CA2473491A1

CA2473491A1 - Apparatus of high power density fuel cell layer with micro structured components

Info

Publication number: CA2473491A1
Application number: CA002473491A
Authority: CA
Inventors: Gerard Francis Mclean
Original assignee: Individual
Current assignee: Angstrom Power Inc
Priority date: 2002-02-06
Filing date: 2003-02-05
Publication date: 2003-08-14
Also published as: WO2003067693A2; AU2003207924A8; EP1506587A2; AU2003207924A1; JP2005517273A; CN1647303A; WO2003067693A3; CN100358177C; KR20040105711A

Abstract

The invention is a fuel cell made of a fuel plenum with fuel, an oxidant plenum with oxidant, a porous substrate communicating the fuel and oxidant plenum, a channel formed by the porous substrate, an anode, a cathode, electrolyte in a portion of the channel contacting the anode and the cathode preventing transfer of fuel to the cathode and preventing transfer of oxidan t to the anode, a first coating to prevent fuel from entering a portion of the porous substrate, a second coating to prevent oxidant from entering a portio n of the porous substrate, two sealant barriers, and a positive and negative electrical connection, wherein the invention also involves a multiple fuel cell layer structure, a bi-level fuel cell layer structure, and a method for making a fuel cell layer.

Description

APPLICATION FOR PATENT
INVENTOR:
GERARD FRANCIS MCLEAN
TITLE:
APPARATUS OF HIGH POWER DENSITY FUEL CELL LAYER WITH MICRO
STRUCTURED COMPONENTS
SPECIFICATION
FIELD OF THE INVENTION
t0 The present invention relates to fuel cells. More specifically the invention relates to a fuel cell layer with multiple cells within distinct channels formed using a single porous substrate.
BACKGROUND OF THE INVENTION
High power density fuel cells have long been desired.
Existing fuel cells generally are a stacked assembly of individual fuel cells, with each cell producing high current at low voltage. The typical cell construction involves reactant distribution and current collection devices brought into contact with a layered electrochemical assembly consisting of a gas diffusion layer, a first catalyst layer, an electrolyte layer, a second catalyst layer and a second gas diffusion layer.
With the exception of high temperature fuel cells, such as molten carbonate cells, most proton exchange membrane, direct methanol, solid oxide or alkaline fuel cells have a layered planar structure where the layers are first formed as distinct components and then assembled into a functional fuel cell stack by placing the layers in contact with each other.
One major problem with the layered planar structure fuel cell has been that the layers must be held in intimate electrical contact with each other, which if intimate contact does not occur the internal resistance of the stack increases, which decreases the overall efficiency of the fuel cell.
A second problem with the layered planar structured fuel cell has been to maintain 3o consistent contact between the layers for sealing and ensuring correct flows of reactants and coolants in the inner recesses of the layer structured fuel cell. Also if the overall area of the cell becomes too large then there are difficulties creating the contacting forces needed to maintain the correct fluid flow distribution of reactant gases over the electrolyte surface.

Existing devices also have the feature that, with the layered planar structure fuel cell 35 since both fuel and oxidant are required to flow within the plane of the layered planar structured fuel cell, at least 4 and up to 10 but typically 8 distinct layers have been required to form a workable cell, typically a first flow field, a first gas diffusion layer, a first catalyst layer, a first electrolyte layer, a second catalyst layer, a second gas diffusion layer, a second flow field layer and a separator. These layers are usually manufactured into separate fuel cell 40 components and then the layers are brought into contact with each other to form a fuel cell stack. When contacting the layers care must be taken to allow gas diffusion within the layers while preventing gas leaking from the assembled fuel cell stack. Furthermore, all electrical current produced by the fuel cells in the stack must pass through each layer in the stack, relying on the simple contacting of distinct layers to provide an electrically conductive path.
45 As a result, both sealing and conductivity require the assembled stack to be clamped together with significant force in order to activate perimeter seals and reduce internal contact resistance.
The manufacture of the layers for existing fuel cell configurations is often expensive and difficult. The bipolar plates, which serve as oxidant and fuel flow fields as well as the 50 separator are often constructed from graphite which is difficult to machine, adding significant cost to the fuel cell stack. The membrane electrode assembly (MEA) is usually constructed by first coating a solid polymer electrolyte with catalyst on either side and then pressing gas diffusion electrodes onto the electrolyte. The fuel cell assembly requires multiple individual bipolar plates and membrane electrode assemblies to be connected together in a serial 55 manner. Usually discrete seals must be attached between neighboring bipolar plates and membrane electrode assemblies and the whole stack of sealed bipolar and MEA
layers must be held together under considerable compressive force.
A need has existed to develop alternative fuel cell designs that do not perpetuate the approach of assembling discrete layers in a serial manner. One way to meet this need is to 60 build fuel cells using a micro-structured approach wherein micro-fabrication techniques and nano-structured materials can be combined to create novel devices not subject to the problems commonly associated with conventional fuel cell designs. The application of micro-scale techniques to fuel cells has a number of distinct advantages.
Specifically, the potential for increased power density due to thinner layers and novel geometries, improved 65 heat and mass transfer, improved and/or more precise catalyst utilization and reduced losses with shorter conductive path lengths will all make fuel cells more efficient and enable higher volumetric power densities. The opportunity to include ancillary systems into the fuel cell design and the potential for new applications to emerge present even more potential benefits.
A need has existed for a micro fuel cell having fewer parts than the layered planar 70 structure fuel cell. Fewer parts would give the micro fuel cell a much lower manufacturing cost than current fuel cells.
A need has existed for a micro fuel cell having the ability to utilize a wide variety of electrolytes.
A need has existed for a micro fuel cell, which has substantially reduced contact 75 resistance within the fuel cell.
A number of prior inventions have used micro-scale manufacturing techniques with fuel cells. US 5,861,221 presents a 'membrane strip' containing a number of conventional MEAs connected to each other in series by connecting the edge of the negative electrode of one MEA to the edge of the positive electrode of the next MEA. Two configurations are 80 considered. The first constructs the 'membrane strip' by placing the MEAs together in a step-like configuration. The second constructs the 'membrane strip' by combining MEAs end-to-end with electrically conductive regions between them that connect the cells in series.
In some follow-up work (US 5,925,477) the same inventors incorporate a shunt between the electrodes to improve the electrical conductivity of the cell. The MEAs themselves are of 85 conventional layered structure design, and the overall edge-collected assembly continues to rely on conventional seals between neighboring MEAs.
US 5,631,099 and US 5,759,721 use similar series connection concepts but apply a number of other micro-scale techniques to the fuel cell design. By doing so multiple fuel cells are formed within a single structure simultaneously. The fuel cells themselves still 90 reside as layered planar devices mounted onto a carrier, with interconnection between neighboring fuel cells requiring a penetration of the carrier layer. Most of the techniques discussed in these patents relate to the creation of methanol tolerant catalysts and the application of palladium layers to the catalyst to prevent methanol crossover within the cells.
WO 01/95406 describes a single membrane device that is segmented to create 95 multiple MEA structures. Complex bipolar plates that are difficult to manufacture provide both fuel and oxidants to both sides of the MEA layer. US 6,127,058 describes a similar structure, but instead of complex manifolds of reactant gases, only one reactant is supplied to either side of the MEA layer. Series interconnection of the fuel cells formed within the single MEA layer is achieved through external current collectors arranged around the perimeter of 100 the device providing electrical connection from the top of the MEA layer to the bottom of the MEA layer. Such perimeter electrical connections are inefficient.
Some prior art fuel cells attempt to reduce size and fabrication costs by applying micro fabrication techniques. For example the Case Western Reserve University device forms multiple fuel cells on a carrier substrate using thin layer processes similar to those used t05 in printing and semiconductor fabrication (Wainwright et al. "A micro fabricated Hydrogen/Air Fuel Cell" 195 Meeting of the Electrochemical Society, Seattle, WA, 1999).
In these designs the fuel cells remain of conventional planar design, with the exception that the fuel cells are built-up on a base substrate. The cathodes must be formed on top of the planar electrolytes and then must be connected to neighboring anodes with an explicit 110 interconnect.
All the cells presented above use current collection on the edge of the electrode. This significantly increases the internal cell resistance of these cells. Each of these cells is also based on solid polymer electrolytes, as this is the only electrolyte that allows for easy manufacture. Furthermore, all of the cells presented above achieve a micro fuel cell design 115 by forming multiple fuel cells within a single electrolyte plane.
The concept of using non-planar electrolytes has been considered in the past.
GB
2,339,058 presents a fuel cell with an undulating electrolyte layer. In this configuration a conventional layered MEA is constructed in an undulating fashion. This MEA is placed between bipolar plates. This design increases the active area that can be packed into a given 12o volume. However, this design still relies on the expensive and complicated layered structure with explicit seals and requires compressive force to maintain internal electrical contact and sealing. JP 50903/1996 presents a solid polymer fuel cell having generally planar separators with alternating protruding parts serving to clamp a power generation element (apparently an MEA) into a non-planar but piecewise linear shape. As with GB 2,339,058, this document 125 continues to rely on the expensive and complicated layered structure but this design also puts undue stress on the MEA by forcing it into a non-planar arrangement using the separator plates.
In addition to non-planar designs, some prior art presents tubular configurations. US
6,060,188 presents a cylindrical fuel cell with a single MEA layer formed into a cylinder.
130 Fuel or oxidant is delivered to the interior recess of the cylinder with the other reactant delivered on the exterior. Within this design, each cylindrical structure creates a single cell, with current flowing through the annular cylindrical wall that is the fuel cell. A method of providing series electrical interconnection between fuel cells or of sealing individual fuel cells is not disclosed. This design is reminiscent of tubular designs for solid oxide fuel cells 135 that are well known.
A need has existed to develop fuel cell topologies or fuel cell architectures that allow increased active areas to be included in the same volume, i.e. higher density of active areas.
This will allow fuel cells to be optimized in a manner different than being pursued by most fuel cell developers today.

