CONDUCTANCE ENHANCEMENT MICROSTRUCTURES FOR BIPOLAR PLATES
Field of the Invention
This invention relates to bipolar plates useful in electrochemical cells such as fuel cells. The bipolar plates of the present invention comprise fluid conducting channels separated by electrical contact surfaces, where the electrical contact surfaces bear microstructured features which enhance electrical conductance.
Summary of the Invention
The present invention provides a bipolar plate (BPP) for use in an electrochemical cell, the BPP comprising electrical contact surfaces and fluid conducting channels or fluid- conducting zones, wherein at least one of the electrical contact surfaces comprises a plurality of contact-enhancing microstructures.
In another aspect, the invention provides a two-layer structure comprising a bipolar plate bearing contact-enhancing microstructures and a diffuser/current collector (DCC). It is an advantage of the present invention to provide a bipolar plate for improved fuel cell performance resulting from improved electrical conductivity. It is a further advantage of the present invention to provide a BPP-DCC combination having improved electrical conductivity.
Brief Description of the Figures
Figure 1 is a graph of resistance vs. pressure across one bipolar plate-DCC interface according to the present invention and one comparative interface.
Figure 2 is a scanning electron micrograph of an electrical contact surface bearing contact-enhancing microstructures according to the present invention. The micrograph includes a 1mm scale bar.
Figure 3 is a light micrograph of an electrical contact surface bearing contact- enhancing microstructures according to the present invention. The micrograph includes a 100 μm scale bar.
Detailed Description of Preferred Embodiments
The present invention provides an improved bipolar plate (BPP) for an electrochemical cell such as a fuel cell. The bipolar plate of the present invention comprises electrical contact surfaces and fluid-conducting channels, wherein one or more of the electrical contact surfaces comprise a plurality of contact-enhancing microstructures, which are microstructures which decrease the electrical resistance between the BPP and an adjacent structure.
Electrochemical cells include fuel cells, sensors, electrolyzers, and electrochemical reactors. Fuel cells utilize a fuel such as hydrogen and an oxidizing agent such as oxygen to produce an electrical current. The two chemical reactants, i.e., the fuel and the oxidizing agent, separately react at two isolated electrodes containing catalyst. An ion exchange element is located between the electrodes to prevent direct reaction of the two reactants and to conduct ions. In the case of a typical hydrogen fuel cell, the ion exchange element is an ion conducting membrane (ICM). The ICM conducts protons (H+) from the hydrogen electrode to the oxygen electrode. Electrons follow a separate electrical path, thereby generating an electric current. The combination of an ICM and electrodes is commonly referred to as a "membrane electrode assembly," or MEA.
In conventional fuel cells, MEA's are arranged in a stack separated by rigid, electrically-conductive plates which may be known as bipolar plates (BPP). The bipolar plate has one or more fluid-conducting channels engraved, milled, or molded in the surface(s) facing the MEA(s). The fluid-conducting channels on one side of the plate direct fuel to the anode of one MEA while the channels on the other side direct oxidant to the cathode of the next MEA in the stack. The bipolar plates conduct the electrical current generated in each MEA throughout the stack. As used herein, "bipolar plate" should be understood to include the end plates of a stack, which perform the functions of the bipolar plate on one side only and
serve the top and bottom MEA's of the stack. A stack having a single MEA has only two end plates, which are both encompassed by the term "bipolar plate" as used herein.
An additional layer, the diffuser/current collector (DCC), may be situated between the bipolar plate and the active catalytic sites of the MEA. Like the bipolar plate, the DCC must conduct fluids and electricity to and from a catalyst surface of the MEA. Unlike the bipolar plate, typical DCC's are porous throughout and malleable rather than rigid. Also, the BPP conducts fluids principally in the XY plane whereas the DCC conducts fluids principally in the Z direction. The DCC preferably comprises carbon fiber paper such as ELAT™ electrode backing material (E-tek, Inc., Natick, MA), preferably at a thickness of about 0.4 mm. Another preferred material is Toray Carbon Paper (Toray Industries, Inc., Tokyo, Japan). The bipolar plate of the present invention is made of an electrically conductive material such as a metal or conductive carbon materials such as graphite. Graphite is preferred due to its resistance to corrosion. Alternately, materials may be used which are plated, sputtered or otherwise coated with conductive layers by wet methods, vacuum methods, or any suitable method.
