Patent classifications
H01M8/0234
BIOPOLAR MEMBRANE CELL FOR THE CAPTURE OF CARBON DIOXIDE
In an aspect, a bipolar membrane cell comprises a separation layer located in between an anode half-cell and a cathode half-cell; wherein the anode half-cell comprises a proton exchange membrane and an anode; where the proton exchange membrane is located in between the anode and the separation layer; wherein the cathode half-cell comprises an anion exchange membrane and a cathode; wherein the anion exchange membrane is located in between the cathode and the separation layer; and an external circuit connecting the anode and the cathode.
BIOPOLAR MEMBRANE CELL FOR THE CAPTURE OF CARBON DIOXIDE
In an aspect, a bipolar membrane cell comprises a separation layer located in between an anode half-cell and a cathode half-cell; wherein the anode half-cell comprises a proton exchange membrane and an anode; where the proton exchange membrane is located in between the anode and the separation layer; wherein the cathode half-cell comprises an anion exchange membrane and a cathode; wherein the anion exchange membrane is located in between the cathode and the separation layer; and an external circuit connecting the anode and the cathode.
GAS DIFFUSION LAYER FOR FUEL CELL INCLUDING CARBOXYMETHYL CELLULOSE AND MEHTOD FOR PRODUCING THE SAME
A method for producing a gas diffusion layer for a fuel cell, includes a substrate preparation step of preparing a substrate for the gas diffusion layer; a slurry preparation step of preparing a slurry for a microporous layer containing carboxymethyl cellulose (CMC) and polytetrafluoroethylene (PTFE) diffused in solvent; a microporous layer forming step of forming a microporous layer by applying the slurry onto the substrate; and a heat-treatment step of controlling the hydrophobicity of the gas diffusion layer by heating the substrate having the microporous layer applied thereonto. Also disclosed is a gas diffusion layer produced thereby. The method may control the hydrophobicity of the gas diffusion layer by variably controlling the heat-treatment temperature.
TUBULAR POLYMER ELECTROLYTE MEMBRANE FUEL CELL STACK
A fuel cell stack including a plurality of fuel cell units having a truncated cone shape and connected in series with each other is proposed. The series connection of the fuel cell units may be made such that a relatively small outer diameter portion of one of the fuel cell units is inserted into a relatively large outer diameter portion of another fuel cell unit adjacent to the one fuel cell unit.
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.
BIPOLAR PLATE FOR FUEL CELLS AND THE METHOD OF FORMING THE SAME
A bipolar plate for a fuel cell is provided. The bipolar plate is formed by pressing a base plate, wherein the base plate is formed by a soft graphite plate. The soft graphite plate has a density of 0.8-1.3 g/cm.sup.3, a carbon content more than 98% and an ash content less than 2%. Based on the thickness of the base plate before pressing, the thickness compression ratio of the bipolar plate is 40-50%.
BIPOLAR SURFACE ELEMENT
A bipolar flat element comprising a coating that contains expanded graphite and a binder, the coating being applied to at least one of the two primary surfaces of a flat, electrically conductive element.
BIPOLAR SURFACE ELEMENT
A bipolar flat element comprising a coating that contains expanded graphite and a binder, the coating being applied to at least one of the two primary surfaces of a flat, electrically conductive element.
GAS DIFFUSION LAYER STRUCTURE FOR FUEL CELL
The present disclosure relates to a gas diffusion layer structure for a unit cell of a fuel cell, the gas diffusion layer structure includes a gas diffusion layer disposed between a catalyst layer and a separator of the unit cell of the fuel cell, in which the gas diffusion layer includes a microporous layer positioned adjacent to the catalyst layer, and a base layer positioned between the microporous layer and the separator, in which the base layer includes: a microporous layer adjacent region disposed adjacent to the microporous layer, and a gas channel adjacent region disposed adjacent to the separator, and in which the gas diffusion layer is pressed so that a solid volume fraction of the gas channel adjacent region and the microporous layer adjacent region increases to a target solid volume fraction.
Electrode gas diffusion layer assembly with controlled binder content and fuel cell stack including the same
Disclosed are an electrode gas diffusion layer assembly (EGA) and a fuel cell stack including the same. The content of the binder in the electrode and the content of the binder in the adhesive layer that attaches the electrode to the gas diffusion layer (GDL) may be optimized. Thus, it is possible to reduce the occurrence of flooding and the deterioration in durability/performance caused by a dry atmosphere in the EGA including the electrode and the adhesive layer, so that the output density per unit area is improved while the trade-off is minimized.