US2006105225A1PendingUtilityA1
Membrane-electrode assembly for fuel cell and fuel cell system comprising same
Est. expiryNov 16, 2024(expired)· nominal 20-yr term from priority
H01M 4/86H01M 8/02Y02E60/50H01M 8/0234H01M 4/8878H01M 4/8882H01M 4/8605Y02P70/50H01M 8/1004H01M 4/8828H01M 4/926H01M 4/921
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Claims
Abstract
A membrane-electrode assembly for a fuel cell of the present invention includes an anode and a cathode facing each other, and a polymer electrolyte membrane interposed therebetween. At least one of the anode and the cathode includes a catalyst layer and an electrode substrate. The catalyst layer includes a catalyst and a porous ionomer. The polymer electrolyte membrane contacts one side of the catalyst layer and the electrode substrate contacts the other side of the catalyst layer.
Claims
exact text as granted — not AI-modified1 . A membrane-electrode assembly for a fuel cell, comprising:
an anode and a cathode facing each other, at least one of the anode and the cathode comprising:
a catalyst layer comprising a catalyst and a porous ionomer layer; and
an electrode substrate enabling a reactant to diffuse into the catalyst layer; and
a polymer electrolyte membrane interposed between the anode and the cathode.
2 . The membrane-electrode assembly of claim 1 , wherein the porous ionomer layer has a porosity ranging from about 40 volume % to about 80 volume %.
3 . The membrane-electrode assembly of claim 1 , wherein the porous ionomer layer has a pore size ranging from about 10 nm to about 1,000 nm.
4 . The membrane-electrode assembly of claim 1 , wherein the porous ionomer layer is present on a surface of the catalyst.
5 . The membrane-electrode assembly of claim 1 , wherein the catalyst comprises a metal catalyst supported on a carrier.
6 . The membrane-electrode assembly of claim 1 , wherein the electrode substrate comprises a conductive substrate selected from the group consisting of a water-repellent treated carbon paper and carbon cloth.
7 . A fuel cell system, comprising:
at least one electricity generating element for generating electricity through oxidation of fuel and reduction of an oxidant, comprising:
a membrane-electrode assembly comprising:
an anode and a cathode facing each other, at least one of the anode and the cathode comprising:
a catalyst layer comprising a catalyst and a porous ionomer layer; and
an electrode substrate enabling the fuel or the oxidant to diffuse into the catalyst layer; and
a polymer electrolyte membrane interposed between the anode and the cathode; and
separators positioned at both sides of the membrane-electrode assembly;
a fuel supplier providing the fuel to the electricity generating element; and an oxidant supplier supplying the oxidant to the electricity generating element.
8 . The fuel cell system of claim 7 , wherein the porous ionomer layer has a porosity ranging from about 40 volume % to about 80 volume %.
9 . The fuel cell system of claim 7 , wherein the porous ionomer layer has a pore size ranging from about 10 nm to about 1,000 nm.
10 . The fuel cell system of claim 7 , wherein the porous ionomer layer is present on a surface of the catalyst.
11 . A method for manufacturing a membrane-electrode assembly, comprising:
preparing an anode and a cathode, at least one of the anode and the cathode comprising:
a catalyst layer comprising a catalyst and a porous ionomer layer; and
an electrode substrate enabling a reactant to diffuse into the catalyst layer; and
preparing a polymer electrolyte membrane interposed between the anode and the cathode.
12 . The method of claim 11 , wherein the catalyst layer is formed by a process comprising:
coating a composition including the catalyst, an ionomer and a plasticizer onto the electrode substrate; and extracting the plasticizer.
13 . The method of claim 12 , wherein the plasticizer is at least one polymer selected from the group consisting of a C1 to C10 polyalkyleneglycol; a C1 to C10 polyalkyleneoxide; a C1 to C10 poly(alkyl)acrylic acid; an aromatic or fluorine polymer having a sulfonic acid group; and a cellulose-based polymer.
14 . The method of claim 12 , wherein the plasticizer is extracted by dipping the coated composition onto the electrode substrate in an extraction solvent.
15 . The method of claim 14 , wherein the extraction solvent is selected from the group consisting of an alcohol-based solvent, an ether-based solvent, tetrahydrofuran, and a mixture thereof.
16 . The method of claim 12 , wherein the weight ratio of the plasticizer to the ionomer ranges from about 20:80 to 70:30.
17 . The method of claim 11 , wherein the catalyst layer is formed by a process comprising:
coating a composition including the catalyst, an ionomer and fumed silica onto the electrode substrate; and firing the coated composition.
18 . The method of claim 17 , wherein the weight ratio of the fumed silica to the ionomer ranges from about 10:90 to 50:50.
19 . An membrane-electrode assembly manufactured according to claim 12 .
20 . The fuel cell system comprising the membrane-electrode assembly of claim 19 .
21 . A membrane-electrode assembly for a fuel cell, comprising:
an anode and a cathode facing each other, at least one of the anode and the cathode formed by coating a composition including a catalyst, an ionomer and one of a plasticizer or fumed silica onto an electrode substrate, and extracting the plasticizer when the plasticizer is used or firing the coated composition when the fumed silica is used; and a polymer electrolyte membrane interposed between the anode and the cathode.
22 . The membrane-electrode assembly of claim 21 , wherein the plasticizer is at least one polymer selected from the group consisting of a C1 to C10 polyalkyleneglycol; a C1 to C10 polyalkyleneoxide; a C1 to C10 poly(alkyl)acrylic acid; an aromatic or fluorine polymer having a sulfonic acid group; and a cellulose-based polymer.
23 . The membrane-electrode assembly of claim 21 , wherein the plasticizer is extracted by dipping the coated composition onto the electrode substrate in an extraction solvent.
24 . The membrane-electrode assembly of claim 21 , wherein the weight ratio of the plasticizer to the ionomer ranges from about 20:80 to 70:30.
25 . The membrane-electrode assembly of claim 21 , wherein the plasticizer has a number average molecular weight ranging from 200 to 50,000.
26 . The membrane-electrode assembly of claim 21 , wherein the weight ratio of the fumed silica to the ionomer ranges from about 10:90 to 50:50.
27 . The membrane-electrode assembly of claim 21 , wherein the fumed silica has a specific surface area ranging from 100 to 1,200 m 2 /g and a particle size of 10 nm to 1,000 nm.Cited by (0)
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