The bipolar plate of the present invention comprises electrical contact surfaces, which are typically land areas between fluid conducting channels. The bipolar plate of the present invention comprises contact-enhancing microstructures borne on the electrical contact surfaces to enhance electrical contact between the bipolar plate and the DCC. It has been found that the use of such structures can reduce electrical resistance in a BPP-DCC combination. The microstructures may comprise any suitable shapes, including points, ridges, bumps, posts or the like. At least one electrical contact surface bears a plurality of such structures. The microstructures preferably have a height that is less than the thickness of the DCC with which they are used. The microstructures preferably have a height that is at least 1% of the thickness of the DCC. hi another preferred embodiment the microstructures have a height that is at least 5% of the thickness of the DCC. In another preferred embodiment the microstructures have a height that is between 10% and 90% of the thickness of the DCC. As used herein, height of a microstructure refers to the difference in elevation, along an axis normal to the plane of the bipolar plate, of a local maximum at the peak of a microstructure and a local minimum between two directly adjacent microstructures. Preferably the
microfeatures have a height of less than 400 μm, more preferably less than 200 μm, more preferably less than 100 μm, and most preferably less than 50 μm. Preferably the microfeatures have a height of at least 1 Oμm. Preferably the distance between microstructures or pitch of the microstructure pattern is less than 400 μm, more preferably less than 200 μm, more preferably less than 100 μm, and most preferably less than 5 Oμm. As used herein, pitch means the smallest distance between analogous structures in a repeating pattern, e.g., peak-to- peak or edge-to-edge. Preferably, the microfeatures have an aspect ratio (ratio of height to pitch, as defined above) of at least 0.1, more preferably at least 0.5, and more preferably about 2. In another preferred embodiment, the microfeatures have an aspect ratio of greater than 2. In another preferred embodiment, the microfeatures have an aspect ratio of greater than 5. In another preferred embodiment, the microfeatures have an aspect ratio of greater than 10.
The bipolar plate of the present invention comprises fluid conducting channels for transport of reactants and products. The channels may conduct gasses, liquids or both; including fuels such as hydrogen, oxidizing agents such as air or oxygen, and products such as water. The channels may be of any suitable design, such as a series of parallel channels, one or more serpentine channels, a gridwork of intersecting channels, or the like. In a preferred embodiment, these microflow channels comprise a highly parallel pattern. These patterns may contain interconnections or branch points. Such patterns include parallel lines, hatching, and grid patterns of channels. The channels can be of any cross-sectional geometry that provides desired fluid transport, but preferably a geometery which is readily replicated. The channels terminate at one or both ends in an inlet, outlet or manifold to allow introduction or removal of fluid.
The channels may be conventional channels or, more preferably, the microstructuxed channels described in copending U.S. patent application serial number 09/430,568. In contrast to the microstructured flow field features of that application, the microstructures of the present invention are situated on the electrically conductive land features of the bipolar plate. The volumes lying between directly adjacent microstructured features according to the present invention do not conduct substantial amounts of any fluid. The volumes defined by adjacent microstructured features may lack substantial communication with any inlet, outlet
or manifolds; they may be substantially occluded by DCC material under conditions of use; and they are accompanied by channels, either conventional or microstructured, which do conduct substantial amounts of fluid.
The bipolar plates of the present invention may be made by any suitable method, including the methods described in U.S. Patent No. 5,728,446, to Johnston, et. ah, and pending U.S. Patent Application S.N. 09/099,269, both of which are incorporated herein in full by reference.
The bipolar plates of the present invention preferably have fluid-conducting channels as described above, but may lack these channels in the case described following. Where the DCC adjacent to the bipolar plate has fluid-conducting channels cut, molded, or otherwise formed into it, the bipolar plate may not require fluid-conducting channels since this function is performed by the DCC. In that case, the surface area of the plate that is opposite a fluid- conducting channel of the DCC is a fluid conducting zone. Such a plate according to the present invention has contact-enhancing microstructures borne on the electrical contact surfaces and may or may not have microstructures on the plate surface constituting a fluid- conducting zone. The present invention contemplates a two-layer construction comprising a plate bearing contact-enhancing microstructures on electrical contact surfaces in contact with a DCC which comprises fluid-conducting channels.
This invention is useful in constructing electrochemical cells such as fuel cells. Objects and advantages of this invention are further illustrated by the following examples, but the particular materials and amounts thereof recited in these examples, as well as other conditions and details, should not be construed to unduly limit this invention.
