H01M8/023

HIGH OR DIFFERENTIAL PRESSURE ELECTROLYSIS CELL

An electrochemical cell has a membrane located between two flow field plates. On a first side of the membrane, there is a porous support surrounded by a seal between the membrane and the flow field plate. There is a gap between the porous support and the seal at the surface of the membrane. On a second side of the membrane, there is a seal between the membrane and the flow field plate located inside of the gap in plan view. The electrochemical cell is useful, for example, in high pressure or differential pressure electrolysis in which the second side of the membrane will be consistently exposed to a higher pressure than the first side of the membrane.

High or differential pressure electrolysis cell

An electrochemical cell has a membrane located between two flow field plates. On a first side of the membrane, there is a porous support surrounded by a seal between the membrane and the flow field plate. There is a gap between the porous support and the seal at the surface of the membrane. On a second side of the membrane, there is a seal between the membrane and the flow field plate located inside of the gap in plan view. The electrochemical cell is useful, for example, in high pressure or differential pressure electrolysis in which the second side of the membrane will be consistently exposed to a higher pressure than the first side of the membrane.

High or differential pressure electrolysis cell

An electrochemical cell has a membrane located between two flow field plates. On a first side of the membrane, there is a porous support surrounded by a seal between the membrane and the flow field plate. There is a gap between the porous support and the seal at the surface of the membrane. On a second side of the membrane, there is a seal between the membrane and the flow field plate located inside of the gap in plan view. The electrochemical cell is useful, for example, in high pressure or differential pressure electrolysis in which the second side of the membrane will be consistently exposed to a higher pressure than the first side of the membrane.

FLOW BATTERIES WITH INSOLUBLE POLYMER SUPPORTED REDOX ACTIVE MATERIALS
20230122822 · 2023-04-20 ·

A redox matched flow battery utilizes insoluble functionalized catholyte and anolyte beads to store charge on redox-active moieties tethered to the beads, with charge being transferred between the electrodes and the bead using a soluble, redox-matched mediator.

FLOW BATTERIES WITH INSOLUBLE POLYMER SUPPORTED REDOX ACTIVE MATERIALS
20230122822 · 2023-04-20 ·

A redox matched flow battery utilizes insoluble functionalized catholyte and anolyte beads to store charge on redox-active moieties tethered to the beads, with charge being transferred between the electrodes and the bead using a soluble, redox-matched mediator.

GAS DIFFUSION LAYERS WITH ENGINEERED SURFACE ROUGHNESS FOR HOSTING CATALYSTS

Disclosed herein are gas diffusion layers (GDLs) for electrochemical devices which have increased surface area for hosting catalysts or contacting a catalyst layer. GDLs with engineered surface roughness increase the effective diffusivities of gas phase reactants in electrochemical devices (e.g., PEMFCs). Also disclosed herein are gas diffusion electrodes, membrane electrode assemblies, and fuel cells comprising GDLs with increased surface area. Also disclosed herein are methods of manufacturing GDLs with increased surface area, as well as gas diffusion electrodes and membrane electrode assemblies comprising GDLs with increased surface area.

ZINC-IODINE BATTERY
20220336866 · 2022-10-20 ·

An aqueous rechargeable zinc-iodine battery includes an aqueous electrolyte solution including zinc-iodine; a zinc anode; and a double-layered cathode having: a conductive substrate, and an adsorptive layer disposed over the conductive substrate.

Separator for fuel cell and fuel cell including the same

A fuel cell includes a separator. A constant amount of air is supplied to the fuel cell irrespective of positions within an air channel, and thus, degradation of the fuel cell is prevented. The separator includes a separator body and a porous structure which has a plurality of pores defined therein to provide a path through which a fluid flows, where the separator body includes: a fluid inlet part having a space into which the fluid is introduced; a reaction region configured to receive the fluid; and a diffusion part which is provided between the fluid inlet part and the reaction region, where the porous structure is stacked on one surface of the reaction region, and the number of pores per unit volume of the porous structure varies in an inlet region.

Separator for fuel cell and fuel cell including the same

A fuel cell includes a separator. A constant amount of air is supplied to the fuel cell irrespective of positions within an air channel, and thus, degradation of the fuel cell is prevented. The separator includes a separator body and a porous structure which has a plurality of pores defined therein to provide a path through which a fluid flows, where the separator body includes: a fluid inlet part having a space into which the fluid is introduced; a reaction region configured to receive the fluid; and a diffusion part which is provided between the fluid inlet part and the reaction region, where the porous structure is stacked on one surface of the reaction region, and the number of pores per unit volume of the porous structure varies in an inlet region.

COMPOSITE ELECTRODE FOR FLOW CELL, FLOW CELL, AND PILE

The present invention relates to the technical field of energy storage. Disclosed in the invention are a composite electrode for a flow cell, a flow cell, and a stack. The composite electrode comprises: a distribution layer, used to distribute an electrolyte; a reaction layer used to receive the electrolyte of the distribution layer and provide an electrochemical reaction site for the electrolyte; and a contact layer, used to reduce the contact resistance of the distribution layer so as to reduce an internal resistance of the flow cell. In the present invention, by means of providing a distribution layer, a reaction layer and a contact layer, an electrochemical reaction site and an electrolyte distribution site of a composite electrode can be effectively separated, the distribution layer being able to greatly reduce dead zones and channeling caused by uneven flow distribution, and the contact layer being able to greatly reduce the internal resistance of the flow cell. Meanwhile, the distribution layer and the reaction layer can be separately and specially designed, thus improving the output power and energy efficiency of a cell or a stack taking the present composite electrode as an anode and/or a cathode.