Mitigation of membrane degradation by multilayer electrode
View Patent ↗An MEA for a fuel cell that employs multiple catalyst layers to reduce the hydrogen and/or oxygen partial pressure at the membrane so as to reduce the fluoride release rate from the membrane and reduce membrane degradation. An anode side multi-layer catalyst configuration is positioned at the anode side of the MEA membrane. The anode side multi-layer catalyst configuration includes an anode side under layer positioned against the membrane and including a catalyst, an anode side middle layer positioned against the anode side under layer and not including a catalyst and an anode side catalyst layer positioned against the anode side middle layer and opposite to the anode side under layer and including a catalyst, where the amount of catalyst in the anode side catalyst layer is greater than the amount of catalyst in the anode side under layer.
1. A membrane electrode assembly (MEA) comprising:
an ion-conducting membrane including an anode side and a cathode side;
at least one catalyst side catalyst layer positioned at the cathode side of the membrane; and
an anode side multi-layer catalyst configuration positioned at the anode side of the membrane, said anode side multilayer catalyst configuration including an anode side under layer positioned against the membrane and including a catalyst, an anode side middle layer positioned against the anode side under layer and not including a catalyst and an anode side catalyst layer positioned against the anode side middle layer and opposite to the anode side under layer and including a catalyst, where the amount of catalyst in the anode side catalyst layer is greater than the amount of catalyst in the anode side under layer and where the anode side middle layer is a low hydrogen permeability non-porous layer of an electron conductive material and ion conducting polymer.
2. The MEA according to claim 1 wherein the membrane is a proton conducting membrane, and wherein the anode side multi-layer configuration reduces the chemical membrane degradation rate by reducing the partial pressure of hydrogen at an interface of the anode side under layer and the membrane.
3. The MEA according to claim 1 wherein the anode side under layer has about 0.005 to 0.20 mg of catalyst per cm 2 and the anode side catalyst layer has 0.01 to 0.40 mg of catalyst per cm 2 .
4. The MEA according to claim 1 wherein the anode side under layer includes carbon black and sulfonic acid based ionomers at ionomer to carbon weight ratios of 2/1 to 6/1 and an overall thickness in the range of 1-10 micrometers.
5. The MEA according to claim 1 wherein the catalyst is selected from the group consisting of platinum, platinum-metal, platinum-metal alloys and platinum-metal-transition-metal alloys.
6. The MEA according to claim 1 wherein the at least one catalyst layer positioned at the cathode side of the membrane includes a cathode side multi-layer catalyst configuration, said cathode side multilayer catalyst configuration including an cathode side under layer positioned against the membrane and including a catalyst, a cathode side middle layer positioned against the cathode side under layer and not including a catalyst and a cathode side catalyst layer positioned against the cathode side middle layer and opposite to the cathode side under layer and including a catalyst, where the amount of catalyst in the cathode side catalyst layer is greater than the amount of catalyst in the cathode side under layer.
7. The MEA according to claim 6 wherein the cathode side under layer has about 0.005 to 0.20 mg of catalyst per cm 2 and the cathode side catalyst layer has 0.01 to 0.40 mg of catalyst per cm 2 .
8. The MEA according to claim 6 wherein the cathode side middle layer is a low hydrogen permeability non-porous layer of an electron conductive material and ion conducting polymer.
9. The MEA according to claim 6 wherein the cathode side under layer includes carbon black and sulfonic acid based ionomers at ionomer to carbon weight ratios of 2/1 to 6/1 and an overall thickness in the range of 1-10 micrometers.
10. The MEA according to claim 1 wherein the MEA is part of a fuel cell that is part of a fuel cell stack that is part of a fuel cell system on a vehicle.
11. A membrane electrode assembly (MEA) comprising:
an ion-conducting membrane including an anode side and a cathode side;
a cathode side multi-layer catalyst configuration, said cathode side multilayer catalyst configuration including an cathode side under layer positioned against the membrane and including a catalyst, a cathode side middle layer positioned against the cathode side under layer and not including a catalyst and a cathode side catalyst layer positioned against the cathode side middle layer and opposite to the cathode side under layer and including a catalyst, where the amount of catalyst in the cathode side catalyst layer is greater than the amount of catalyst in the cathode side under layer; and
at least one anode side catalyst layer positioned at the cathode side of the membrane wherein the cathode side middle layer is a low hydrogen permeability non-pours layer of an electron conductive material and ion conducting polymer.
12. The MEA according to claim 11 wherein the membrane is a proton-conducting membrane, and wherein the cathode side multi-layer configuration reduces the chemical membrane degradation rate by reducing the partial pressure of oxygen at an interface of the cathode side under layer and the membrane.
13. The MEA according to claim 11 wherein the cathode side under layer has about 0.005 to 0.20 mg of catalyst per cm 2 and the cathode side catalyst layer has 0.01 to 0.40 mg of catalyst per cm 2 .
14. The MEA according to claim 11 wherein the cathode side under layer includes carbon black and sulfonic acid based ionomers at ionomer to carbon weight ratios of 2/1 to 6/1 and an overall thickness in the range of 1-10 micrometers.
15. The MEA according to claim 11 wherein the catalyst is selected from the group consisting of platinum, platinum-metal, platinum-metal alloys and platinum-metal-transition-metal alloys.
16. A membrane electrode assembly (MEA) comprising:
an ion-conducting membrane including an anode side and a cathode side;
a cathode side multi-layer catalyst configuration, said cathode side multilayer catalyst configuration including an cathode side under layer positioned against the membrane and including a catalyst, a cathode side low oxygen permeability middle layer positioned against the cathode side under layer and not including a catalyst and a cathode side catalyst layer positioned against the cathode side middle layer and opposite to the cathode side under layer and including a catalyst, where the amount of catalyst in the cathode side catalyst layer is greater than the amount of catalyst in the cathode side under layer; and
an anode side multi-layer catalyst configuration positioned at the anode side of the membrane, said anode side multilayer catalyst configuration including an anode side under layer positioned against the membrane and including a catalyst, an anode side low hydrogen permeability middle layer positioned against the anode side under layer and not including a catalyst and an anode side catalyst layer positioned against the anode side middle layer and opposite to the anode side under layer and including a catalyst, where the amount of catalyst in the anode side catalyst layer is greater than the amount of catalyst in the anode side under layer, wherein the catalyst is platinum wherein the cathode side and anode side middle layers are non-porous layers of carbon and ionomer composite.
17. The MEA according to claim 1 wherein the cathode and anode side under layers have about 0.005 to 0.20 mg of catalyst per cm 2 and the cathode and anode side catalyst layers have 0.01 to 0.40 mg of catalyst per cm 2 .