SUMMARY OF THE INVENTION
The present invention relates to a specific fuel cell layer architecture that is of an integrated design in which the functions of gas diffusion layers, catalyst layers, and 145 electrolyte layers are integrated into a single substrate. This integrated design enables simpler manufacturing processes and scaling of the design.
More specifically, such a fuel cell layer for connecting to an external load with a fuel plenum; an oxidant plenum; a porous substrate communicating with the fuel plenum and the oxidant plenum. The fuel call layer also has a porous substrate and numerous fuel cells 150 formed using the porous substrate. Each fuel cell has a distinct channel, a first catalyst layer disposed on the first channel wall, a second catalyst layer disposed on the second channel wall, an anode formed from the first catalyst layer and an cathode formed from the second catalyst layer, and an electrolyte disposed in the distinct channel to prevent transfer of fuel to the cathode and to prevent transfer of oxidant to the anode. The fuel cell also has a first 155 coating disposed on at least a portion of the porous substrate to prevent fuel from entering a portion of the porous substrate, a second coating disposed on at least a portion of the porous substrate to prevent oxidant from entering a portion of the porous substrate, a first sealant barrier disposed on the first side, a second sealant barrier disposed on the second side, a third sealant barrier disposed between the fuel cells, a positive electrical connection disposed on 160 the first side, and a negative electrical connection disposed on the second side.
When a plurality of microscopically dimensioned fuel cells are formed within a single substrate, higher overall power densities can be achieved. In addition, the multiple fuel cells within the single substrate can be formed in parallel, conducive to the utilization of high volume automated manufacture to construct the fuel cell layer. The combination of fuel cells 165 within a single substrate minimizes the reliance on externally applied seals and clamps.
A number of variations on the design of the fuel cell layer are envisioned.
Some of the variations include having the fuel and oxidant plenums dead-ended, having the fuel cell layer enclosing a volume, having the porous substrate in a non-planar, or alternately planar, configuration and having the fuel cell layer enclose a volume in a cylindrical shape. The 170 substrate can be formed from a variety of conductive and non-conductive porous media.
Dimensionally, the channel can have a dimension ranging from 1 nanometer to 10 cm in height, 1 nanometer to 1 mm in width and from 1 nanometer to 100 meters in length. A
single fuel cell of the invention is contemplated of being capable of producing between approximately 0.25 volts and approximately 4 volts.
1'75 Between 1 and 5000 fuel cells are contemplated as usable in one fuel cell layer in this design, however in a preferred embodiment, the fuel cell layer has between 75 and 150 joined fuel cells. This fuel cell layer is contemplated to be capable of producing a voltage between 0.25 volts and 2500 volts. A fuel cell with more channels will be capable of producing higher voltages.
180 Electrolyte usable in this invention can be a gel, a liquid or a solid material. It is contemplated that the electrolyte can be between 1 nanometer and 1.0 mm in thickness, or alternatively simply filling each channel from first wall to second wall without a gap. Having a thin channel, and therefore a thin electrolyte, increases the efficiency of the fuel cell.
The fuel cell layer of the invention can be used by first, connecting a fuel source to a 185 fuel plenum inlet; second, connecting a fuel plenum outlet to a re-circulating controller; third, connecting an oxidant plenum inlet to an oxidant source; fourth, connecting an oxidant plenum outlet to a flow control system, fifth, connecting a positive electrical connection and a negative electrical connection to an external load; sixth, flowing fuel and oxidant to the inlets; and finally, driving load with electricity produced by the fuel cell.

BRIEF DESCRIPTION OF THE FIGURES
A specific embodiment of the invention will be described by way of example with reference to the accompanying drawings, in which:
195 Figure 1 is a cross-sectional view of a first embodiment of the inventive fuel cell;
Figure 1 a is a cross-sectional detailed view of the anode with the catalyst at a first depth in the porous substrate;
Figure lb is a cross sectional detailed view of the anode with the catalyst at a second depth in the porous substrate;
20o Figure 1 c is a cross sectional detailed view of the cathode;

Figure 2 is a cross-sectional view of a dead ended embodiment of the inventive fuel cell;
Figure 2a is embodiment of the fuel cell according to the invention with the fuel and oxidant plenums being solid with flow channels contained therein;
205 Figure 3 is a cross-sectional view of another embodiment of a dead ended fuel cell;
Figure 3a is an embodiment of the invention with an oxidant plenum open to the ambient environment;
Figure 3b is an embodiment of the invention with a fuel plenum open to the ambient environment;
210 Figure 4 is a cross-sectional view of a fuel cell layer formed by combining multiple fuel cells of the type described in Figure 1;
Figure 4a is a cross sectional view of a multiple porous substrate fuel cell layer with the fuel plenum open to the ambient environment;
Figure 4b is a cross sectional view of a multiple porous substrate fuel cell layer with 215 the oxidant plenum open to the ambient environment;
Figure 4c is a cross sectional view of a fuel cell layer with up to 5000 fuel cells;
Figure S is a cross-sectional view of a fuel cell with multiple fuel cells of the type described in Figure 1 formed within a single substrate;
Figure Sa is another embodiment of a fuel cell with multiple cells;
220 Figure 6 is a perspective view of a fuel cell layer containing multiple fuel cells of the type described in Figure 1;
Figure 7 is another detailed perspective view of the fuel cell of the invention with undulating channels;
Figure 8 is a perspective view of a cylindrical version of a fuel cell according to the 225 invention;
Figure 8a is a cross-sectional view of an embodiment of the fuel cell of Figure 1 in which the substrate is irregularly shaped;
Figure 9 is a cross sectional view of a cylindrical version of a fuel cell according to the invention;
23o Figure 10 is another embodiment of the inventive fuel cell of the invention with the channels in the form of a set of stacked annular rings;
Figure 11 is another embodiment of the inventive fuel cell with the channels in the form of a spiral around the cylinder; and Figure 12 is a perspective view of a bi-level fuel cell structure.

