A layer system (1) for coating a bipolar plate (2), including at least one cover layer (1a) made of tin oxide, wherein at least one metal oxide of the group comprising tantalum oxide, niobium oxide, titanium oxide, zirconium oxide, and hafnium oxide is homogenously dissolved in the tin oxide, and the electric conductivity of the cover layer (1a) is greater than or equal to 10.sup.2 S/cm. A bipolar plate (2, 2′) is also provided with an anode side and a cathode side, comprising a substrate (2a, 2a′) and such a layer system (1), and to a fuel cell (10) or an electrolyzer comprising such a bipolar plate (2, 2′).

The present disclosure generally relates to systems and methods for impregnating resin in one or more coolant channels in a bipolar plate before or after assembly of the bipolar plates into a fuel cell stack.

The present disclosure generally relates to systems and methods for impregnating resin in one or more coolant channels in a bipolar plate before or after assembly of the bipolar plates into a fuel cell stack.

A fuel cell single cell includes a pair of separators each having manifold holes, a frame disposed between the separators, a power generating unit disposed in an opening of the frame, and a plurality of gas flow channels configured to connect the power generating unit with the manifold holes. Each of the gas flow channels has a distal channel portion defined by a frame groove provided in the frame and configured to communicate with the manifold holes, and a proximal channel portion defined by a separator groove provided in the corresponding separator and configured to communicate with the power generating unit. Each of the gas flow channels is configured to be independent of adjacent other gas flow channels, at least over a range from a distal end of the distal channel portion, which communicates with the manifold holes, to a point in the proximal channel portion.

A fuel cell single cell includes a pair of separators each having manifold holes, a frame disposed between the separators, a power generating unit disposed in an opening of the frame, and a plurality of gas flow channels configured to connect the power generating unit with the manifold holes. Each of the gas flow channels has a distal channel portion defined by a frame groove provided in the frame and configured to communicate with the manifold holes, and a proximal channel portion defined by a separator groove provided in the corresponding separator and configured to communicate with the power generating unit. Each of the gas flow channels is configured to be independent of adjacent other gas flow channels, at least over a range from a distal end of the distal channel portion, which communicates with the manifold holes, to a point in the proximal channel portion.

Various embodiments include fuel cell interconnects having a fuel distribution portion having an inlet opening, a fuel collection portion having an outlet opening, and a primary fuel flow field containing channels, wherein the fuel distribution portion comprises at least one raised feature defining a fuel distribution flow path, and the fuel distribution flow path is not continuous with the channels in the primary fuel flow field. The at least one raised feature may include, for example, a network of ribs and/or dots. Further embodiments include interconnects having a fuel distribution portion with a variable surface depth to provide variable flow restriction and/or a plenum with variable surface depth and raised a raised relief feature on the cathode side, and/or varying flow channel depths and/or rib heights adjacent a fuel hole.

Benthic microbial biofuel cells (BMFCs) are a potential non-toxic and renewable source of underwater power. BMFCs function by coupling an anaerobic anode to an oxygenated cathode. However, current in-situ BMFCs on average produce less than 1W of power. Potential causes are internal ohmic resistance and low capture efficiency of the bacteria-generated charge due to macroscopic average distances between bacteria and electrodes. A microfluidic BMFC chip is enclosed to study those potential causes. The chip is built using elastomer microfluidics to provide biologically-inert microfluidic confinement of the bacteria, forcing them to be no further away than the height of the containment microchamber (‥90 μm) from the microelectrode matrix built on the glass substrate of the chip. The matrix captures the charge without location bias (due to its H-architecture) and conducts it to the outside circuit. The microfluidic chip system can be used as an evaluation station to optimize biological parameters, geometry, and electrode scaling towards increased power. That would lead to the development of an optimized power unit that can then be arrayed to build renewable power stations in maritime environments.

Benthic microbial biofuel cells (BMFCs) are a potential non-toxic and renewable source of underwater power. BMFCs function by coupling an anaerobic anode to an oxygenated cathode. However, current in-situ BMFCs on average produce less than 1W of power. Potential causes are internal ohmic resistance and low capture efficiency of the bacteria-generated charge due to macroscopic average distances between bacteria and electrodes. A microfluidic BMFC chip is enclosed to study those potential causes. The chip is built using elastomer microfluidics to provide biologically-inert microfluidic confinement of the bacteria, forcing them to be no further away than the height of the containment microchamber (‥90 μm) from the microelectrode matrix built on the glass substrate of the chip. The matrix captures the charge without location bias (due to its H-architecture) and conducts it to the outside circuit. The microfluidic chip system can be used as an evaluation station to optimize biological parameters, geometry, and electrode scaling towards increased power. That would lead to the development of an optimized power unit that can then be arrayed to build renewable power stations in maritime environments.

A fuel cell includes a flow field plate having at least one channel and at least one land, where each of the at least one channel is positioned between two adjacent lands. The fuel cell further includes a gas diffusion layer (GDL) positioned between the flow field plate and a catalyst layer, where the catalyst layer has a first region aligned with the at least one channel and a second region aligned with the at least one land. The first region may have a first catalyst material supported by a first catalyst support region, and the second region may have a second catalyst material supported by a second catalyst support region.

A fuel cell includes a flow field plate having at least one channel and at least one land, where each of the at least one channel is positioned between two adjacent lands. The fuel cell further includes a gas diffusion layer (GDL) positioned between the flow field plate and a catalyst layer, where the catalyst layer has a first region aligned with the at least one channel and a second region aligned with the at least one land. The first region may have a first catalyst material supported by a first catalyst support region, and the second region may have a second catalyst material supported by a second catalyst support region.