer compound, preferably for use for the humidification of process gases for fuel cells, comprising:—a water-permeable and essentially gas-impermeable water transfer layer as well as—at least one thermoplastic protection layer which is water- and gas-permeable at least in sections, where—the water transfer layer and the thermoplastic protection layer overlap each other at least in sections and comprise a first and a second overlapping area, where—the water transfer layer in the first overlapping area is accessible for humid gases through the thermoplastic protection layer and the water transfer compound is thermocompressed in the second overlapping area so that the water transfer layer in the second overlapping area is not accessible for humid gases through the compressed thermoplastic protection layer.

Abstract: The application relates to a water transfer compound, preferably for use for the humidification of process gases for fuel cells, comprising: —a water-permeable and essentially gas-impermeable water transfer layer as well as—at least one thermoplastic protection layer which is water- and gas-permeable at least in sections, where—the water transfer layer and the thermoplastic protection layer overlap each other at least in sections and comprise a first and a second overlapping area, where—the water transfer layer in the first overlapping area is accessible for humid gases through the thermoplastic protection layer and the water transfer compound is thermocompressed in the second overlapping area so that the water transfer layer in the second overlapping area is not accessible for humid gases through the compressed thermoplastic protection layer.

Abstract: An electrochemical system has two separator plates as well as a membrane-electrode assembly arranged at least in regions between the separator plates. The separator plates and the membrane-electrode assembly each have at least two passage openings for a flush arrangement of the separator plates and the membrane-electrode assembly at positioning devices during the assembly of the electrochemical system. At least one resilient bridge is arranged at the periphery of at least one passage opening for a mechanical butting to the at least one positioning device in such a manner that during the stacking of the separator plates and the membrane-electrode assemblies, the membrane-electrode assemblies center themselves in a direction orthogonal to the stack direction between the separator plates.

Abstract: An integrated gas management device (GMD) for a fuel cell comprises a gas-to-gas humidifier for transferring water from a second gas to a first gas; a heat exchanger attached to a first end of the humidifier core for cooling the first gas; and/or a water separator attached to a second end of the humidifier core for removing liquid water from the second gas. The GMD may optionally comprise a thermal isolation plate between the heat exchanger and the first end of the humidifier core. The GMD further comprises a bypass line to allow the first gas to bypass the humidifier. The first gas may comprise cathode charge air and the second gas may comprise cathode exhaust.

Abstract: The present invention relates to a bipolar plate (1) for electrochemical systems which contains a first plate (2) with a first flowfield (2a) for media distribution as well as a second plate (3) with a second flowfield (3a) for media distribution. This first plate in the region of the first flow field at least in regions comprises a plane surface section (4) from which discrete projections (5) distanced to one another project arranged in a distributed manner. Furthermore a method for manufacturing this bipolar plate is suggested as well as an electrochemical system which contains this bipolar plate. According to the invention it is possible in an inexpensive manner to manufacture a bipolar plate which permits the construction of fuel cells functioning with a low peripheral consumption (pumps, compressors) and which are safer with regard to their operation.

Abstract: The present invention relates to a contact plate for fuel cells with a coherent active area (11) on at least one side of the contact plate, wherein the active area (11) consists of a contact surface (2) which over the whole surface comprises a coating (4) of an electrically conductive, corrosion-resistant material, and of recesses (3) so that the recesses (3) form a channel structure, wherein the coating (4) furthermore at least in the bottom regions (5) of the recesses (3) is omitted. The invention further relates to a corresponding fuel cell or to a fuel cell stack with at least one such contact plate as well as to various methods for manufacturing such contact plates which may serve as bipolar plates as well as monopolar plates or end plates. With the contact plate according to the invention, one achieves an optimally reduced contact resistance with a minimal material expense for the coating (4).

Abstract: The present invention relates to a new method for the production of electrochemical cells, in particular individual cells for fuel cells and stacks as well as components and semi-finished parts required for this purpose. The gas diffusion layer is fixed on the bipolar plate by constructional measures and thus an improved positioning of the individual components of an electrochemical cell, in particular an individual cell for fuel cells is achieved. The method according to the invention allows for a flexible production. The semi-finished parts according to the invention are valuable, storable intermediate products which substantially reduce the lead times in the production of electrochemical cells, in particular individual cells for fuel cells.