BACKGROUND OF THE INVENTION Field of the Invention [0001] This invention relates in general to fuel cell structures and assemblies, and method of making the same.

Description of the Art [0002] U.S. Patent Nos. 5,916,514; 5,928,808; 5,989,300; 6,004,691; 6,338,913; 6,399,232; 6,403,248; 6,403,517; 6,444,339; and 6,495,281 describe microfibrous electrochemical cell structures that each contain an inner current collector, an inner electrocatalyst layer, a hollow fibrous membrane separator with electrolyte medium therein, an outer electrocatalyst layer, and an outer current collector. Specifically, both the inner and outer current collects are made of metal fibers and are disposed respectively on the inner and the outer surface of the hollow fibrous membrane separator.

[0003] Since such metal-fiber-formed current collectors are directly exposed to the harsh electrochemical environment near the membrane separator surfaces, they are especially susceptible to corrosion. Corrosion of the current collectors can result in ionic contamination of the polymer membrane electrolyte and reduction in ionic conductivity of the cell for transport of protons. In severe cases, electrical disconnection may occur within individual cells or between adjacent cells that are serially or parallelly connected together, which shortens the useful life of such microfibrous electrochemical cells and reduces the power density of electrochemical assemblies comprising same. [0004] It is accordingly an object of the present invention to provide corrosion-resistant current collectors for prolonging the useful life and enhancing the reliability of such microfibrous electrochemical cells or assemblies comprising same.

[0005] Further, for fuel cell applications, the hollow fibrous membrane separator must further provide an inner fluid passage at its bore side, for passing a fuel- or oxidant-containing fluid therethrough. Such inner fluid passage can be easily blocked upon deformation of the hollow fibrous membrane separator, which will in turn reduce the power output of the electrochemical cells. The need for providing and maintaining such inner fluid passage increases the manufacturing costs of the microfibrous fuel cells.

[0006] It is therefore another object of the present invention to provide microfibrous fuel cells with inner fluid passage(s) that is easy to produce and blockage-resistant.

[0007] Furthermore, for fuel cell applications, the electrical contact generated between the surface of the catalyst and the current collector plays a significant role in the performance of the fuel cell. In general the higher the contact surface area, the lower the contact resistance in the cell, which translates into higher and more efficient power generation.

[0008] It is therefore another object of this invention to provide a microfibrous fuel cell with excellent contact between the catalyst layer and the current collector at the bore side of the cell.

[0009] Other objects of the present invention will be more fully apparent from the ensuing disclosure and appended claims.

SUMMARY OF THE INVENTION [0010] The present invention in one aspect relates to a fibrous article having a longitudinal axis. Such fibrous article comprises two or more metal layers bonded together by solid-phase bonding, and one or more surface channels extending along directions that are substantially parallel to its longitudinal axis.

[0011] Another aspect of the present invention relates to a method for producing a metal clad fiber with surface channels as described hereinabove, by the steps of: forming a precursor structure that has a longitudinal axis and comprises a metal core and one or more metal protective layers formed over the metal core, with at least one removable metal component partially embedded in at least one of such metal protective layers and partially exposed on a surface of the precursor structure, wherein such one or more metal protective layers are bonded to the metal core as well as to one another by solid-phase bonding, and wherein the removable metal component extends along the longitudinal axis of such precursor structure; and drawing the precursor structure into a fibrous structure; and selectively removing the removable metal component from the fibrous structure, in such manner that the metal core and the one or more protective metal layers form a metal clad fiber that has one or more surface channels extending along directions that are substantially parallel to the longitudinal axis of such metal clad fiber.

[0012] Still another aspect of the present invention relates to a microfibrous fuel cell comprising: a hollow microfibrous membrane separator containing an electrolyte medium and defining a bore side and a shell side; an inner current collector and an inner electrocatalyst structure at the bore side of such hollow microfibrous membrane separator; and an outer current collector and an outer electrocatalyst structure at the shell side of such hollow microfibrous membrane separator, wherein the inner current collector comprises a metal clad fiber having a longitudinal axis, and wherein such metal clad fiber comprises two or more metal layers bonded together by solid-phase bonding and one or more surface channels extending along directions that are substantially parallel to its longitudinal axis.

[0013] Yet another aspect of the present invention relates to a microfibrous fuel cell comprising: a hollow microfibrous membrane separator containing an electrolyte medium and defining a bore side and a shell side; an inner current collector and an inner electrocatalyst structure at the bore side of such hollow microfibrous membrane separator; and an outer current collector and an outer electrocatalyst structure at the shell side of such hollow microfibrous membrane separator, wherein the inner current collector comprises a metal fiber having a longitudinal axis and one or more surface channels extending along directions that are substantially parallel to its longitudinal axis.

