HIGH POWER DENSITY FUEL CELL

Abstract

A fuel cell includes a plurality of fuel cell layers stacked along a stacking axis. Each fuel cell layer includes a stacked arrangement of elements including a cathode, an anode, an electrolyte positioned between the anode and the cathode, a support layer positioned at the anode opposite the electrolyte, and a separator plate located at the support layer opposite the anode. The support layer is configured to contact the cathode of an adjacent fuel cell layer of the plurality of fuel cell layers. The separator plate defines a plurality of anode flow channels configured to deliver a fuel therethrough and a plurality of cathode flow channels configured to deliver an air flow therethrough.

Claims

1. A fuel cell, comprising: a plurality of fuel cell layers stacked along a stacking axis, each fuel cell layer including a stacked arrangement of elements including: a cathode; an anode; an electrolyte disposed between the anode and the cathode; a support layer disposed at the anode opposite the electrolyte; a separator plate disposed at the support layer opposite the anode, the support layer configured to contact the cathode of an adjacent fuel cell layer of the plurality of fuel cell layers, the separator plate defining a plurality of anode flow channels configured to deliver a fuel therethrough and a plurality of cathode flow channels configured to deliver an air flow therethrough.

2. The fuel cell of claim 1, wherein the electrolyte is formed from a solid oxide material.

3. The fuel cell of claim 1, wherein the separator plate defines the plurality of anode flow channels at a first side of the separator plate and the plurality of cathode flow channels at a second side of the separator plate opposite the first side.

4. The fuel cell of claim 1, wherein the separator plate includes a plurality of curved portions separated by flat support portions, with the support portions interfacing with the support layer and curved portions contacting the cathode of the adjacent fuel cell layer.

5. The fuel cell of claim 1, wherein the wherein the plurality of anode flow channels at least partially overlap the plurality of cathode flow channels along the stacking axis.

6. The fuel cell of claim 1, wherein the support layer includes a porous portion disposed at the anode flow channels configured to allow fuel flow from the anode fuel channels to the anode through the porous portion.

7. The fuel cell of claim 6, the support layer further comprising a non-porous portion surrounding the porous portion.

8. The fuel cell of claim 7, further comprising one or more manifolds disposed in the solid portion to distribute fuel to the plurality of anode flow channels.

9. The fuel cell of claim 1, wherein the support layer is formed from a metal material.

10. The fuel cell of claim 1, further comprising a metal catalyst foam disposed between the support layer and the separator plate.

11. A fuel cell layer of a multi-layer fuel cell, comprising: a cathode; an anode; an electrolyte disposed between the anode and the cathode; a support layer disposed at the anode opposite the electrolyte; a separator plate disposed at the support layer opposite the anode, the support layer configured to contact the cathode of an adjacent fuel cell layer, the separator plate defining a plurality of anode flow channels configured to deliver a fuel therethrough and a plurality of cathode flow channels configured to deliver an air flow therethrough.

12. The fuel cell layer of claim 11, wherein the electrolyte is formed from a solid oxide material.

13. The fuel cell layer of claim 11, wherein the separator plate defines the plurality of anode flow channels at a first side of the separator plate and the plurality of cathode flow channels at a second side of the separator plate opposite the first side.

14. The fuel cell layer of claim 11, wherein the separator plate includes a plurality of curved portions separated by flat support portions, with the support portions interfacing with the support layer and curved portions contacting the cathode of the adjacent fuel cell layer.

15. The fuel cell layer of claim 11, wherein the plurality of anode flow channels at least partially overlap the plurality of cathode flow channels along the stacking axis.

16. The fuel cell layer of claim 11, wherein the support layer includes a porous portion disposed at the anode flow channels configured to allow fuel flow from the anode fuel channels to the anode through the porous portion.

17. The fuel cell layer of claim 16, the support layer further comprising a non-porous portion surrounding the porous portion.

18. The fuel cell layer of claim 17, further comprising one or more manifolds disposed in the solid portion to distribute fuel to the plurality of anode flow channels.

