A fuel cell stack in which unit cells are stacked, wherein the unit cell includes: a membrane electrode assembly; an insulating member; a first separator; a second separator; and a gasket, a hole penetrates through the insulating member and the first and second separators, the gasket extends around the hole on the insulating member, a flow path portion is formed in at least one of the first and second separators, the first and second separators define a communicating portion, one of the first and second separators includes: first and second protruding portions; and a recessed portion, at least a part of the communicating portion is defined by the first and second protruding portions, the recessed portion, and the other of the first and second separators, and the first separator includes a support portion contacting and supporting the insulating member on a back side of the gasket.

A fuel cell stack in which unit cells are stacked, wherein the unit cell includes: a membrane electrode assembly; an insulating member; a first separator; a second separator; and a gasket, a hole penetrates through the insulating member and the first and second separators, the gasket extends around the hole on the insulating member, a flow path portion is formed in at least one of the first and second separators, the first and second separators define a communicating portion, one of the first and second separators includes: first and second protruding portions; and a recessed portion, at least a part of the communicating portion is defined by the first and second protruding portions, the recessed portion, and the other of the first and second separators, and the first separator includes a support portion contacting and supporting the insulating member on a back side of the gasket.

An illustrative example fuel cell cooler plate includes a first side configured to be received adjacent a fuel cell component and a second side facing opposite the first side. The first side defines a first surface area of the plate. An edge is transverse to the first side and the second side. The edge has a surface area that is less than the first surface area. A first coolant passage within the plate is closer to the second side than the first side. A second coolant passage is between the first side and the first coolant passage. The second coolant passage is in a heat exchange relationship with the first coolant passage.

An illustrative example fuel cell cooler plate includes a first side configured to be received adjacent a fuel cell component and a second side facing opposite the first side. The first side defines a first surface area of the plate. An edge is transverse to the first side and the second side. The edge has a surface area that is less than the first surface area. A first coolant passage within the plate is closer to the second side than the first side. A second coolant passage is between the first side and the first coolant passage. The second coolant passage is in a heat exchange relationship with the first coolant passage.

An electrochemical reaction cell comprising an anode electrode, a cathode electrode, and a membrane electrode assembly (MEA). The MEA is positioned between the anode electrode and the cathode electrode. The anode electrode, the cathode electrode, and the MEA each have a corrugated shape and are contained within a recess of a housing.

An electrochemical reaction cell comprising an anode electrode, a cathode electrode, and a membrane electrode assembly (MEA). The MEA is positioned between the anode electrode and the cathode electrode. The anode electrode, the cathode electrode, and the MEA each have a corrugated shape and are contained within a recess of a housing.

Electrode plates with feed and product channels are provided that present more spatially uniform chemical and electrochemical compositions to catalytically active electrode structures and ion-conducting electrolyte membrane layers to improve the performance and increase the longevity of the electrochemical devices (e.g., membrane reactors, gas-separation cells, electrochemical compressors, fuel cells, and electrolyzers). Each plate can have a single channel that extends between an inlet and an outlet, and each channel can have a first segment that spirals inwardly from the inlet to a midpoint and a second segment that spirals outwardly from the midpoint to the outlet. The segments are interleaved with each other such that there are alternating flows of less-depleted feed or product and more-depleted feed or product. Consequently, chemical, electrochemical, and thermal behaviors are more uniformly distributed across the membrane-electrode assembly to increase performance and longevity of the assembly.

A fuel cell assembly includes at least a first flow field plate and a second flow field plate sandwiching a multilayer membrane electrode assembly, wherein the multilayer membrane electrode assembly comprises at least a 3-layer membrane electrode assembly including a first electrode facing the first flow field plate, a second electrode facing the second flow field plate and a membrane separating the electrodes, wherein each flow field plate has a flow field structure protruding from a base level of the flow field plate for distributing reactant over the respective electrode, and wherein further at least one sealing element is arranged between the first and the second flow field plate, which is adapted to prevent leakage of the reactants to an environment, wherein in a boundary area between the flow field structure and the sealing element of at least one of the flow field plates at least one bypass stopping element is arranged for avoiding the reactant bypassing the flow field structure, wherein the bypass stopping element protrudes from the respective base level of the flow field plate, wherein the at least one bypass stopping element has a pointed portion, which is adapted to compress the multilayer membrane electrode assembly, as well as a flow field plate for such a fuel cell assembly.

A fuel cell assembly includes at least a first flow field plate and a second flow field plate sandwiching a multilayer membrane electrode assembly, wherein the multilayer membrane electrode assembly comprises at least a 3-layer membrane electrode assembly including a first electrode facing the first flow field plate, a second electrode facing the second flow field plate and a membrane separating the electrodes, wherein each flow field plate has a flow field structure protruding from a base level of the flow field plate for distributing reactant over the respective electrode, and wherein further at least one sealing element is arranged between the first and the second flow field plate, which is adapted to prevent leakage of the reactants to an environment, wherein in a boundary area between the flow field structure and the sealing element of at least one of the flow field plates at least one bypass stopping element is arranged for avoiding the reactant bypassing the flow field structure, wherein the bypass stopping element protrudes from the respective base level of the flow field plate, wherein the at least one bypass stopping element has a pointed portion, which is adapted to compress the multilayer membrane electrode assembly, as well as a flow field plate for such a fuel cell assembly.

Separator plates (108; 300; 400; 410) for fuel cell assemblies have a first edge (110, 310) and a second, opposing edge (111, 311). The fuel cell separator plates define a series of airflow channels (112, 113, 312, 313, 401, 411) extending longitudinally between the first and second edges. The airflow channels can be non-linear airflow channels formed from a linked series of bumps (320) opposite to corresponding recesses (321) in the facing channel walls. The linked series of bumps and recesses can run the entire channel length. The linked series of bumps and recesses can be formed as a sinusoidal wave having an amplitude and a frequency.