DETAILED DESCRIPTION OF INVENTION
The present invention relates to a microstructure fuel cell having a substrate, which is preferably porous, an assembly of fuel cells having a single or multiple substrate structure 24o and methods for manufacturing such fuel cells and fuel cell layers.
The invention relates to a specific fuel cell architecture that is of an integrated design in which the functions of gas diffusion layers, catalyst layers, and electrolyte layers are integrated into a single substrate. This architecture makes it possible to fold together the various 'layers' of which a working fuel cell is formed and produce linear, curvilinear, 245 undulating or even fractal shaped electrolyte paths that allow for higher volumetric power density to be achieved by increasing the electrochemically active surface area. In addition, by forming the various fuel cell layers within a single substrate the problem of simple contacting of fuel cell components to create electrical connections is eliminated, thus creating the potential for lower internal cell resistances to be achieved. The cell layers themselves can 250 be constructed in planar, non-planar or involute configurations providing further advantages in increasing surfaces areas and providing flexibility in applications. This integrated design enables simpler manufacturing processes and scaling of the design.
Unlike existing fuel cell designs, the present invention, in one embodiment, provides convoluted electrolyte layers, which do not smoothly undulate. Other embodiments of the 255 invention include shapes that are essentially non-smooth. Utilizing such non-smooth electrolyte paths allows for greater overall surface areas for the fuel cell reactions to be packed into a given volume than can be achieved when planar electrolyte layers are employed as in conventional fuel cell designs. The present invention also allows for significantly decreased distances between separate electrolyte layers, thereby allowing for a greater surface 260 area in a given volume than conventional designs.
The present invention contemplates the use of a design inspired by fractal patterns, which provides long electrolyte path lengths. The invention includes a method for building fuel cells and "stacks" that are not dependent on the layered process and which do not require the post-manufacturing assembly of distinct layered components. The conventional 265 relationship between MEA layers and bipolar plates is eliminated, as is the reliance on multiple discrete layered structures. The invention also contemplates a design with individual fuel cells turned on their side relative to the overall footprint of the assembled fuel cell device. The invention contemplates building multiple fuel cells with an integrated structure on a single substrate using parallel manufacturing methods.
270 Specifically, it is contemplated to use a porous substrate for the fuel cell through which reactant gas will diffuse with little driving force. The substrate may or may not be electrically conductive. If it is conductive, it is contemplated to insulate at least a portion of the substrate, which typically would separate the anode from the cathode, this insulation may be formed by the electrolyte separating the anode from the cathode and, if necessary, an 275 optional insulating structural member may be added. More specifically, the fuel cell is contemplated to have: (a) a fuel plenum with fuel; (b) an oxidant plenum with oxidant; (c) a porous substrate communicating with the fuel plenum, and the oxidant plenum further with a top, a bottom, a first side, and a second side; (d) a channel formed using the porous substrate, wherein the channel has a first channel wall and a second channel wall; (e) an anode formed 280 from a first catalyst layer disposed on the porous substrate of the first channel wall; (f) a cathode formed from a second catalyst layer disposed on the porous substrate of the second channel wall; (g) electrolyte disposed in at least a portion of the channel contacting the anode and the cathode preventing transfer of fuel to the cathode and preventing transfer of oxidant to the anode; (h) a first coating disposed on at least a portion of the porous substrate to 285 prevent fuel from entering at least a portion of the porous substrate; (i) a second coating disposed on at least a portion of the porous substrate to prevent oxidant from entering at least a portion of the porous substrate; (j) a first sealant barner disposed on the first side and the second sealant barner disposed on the second side; (k) a positive electrical connection disposed on the first side; (1) a negative electrical connection disposed on the second side;
290 and wherein the resulting fuel cell generates current to drive an external load.
Refernng to Figure 1, which is a cross-sectional view of one embodiment of the invention, a fuel cell 8 has an optional fuel plenum 10 containing fuel 11. A
porous substrate 12 is adjacent the optional fuel plenum 10. The fuel plenum can have an optional fuel plenum inlet 18. The fuel plenum can also have an optional fuel plenum outlet 20. An 295 optional oxidant plenum 16 containing oxidant 13 is adjacent the porous substrate 12. The oxidant plenum can have an optional oxidant plenum inlet 52. The oxidant plenum can also have an optional oxidant plenum outlet 54. If no oxidant plenum is used the fuel cell uses the ambient environment as a source of oxidant.
The porous substrate 12 can have a shape that is rectangular, square or orthogonal or 30o alternatively, it can be irregularly shaped. In this embodiment it is pictured as being formed within a single plane, although non-planar substrates or multiple substrate configurations are envisioned.
A channel 14, formed using the porous substrate, can be straight or of arbitrary design. If of arbitrary design the channel is referred to throughout this application as 305 "undulating." If multiple channels are present at least one may be undulating. The channel 14 has a first channel wall 22 and a second channel wall 24. Additionally the porous substrate 12 has a top 100, bottom 102, first side 104 and a second side 106.
The channel can have an undulating channel, a straight channel or an irregular channel. If undulating, the channel can be sinusoidal in shape and if undulating, the channel 310 may be of a shape that is in at least three planes.
An anode 28 is created on or alternately in the surface of the first channel wall 22, although the anode could be embedded in the wall as well. Anode 28 is created using a first catalyst layer 38 on or into the surface of the first channel wall 22.
A cathode 30 is formed on the surface or alternately in the second channel wall 24.
315 Like the anode 28, the cathode 30 could be embedded in the second channel wall 24.
Cathode 30 is created using a second catalyst layer 40.
Figures la, lb and lc provide details of the cathode and anode of the fuel cell. Figure la shows the anode 28 at a first depth within the porous substrate 12, Figure lb shows the anode 28 at a second depth within the porous substrate 12 and Figure lc shows the cathode 320 30.
The catalyst layers can be deposited on the first and channel walls or can be formed in the channel walls. In one embodiment the first and second catalyst layers are disposed in the porous substrate to at least a minimum depth to cause catalytic activity.
Referring back to Figure 1, an electrolyte 32 is disposed in the channel 14.
325 A first coating 34 is disposed on at least a portion of the porous substrate 12 preventing fuel from entering at least a portion of the porous substrate 12. A
second coating 36 is disposed on at least a portion of the porous substrate 12 preventing oxidant from entering at least a portion of the porous substrate 12.
A first sealant barrier 44 is disposed on the first side of the porous substrate and a 330 second sealant barrier 46 is disposed on the second side of the porous substrate. The sealant barners can optionally be disposed within a sealant barrier channel 43.
A positive electrical connection 50 is engaged with the porous substrate 12 on the first side of the porous substrate.

A negative electrical connection 48 is engaged with the porous substrate 12 on the 335 second side of the porous substrate.
The resulting fuel cell generates current 56 to drive an external load 58.
Figure 2 is another embodiment of the invention showing a dead ended version of the fuel cell 108 specifically excluding the fuel outlet 20 and the oxidant outlet 54 of the Figure 1 embodiment.
34o In one version of this embodiment of the invention, it is contemplated that the electrolyte 32 can be mounted in the channel 14 at an angle 76, preferable at an angle, which is perpendicular to the longitudinal or horizontal axis 74 of the predominant portion of the porous substrate 12.
In Figure 2 an optional support member 26 separates first channel wall 22 from 345 second channel wall 24 however the support member is not required in every embodiment.
Some alternatives envision multiple support members as shown in Figure 2a.
Between one and 50 or more support members are contemplated herein.
Now referring to Figure 2a, a fuel cell is shown with a solid fuel plenum 10 with flow fields 126 and a solid oxidant plenum 16 with flow fields 126. It is also envisioned that the 35o fuel plenum has a permeable material containing the fuel. The oxidant plenum can also have a permeable material. It is understood that the fuel plenum and oxidant plenum need not be constructed in the same manner and a variety of combinations of oxidant and fuel plenum configurations can be used. The fuel plenum and the oxidant plenum can each have a variety of shapes, round, ellipsoid, rectangular or square. It is particularly contemplated that the fuel 355 plenum has a rectangular cross-section.
Figure 3 is a cross-section of another embodiment of a dead ended version of the fuel 110 that excludes both the fuel inlet 18 and the fuel outlet 20 as well as the oxidant inlet 52 and the oxidant outlet 54 of the embodiment of Figure 1. Figure 3a shows an embodiment of the fuel cell where the oxidant plenum 16 is entirely removed. In such an embodiment the 36o cell would use the ambient environment as an oxidant supply. Figure 3b shows an embodiment of the fuel cell where the fuel plenum 10 is removed entirely. In this configuration the fuel cell uses the ambient environment as a fuel supply.
Figure 4 shows a first fuel cell 66 formed from a substrate 12 that is made adjacent a second fuel cell 114 formed from a second substrate 62. The first and second fuel cells may 365 be formed from either the association of multiple substrates or, as shown in Figure 5, the first fuel cell 66 and the second fuel cell 114 may be formed by creating multiple channels 14 within a single substrate 12.