19. The fuel cell layer of claim 11, wherein the support layer is formed from a metal material.

20. The fuel cell layer of claim 11, further comprising a metal catalyst foam disposed between the support layer and the separator plate.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0025] The following descriptions should not be considered limiting in any way. With reference to the accompanying drawings, like elements are numbered alike:

[0026] FIG. 1 is a schematic illustration of an embodiment of a solid oxide fuel cell;

[0027] FIG. 2 is a schematic illustration of an embodiment of a fuel cell having a multilayer structure;

[0028] FIG. 3 is a schematic illustration of an embodiment of a fuel cell layer;

[0029] FIG. 4 is another schematic illustration of an embodiment of a fuel cell layer; and

[0030] FIG. 5 is a partially exploded view of an embodiment of a fuel cell layer.

DETAILED DESCRIPTION

[0031] A detailed description of one or more embodiments of the disclosed apparatus and method are presented herein by way of exemplification and not limitation with reference to the Figures.

[0032] Referring to FIG. 1, shown is a schematic illustration of an embodiment of a fuel cell (10). In some embodiments, the fuel cell 10 is a solid oxide fuel cell, a proton conducting fuel cell, an electrolyzer, or other fuel cell apparatus. The fuel cell 10 includes an anode 12 and a cathode 14 with an electrolyte 16 disposed between the anode 12 and the cathode 14. In the case of the solid oxide fuel cell 10, the electrolyte 16 is a solid oxide material such as, for example, a ceramic material. A flow of fuel is introduced to the fuel cell 10 along with a flow of air. Chemical reactions of the fuel and air with the electrolyte 16 produces electricity. In some embodiments, an operating temperature of the fuel cell 10 is in the range of 400-900 degrees Celsius, while in other embodiments the operating temperature is in the range of 400-750 degrees Celsius. The flow of fuel may comprise, for example, natural gas, coal gas, biogas, hydrogen, or other fuels such as jet fuel.

[0033] Referring now to FIG. 2, the fuel cell 10 includes a plurality of fuel cell layers 18 stacked along a stacking axis 60. In some embodiments, each fuel cell layer 18 has a rectangular shape. It is to be appreciated, however, that the fuel cell layers 18 may have other polygonal shapes or may be, for example, circular, elliptical or oval in shape. As shown in FIG. 3, each fuel cell layer 18 includes a separator plate 20 and a support 22 located over the separator plate 20 with the support 22 secured to the separator plate 20. Joining the support 22 to the separator plate 20 increases their individual strength and rigidity, and allows for using thinner, lighter materials in forming the support 22 and the separator plate 20 than would be otherwise feasible. An anode 24, electrolyte 26 and a cathode 28 are stacked atop the support 22 in that order. In some embodiments, the electrolyte 26 is formed from a solid oxide material, such as a ceramic material. The fuel cell layers 18 are stacked such that the cathode 28 contacts the separator plate 20 of the neighboring fuel cell layer 18.

[0034] The separator plate 20 is compliant and lightweight and is shaped to define a plurality of anode flow channels 30 and a plurality of cathode flow channels 32 and separate the anode flow channels 30 from the cathode flow channels 32. The plurality of anode flow channels 30 are defined at a first side of the separator plate 20 and the plurality of cathode flow channels 32 are defined at a second side of the separator plate 20 opposite the first side. As illustrated the anode flow channels 30 and the cathode flow channels 32 at least partially overlap along the stacking axis 60. This improves a density of the fuel cell 10 along the stacking axis 60.

