The field to which the disclosure generally relates includes electrodes for use in fuel cells.
Hydrogen is a very attractive fuel because it is clean and can be used to efficiently produce electricity in a fuel cell. The automotive industry expends significant resources in the development of hydrogen fuel cells as a source of power for vehicles. Such vehicles would be more efficient and generate fewer emissions than today's vehicles employing internal combustion engines.
A hydrogen fuel cell is an electro-chemical device that includes an anode and a cathode with an electrolyte between the anode and the cathode. The anode receives hydrogen-rich gas or pure hydrogen and the cathode receives oxygen or air. The hydrogen gas is dissociated in the anode to generate free protons and electrons. The protons pass through the electrolyte to the cathode, where the protons react with the oxygen and the electrons in the cathode to generate water. The electrons from the anode are unable to pass through the electrolyte. Therefore, the electrons are directed through a load to perform work before they are sent to the cathode. The work may be used, for example, to operate a vehicle.
Several fuel cells are typically combined in a fuel cell stack to generate the desired power. The fuel cell stack includes a series of bipolar plates. For the automotive fuel cell stack mentioned above, the stack may include about two hundred or more bipolar plates. The fuel cell stack receives a cathode reactant gas, typically a flow of air forced through the stack by a compressor. Not all of the oxygen is consumed by the stack and some of the air is output as a cathode exhaust gas that may include liquid water as a stack by-product. The fuel cell stack also receives an anode hydrogen reactant gas that flows into the anode side of the stack.
One embodiment of the invention includes a method including applying a first ink comprising carbon over a substrate and drying the first ink to form a first electrode layer, applying a second ink including a second catalyst over the first electrode layer and drying the second ink to form a second electrode layer, and applying a third ink comprising an ionomer solution over the second electrode layer and drying the third ink to form an ionomer overcoat.
Other exemplary embodiments of the invention will become apparent from the detailed description of exemplary embodiments provided hereinafter. It should be understood that the detailed description and specific examples, while indicating the exemplary embodiments of the invention, are intended for purposes of illustration only and are not intended to limit the scope of the invention.
Exemplary embodiments of the invention will become more fully understood from the detailed description and the accompanying drawings.
The following description of the embodiments is merely exemplary in nature and is in no way intended to limit the invention, its application, or uses.
In one embodiment of the invention, a method is provided by which an electrode and a membrane electrode assembly may be produced where the ionomer loading and the platinum catalyst loading may vary across the thickness.
In one embodiment of the invention shown in
The first ink may include no catalyst, or it may include a carbon support and a relatively low weight percent catalyst powder, for example 0.1 to 40 weight percent catalyst powder. In one embodiment, the catalyst in the first ink may be platinum. For example, the first ink may include 20 weight percent platinum catalyst powder. In another embodiment, the substrate 18 may be an electrode and may consist essentially of carbon (e.g., pure carbon) or may consist essentially of carbon and a binder and being substantially free of a catalyst.
As shown in
In one embodiment, the first electrode layer 12 and the second electrode layer 14 may include a group of finely divided particles supporting finely divided catalyst particles. The catalyst particles may include metals such as platinum, palladium, and mixtures of metals such as platinum and molybdenum, platinum and cobalt, platinum and ruthenium, platinum and nickel, platinum and tin, other platinum transitional metal alloys, intermetallic compounds, and other fuel cell electrocatalysts known in the art. The catalyst may be supported or unsupported. The support particles are electrically conductive and may include carbon. The support particles may include, but are not limited to, electrically conductive macromolecules of activated carbon, carbon nanotubes, carbon fibers, mesopore carbon, and other electrically conductive particles with suitable surface area to support the catalyst. In one embodiment the first electrode 12 may not include a catalyst.
Referring now to
According to one embodiment of the invention as shown in
According to another embodiment, a microporous layer 24 may be applied to a gas diffusion media layer 22. The first electrode layer 12 may be applied over the microporous layer 24 and the gas diffusion media layer 22 such that the microporous layer 24 faces the first electrode layer 12, as shown in
Consistent with an above-described embodiment, a first ink including 20 weight percent platinum catalyst powder was applied over a decal backing including ePTFE decal material. When a third ink including 5 weight percent ionomer solution (available from Asahi Kasei Corporation) was dropped onto the dried first ink, the ePTFE was not wetted, implying that the ionomer solution did not penetrate through the entire thickness of the electrode layer. However, when the same test was performed with an electrode prepared using 50 weight percent platinum catalyst powder, the ePTFE was very quickly wetted.
Referring now to
Similarly, on a cathode side 15c, an ionomer overcoat 16c is interposed between the polyelectrolyte membrane 20 and a second electrode layer 14c having a catalyst. A first electrode layer 12c including carbon and which may or may not include a catalyst underlies the second electrode layer 14c. The first electrode layer 12c may consist essentially of carbon (e.g., pure carbon) or may consist essentially of carbon and a binder and be substantially free of a catalyst. An optional microporous layer 24c underlies the first electrode layer 12c. A gas diffusion media layer 22c underlies the microporous layer 24c or the first electrode layer 12c. A second bipolar plate 26c underlies the cathode gas diffusion media layer 22c. The second bipolar plate 26c includes a first face 28c including a plurality of lands 30c and channels 32c defined therein to provide a reactant gas flow field. The second bipolar plate 26c may include a second face 34c including cooling channels 36c formed therein. In one embodiment, on at least one of the anode side 15a or the cathode side 15c, the catalyst loading and ionomer loading varies over the total thickness of the first electrode layer and the second electrode layer together.
The above description of embodiments of the invention is merely exemplary in nature and, thus, variations thereof are not to be regarded as a departure from the spirit and scope of the invention.
Number | Name | Date | Kind |
---|---|---|---|
4871703 | Beaver et al. | Oct 1989 | A |
6500217 | Starz et al. | Dec 2002 | B1 |
6696382 | Zelenay et al. | Feb 2004 | B1 |
7410930 | Wakita et al. | Aug 2008 | B2 |
20060029757 | Komada | Feb 2006 | A1 |
Number | Date | Country |
---|---|---|
1425207 | Jun 2003 | CN |
1553534 | Dec 2004 | CN |
1806356 | Jul 2006 | CN |
Entry |
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Chinese Office Action dated Jun. 30, 2015; Application No. 201010243334.3; Applicant:GM Global Technology Operations, Inc..; 7 pages. |
Number | Date | Country | |
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20110027696 A1 | Feb 2011 | US |