In Figure 4, a plurality of fuel cell structures are formed using separate porous substrates and they are then connected to each other at the sealant barriers 44 forming a fuel 370 cell layer. In this figure a first fuel cell 66 is connected to a second fuel cell 114. Multiple fuel cells can be connected together in this manner to create a fuel cell layer 64 with a fuel side 116 and an oxidant side 118. The details in the figure can be easily understood by referring to the items numbers in the description of Figure 1 and will therefore not be elaborated here.
375 In this embodiment it is envisioned that the fuel cell be connected in series, in parallel or in combinations thereof to allow the fuel cell layer to produce current to drive an external load.
Figure 4a shows a fuel cell layer with the fuel plenum open to the ambient environment. The fuel plenum can be a permeable material or a solid material with a flow 380 field. The fuel plenum can also have a rectangular cross-section. Figure 4b shows a fuel cell layer with the oxidant plenum open to the ambient environment. In this figure at least one optional support member 26 is shown on at least one of the fuel cells. Figure 4c shows an embodiment of the fuel cell layer wherein up to 5000 cells are connected together in the manner explained for Figure 4.
385 In Figure 5, the same fuel cell structures are formed in a single porous substrate 12.
In this embodiment a plurality of fuel cells are created within the porous substrate in the same manner as described for Figure 1. Since, in this case, the fuel cells are formed within a single substrate the sealant barners and electrical connections associated with each fuel cell are not required. Instead a first sealant barrier 44 is disposed on the first side of the porous substrate, 390 a second sealant barner 46 is disposed on the second side of the porous substrate and a plurality of third sealant barners 45 are disposed between the fuel cells. The sealant barners provide gas impermeable separators between the fuel cells within the fuel cell layer.
It is understood that the same embodiments shown for the multiple substrate structure in Figures 4a, 4b and 4c can be used with the single substrate structure shown in Figure 5.
395 This association of two fuel cells, either by the structure of Figure 4 or the structure of Figure 5, can be extended to place an arbitrary number of fuel cells in association with each other. In both embodiments, the ends of the multiple structures are sealed with a sealant barrier 44 and a second sealant barner 46. In both embodiments, negative electrical connection 48 is attached on one end of the multiple fuel cell assembly and positive electrical 400 connection 50 is attached on the other end of the multiple fuel cell assembly to allow the multiple fuel cell assembly to drive an external electrical load.