[0035] Compliance of the separator plate 20 ensures good contact with the cathode 28 for high performance, and the separator plate 20 is configured for light weight to enable high power density of the fuel cell 10. The fuel flows through the anode flow channels 30 and the air flows through the cathode flow channels 32. In some embodiments, such as in FIG. 3, the separator plate 20 includes a plurality of curved portions 34 separated by flat support portions 36, with the support portions 36 interfacing with the support 22 and curved portions 34 contacting the cathode 28 of the neighboring fuel cell layer 18. The waveform shape of the separator plate 20 with the plurality of curved portions 34 allows for greater levels of fuel flow coverage to the anode 24 and a greater level of airflow coverage to the cathode 28. In other embodiments, the curved portions 34 may have other shapes, such as rectilinear as shown in FIG. 4. The shapes illustrated in FIGS. 3 and 4 are merely exemplary, with the shapes of anode flow channels 30 and cathode flow channels 32 selected to provide the desired compliance in the stacking axis 60 direction, while allowing for selected anode and cathode flows which may be at significantly different flow rates. The separator plate 20 may be formed from corrugated sheet stock with features on the order of millimeters to centimeters. Alternatively, the separator plate 20 may be formed from sheet material by, for example, stamping, extrusion, folding, bending, roll forming, hydroforming, or the like. Other methods may include injection molding, additive manufacturing including laser powder bed fusion, electron beam melting, directed energy deposition, or laminated object manufacture. In still other embodiments, the separator plate may be formed at least partially by a process such as ultraviolet lithography and etching which may be used to form features with a resolution below 10 microns, or by micro-EDM (electrical discharge machining) or laser micromachining, both of which that may be utilized to produce features with a resolution in the range of 50 to 100 microns. In some embodiments, the separator plate 20 is formed from a stainless steel or titanium material.

[0036] Referring again to FIG. 3 and also to the partially exploded view of FIG. 5, fuel is distributed to the anode fuel channels 30 via a primary manifold 38 and a secondary manifold 40. The primary manifold 38 extends between the fuel cell layers 18 to distribute fuel to each fuel cell layer 18 of the plurality of fuel cell layers 18. Each fuel cell layer 18 includes a secondary manifold 40 located at, for example, a first end 42 of the anode flow channels 30. The secondary manifold 40 is connected to the primary manifold 38 and the plurality of anode flow channels 30 to distribute fuel from the primary manifold 38 to each of the anode flow channels 30 of the fuel cell layer 18. The anode flow channels 30 extend from the secondary manifold 40 at the first end 42 of the anode flow channels 30 to a collection manifold 44 at a second end 46 of the anode flow channels 30. Fuel flows from the primary manifold 38 through the secondary manifold 40, and through the anode flow channels 30 with anode byproducts such as water vapor and carbon dioxide exiting the anode flow channels 30 and flowing into the collection manifold 44.

[0037] The support layer 22 is formed from a metal material in some embodiments, and includes a porous section 48 and a non-porous or solid section 50, with the solid section 50 surrounding the porous section 48 and defining an outer perimeter of the support layer 22. The porous section 48 may be formed by, for example, laser drilling of a metal sheet. or sintering of metal powder, or additive manufacturing. The porous section 48 is located over the anode flow channels 30 to allow the fuel flow to reach the anode 24 through the porous section 48. In some embodiments, a metal catalyst foam layer 52 is located between the separator plate 20 and the support layer 22.

[0038] The fuel cell 10 configurations disclosed herein enable a high performance electrical power system for, for example, an aircraft, especially for long duration operation. The configurations further reduce startup times and provide power densities in the range of 1-3 kilowatts/kilogram with a cell performance of 0.8 W/cm.sup.2. Further, the improved power density may be achieved utilizing a lightweight separator plate 20, with a separator plate 20 formed from, for example, stainless steel having a thickness of 2 mil to 10 mil. Further, other materials such as titanium alloys, or other materials at lower operating temperatures may be used to form a lightweight separator plate 20.

[0039] The term “about” is intended to include the degree of error associated with measurement of the particular quantity based upon the equipment available at the time of filing the application.

[0040] The terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the present disclosure. As used herein, the singular forms “a”, “an” and “the” are intended to include the plural forms as well, unless the context clearly indicates otherwise. It will be further understood that the terms “comprises” and/or “comprising,” when used in this specification, specify the presence of stated features, integers, steps, operations, elements, and/or components, but do not preclude the presence or addition of one or more other features, integers, steps, operations, element components, and/or groups thereof

[0041] While the present disclosure has been described with reference to an exemplary embodiment or embodiments, it will be understood by those skilled in the art that various changes may be made and equivalents may be substituted for elements thereof without departing from the scope of the present disclosure. In addition, many modifications may be made to adapt a particular situation or material to the teachings of the present disclosure without departing from the essential scope thereof. Therefore, it is intended that the present disclosure not be limited to the particular embodiment disclosed as the best mode contemplated for carrying out this present disclosure, but that the present disclosure will include all embodiments falling within the scope of the claims.