A bipolar plate for a proton exchange membrane fuel cell includes a laminate of carbon fiber reinforced plastic (CFRP) with a first outer ply. The CFRP includes a resin and carbon fibers. The first outer ply is arranged at a first lateral surface of the laminate, wherein the laminate includes a first plurality of carbon nanotubes (CNTs). The first outer ply includes a first groove, wherein the first groove is configured to define a first gas diffusion channel. At least some of the first plurality of CNTs extend through the first outer ply in a direction transversely to the first lateral surface of the laminate.

A fuel cell stack is provided that includes a top end plate, a bottom end plate, a plurality of fuel cells provided between the top end plate and the bottom end plate, at least one bipolar plate, a plurality of hollow fasteners, and a plurality of sleeves. Each of the at least one bipolar plate is formed between two of the plurality of fuel cells. The plurality of hollow fasteners and the plurality of sleeves extend through holes in each of the top end plate, the bottom end plate, the plurality of fuel cells and the at least one bipolar plate. Each of the plurality of sleeves surrounds one of the plurality of hollow fasteners. Each of the plurality of hollow fasteners comprises a top surface, a hole in the top surface, a side surface, and a plurality of holes formed in the side surface.

A fuel cell stack is provided that includes a top end plate, a bottom end plate, a plurality of fuel cells provided between the top end plate and the bottom end plate, at least one bipolar plate, a plurality of hollow fasteners, and a plurality of sleeves. Each of the at least one bipolar plate is formed between two of the plurality of fuel cells. The plurality of hollow fasteners and the plurality of sleeves extend through holes in each of the top end plate, the bottom end plate, the plurality of fuel cells and the at least one bipolar plate. Each of the plurality of sleeves surrounds one of the plurality of hollow fasteners. Each of the plurality of hollow fasteners comprises a top surface, a hole in the top surface, a side surface, and a plurality of holes formed in the side surface.

A fuel cell anode flow field includes at least one flow channel with a cross-sectional area that varies along at least a portion of its length. In some embodiments, the channel width decreases along at least a portion of the channel length according to a natural exponential function. This type of anode flow field can improve performance, reduce fuel consumption and/or reduce detrimental effects such as carbon corrosion and catalyst degradation, thereby improving fuel cell longevity and durability. When operating the fuel cell on either a substantially pure or a dilute fuel stream, this type of anode flow field can provide more uniform current density. These flow channels can be incorporated into reactant flow field plates, fuel cells and fuel cell stacks.

A fuel cell anode flow field includes at least one flow channel with a cross-sectional area that varies along at least a portion of its length. In some embodiments, the channel width decreases along at least a portion of the channel length according to a natural exponential function. This type of anode flow field can improve performance, reduce fuel consumption and/or reduce detrimental effects such as carbon corrosion and catalyst degradation, thereby improving fuel cell longevity and durability. When operating the fuel cell on either a substantially pure or a dilute fuel stream, this type of anode flow field can provide more uniform current density. These flow channels can be incorporated into reactant flow field plates, fuel cells and fuel cell stacks.

A Solid Oxide Cell stack has an integrated interconnect and spacer, which is formed by bending a surplus part of the plate interconnect 180° to form a spacer part on top of the interconnect and connected to the interconnect at least by the bend.

A Solid Oxide Cell stack has an integrated interconnect and spacer, which is formed by bending a surplus part of the plate interconnect 180° to form a spacer part on top of the interconnect and connected to the interconnect at least by the bend.

The invention relates to a flow element, in particular, as a component of a bipolar plate of an electrochemical device, comprising a plate-like base body that extends in two main directions of extension that are oriented at an angle in relation to one another, and has an extension in a height direction that is oriented transversely and in particular perpendicularly thereto, wherein the base body has a channel structure having a plurality of channels that are arranged laterally adjacent to one another, wherein the channels are formed by recesses in the base body and are separated from one another by raised portions, arranged between the recesses, of the base body, wherein regions having a normal level difference, defined in the height direction, as a height difference between a raised portion and an adjoining recess are provided, as well as regions having a level difference, reduced in comparison with the normal level difference, as a height difference between a raised portion and an adjoining recess, wherein, in the running direction of the channels, at least in some portions thereof, regions having a normal level difference and regions having a reduced level difference are provided repeatedly, and regions having a reduced level difference of adjacent channels are offset in relation to one another with respect to the respective running direction thereof, wherein the regions having a reduced level difference are formed on the base body by means of saddle regions, and the regions having a normal level difference are formed by means of valley regions arranged therebetween, and wherein a valley region of an adjacent channel is in each case located opposite the saddle regions. In addition, the invention relates to a use, a bipolar plate, and a method for producing a flow element.

The invention relates to a flow element, in particular, as a component of a bipolar plate of an electrochemical device, comprising a plate-like base body that extends in two main directions of extension that are oriented at an angle in relation to one another, and has an extension in a height direction that is oriented transversely and in particular perpendicularly thereto, wherein the base body has a channel structure having a plurality of channels that are arranged laterally adjacent to one another, wherein the channels are formed by recesses in the base body and are separated from one another by raised portions, arranged between the recesses, of the base body, wherein regions having a normal level difference, defined in the height direction, as a height difference between a raised portion and an adjoining recess are provided, as well as regions having a level difference, reduced in comparison with the normal level difference, as a height difference between a raised portion and an adjoining recess, wherein, in the running direction of the channels, at least in some portions thereof, regions having a normal level difference and regions having a reduced level difference are provided repeatedly, and regions having a reduced level difference of adjacent channels are offset in relation to one another with respect to the respective running direction thereof, wherein the regions having a reduced level difference are formed on the base body by means of saddle regions, and the regions having a normal level difference are formed by means of valley regions arranged therebetween, and wherein a valley region of an adjacent channel is in each case located opposite the saddle regions. In addition, the invention relates to a use, a bipolar plate, and a method for producing a flow element.

A fuel cell anode flow field includes at least one flow channel with a cross-sectional area that varies along at least a portion of its length. In some embodiments, the channel width decreases along at least a portion of the channel length according to a natural exponential function. This type of anode flow field can improve performance, reduce fuel consumption and/or reduce detrimental effects such as carbon corrosion and catalyst degradation, thereby improving fuel cell longevity and durability. When operating the fuel cell on either a substantially pure or a dilute fuel stream, this type of anode flow field can provide more uniform current density. These flow channels can be incorporated into reactant flow field plates, fuel cells and fuel cell stacks.