Examples Three test plates were tested, each representing the land area of a bipolar plate with conductivity-enhancing microstructures according to the present invention. In examples of the invention, the microstructures were pressed against a DCC layer, which comprises carbon paper. For the comparative examples, each of the three test plates was reversed so that its flat back surface contacted the DCC layer. Thus, the comparative trials represent plates of exactly equal mass, composition and outer dimensions but lacking microstructure-DCC contact. All
plates were made of nickel metal. The test plates had dimensions of approximately 22.4 mm x 22.4 mm for an area of 5.0 cm2. Figs. 2 and 3 are micrographs of a test plate made identically to those used in the present Examples.
Test plates 1, 2 , 3 and the test plate appearing in Figs. 2 and 3 were cut from a large plate made using a nickel tool as described in U.S. Patent No. 5,728,446, Comparative
Example 1, also described as pattern 2 of Table I. (U.S. Patent No. 5,728,446 is incorporated herein by reference.) The tool, which was a negative image of the plate, was first passivated by washing with a potassium dichromate solution. Nickel metal was electrodeposited from a solution of nickel sulfonate to form a positive image, which was the large plate. Nickel was deposited to a plate thickness of about 3.0 mm. The large plate was separated from the tool by hand and individual test plates were cut from it. The pattern of the test plates comprised parallel linear grooves 532 μm deep, on a 330 μm pitch, with wall angles for each groove of 5° from vertical and a peak top width of 29 μm.
Test plates 1, 2 and 3 were tested. Examples 1A, 2 A and 3 A are examples of the present invention and Examples 1C, 2C and 3C are comparative examples, performed with the flat side of the plate facing the DCC material. For each test plate, the face to be tested was placed against a layer of 0.404 mm thick DS (double sided) ELAT™ electrode backing material (E-tek, Inc., Natick, MA), all ELAT sample being taken from the same lot. The two layer construction was then tested for electrical resistance through its thickness under varying degrees of compression, as described following. Each series of tests was performed with a new piece of ELAT.
Electrical resistance was measured as a function of compression pressure using an apparatus comprising a pneumatic press (Bellofram, State Route 2, Newell, West Virginia).
The press was equipped with two parallel platens each having an area of lOOcm^. The platen surface was polished brass and was electrically isolated from the rest of the press. The press includes a pressure meter with a digital output. The press includes a displacement meter (3 sensors, Sensotec, Columbus, OH) with a digital output serially interfaced to the computer. A regulated power supply (model HP 6269B, Hewlett-Packard, 3000 Hanover Street, Palo Alto, CA) was electrically connected to the platens so a fixed current could be applied between the
platens when a sample was in place. A voltmeter with a digital output (model Fluke 45 Dual Display Multimeter, Fluke Corporation, P.O. Box 9090, Everett, WA) was electrically connected to the platens so the voltage difference between the platens could be measured when a sample was in place. Data was collected from the pressure meter and voltmeter using a serial hardware interface and Lab View data acquisition software (National Instruments Corporation, 11500 N Mopac Expwy, Austin, TX).
For the resistance measurements, each of the plates were sandwiched between steel shims, with a DCC layer against one face, and pressed between the platens of the press. The voltage drop across each plate/DCC sample was measured as a function of applied pressure under a constant current of 2 A/cm . Current loads as high as 20 A/cm were also tested to verify the data. It was found that at maximum pressure the value of measured resistance was independent of current density.
Fig. 1 is a graph of resistance vs. pressure for Examples 3 A (Trace A) and 3C (Trace C). The data indicate that the microstructure-DCC contact arrangement demonstrated consistently lower resistance in comparison with the flat surface-DCC contact arrangement. Furthermore, upon release of pressure to less than 1.4 MPa (200 PSI) the microstructure-DCC contact sample retained its low resistance, whereas the flat surface-DCC contact sample recovered some of its resistance.
Table I presents resistance measurements for Examples 1 A, 2 A, 3 A and an average of the three and for Examples IC, 2C, 3C and an average of the three. The given measurements are for total resistance (mΩ*cm2). Each resistance is the average of at least 30 data points gathered at the peak pressure, about 17 MPa (2500 PSI). Also presented is the standard deviation of each set of the last 30 data points. Table I also reports the difference in resistance between the examples of the invention and corresponding comparative examples, with standard deviation again given.
Table I
The data in Table I again demonstrate that the microstructure-DCC contact arrangement had consistently lower electrical resistance in comparison with the flat surface- DCC contact arrangement.
Various modifications and alterations of this invention will become apparent to those skilled in the art without departing from the scope and principles of this invention, and it should be understood that this invention is not to be unduly limited to the illustrative embodiments set forth hereinabove.