Solid polymer electrolyte fuel cell stacks require a significant nominal compressive loading for proper operation and sealing. This loading is typically provided using relatively thick end plates and tight straps. In certain fuel cell applications, one or more solid polymer electrolyte fuel cell stacks are secured in larger enclosures (e.g. for isolation and crashworthiness in automotive applications). The enclosures however can themselves be sturdy enough to provide the necessary loading on the fuel cell stacks within. The present invention takes advantage of that to allow for use of thinner end plates and/or weaker straps which would otherwise be insufficient for use.

A battery with a corrosion-resistant ion-exchange membrane system is presented. The battery has an acidic catholyte, an anode metal that is chemically reactive towards water, and an ion-exchange membrane system. Some examples of anode metals include alkali metals, alkaline earth metals, and aluminum (Al). The ion-exchange membrane system includes a solid, cation-permeable, water-impermeable first membrane adjacent to the anode, prone to decomposition upon chemical reaction with an acid, an anion-permeable second membrane adjacent to the cathode, and a buffer compartment including a solution, interposed between the first membrane and the second membrane. In response to discharging the battery, the solution in the buffer compartment accepts cations from the anode and anions from the cathode, forming a cation-anion salt solution in the buffer compartment. The second membrane prevents the transportation of protons from the catholyte to the buffer compartment, and so prevents the corrosion of the first membrane.

A battery with a corrosion-resistant ion-exchange membrane system is presented. The battery has an acidic catholyte, an anode metal that is chemically reactive towards water, and an ion-exchange membrane system. Some examples of anode metals include alkali metals, alkaline earth metals, and aluminum (Al). The ion-exchange membrane system includes a solid, cation-permeable, water-impermeable first membrane adjacent to the anode, prone to decomposition upon chemical reaction with an acid, an anion-permeable second membrane adjacent to the cathode, and a buffer compartment including a solution, interposed between the first membrane and the second membrane. In response to discharging the battery, the solution in the buffer compartment accepts cations from the anode and anions from the cathode, forming a cation-anion salt solution in the buffer compartment. The second membrane prevents the transportation of protons from the catholyte to the buffer compartment, and so prevents the corrosion of the first membrane.

A bipolar plate for a fuel cell is provided, which includes: a metal substrate having a flow field structure; a conducting adhesion layer formed on the metal substrate and having a polymeric adhesive and a plurality of conductive particles; and a pure graphite layer formed on the conducting adhesion layer and structurally corresponding to the flow field structure of the metal substrate. The graphite layer including expanded graphite powder is adhered to the metal substrate via the conducting adhesion layer, and a portion of the expanded graphite powder is embedded into the conducting adhesion layer.

A method for manufacturing a separator of a fuel cell stack includes: forming a gasket on the separator of the fuel cell stack; masking a surface of the separator except for a region of the surface of the separator on which the gasket is formed; and inserting the partially masked separator into a chamber to cross-link the gasket.

An electrochemical device and methods of using the same. In one embodiment, the electrochemical device may be used as a fuel cell and/or as an electrolyzer and includes a membrane electrode assembly (MEA), an anodic gas diffusion medium in contact with the anode of the MEA, a cathodic gas diffusion medium in contact with the cathode, a first bipolar plate in contact with the anodic gas diffusion medium, and a second bipolar plate in contact with the cathodic gas diffusion medium. Each of the bipolar plates includes an electrically-conductive, chemically-inert, non-porous, liquid-permeable, substantially gas-impermeable membrane in contact with its respective gas diffusion medium, as well as a fluid chamber and a non-porous an electrically-conductive plate.

An electrochemical device and methods of using the same. In one embodiment, the electrochemical device may be used as a fuel cell and/or as an electrolyzer and includes a membrane electrode assembly (MEA), an anodic gas diffusion medium in contact with the anode of the MEA, a cathodic gas diffusion medium in contact with the cathode, a first bipolar plate in contact with the anodic gas diffusion medium, and a second bipolar plate in contact with the cathodic gas diffusion medium. Each of the bipolar plates includes an electrically-conductive, chemically-inert, non-porous, liquid-permeable, substantially gas-impermeable membrane in contact with its respective gas diffusion medium, as well as a fluid chamber and a non-porous an electrically-conductive plate.

An electrically conductive member includes a first portion and a second portion having a resistivity different from that of the first portion. An electrochemical cell device includes an electrically conductive member and an electrochemical cell connected to the electrically conductive member. The electrochemical cell includes a first part connected to the first portion, and a second part connected to the second portion. A temperature of the first part is higher than a temperature of the second part. A resistivity of the first portion is larger than a resistivity of the second portion.

Systems and methods for separator plates, bipolar plates, stacks of plates, and electrochemical systems, comprising at least one through-opening for the passage of a fluid and a rim that delimits the through-opening. The rim having a curved course and a rectilinear course that adjoins the curved course. A bead arrangement extends around the curved course and the rectilinear course. An edge portion spans the bead arrangement and the rim, so that the bead arrangement is situated at a distance from the rim. A cutout formed in the curved course, so that a minimum distance of the bead arrangement from the rim is smaller in the curved course than in the rectilinear course.

A bipolar plate for an electrochemical system. The bipolar plate comprising a first individual plate and a second individual plate which are joined together. Each individual plate comprising: an electrochemically active region, an outer edge, and a perimeter sealing element. The outer edge region spans between the edge of the perimeter sealing element and the outer edge. Some embodiments of the outer edges protrude out of a plate plane defined by the bipolar plate. A plurality of stiffening structures stiffening the outer edge region of the bipolar plate.