The association of multiple fuel cells produces a fuel cell layer 64 having a fuel side 116 that is brought into association with a fuel plenum 10 and an oxidant side 118 that is brought into association with an oxidant plenum 16.
405 If the substrate material from which the fuel cells within the fuel cell layer 64 is formed is conductive, then electrical current produced by the individual fuel cells is able to flow directly through the substrate material and the sealant barners 44 to create a bipolar fuel cell structure within the formed fuel cell layer. If the substrate material from which the fuel cells within the fuel cell layer are formed is not electrically conductive then the first coating 410 34 and second coating 36 should both be made of an electrically conducting material and formed so that the first coating 34 is in electrical contact with the anode 40 while second coating 36 is in electrical contact with cathode 38. The first coating 34 and the second coating 36 are also made in electrical contact with the conductive sealant barrier 44. In either case, with a conductive or non-conductive substrate the electrical current produced by the 415 fuel cell can be transported to the positive and negative electrical connections.
An alternate configuration for the fuel cell layer is shown in Figure 5a. In this configuration the first coating 34 is extended to connect the anode of the first fuel cell to the cathode of the second fuel cell. The second coating 36 is likewise extended to contact the anode of the first fuel cell. The first coating on the end and the second coating on the end can 42o be used to connect the fuel cells on the ends to the positive electrical connection 50 and the negative electrical connection 48. In this configuration portions of the first coating are porous to allow fuel to reach the anode and portions of the second coating are porous to allow oxidant to reach the cathode. In this configuration neither the porous substrate nor the sealant barrier need be electrically conductive. It is also envisioned that only the first coating be 425 extended to provide electrical contact between the cells or that only the second coating be extended to provide electrical contact between the cells.
When multiple fuel cells are formed into a fuel cell layer, as described in figures 4 and 5 a series electrical connection of the individual fuel cells results. The summed voltages of the multiple fuel cells produce a potential difference between the positive and negative 430 electrical connections at either end of the fuel cell layer. A larger number of fuel cells will enable the fuel cell layer to produce a higher voltage between the electrical connections. Any combination of conductive or non-conductive substrates, barriers and caps may be used so long as an electrically conductive path between neighboring anodes and cathodes is created.
In this manner either an edge collected or preferably a bipolar series electrical connection of 435 each of the fuel cells in the fuel cell layer is achieved without the need to clamp distinct components together and without the use of independently formed layered components.
Also, the direction of current flow in the fuel cell layer is overall in the plane of the fuel cell layer rather than being orthogonal to the fuel cell layer as is the case in most current designs.
It is also envisioned to electrically connect the fuel cells within a fuel cell layer together in 440 parallel or in a combination of series and parallel.
Figure 6 is a cutaway perspective view of a fuel cell layer 64. In this figure a first fuel cell 66 is separated from a second fuel cell 114 by a sealant barner 44. A
third fuel cell 115 is separated from the second fuel cell 114 by another sealant barrier 44. The layer has the same structure as the layers described in Figures 4 and 5. The single fuel cell layer 64 can 445 contain as many sealant barriers and cells as desired. The determination of the spacing between individual fuel cells within the fuel cell layer is at the discretion of the designer, limited by pragmatic issues of manufacturability and mass transport issues within the porous substrate.
The overall structure of the fuel cell layer 64 creates a series connection of the 450 individual fuel cells. Positive electrical connection 50 and negative electrical connection 48 allow an external load to be connected to the fuel cell layer, which produces a voltage that is a multiple of the single cell voltages produced within the fuel cell layer.
Figure 7 shows a similar view as Figure 6 of the fuel cell layer 64 but in this Figure, each of the fuel cells 8 have a channel 14 with a less straight structure.
Again, as with Figure 455 6, Figure 7 uses essentially the same structure as shown in Figure 4 and 5, but repeated multiple times creating a mufti-cell structure. The less straight structure of the channels allows for increased electrochemically active areas for the anodes and cathodes formed on the channel walls. The less straight channels can be smoothly undulating or can be irregular in shape resembling a fractal structured path which is known to have extremely high area. Any 460 arbitrary channel structure can be used with this invention allowing for the optimization of the area of the electrodes in each fuel cell. A preferred embodiment includes a plurality of thin channels that run parallel to each other and follow an irregular path that folds back on itself in a manner suggestive of a fractal pattern. Another preferred embodiment of the invention includes at least one channel that is in at least three planes.
465 Figure 8 shows a perspective view of a cylindrical version 250 of a multiple fuel cell layer. In this version a multitude of non-planar fuel cells 208 are combined to create a fuel cell layer 64 that encloses a volume 210. The enclosed volume 210 is used as the fuel plenum while the environment outside the cell supplies the oxidant. It is also envisioned that the fuel be supplied by the environment outside the cylinder and that the enclosed volume 470 210 be used as an oxidant plenum. The cylindrical fuel cell 250 can either be constructed using a single porous substrate which is in the shape of a cylinder using the method discussed for combining cells in figure 5 or with multiple porous substrates that are brought together into a cylinder using the method discussed for combining cells in figure 4.
Figure 8a is a cross-section of a non-planar version of the fuel cell 208. The fuel cell 475 has a fuel plenum 10 with fuel inlet 18 and fuel outlet 20 and an oxidant plenum 16 with oxidant inlet 52 and oxidant outlet 54. A non-planar porous substrate 212 is in communication with both the fuel plenum 10 and the oxidant plenum 16. A
channel 14 is formed within the non-planar porous substrate 212. The channel 14 has an anode 40 and a cathode 38 constructed as described for figure 1 and is filled with electrolyte 32. The fuel 480 cell has a support member 26 a first coating 34 and a second coating 36.
The negative electrical connector 48 is shown adjacent sealant barrier 44. The positive electrical connector 50 is shown adjacent the optional sealant barrier 46. Although in this figure an arc is used to show the non-planar nature of the fuel cell, any arbitrary configuration could be used. As with the fuel cells of figure 1 the non-485 planar fuel cell can be combined to form a non-planar fuel cell layer with multiple cells and can be associated with fuel and optional oxidant plenums of various configurations.
Figure 9 shows a cross sectional view of a cylindrical version of a fuel cell.
In this case the non-planar substrate 212 is shaped in the form of a cylinder to enclose a volume 210.
The fuel cell in this figure is shown with fuel 11 in the enclosed volume 210 providing fuel to 490 the fuel cell. In this configuration the ambient environment outside the cell supplies oxidant.
It is also envisioned that oxidant be contained within the enclosed volume 210 and that the ambient environment supply the fuel.
Figure 10 is another embodiment of a cylindrical fuel cell 251 having the channels 14 of the non-planar fuel cells 208 configured radially and orthogonal to the axis of the cylinder.
495 It is understood that the fuel cells 208 within this figure can either be constructed or assembled, as described for Figure 4 or that they be formed within a single cylindrical substrate as described for Figure 5.
Figure 11 is another embodiment of a cylindrical fuel cell 252 having the channel 14 of the non-planar fuel cell disposed in a wound or spiral fashion around the perimeter of the 500 cylinder. Although, in this figure, only a single spiral channel 14 is shown, multiple fuel cells with multiple channels could be formed using the porous substrate.
Although only cylindrical cells have been shown enclosing a volume it is contemplated herein that shapes such as extruded rectangles, squares, ovals, triangles and other shapes as well as non-extruded shapes such as cones, pyramids, football shaped objects 505 and other shapes that enclose a volume are included as part of the invention.
Figure 12 is a cutaway perspective view of a bi-level fuel cell layer structure 254 with two fuel cell layers, a first fuel cell layer 64 and a second fuel cell layer 112 each with an anode side and a cathode side wherein the first fuel cell layer 64 is stacked on top of the second fuel cell Layer 112 such that the anode side 264 of the first fuel cell layer and the 51o anode side 268 of the second fuel cell layer adjoin.
In figure 12, a seal 130 is disposed between the first and second fuel cell layer to form a fuel plenum 124. The two positive electrical connections are connected to positive connector 120 and the two negative electrical connections are connected to negative connector 122 so that the individual fuel cell layers are now connected in an electrically 515 parallel configuration. The resulting assembly is a bi-level fuel cell layer structure 254 having a top 70 and a bottom 72, the top and bottom being the cathode sides of the respective fuel cell layers. The resulting structure is an enclosed plenum air breathing fuel cell that achieves a series electrical connection of the individual fuel cells in each fuel cell layer and a parallel electrical connection of the two fuel cell layers. Only fuel is required to be fed to the 520 interior of the structure and electrical current flows within the two fuel cell layers independently of one another. There is no electrical connection between the two fuel cell layers except at the parallel connection of the positive and negative electrical connections at either end of the fuel cell layers in the structure.
It is also envisioned that the fuel cell layers be placed cathode to cathode thereby 525 creating a common plenum that can be filed with oxidant. In this configuration the fuel cell sandwich uses the ambient environment as a fuel supply.
Although various materials could be used for the porous substrate of the invention, one usable material could be a conductive material. Materials such as a metal foam, graphite, graphite composite, at least one silicon wafer, sintered polytetrafluoroethylene, crystalline 53o polymers, composites of crystalline polymers, reinforced phenolic resin, carbon cloth, carbon foam, carbon aerogel, ceramic, ceramic composites, composites of carbon and polymers, ceramic and glass composites, recycled organic materials, and combinations thereof are contemplated as usable in this invention.
The channel is contemplated to have up to 50 optional support members separating 535 the walls of the channel. The channel is envisioned to be formed within the porous substrate.
The channel is formed by a technique of cutting, ablating, molding, etching, extruding, embossing, laminating, embedding, melting, or combinations thereof. The channel can be undulating or in at least three planes.
The support members can be located at the extreme ends of the channel, such as 540 forming a top or bottom, or can be located in the middle portion of the channel, or be oriented at an angle to the center of the channel. It is contemplated that the support member can be an insulating material. If an insulating material is used, it is contemplated that silicon, graphite, graphite composite, polytetrafluoroethyIene, polymethamethacrylate, crystalline polymers, crystalline copolymers, cross-linked polymers thereof, wood, and combinations thereof can 545 be usable in the invention.
Dimensionally, the channel can have a dimension ranging from 1 nanometer to 10 cm in height, I nanometer to 1 mm in width and from I nanometer to 100 meters in length.
A single fuel cell of the invention, optionally within a fuel cell layer, is contemplated of being capable of producing between approximately 0.25 volts and approximately 4 volts.
550 Between 1 and 5000 fuel cells are contemplated as usable in one fuel cell layer in this design, however in a preferred embodiment, the fuel cell layer has between 75 and 150 joined fuel cells. This fuel cell layer is contemplated to be capable of producing a voltage between 0.25 volts and 2500 volts. A fuel cell with more channels will be capable of producing higher voltages.
555 The invention can be constructed such that the fuel is pure hydrogen, gas containing hydrogen, formic acid, or an aqueous solution with ammonia, methanol, ethanol and sodium borohydride, or combinations thereof. The invention can be constructed such that the oxidant is pure oxygen, gas containing oxygen, air, oxygen-enriched air, or combinations thereof.
Electrolyte usable in this invention can be a gel, a liquid or a solid material. Various 56o materials are contemplated as usable and include: a perfluoronated polymer containing sulphonic groups, an aqueous acidic solution having a pH of at most 4, an aqueous alkaline solution having a pH greater than 7, and combinations thereof. Additionally, it is contemplated that the electrolyte layer can be between 1 nanometer and 1.0 mm in thickness, or alternatively simply filling each undulating channel from first wall to second wall without 565 a gap.
The fuel cell is manufactured using a first and second coating on the porous substrate.
These coatings can be the same material or different materials. At least one of the coatings can be polymer coating, epoxies, polytetrafluoro ethylene, polymethyl methacrylate, polyethylene, polypropylene, polybutylene, copolymers thereof, cross-linked polymers 570 thereof, conductive metal, or combinations thereof. Alternatively, the first or second coating can have a thin metallic layer such as a coating of gold, platinum, aluminum or tin as well as alloys of these or other metals or metallic combinations.
The first and second catalyst layers that are contemplated as usable in the invention can be a noble metal, alloys with noble metals, platinum, alloys of platinum, ruthenium, 575 alloys of ruthenium, and combinations of these materials. It is contemplated that ternary alloys having at least one noble metal are usable for good voltage creation.
Platinum-ruthenium alloys and platinum are also contemplated as usable in this invention. The catalyst layers should each have a catalyst loading quantity wherein the amount of catalyst may be different for each layer.
580 The first and second catalyst layers are disposed in the porous substrates at least at a minimum depth to cause catalytic activity. The porous substrate connects to fuel plenum further making a horizontal axis. The electrolyte disposed in the channel is oriented at an angle perpendicular to the horizontal axis. The porous substrate can be a planar shape, a shape that encloses a volume, or a cylinder. The porous substrate can also be a conductive 585 material.
The materials for the optional sealant barriers contemplated herein can silicon, epoxy, polypropylene, polyethylene, polybutylene, copolymers thereof, composites thereof, or combinations thereof.
One method for making the fuel cell contemplates the following steps:
590 a. forming a porous substrate having a top and bottom having a first side and a second side;
b. coating at least a portion of the top with a first coating;
c. coating at least a portion of the bottom with a second coating;
d. forming a channel using the porous substrate, wherein the channel has a first 595 channel wall and a second channel wall;
e. forming an anode by depositing a first catalyst layer on the first channel wall;
f. forming a cathode by depositing a second catalyst layer in the second channel wall;
g. disposing electrolyte in at least a portion of the channel contacting the anode 600 and the cathode;
t8 h. attaching a positive electrical connection on one end to the first side of the porous substrate, and attaching a negative electrical connection on one end to the second side of the porous substrate;
i. attaching a fuel plenum to the porous substrate forming a fuel cell;
605 j. attaching an oxidant plenum to the porous substrate;
k. disposing a sealant barrier around at least a portion of the fuel cell; and I. loading the fuel plenum with fuel and the oxidant plenum with oxidant.
The sequence of operations described may be varied and steps combined as required to suit the particular material requirements and fabrication processes used.
As well, the 610 method can form between one and 250 or more channels in the porous substrate.
Another method for forming a fuel cell envisioned in the invention contemplates the following steps:
a. repeating steps a through h of the method above as many times as needed prior to joining the porous substrate to the fuel plenum forming at least one 615 additional fuel cell;
b. securing the porous substrate at the sealant barriers to at least on additional fuel cell at its sealant barrier forming a fuel cell layer and extending the fuel cell layer securing additional formed fuel cells to the fuel cell layer at respective sealant barriers;
620 c. attaching the positive electrical connections and the negative electrical connections of the fuel cell layer together;
d. attaching the joined fuel cells to the fuel plenum; and e. attaching the joined fuel cells to the oxidant plenum.
The positive electrical connections and the negative electrical connections of the fuel 625 cells within the fuel cell layer can be connected in series, in parallel or in a combination of series and parallel.
Yet another method for making a fuel cell layer is contemplated which has the steps of:
a. forming a porous substrate with a top and bottom, a first side and a second 630 side;
b. coating at least a portion of the top with a first coating;
c. coating at least a portion of the bottom with a second coating;
d. forming a plurality of distinct channels using the porous substrate, wherein each distinct channel has a first channel wall and a second channel wall;

