Method for producing carrier for electrode catalyst, precursor of carrier for electrode catalyst, and carrier for electrode catalyst, comprising same
US-12057587-B2 · Aug 6, 2024 · US
US2019221873A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2019221873-A1 |
| Application number | US-201916243275-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jan 9, 2019 |
| Priority date | Jan 18, 2018 |
| Publication date | Jul 18, 2019 |
| Grant date | — |
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An assembly of electrochemical cells for an electrochemical reactor, including a first electrochemical cell, including a first membrane/electrode assembly including a first anode and a first cathode on either side of a proton exchange membrane; first and second flow guides positioned on either side of the first assembly; a second electrochemical cell, including a second membrane/electrode assembly including a second anode and a second cathode on either side of a proton exchange membrane; third and fourth flow guides on either side of the second membrane/electrode assembly; the first and third flow guides have one and the same geometry; the first anode and the second anode have different distributions of surface densities of electrocatalytic material on respective faces of the first and second proton exchange membranes.
Opening claim text (preview).
1 . An assembly of electrochemical cells for an electrochemical reactor, comprising: a first electrochemical cell, including: a first membrane/electrode assembly comprising a first proton exchange membrane, a first anode and a first cathode positioned on either side of the proton exchange membrane and each including an electrocatalytic material; first and second flow guides positioned on either side of the first membrane/electrode assembly; a second electrochemical cell, including: a second membrane/electrode assembly comprising a second proton exchange membrane, a second anode and a second cathode positioned on either side of the proton exchange membrane and each including an electrocatalytic material; third and fourth flow guides positioned on either side of the second membrane/electrode assembly; wherein: the first and third flow guides have one and the same geometry; the second and fourth flow guides have one and the same geometry; the first anode and the second anode have different distributions of surface densities of electrocatalytic material on respective faces of the first and second proton exchange membranes, or the first cathode and the second cathode have different distributions of surface densities of electrocatalytic material on respective faces of the first and second proton exchange membranes, the first proton exchange membrane comprising a central portion completely covered by the first anode and by the first cathode, the second proton exchange membrane comprising a central portion having a zone not covered by the second anode and by the second cathode. 2 . The assembly of electrochemical cells according to claim 1 , wherein the first anode and the second anode include one and the same electrocatalytic material, and wherein the first cathode and the second cathode include one and the same electrocatalytic material. 3 . The assembly of electrochemical cells according to claim 1 , wherein the second anode and the second cathode have an identical shape in projection according to a normal to the second proton exchange membrane. 4 . The assembly of electrochemical cells according to claim 1 , wherein at least part of said zone that is not covered is defined by multiple recesses of the second anode and second cathode, said recesses being distributed uniformly in the second anode and in the second cathode. 5 . The assembly of electrochemical cells according to claim 4 , wherein said recesses have one and the same geometry. 6 . The assembly of electrochemical cells according to claim 1 , wherein said zone that is not covered is defined by at least one recess of the second anode and one recess of the second cathode extending over the full width of the latter. 7 . The assembly of electrochemical cells according to claim 1 , wherein the second anode covers a surface area of the second proton exchange membrane between 10 and 80% of the area of overlap of the first proton exchange membrane by the first anode. 8 . The assembly of electrochemical cells according to claim 1 , wherein said second anode is formed in a single piece, and wherein said second cathode is formed in a single piece. 9 . The assembly of electrochemical cells according to claim 1 , wherein said second anode is formed of several separate elements, and wherein said second cathode is formed of several separate elements. 10 . The assembly of electrochemical cells according to claim 8 , wherein: the first and third flow guides comprise flow channels, flow through these different flow channels running along one and the same length of the anode; or the second and fourth flow guides comprise flow channels, flow through these different flow channels running along one and the same length of the cathode. 11 . The assembly of electrochemical cells according to claim 1 , wherein the second anode has at least one part extending over the same width as the first anode. 12 . An electrochemical reactor, comprising a stack of electrochemical cells, said stack including an assembly of electrochemical cells according to claim 1 . 13 . A fuel cell, comprising a stack of electrochemical cells, said stack including an assembly of electrochemical cells according to claim 1 .
characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant · CPC title
with a gradient in another property than porosity (H01M4/861 takes precedence) · CPC title
characterised by membrane-electrode assemblies [MEA] (H01M8/12 takes precedence) · CPC title
Supplying or removing reactants or electrolytes; Regeneration of electrolytes · CPC title
Fuel cells with polymeric electrolytes · CPC title
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