Patent classifications
H01M4/8807
Proton Exchange Membrane Fuel Cell and Preparation Method Therefor, and Proton Exchange Membrane Fuel Cell Stack
A proton exchange membrane fuel cell that uses hydrogen peroxide as an oxidant is disclosed. The proton exchange membrane fuel cell includes an anode gas diffusion layer, an anode catalyst layer, a proton exchange membrane and a cathode catalyst layer arranged sequentially. The proton exchange membrane fuel cell further includes a single electrode plate, and does not include a cathode gas diffusion layer. A cell stack including the proton exchange membrane fuel cell is also disclosed, as well as a method for preparing the proton exchange membrane fuel cell.
CATALYST
The present invention provides a method of preparing a catalyst material which comprises electrocatalyst particles, a support material, and graphitic carbon nitride, wherein the method comprises applying graphitic carbon nitride to a catalyst material precursor. Also provided is a catalyst material comprising graphitic carbon nitride.
CATALYST PREPARATION
The present invention provides a method of preparing a catalyst material, said catalyst material comprising a support material and an electrocatalyst dispersed on the support material; said method comprising the steps: i) providing a support material; then ii) 10 depositing a silicon oxide precursor on the support material; then iii) carrying out a heat treatment step to convert the silicon oxide precursor to silicon oxide; then iv) depositing said electrocatalyst or a precursor of said electrocatalyst on the support material; then v) removal of at least some of the silicon oxide.
Electrochemically active unit for an electrochemical device
In order to provide an electrochemically active unit for an electrochemical device including a membrane electrode assembly, at least one gas diffusion layer and a seal that is linked to at least one of the at least one gas diffusion layers, in the manufacture whereof as even as possible a construction of the penetration region in which the gas diffusion layer of the electrochemically active unit is penetrated by the sealing material of the seal over the periphery of the gas diffusion layer is achievable, the seal includes a linking region, a distribution region and a connection region that connects the linking region and the distribution region to one another, wherein the connection region has a minimum height that is less than a quarter of the maximum height of the distribution region and less than a quarter of the maximum height of the linking region.
Proton exchange membrane fuel cell
A proton exchange membrane fuel cell includes an anode catalyst layer, a cathode catalyst layer, a proton exchange membrane separating the anode catalyst layer from the cathode catalyst layer, an oxygen inlet configured to supply oxygen to the cathode catalyst layer, and a hydrogen inlet separate from the oxygen inlet and configured to supply hydrogen to the anode catalyst layer. The fuel cell is operable to convert the hydrogen from the hydrogen inlet to hydrogen ions at the anode catalyst layer and to produce an H2O byproduct at the cathode catalyst layer where the oxygen reacts with the hydrogen ions. The fuel cell includes a water outlet for the H2O byproduct that is separate from the oxygen inlet.
ELECTROCHEMICAL CATALYSTS WITH ENHANCED CATALYTIC ACTIVITY
A catalyst structure includes: (1) a substrate; (2) a catalyst layer on the substrate; and (3) an adhesion layer disposed between the substrate and the catalyst layer. In some implementations, an average thickness of the adhesion layer is about 1 nm or less. In some implementations, a material of the catalyst layer at least partially extends into a region of the adhesion layer. In some implementations, the catalyst layer is characterized by a lattice strain imparted by the adhesion layer.
Method for producing membrane electrode
A method for producing a membrane electrode comprises a thermal transfer printing step, a thermal combining step, a carbon paper attaching step and a hot-pressing step. The invention realizes the continuous automatic production of the membrane electrode and improves the production efficiency and the quality of the membrane electrode.
FABRICATION OF MEMBRANE ELECTRODE ASSEMBLY WITH FILAMENT EXTENSION ATOMIZER SPRAY
A method and apparatus are described for forming a multilayer assembly. The method includes adhering first and second catalyst layers to opposed sides of a polymer membrane. At least one of the first catalyst layer, the second catalyst layer, and the polymer membrane is formed by filament extension atomization of a fluid material to form atomized droplets that are sprayed to form the respective membrane or layer.
Systems and methods for processing hydrogen
The present disclosure provides a fuel cell, comprising: an anode; a cathode; and a membrane electrode assembly disposed between the anode and the cathode. The anode may comprise a gas diffusion layer with one or more channels for directing a source material through the gas diffusion layer of the anode to facilitate processing of the source material to generate an electrical current. The one or more channels may comprise one or more features configured to enhance a diffusion of the source material through the gas diffusion layer of the anode. The source material may comprise hydrogen and nitrogen.
Membrane electrode, fuel cell gas diffusion layer and process for preparing the fuel cell gas diffusion layer
Disclosed is a membrane electrode, fuel cell gas diffusion layer, and process for preparing the fuel cell gas diffusion layer, the process comprising: S1 coating microporous layer slurry on the surface of hydrophobic carbon paper; the microporous layer slurry was obtained by dispersing mixture of carbon powder, polytetrafluoroethylene dispersion solution, thickener, and solvent; S2 moving the hydrophobic carbon paper coated with the microporous layer slurry to a porous ceramic plate, and connecting a vacuum pump to the porous ceramic plate, vacuumed for adsorption pre-infiltration treatment, and then dried. S3 continuing to coat the microporous layer slurry on the hydrophobic carbon paper dried in step S2, then drying, and then sintering at 250-400° C. to obtain a gas diffusion layer. The beneficial effects of this disclosure include: this disclosure improve the water vapor erosion resistance of the microporous layer and the durability of the gas diffusion layer.