635 e. forming a plurality of anodes by depositing a plurality of first catalyst layers on the first channel walls;
f. forming a plurality of cathodes by depositing a plurality of second catalyst layers in the second channel walls;
g. disposing electrolyte in at least a portion of each distinct channel;
64o h. disposing a first sealant barner on at least a portion of the first side;
i. disposing a second sealant barrier on at least a portion of the second side;
j. forming a plurality of third sealant barriers between each of the distinct channels creating a plurality of independent fuel cells adjacent each other in the porous substrate;
645 k. attaching a positive electrical connection to the first side of the porous substrate;
1. attaching a negative electrical connection to the second side of the porous substrate;
m. attaching a fuel cell positive electrical connection to each independent fuel 650 cells n. attaching a fuel cell negative electrical connection to each independent fuel cell forming a fuel cell layer; and o. disposing a sealant barner around at least a portion of the fuel cell layer.
In any of the methods described above a number of different methods of forming the 655 porous substrate are contemplated herein. The porous substrate can be formed by a method of casting and then baking, slicing layers from a pre-formed brick, molding, extruding, or combinations thereof. The formed porous substrate may be non-planar or enclose a volume.
Any of the methods described can also entail any of the additional steps. A
step can be added of masking the porous substrate prior to coating the substrate top and bottom. A
660 step can be added of inserting a support member between each the first channel wall and the second channel wall. A step can also be added of selecting removing a portion of the coating deposited on the top and bottom prior to adding the electrolyte.
The step of forming distinct channels can be a method of embossing, ablating, etching, extruding, laminating, embedding, melting, molding, cutting or combinations 665 thereof. The etching can be by laser etching, deep reactive ion etching, or alkaline etching.
The fuel cell positive electrical connections and the fuel cell negative electrical connections of the independent fuel cells in the fuel cell layer can be connected in series, in parallel, or in a combination of in series and in parallel.

If at least one of the coatings is deposited with thin film deposition techniques, the 67o technique may include sputtering, electroless plating, electroplating, soldering, physical vapor deposition, and chemical vapor deposition. If at least one of the coatings is an epoxy coating the coating can be disposed on the substrate by a method selected from the group:
screen printing, ink jet printing, spreading with a spatula, spray gun deposition, vacuum bagging and combinations thereof. A mask can be used when applying the coatings to the 675 porous substrate. If required, a portion of the coating can be removed prior to adding the electrolyte.
The porous substrate can be formed by casting and then by baking, by slicing thin layers from a preformed brick, by molding, or by extruding. The porous substrate can be formed into a non-planar shape prior to forming each distinct channel. The porous substrate 68o can also be formed into a shape that encloses a volume prior to forming each distinct channel.
The invention is also a micro structured fuel cell system with the fuel cell layer. The fuel cell layer has an anode side and a cathode side, a positive end and a negative end. At least one surface is located between the positive end and the negative ,end and at least one electronic system is mounted on the at least one surface.
685 The electronic system is a cellular phone, a PDA, a satellite phone, a laptop computer, portable DVD, portable CD player, portable personal care electronics, portable boom boxes, portable televisions, radar, radio transmitters, radar detectors, or combinations thereof.
Electricity produced by the fuel cell layer on which the system is mounted powers the electronic system. The electronic system also serves an ancillary function for fuel cell 690 operation. The ancillary functions include fuel cell performance monitoring, fuel cell control, fuel cell fault diagnostics, fuel cell performance optimization, fuel cell performance recording or combinations thereof. More than one electronic system can be mounted on each side of the fuel cell layer.
The invention is also multiple fuel cell layer structure with a numerous fuel cell 695 layers. A first fuel cell layer is stacked on top of a second fuel cell layer such that the anode side of the first fuel cell layer and the anode side of the second fuel cell layer adjoin. A third fuel cell layer is stacked on the second fuel cell layer such that the third fuel cell layer cathode side adjoins the second fuel cell layer cathode side forming a stack with adjacent fuel cell layers. Additional fuel cell layers can then be added on the first, second and third fuel 700 cell layers in a like manner. A bi-level fuel cell layer structure is formed when the first fuel cell layer is stacked on top of the second fuel cell layer such that the anode side of the first fuel cell layer and the anode side of the second fuel cell layer adjoin forming a bi-level stack.

The multiple fuel and bi-level cell layer structure also have at least one seal between the adjacent fuel cell layers forming at least one plenum, a positive connector for connecting 7o5 the stack to an outside load, and a negative connector for connecting the stack to the outside Load. When fuel is presented to the anode sides of the fuel cell layers and oxidant is presented to the cathode sides of the plurality of fuel cell layers, a current is produced to drive the outside load.
In another embodiment, the multiple fuel cell layer structure or bi-level cell layer 710 structure can also have at least one flow field formed in at least one fuel cell layer of the stack. The flow field can be by cutting, ablating, molding, embossing, etching, laminating, embedding, melting or combinations thereof The plenum in fuel cell layer structure can be a fuel plenum, an oxidant plenum, or combinations thereof. The positive and negative ends can be connected in series between the 715 positive and negative connectors, in parallel to the positive and negative connectors, or a combination of both.
The fuel cell of the invention can be used by first, connecting a fuel source to a fuel plenum inlet; second, connecting a fuel plenum outlet to a re-circulating controller; third, connecting an oxidant plenum inlet to an oxidant source; fourth, connecting an oxidant 720 plenum outlet to a flow control system, fifth, connecting a positive electrical connection and a negative electrical connection to an external load; sixth, flowing fuel and oxidant to the inlets; and finally, driving load with electricity produced by the fuel cell.
If a dead-ended version of the fuel cell is used the operation is much simpler. First, the fuel inlet is connected to a fuel supply, second, the oxidant inlet is connected to an 725 oxidant supply, third, the positive electrical connection and the negative electrical connection are connected to an external load; and finally, the load is driven with electricity produced by the fuel cell.
The method of the invention can further have the step of sealing the plenum outlets and inlets after the fuel and oxidant is loaded into their respective plenums creating a dead 73o ended fuel cell. The fuel cell can then be connected to an external load using the positive and negative electrical connections and used to drive the external load.
It is envisioned within this invention to use any combination of fuel and oxidant inlets and outlets to operate the fuel cell.
The invention has been described in detail with particular reference to certain 735 preferred embodiments thereof, but it will be understood that variations and modifications can be effected within the scope of the invention.

Claims

1. A fuel cell comprising:
a. a fuel plenum comprising fuel;
b. an oxidant plenum comprising oxidant;
c. a porous substrate communicating with said fuel plenum, and said oxidant plenum, further comprising a top, a bottom, a first side, and a second side;
d. a channel formed using said porous substrate, wherein said channel comprises a first channel wall and a second channel wall;
e. an anode formed from a first catalyst layer disposed on the porous substrate of said first channel wall;
f. a cathode formed from a second catalyst layer disposed on the porous substrate of said second channel wall;
g. electrolyte disposed in at least a portion of said channel contacting the anode and the cathode preventing transfer of fuel to the cathode and preventing transfer of oxidant to the anode;
h. a first coating disposed on at least a portion of said porous substrate to prevent fuel from entering at least a portion of said porous substrate;
i. a second coating disposed on at least a portion of said porous substrate to prevent oxidant from entering at least a portion of said porous substrate;
j. a first sealant barrier disposed on the first side and the second sealant barrier disposed on the second side;
k. a positive electrical connection disposed on said first side; and

1. a negative electrical connection disposed on said second side; and wherein the resulting fuel cell generates current to drive an external load.

2. The fuel cell of claim 1, wherein said anode formed from said first catalyst layer is disposed in the porous substrate of said first channel wall; and said cathode formed from said second catalyst layer is disposed in the porous substrate of said second channel wall.