[0014] A further aspect of the present invention relates to a method for producing a metal fiber with surface channels as described hereinabove, by the steps of: forming a precursor structure that has a longitudinal axis and comprises at least one supporting metal component and at least one removable metal component that is partially embedded in such supporting metal component and partially exposed to a surface of the precursor structure, wherein such removable metal component extends along the longitudinal axis of the precursor structure; and drawing the precursor structure into a fibrous structure; and selectively removing the removable metal component from the fibrous structure, in such manner that the supporting metal component forms a metal fiber having one or more surface channels extending along directions that are substantially parallel to the longitudinal axis of the metal fiber.

[0015] The terms "microfibrous," "fibrous," and "fiber" are used interchangeably herein to refer to fibrous structures having a cross-sectional outer diameter in a range of from about 10 microns to about 10 millimeters, preferably from about 10 microns to about 5 millimeters, and more preferably from about 100 microns to about 1 millimeter.

[0016] Other aspects, features and advantages of the invention will be more fully apparent from the ensuing disclosure and appended claims.

BRIEF DESCRIPTION OF THE DRAWINGS

[0017] Figure IA is a cross-sectional view of a double-layer metal clad fiber having one surface channel, according to one embodiment of the present invention.

[0018] Figure IB is a perspective view of the metal clad fiber of Figure IA.

[0019] Figure 2A is a cross-sectional view of a double-layer metal clad fiber having four surface channels, according to one embodiment of the present invention.

[0020] Figure 2B is a perspective view of the metal clad fiber of Figure 2A.

[0021] Figure 3 is a cross-sectional view of a double-layer metal clad fiber having six surface channels, according to one embodiment of the present invention. [0022] Figure 4 is a cross-sectional view of a double-layer metal clad fiber having multiple surface channels, according to one embodiment of the present invention.

[0023] Figure 5 is a cross-sectional view of a three-layer metal clad fiber having four surface channels, according to one embodiment of the present invention.

[0024] Figure 6 illustrates a process for forming the channeled metal clad fibers, according to one embodiment of the present invention.

[0025] Figure 7 is a cross-sectional view of a microfibrous fuel cell comprising an inner current collector formed of a channeled metal clad fiber, according to another embodiment of the present invention.

[0026] Figure 8 is a cross-sectional view of a microfibrous fuel cell comprising an inner current collector formed of a channeled metal fiber, according to another embodiment of the present invention.

DETAILED DESCRIPTION OF THE INVENTION, AND PREFERRED EMBODIMENTS THEREOF

[0027] Disclosures of the following U.S. patents and applications are incorporated herein by reference, in their respective entireties and for all purposes:

