The present disclosure is directed to triblock copolymer based anion exchange membranes (AEMs) and methods for making same. The membranes are useful as separators in electrochemical devices, such as fuel cells, electrolyzers, water desalination systems, and redox flow batteries.

The present disclosure is directed to triblock copolymer based anion exchange membranes (AEMs) and methods for making same. The membranes are useful as separators in electrochemical devices, such as fuel cells, electrolyzers, water desalination systems, and redox flow batteries.

A separator plate is produced by hot compacting a pliable and malleable material made from a blend of powder containing at least 70% carbon powder, 10-20% of poly-phenylene sulfide, PPS, and 0.005-10% PolyTetraFluoroEthylene, PTFE. Advantageously, the powder is suspended in water without using isopropanol. A method of producing a separator plate is also disclosed.

A separator plate is produced by hot compacting a pliable and malleable material made from a blend of powder containing at least 70% carbon powder, 10-20% of poly-phenylene sulfide, PPS, and 0.005-10% PolyTetraFluoroEthylene, PTFE. Advantageously, the powder is suspended in water without using isopropanol. A method of producing a separator plate is also disclosed.

Disclosed is a manufacture method including providing a separator plate including a distribution face configured to channel a fluid along a face of a membrane/electrode assembly applied against the separator plate, and applying a sealing film to the distribution face of the separator plate to seal between the separator plate and the membrane/electrode assembly and/or a further separator sandwiching the membrane/electrode assembly with the separator the sealing film being adhesive on a first face facing the separator plate to adhere thereto and non-adhesive on a second face opposite the separator plate.

A production method for a fuel cell separator comprises the steps of providing a powder blend of at least 70% carbon powder, 0.5-5% PTFE, PolyTetraFluoroEthylene, and 0-20% thermoplastic polymer different from PTFE. The powder is sedimented as slurry in a suspension, excess liquid removed from the slurry, and the remaining slurry press-moulded into a shape of a separator plate, for example for use in a fuel cell stack.

A production method for a fuel cell separator comprises the steps of providing a powder blend of at least 70% carbon powder, 0.5-5% PTFE, PolyTetraFluoroEthylene, and 0-20% thermoplastic polymer different from PTFE. The powder is sedimented as slurry in a suspension, excess liquid removed from the slurry, and the remaining slurry press-moulded into a shape of a separator plate, for example for use in a fuel cell stack.

The present invention relates to a bipolar plate for a low-temperature fuel cell, in particular for a polymer electrolyte fuel cell, including a metal substrate with a coating on a surface of the substrate, the coating including an organic polymer and an electroconductive filler. The organic polymer is formed by chemical reaction of at least two components, including a bi- or polyfunctional isocyanate compound as the first component and one or more compounds having at least two free hydroxy or amino groups, as the second component.

The present invention relates to a bipolar plate for a low-temperature fuel cell, in particular for a polymer electrolyte fuel cell, including a metal substrate with a coating on a surface of the substrate, the coating including an organic polymer and an electroconductive filler. The organic polymer is formed by chemical reaction of at least two components, including a bi- or polyfunctional isocyanate compound as the first component and one or more compounds having at least two free hydroxy or amino groups, as the second component.

A fuel cell system includes a first fluid flow plate including a first plurality of first channels for flow of an oxidant or a fuel. The plurality of first channel has first channel cross-sectional flow areas. A second fluid flow plate includes a second plurality of second channels for flow of an oxidant or a fuel. The plurality of second channels has second channel cross-sectional flow areas. A membrane electrode assembly is located between the first plate and the second plate. The first flow plate includes a passage for a flow of a fluid entirely on a seam side of the first flow plate as the first plurality of first channels. The passage has a cross-sectional area for flow of the fluid smaller than the first channel cross-sectional flow area.