3. The fuel cell of claim 2, wherein said first and second catalyst layers are disposed in the porous substrate from a minimum depth to cause catalytic activity to a maximum depth selected from the group: a distance from the first channel wall to the first side, and a distance from the second channel wall to the second side.

4. The fuel cell of claim 1, wherein said first sealant barrier is disposed on the first side opposite the anode, and the second sealant barner is disposed on the second side opposite the cathode.

5. The fuel cell of claim 1, wherein said channel is formed within said porous substrate

6. The fuel cell of claim 5, wherein said channel is formed using a technique selected from the group: cutting, ablating, molding, etching, extruding, embossing, laminating, embedding, melting, and combinations thereof

7. The fuel cell of claim 1, wherein said channel is undulating.

8. The fuel cell of claim 1, wherein said channel is in at least three planes.

9. The fuel cell of claim 1, wherein said oxidant comprises a member of the group, pure oxygen, gas containing oxygen, air, oxygen enriched air, and combinations thereof.

10. The fuel cell of claim 1, wherein said fuel comprises a member of the group:
pure hydrogen, gas containing hydrogen, formic acid, an aqueous solution comprising a member of the group: ammonia, methanol, ethanol, and sodium borohydride and combinations thereof.

11. The fuel cell of claim 1, wherein said porous substrate comprises a planar shape.

12. The fuel cell of claim 1, wherein said porous substrate comprises a shape that encloses a volume.

13. The fuel cell of claim 12, wherein said porous substrate shape comprises a cylinder.

14. The fuel cell of claim 1, wherein said porous substrate is a conductive material.

15. The fuel cell of claim 1 wherein said porous substrate comprises a member of the group: a metal foam, graphite, graphite composite, at least one silicon wafer, sintered polytetrafluoroethylene, crystalline polymers, composites of crystalline polymer, reinforced phenolic resin, carbon cloth, carbon foam, carbon aerogel, ceramic, ceramic composites, composites of carbon and polymers, ceramic and glass composites, recycled organic material, and combinations thereof.

16. The fuel cell of claim 1, further comprises a support member disposed between the first channel wall and the second channel wall, and said support member comprises a member of the group: silicon, graphite, graphite composite, polytetrafluoroethylene, polymethamethacrylate, crystalline polymers, crystalline copolymers, cross-linked polymers thereof, wood, and combinations thereof.

17. The fuel cell of claim 1, further comprising a fuel plenum outlet connected to the fuel plenum.

18. The fuel cell of claim 1, further comprising a fuel plenum inlet connected to the fuel plenum.

19. The fuel cell of claim 1, further comprising an oxidant plenum inlet in communication with the oxidant plenum.

20. The fuel cell of claim 1, further comprising an oxidant plenum outlet in communication with the oxidant plenum.

21. The fuel cell of claim 1, wherein said fuel plenum comprises a permeable material.

22. The fuel cell of claim 1, wherein said fuel plenum comprises a solid material with a flow field.

23. The fuel cell of claim 1, wherein said fuel plenum is open to an ambient environment.

24. The fuel cell of claim 1, wherein said electrolyte is a member of the group comprising: a perfluoronated polymer containing sulphonic groups, an aqueous acidic solution having a ph of at most 4, an aqueous alkaline solution having a ph greater than 7, and combinations thereof.

25. The fuel cell of claim 1, wherein said first coating and said second coating are the same material.

26. The fuel cell of claim 1, wherein said first coating and said second coating are different materials.

27. The fuel cell of claim 1, wherein at least one of said coatings can comprise a member of the group: polymer coating, epoxies, polytetrafluoro ethylene, polymethyl methacrylate, polyethylene, polypropylene, polybutylene, and copolymers thereof, cross-linked polymers thereof, conductive metal, and combinations thereof.

28. The fuel cell of claim 1, wherein at least one of said catalyst layers is a member of the group: noble metals, alloys comprising noble metals, platinum, alloys of platinum, ruthenium, alloys of ruthenium, and combinations thereof.

29. The fuel cell of claim 28, wherein at least one of said catalyst layers comprises a ternary alloy comprising at least one noble metal.

30. The fuel cell of claim 28, wherein at least one of said catalyst layers comprises platinum.

31. The fuel cell of claim 28, wherein at least one of said catalyst layers comprises a platinum-ruthenium alloy.

32. The fuel cell of claim 28, wherein at least one of said catalyst layers has a different catalyst loading quantity from the other catalyst layer.

33. The fuel cell of claim 1, wherein said channel has a dimension ranging from 1 micron to 10 cm in height, 1 manometer to 1 mm in width, and from 1 manometer to 100 meters in length.

34. The fuel cell of claim 1, wherein said fuel cell produces a voltage between approximately 0.25 volts and approximately 4 volts.

35. The fuel cell of claim 1, wherein said fuel plenum has a rectangular cross-section.

36. The fuel cell of claim 1, wherein said porous substrate communicating with said fuel plenum further comprises a horizontal axis, and said electrolyte disposed in said channel is oriented at an angle perpendicular to said horizontal axis.

37. The fuel cell of claim 1, wherein said oxygen plenum comprises a permeable material.

38. The fuel cell of claim 1, wherein said oxygen plenum comprises a solid material with a flow field.

39. The fuel cell of claim 1, wherein said oxygen plenum is open to an ambient environment.

40. A fuel cell layer for connecting to an external load comprising at least two fuel cells of claim 1.

41. The fuel cell layer of claim 40, wherein said anodes formed from said first catalyst layers are disposed in the porous substrate of said first channel walls;

and said cathodes formed from said second catalyst layers are disposed in the porous substrate of said second channel walls.

42. The fuel cell layer of claim 40, wherein said first and second catalyst layers are disposed in the porous substrates at least at a minimum depth to cause catalytic activity.

43. The fuel cell layer of claim 40, wherein said channels are formed within said porous substrates.

44. The fuel cell layer of claim 43, wherein said channels are formed using a technique selected from the group: cutting, ablating, molding, etching, extruding, embossing, laminating, embedding, melting, and combinations thereof.

45. The fuel cell layer of claim 40, wherein at least one of said channels is undulating.

46. The fuel cell layer of claim 40, wherein at least one of said channels is in at least three planes.

47. The fuel cell layer of claim 40, wherein at least one of said fuel cells further comprises: a support member disposed between the first channel wall and the second channel wall, and said support member comprises a member of the group: silicon, graphite, graphite composite, polytetrafluoroethylene, polymethamethacrylate, crystalline polymers, crystalline copolymers, cross-linked polymers thereof, wood, and combinations thereof.

48. The fuel cell layer of claim 40, wherein at least one of said fuel cells comprises an electrolyte selected from the group comprising: a perfluoronated polymer containing sulphonic groups, an aqueous acidic solution having a ph of greater than 7, an aqueous alkaline solution having a ph of at most 4, and combinations thereof.

49. The fuel cell layer of claim 40, wherein at least one of said coatings can comprise a member of the group: polymer coating, epoxies, polytetrafluoro ethylene, polymethyl methacrylate, polyethylene, polypropylene, polybutylene, and copolymers thereof, cross-linked polymers thereof, conductive metal and combinations thereof.

50. The fuel cell layer of claim 40, wherein at least one of said catalyst layers is a member of the group, noble metals, alloys comprising noble metals, platinum, alloys of platinum, ruthenium, alloys of ruthenium, and combinations thereof.

51. The fuel cell layer of claim 50, wherein at least one of said catalyst layers is a ternary alloys comprising at least one noble metal.

52. The fuel cell layer of claim 50, wherein at least one of said catalyst layers is platinum.

53. The fuel cell layer of claim 50, wherein at least one of said catalyst layers is a platinum-ruthenium alloy.

54. The fuel cell layer of claim 50, wherein at least one of said catalyst layers has a different catalyst loading quantity from other catalyst layers.

55. The fuel cell layer of claim 40, wherein at least one of said channels has a dimension ranging from 1 micron to 10 cm in height, 1 nanometer to 1 mm in width, and from 1 nanometer to 100 meters in length.

56. The fuel cell layer of claim 40, wherein each fuel cell layer produces a voltage between approximately 0.25 volts and approximately 2500 volts.