U.S. Patent No. 5,916,514 issued on June 29, 1999 for "PROCESS OF FABRICATING FIBROUS ELECTROCHEMICAL CELLS;" 1TϊS. Patent No. 5,928,808 issued on July 27, 1999 for "FIBROUS ELECTROCHEMICAL FEED CELLS;" U.S. Patent No. 5,989,300 issued on November 23, 1999 for "PROCESS OF PRODUCING ELECTROCHEMICAL PRODUCTS OR ENERGY FROM A FIBEROUS ELECTROCHEMICAL CELL;" U.S. Patent No. 6,004,691 issued on December 21, 1999 for "FIBROUS BATTERY CELLS;" U.S. Patent No. 6,338,913 issued on July 15, 2002 for "DOUBLE-MEMBRANE MICROCELL ELECTROCHEMICAL DEVICES AND ASSEMBLIES, AND METHOD OF MAKING AND USING THE SAME;" U.S. Patent No. 6,399,232 issued on June 4, 2002 for "SERIES-CONNECTED MICROCELL ELECTROCHEMICAL DEVICES AND ASSEMBLIES, AND METHOD OF MAKING AND USING THE SAME;" U.S. Patent No. 6,403,248 issued on June 11, 2002 for "MICROCELL ELECTROCHEMICAL DEVICES ASSEMBLIES WITH WATER MANAGEMENT SUBSYSTEM, AND METHOD OF MAKING AND USING THE SAME;" U.S. Patent No. 6,403,517 issued on June 11, 2002 for "SYSTEM AND PROCESS FOR MANUFACTURING MICROCELL ELECTROCHEMICAL DEVICES AND ASSEMBLIES;" U.S. Patent No. 6,444,339 issued on September 3, 2002 for "MICROCELL ELECTROCHEMICAL DEVICE ASSEMBLIES WITH THERMAL MANAGEMENT SUBSYSTEM, AND METHOD OF MAKING AND USING THE SAME;" U.S. Patent No. 6,495,281 issued on December 17, 2002 for "MICROCELL ELECTROCHEMICAL DEVICES ASSEMBLIES WITH CORROSION MANAGEMENT SUBSYSTEM, AND METHOD OF MAKING AND USING THE SAME;" U-S. Patent Application Nos. 10/188,471 filed on July 2, 2002 for "MICROCELL ELECTROCHEMICAL DEVICES AND ASSEMBLIES WITH CORROSION- RESISTANT CURRENT COLLECTORS, AND METHOD FO MAKING THE SAME;" U.S. Patent Application No. 10/253,371 filed on September 24, 2002 for "MICROCELL FUEL CELLS, FUEL CELL ASSEMBLIES, AND METHODS OF MAKING THE SAME;" U.S. Patent Application No. 10/744,203 filed on December 23, 2003 for "SUBSTRATE-SUPPORTED PROCESS FOR MANUFACTURING MICROFIBROUS FUEL CELLS;" U.S. Patent Application No. 10/811,347 filed on March 26, 32004 for "PROCESS FOR MANUFACTURING HOLLOW FIBERS;" U.S. Patent Application No. 10/767,107 filed on January 28, 2004 for "HYDROGEN STORAGE SYSTEMS AND FUEL CELL SYSTEMS WITH HDYROGEN STORAGE CAPACITY;" and U.S. Patent Application No. 10/794,687 filed on March 5, 2004 for "FUEL CELL STRUCTURES AND ASSEMBLIES."

[0028] The present invention provides a metal clad fiber having one or more surface channels that extend along directions that are substantially parallel to the longitudinal axis of such metal fiber, for forming the inner current collector of a microfibrous fuel cell.

[0029] Specifically, such metal clad fiber comprises two or more metal layers, including at least a metal core and one or more metal protective layers formed over such metal core. Such metal protective layers contain metal or metal alloy that is different from that contained in the metal core, and they are bonded to the metal core as well as to one another at the respective interfaces by solid-phase bonding, which is described in greater detail hereinafter. [0030] The surface channels of such metal clad fiber are formed of longitudinally-extending surface cavities that are partially embedded in at least one of the metal protective layers. Such surface channels are separated from the metal core of the metal clad fiber, while being partially exposed to a surface of such fiber, so that a fluid being passed through such surface channels is isolated from the metal core, but not from the fiber surface.

[0031] Figure IA shows a cross-section view of an exemplary metal clad fiber 10, according to one embodiment of the present invention.

[0032] The clad fiber 10 specifically comprises a metal core 12 and a metal protective layer 14 encapsulating such metal core. A single surface channel 1 1 is partially embedded in the metal protective layer 14 and partially exposed to a surface of the clad fiber 10. Further, the metal core 12 is isolated from such surface channel 11. With such configuration, a fluid passing through such surface channel 1 1 contacts the surface of the clad fiber 10 without contacting the metal core.

[0033] Figure IB shows a perspective view of the metal clad fiber 10, with the surface channel 11 extending along a direction that is parallel to the longitudinal axis 13 of the metal clad fiber 10. A fluid can therefore be passed from one terminal end of the fiber 10 to the other through such longitudinally-extending surface channel 11.

[0034] The metal core of the metal clad fiber is preferably formed of metal or metal alloy characterized by low electrical resistance (e.g., resistance less than 10 μωxm, preferably less than 5 μωxm), high mechanical strength, good formability, and low manufacturing cost. Suitable metals or metal alloys for forming the metal core include, but are not limited to: copper, aluminum, brass, bronze, nickel, silver, and alloys thereof. 10UJ5J l he one or more metal protective layers are preferably formed of metal or metal alloy characterized by high corrosion-resistance, high mechanical strength, and good formability. Suitable metals or metal alloys for forming the metal protective layers include, but are not limited to: titanium, niobium, nickel, zirconium, gold, tantalum, platinum, palladium, silver, and alloys thereof.

[0036] The above lists of metals and metal alloys are only exemplary and are not intended to limit the broad scope of the present invention.

