H01M4/8663

Flexible electrode, biofuel cell using same, and method for manufacturing same

The present invention relates to a flexible electrode, a biofuel cell using the same, and a method for manufacturing the same. The electrode according to the present invention comprises: a non-electrically conductive substrate (10); a base layer (20) disposed on the outer surface of the substrate (10); a nanoparticle layer (31) including metallic nanoparticles and disposed on the outer surface of the base layer (20); and a monomolecular layer (33) including a monomolecular material having an amine group and disposed on the outer surface of the nanoparticle layer (31).

Cathode of metal air battery, metal air battery including the same, and method of manufacturing the same

A cathode of a metal-air battery includes an electrically conductive metal oxide in a three-dimensional (3D) network structure, wherein the electrically conductive metal oxide of the three-dimensional network structure is in a form of a plurality of strands, wherein a strand of the plurality of strands has an aspect ratio in a range of about 10 to about 10.sup.7, and wherein the three-dimensional network structure has a porosity of about 70 volume percent to about 95 volume percent, based on a total volume of the three-dimensional network structure.

HALOGEN COMPLEXING AGENTS BOUND TO THE CATHODE SURFACE IN A STATIC ZINC HALIDE BATTERY
20220320514 · 2022-10-06 · ·

A bipolar electrode comprising a cathode substrate loaded with a halogen complexing agent that has a structure of formula Q.sup.+(R.sup.A)(R.sup.B)(R.sup.C)(R.sup.D)X.sup.−, is disclosed. The bipolar electrode also comprises a bipolar electrode plate having a cathode surface and an anode surface, wherein the cathode surface opposes the anode surface. The cathode surface at least partially contacts the cathode substrate. An electrochemical cell and a battery stack comprising the bipolar electrode, and a process for manufacturing the bipolar electrode are also disclosed.

MEMBRANE ELECTRODE ASSEMBLY, AND PRODUCTION METHOD FOR MEMBRANE ELECTRODE ASSEMBLY
20230207848 · 2023-06-29 · ·

To make adhesiveness of a catalyst layer and a solid polymer electrolyte membrane be compatible with electrolysis performance without the need for weighting components even when an electrolyte is included in the catalyst layer, the rate of mass of the electrolyte/the catalyst of the catalyst layer including a catalyst and the electrolyte is more than 0.05 and less than 0.2.

Electrode for membrane-electrode assembly, method of manufacturing same and membrane-electrode assembly using same

Disclosed are an electrode for a membrane-electrode assembly, a method of manufacturing the same and a membrane-electrode assembly using the same. The electrode may include the pores and pore density around a catalyst contained in the electrode may be selectively increased using a thermally decomposable chemical blowing agent, thereby improving mass transfer through the catalyst.

Fuel cell electrode catalyst layer, fuel cell electrode, fuel cell membrane electrode assembly and fuel cell having a proton-conductive material coated on a catalyst thereof

A fuel cell electrode catalyst layer (13) of the preset invention includes: a catalyst (131b); a support (131a) that supports the catalyst; and two or more proton-conductive materials (133) different in dry mass value per mole of a proton-donating group, the proton-conductive materials being in contact with at least a part of the catalyst and at least a part of the support. Then, a proton-conductive material in which a dry mass value per mole of the proton-donating group is highest among the proton-conductive materials is in contact with at least a part of the catalyst, and has a largest contact ratio with a surface of the catalyst.

Compositions for electrolyte fuel cells and other electrochemical conversion devices

The present disclosure relates to a composition that includes a fluoropolymer, a polymerized ionic liquid block copolymer (PILBC), and a catalyst, where the fluoropolymer is configured to affect ionic mobility, and the PILBC is configured to affect a property of the catalyst. In some embodiments of the present disclosure, the property may include at least one of oxygen transport and/or an active site functionality of the catalyst.

Electrodes and electrochemical devices and methods of making electrodes and electrochemical devices
09831503 · 2017-11-28 · ·

Dual use gas diffusion-gas evolution electrodes containing diamond-like carbon are described, which can act as gas diffusion electrodes during discharge, and gas evolution electrodes during recharge. Electrodes of the disclosed materials are electrochemically robust, inhibit multi-step reactions, and have high, isotropic thermal conductivity. The disclosed electrodes can be used as air electrodes of rechargeable metal-air batteries.

Stable catalyst ink formulations, methods of using such inks in fiber formation, and articles comprising such fibers

The present invention relates to stable catalyst ink formulations comprising am electrospinning polymer selected from halogen-comprising polymers. The present invention further relates to electrospinning of such ink formulation, to the so-obtained electrospun fibrous mat as well as to articles comprising such electrospun fibrous mat.

FUEL CELL
20170331119 · 2017-11-16 · ·

A fuel cell includes: an electrolyte membrane; an anode catalyst layer; a cathode catalyst layer; and a cathode gas diffusion layer. The cathode catalyst layer includes an ionomer, the ionomer includes copolymers each of which has a hydrophilic block. The hydrophilic block is positioned at a terminal of a copolymer which includes a hydrophobic portion and a hydrophilic portion having a sulfonic acid group. The hydrophilic block has an aggregated structure of the hydrophilic portion. A gas diffusion resistance coefficient of the cathode gas diffusion layer is 3.2×10.sup.−4 m or lower. The gas diffusion resistance coefficient is expressed by “Gas Diffusion Resistance Coefficient=Thickness of Cathode Gas Diffusion Layer/(Porosity of Cathode Gas Diffusion Layer).sup.4”.