[0037] The metal core 12 and the metal outer layer 14 are preferably bonded together at their interfacial surface by solid-phase bonding, which is the bonding of two different metals or metal alloys without the formation of any liquid phase material at their interfaces.

[0038] The solid-phase bonding of two different metals is achieved by a hot co-extrusion process that is well known in the art, in which two metals are pressed together at an elevated temperature, to cause deformation of such metals in form of reduction in cross-sectional area of the metals. The elevated temperature is within a range of from just above the minimum re-crystallization temperature of the metal that has the lower re-crystallization temperature to the highest temperature at which both metals may be deformed without any pulling apart or any formation of brittle compounds or liquid phase material at the interface of the metals being bonded. By applying pressure at such elevated temperature, it is possible to solid-phase bond layers of any two or more metals or metal alloys to form a multiple-layer metal clad composite.

[0039] The strength of the solid-phase bonding is a function of the elevated temperature and the amount of deformation that such metals undergo. Preferably, the elevated temperature is within a range of from about 4000C to about 9000C, and the amount of deformation that such metals undergo is expressed as a reduction in cross-sectional area ratios of such metals, e.g., in a range of from about 7: 1 (i.e., the cross-sectional area reduces from 7 to 1 due to such deformation) to about 64: 1 (i.e., the cross-sectional area reduces from 64 to 1 due to such deformation).

[0040] The solid-phase bonding formed according to the above-described method can be further strengthened by a subsequent sintering step. The thermal energy provided by such sintering step increases atomic mobility of the metals and effects growth of the bond areas at the bonding interface between the metals. As a result, the solid-phase bonding between such metals is further strengthened.

[0041] The metal clad fiber of the present invention may comprise any number of surface channels without limitation. For example, Figures 2A and 2B shows an exemplary metal clad fiber 20 having four longitudinally-extending surface channels 21. Figure 3 shows another metal clad fiber 30 having six longitudinally-extending surface channels 31, and Figure 4 shows still another metal clad fiber 40 having more than twenty surface channels 41.

[0042] Such surface channels can have any cross-sectional shape or configuration, either regular or irregular, including but not limited to circular, semi-circular, oval, crescent, cross, triangle, square, rectangular, parallelogram, trapezoidal, polyhedron, star-like, etc. Figures 1-4 only provide illustrative examples and should be construed to limit the broad scope of the present invention.

[0043] The metal clad fiber of the present invention may comprise more than two metal layers, as shown in Figure 5. Specifically, the metal clad fiber 50 comprises a metal core 52 formed of a first metal or metal alloy, a first metal protective layer 54 formed of a second metal or metal alloy and encapsulating the metal core 52, and a second metal protective layer 56 formed of a third metal or metal alloy and encapsulating the first metal protective layer 54, wherein the metal core 52 and the first and second metal protective layers 54 and 56 are bonded to one another at their respective interfaces by solid-phase bonding.

[0044] Four longitudinally-extending surface channels 52 are partially embedded in the metal protective layers 56 and 54, with openings to the surface of the clad fiber 50.

[0045] The metal core 52 is preferably formed of metal or metal alloy having low electrical resistance (i.e., resistance less than 10 μωxm, preferably less than 5 μωxm), high mechanical strength, good formability, and low manufacturing cost, such as copper, aluminum, brass, bronze, nickel, silver, etc., and alloys thereof. More preferably, the metal core 52 is formed of a metal selected from the group consisting of copper and aluminum, and alloys thereof, and most preferably, the metal core 52 is formed of copper or copper-containing metal alloy.

[0046] The first metal protective layer 54 and the second metal protective layer 56 are preferably formed of metal or metal alloy having high corrosion-resistance, high mechanical strength, and good formability, such as titanium, niobium, nickel, zirconium, gold, tantalum, platinum, palladium, silver, etc., and alloys thereof. More preferably, the metal or metal alloy for forming the first metal protective layer 54 is selected from the group consisting of titanium, niobium, nickel, and alloys including the same, and the metal or metal alloy for forming the second metal protective layer 56 is selected from the group consisting of niobium, platinum, tantalum, gold, zirconium, and alloys including the same. Most preferably, the first metal protective layer 54 is formed of titanium or titanium-containing alloy, and the second metal protective layer 56 is formed of niobium, tantalum, or niobium- and/or tantalum-containing alloy.

[0047] As mentioned hereinabove, the specific metals and metal alloys identified herein are only exemplary and are not intended to limit the broad scope of the present invention. [0048] The following is a list of preferred compositions of two- or three-layer metal clad fibers useful for practice of the present invention:

[0049] The above-described channeled metal clad fibers can be formed by a process illustrated in Figure 6: (1) forming a composite metal billet 6OA (i.e., a precursor structure) having a longitudinal axis and comprising a metal core 62 and one or more metal protective layers 64 encapsulating such metal core, with one or more removable metal components 63 partially embedded in at least one of such metal protective layers 64 and partially exposed on a surface of such metal billet 6OA. Such removable metal components 63 extend along the longitudinal axis of such metal billet 6OA. Such composite metal billet 6OA are preferably formed by the well-known hot co-extrusion techniques as described hereinabove, so that the one or more metal protective layers 64 are bonded to the metal core 62 as well as to one another by solid-phase bonding; (2) drawing the metal billet 6OA into a thin metal wire or a metal fiber 6OB, via a series of cold drawing and annealing steps, wherein the metal fiber 6OB so formed comprises the metal core 62, the one or more metal protective layers 64, and the one or more removable metal components 63 (see the enlarged cross-sectional view of the metal fiber 60B); and (3) selectively removing the removable metal components from the metal fiber 6OB, via acid-leaching or other material-removal techniques, in such manner that the metal core 62 and the one or more metal protective layers 64 remain intact and form a metal fiber 6OC having one more longitudinally-extending surface channels 61 (see the enlarged cross-sectional view of the channeled metal fiber 60C).

[0050] The removable metal components 63 may comprise any metal or metal alloy that can be selectively removed without impairing the structural integrity of the metal core and the metal protective layers. Such removable metal components preferably comprise metal or metal alloy with sufficient formability, good removability, and low manufacturing cost, such as copper, aluminum, brass, bronze, nickel, silver, etc., and alloys thereof. More preferably, the removable metal components 63 are formed of a metal selected from the group consisting of copper and aluminum, and alloys thereof, and most preferably, the removable metal components 63 are formed of copper or copper-containing metal alloy.

[0051] Because the metal core 62 are encapsulated by the metal protective layers 64 and is not exposed to the surface of the metal fiber 6OB (see Figure 6), such metal core 62 may comprise the same metal or metal alloy as that of the removable metal components 63, and such metal core 62 will remain intact during the removal step when the removable metal components 63 (which are partially exposed on the surface of the metal fiber 60B) is selectively removed. [0052) The selective removal of the removable metal components 63 may be carried out by any suitable techniques, which include but are not limited to acid-leaching techniques.

[0053] The above-described channeled metal clad fibers can be advantageously used for forming inner current collectors in microfibrous fuel cell structures described in U.S. Patents No. 5,916,514; 5,928,808; 5,989,300; 6,004,691 ; 6,338,913; 6,399,232; 6,403,248; 6,403,517; 6,444,339; and 6,495,281 and U.S. Patent Applications No. 10/188,471; 10/253,371; 10/744,203; 10/81 1,347; 10/767,107; and 10/794,687. The surface channels of such metal clad fibers can function as the inner fluid passages that are required for such microfibrous fuel cells.

[0054] Figure 7 shows a cross-sectional view of an exemplary microfibrous fuel cell 70, which comprises a hollow microfibrous membrane separator 75 that contains an electrolyte medium therein and defines a bore side and a shell side. At the bore side of such membrane separator 75 are placed an inner current collector 72 and an inner electrocatalyst layer 74, and at the shell side of such membrane separator 75 are placed an outer current collector 78 and an outer electrocatalyst layer 76. A wrapping element 79 winds around such microfibrous fuel cell 70 and wraps it into a compact and unitary cell.

[0055] The inner current collector 72 is formed of a double-layer metal clad fiber having four surface channels 71, as described hereinabove. A fuel- or oxidant-containing fluid can be passed through such surface channels 71 of the inner current collector 72 to feed the electrochemical reaction at the interface between the membrane separator 75 and the inner electrocatalyst layer 74.

[0056] Such configuration not only obviates the need for providing a separate inner fluid passage, but also significantly increases the contacting surface area between the inner current collector 72 and the inner electrocatalyst layer 74, thereby increasing the performance of the fuel cell and reducing the risk of electrical disconnection. [0057] Further, since the inner fluid passages 71 are partially embedded in the inner current collector 72 and structurally supported thereby, the risk of blockage of such passages due to deformation of the membrane separator 75 is significantly reduced. Therefore, the microfϊbrous fuel cell 70 can be tightly wrapped by the wrapping element 79 to reduce the contact resistance between the outer current collector 78 and the outer electrocatalyst layer 76 and to achieve higher and more efficient power generation, without deforming the inner fluid passages 71.

[0058] For microfibrous fuel cell applications, the above-described channeled metal clad fibers preferably have an outer diameter within a range of from about 100 μm to about 10 mm, more preferably from about 100 μm to about 1000 μm, and most preferably from about 200 μm to about 500 μm.

[0059] If the channeled metal clad fiber comprises a double-layer structure as described hereinabove, the metal core may have an outer diameter within a range of from about 10 μm to about 10 mm, more preferably from about 100 μm to about 1000 μm, and most preferably from about 150 μm to about 500 μm.

[0060] If the channeled metal clad fiber comprises a three-layer structure as described hereinabove, the first metal protective layer may have an outer diameter within a range of from about 100 μm to about 10 mm, more preferably from about 100 μm to about 1000 μm, and most preferably from about 200 μm to about 500 μm, while the metal core may have an outer diameter within a range of from about 10 μm to about 10 mm, more preferably from about 100 μm to about 1000 μm, and most preferably from about 150 μm to about 500 μm.

[0061] However, the microcell current collectors of the present invention are not limited to the two-layer or three-layer structures. A person ordinarily skilled in the art can readily design channeled metal clad fibers having additional layers of metal or non-metal conductive materials, such as conductive polymers, carbonaceous materials, or conductive ceramics, etc., for the purpose of further enhancing the corrosion resistance and mechanical strength of such channeled metal clad fibers for forming microcell current collectors useful for practicing the present invention. Moreover, the metal core of such channeled metal clad fiber is not limited to the solid form as described hereinabove. In a preferred embodiment of the present invention, such metal core may be a hollow, tubular metal element, through which heat-exchanging fluid (such as air or heat- exchanging liquids) can be passed. In such configuration, the inner current collectors concurrently function as heat-exchanging tubes, for conducting heat generated by the electrochemical reaction out of the microcell system.

[0062] In an alternative embodiment, the present invention provides a microfibrous fuel cell structure comprising an inner current collector formed of a channeled metal fiber having a single, un-clad metal layer, as shown in Figure 8.

[0063] Specifically, the microfibrous fuel cell 80 comprises a hollow microfibrous membrane separator 85 that contains an electrolyte medium therein and defines a bore side and a shell side. At the bore side of such membrane separator 85 are placed an inner current collector 82 and an inner electrocatalyst layer 84, and at the shell side of such membrane separator 85 are placed an outer current collector 88 and an outer electrocatalyst layer 86. A wrapping element 89 winds around such microfibrous fuel cell 80 and wraps it into a compact and unitary cell.

[0064] The inner current collector 82 is formed of a single-layer, unclad metal fiber, which has four surface channels 81. A fuel- or oxidant-containing fluid can be passed through such surface channels 81 of the inner current collector 82 to feed the electrochemical reaction at the interface between the membrane separator 85 and the inner electrocatalyst layer 84. [0065] Such unclad, channeled metal fiber of Figure 8 functions in a manner similar to the double-layer metal clad fiber of Figure 7, and is therefore included in the broad scope of the present invention.

[0066] The process described hereinabove for forming the channeled metal clad fibers can be applied for forming channeled metal fibers that are unclad.

[0067] Specifically, a composite metal billet (i.e., a precursor structure) can be formed by hot co- extrusion, which has a longitudinal axis and comprises a supporting metal component with one or more removable metal components partially embedded in such supporting metal component and partially exposed on a surface of such metal billet, while such removable metal components extend along directions that are parallel to the longitudinal axis of such metal billet. Such composite metal billet can be drawn into a metal fiber via a series of cold drawing and annealing steps, wherein such metal fiber comprises the supporting metal component and the one or more removable metal components, in correspondence with those of the composite metal billet. Subsequently, the removable metal components are selectively removed from such metal fiber, via acid-leaching or other material-removal techniques, in such manner that the supporting metal component remains intact and forms a metal fiber having one or more longitudinally-extending surface channels.

INDUSTRIAL APPLICABILITY

The channeled metal clad fiber of the invention is usefully employed for fabricating fuel cells of a highly compact and efficient character. Fuel cells of the invention, including channeled current collectors, provide corrosion-resistant current collector arrangements affording extended service life and reliability, with high contact surface area between the catalyst and current collector, and low contact resistance in the electrochemical cell. The fuel cells of the invention are usefully employed as power sources, e.g., for vehicular propulsion systems, portable power generators, emergency backup power generation systems, and the like.