57. The fuel cell layer of claim 40, wherein said fuel cell layer comprises between 1 and 5000 fuel cells.

58. The fuel cell layer of claim 57, wherein said fuel cell layer comprises between 75 and 150 fuel cells.

59. A fuel cell layer comprising at least two connected fuel cells of claim 1.

60. The fuel cell layer of claim 59, wherein said anodes formed from said first catalyst layers are disposed in the porous substrate of said first channel walls;
and said cathodes formed from said second catalyst layers are disposed in the porous substrate of said second channel walls.

61. The fuel cell layer of claim 60, wherein said first and second catalyst layers are disposed in the porous substrates at least at a minimum depth to cause catalytic activity.

62. The fuel cell layer of claim 59, wherein said channels are formed within said porous substrates.

63. The fuel cell layer of claim 62, wherein said channels are formed using a technique selected from the group: cutting, ablating, molding, etching, extruding, embossing, laminating, embedding, melting, and combinations thereof.

64. The fuel cell layer of claim 59, wherein at least one of said channels is undulating.

65. The fuel cell layer of claim 59, wherein at least one of said channels is in at least three planes.

66. The fuel cell layer of claim 59, wherein at least one of said porous substrates comprises a planar shape.

67. The fuel cell layer of claim 59, wherein said plurality of fuel cells comprise a shape that encloses a volume.

68. The fuel cell layer of claim 59, wherein said shape of said plurality of fuel cells comprises a cylinder.

69. The fuel cell layer of claim 59, wherein at least one of said porous substrates is a conductive material.

70. The fuel cell layer of claim 59, wherein at least one of said porous substrates comprises a member of the group: a metal foam, graphite, graphite composite, at least one silicon wafer, sintered polytetrafluoroethylene, crystalline polymers, composites of crystalline polymer, reinforced phenolic resin, carbon cloth, carbon foam, carbon aerogel, ceramic, ceramic composites, composites of carbon and polymers, ceramic and glass composites, recycled organic material, and combinations thereof.

71. The fuel cell layer of claim 59, wherein at least one of said fuel cells further comprises: a support member disposed between the first channel wall and the second channel wall, and said support member comprises a member of the group: silicon, graphite, graphite composite, polytetrafluoroethylene, polymethamethacrylate, crystalline polymers, crystalline copolymers, cross-linked polymers thereof, wood, and combinations thereof.

72. The fuel cell layer of claim 59, wherein at least one of said fuel cells comprises an electrolyte selected from the group comprising: a perfluoronated polymer containing sulphonic groups, an aqueous acidic solution having a ph of greater than 7, an aqueous alkaline solution having a ph of at most 4, and combinations thereof.

73. The fuel cell layer of claim 59, wherein at least one of said fuel cells comprises a first coating and a second coating of the same material.

74. The fuel cell layer of claim 59, wherein at least one of said fuel cells comprises a first coating and a second coating of different materials.

75. The fuel cell layer of claim 59, wherein at least one of said coatings can comprise a member of the group: polymer coating, epoxies, polytetrafluoro ethylene, polymethyl methacrylate, polyethylene, polypropylene, polybutylene, and copolymers thereof, cross-linked polymers thereof, conductive metal and combinations thereof.

76. The fuel cell layer of claim 59, wherein at least one of said catalyst layers is a member of the group, noble metals, alloys comprising noble metals, platinum, alloys of platinum, ruthenium, alloys of ruthenium, and combinations thereof.

77. The fuel cell layer of claim 76, wherein at least one of said catalyst layers is a ternary alloys comprising at least one noble metal.

78. The fuel cell layer of claim 76, wherein at least one of said catalyst layers is platinum.

79. The fuel cell layer of claim 76, wherein at least one of said catalyst layers is a platinum-ruthenium alloy.

80. The fuel cell layer of claim 76, wherein at least one of said catalyst layers has a different catalyst loading quantity from other catalyst layers.

81. The fuel cell layer of claim 59, wherein at least one of said channels has a dimension ranging from 1 micron to 10 cm in height, 1 manometer to 1 mm in width, and from 1 manometer to 100 meters in length.

82. The fuel cell layer of claim 59, wherein said fuel cell layer produces a voltage between approximately 0.25 volts and approximately 2500 volts.

83. The fuel cell layer of claim 59, wherein said fuel cell layer comprises between 1 and 5000 joined fuel cells.

84. The fuel cell layer of claim 83, wherein said fuel cell layer comprises between 75 and 150 joined fuel cells.

85. A method for making a fuel cell layer comprising the steps of:
a. forming a porous substrate comprising a top and bottom, a first side and a second side;
b. coating at least a portion of said top with a first coating;
c. coating at least a portion of said bottom with a second coating;
d. forming a plurality of distinct channels using the porous substrate, wherein each distinct channel comprises a first channel wall and a second channel wall;
e. forming a plurality of anodes by depositing a plurality of first catalyst layers on said first channel walls;

f. forming a plurality of cathodes by depositing a plurality of second catalyst layers in said second channel walls;
g. disposing electrolyte in at least a portion of each distinct channel;
h. disposing a first sealant barrier on at least a portion of said first side;
i. disposing a second sealant barrier on at least a portion of said second side;
j. forming a plurality of third sealant barriers between each of said distinct channels creating a plurality of independent fuel cells adjacent each other in the porous substrate;
k. attaching a positive electrical connection to the first side of said porous substrate;
l. attaching a negative electrical connection to said second side of said porous substrate;
m. attaching a fuel cell positive electrical connection to each independent fuel cells;
n. attaching a fuel cell negative electrical connection to each independent fuel cell forming a fuel cell layer; and o. disposing a sealant barrier around at least a portion of said fuel cell layer.

86. The method of claim 85, wherein the porous substrate is formed by casting and then by baking.

87. The method of claim 85, wherein the porous substrate is formed by slicing thin layers from a preformed brick.

88. The method of claim 85, wherein the porous substrate is formed by molding.

89. The method of claim 85, the porous substrate is formed by extruding.

90. The method of claim 85, wherein the porous substrate is formed in a non-planar shape prior to forming each distinct channel.

91. The method of claim 85, wherein said porous substrate is formed into a shape that encloses a volume prior to forming each distinct channel.

92. The method of claim 85, further comprising using a material for said first coating that differs from said second coating.

93. The method of claim 85, further comprising using a material for said first coating that is the same as the second coating.

94. The method of claim 85, further comprising using a coating selected from the group: conductive metal, epoxies, polymer coatings, polytetrafluroethylene, polymethylmethacrylate, polyethylene, polypropylene, polybutylene, and copolymers thereof, and cross-linked polymers thereof, and combinations thereof.

95. The method of claim 94, wherein said coating is a metal coating and said metal coating is disposed on said top by a thin film deposition process.

96. The method of claim 95, wherein said thin film deposition method includes a member of the group comprising: sputtering, electroless plating, electroplating, soldering, physical vapor deposition, chemical vapor deposition.

97. The method of claim 94, wherein said coating is an epoxy coating, and said epoxy coating is disposed on said top by a method selected from the group:
screen printing, ink jet printing, spreading with a spatula, spray gun deposition, vacuum bagging and combinations thereof.

98. The method of claim 85, further comprising the step of masking said porous substrate prior to coating said substrate top and bottom.

99. The method of claim 85, further comprising the step of inserting a support member between each said first channel wall and said second channel wall.

100. The method of claim 85, further comprising the step of selecting removing a portion of the coating deposited on the top and bottom prior to adding said electrolyte.

101. The method of claim 85, further comprising forming between one and 250 or more distinct channels in said porous substrate.

102. The method of claim 85, wherein said step of forming said distinct channels is by a method selected from the group: embossing, ablating, etching, extruding, laminating, embedding, melting, molding, cutting and combinations thereof.

103. The method of claim 102, wherein said etching is by a method selected from the group: laser etching, deep reactive ion etching, and alkaline etching.

104. The method of claim 85, further comprising using a material for said sealant barriers which is selected from the group comprising: silicon, epoxy, metals, polypropylene, polyethylene, polybutylene, and copolymers thereof, composites thereof and combinations thereof.

105. The method of claim 104, further comprising using a material for said support member selected from the group comprising: silicon, graphite, graphite composite, polytetrafluroethylen, polymethylmethacrylate, crystalline polymers, crystalline copolymers, crosslinked polymers thereof, wood, and combinations thereof.

106. The method of claim 85, further comprising using an electrolyte selected from the group comprising: a perfluoronated polymer containing sulphonic groups, an aqueous acidic solution having a ph of greater than 7, an aqueous alkaline solution having a ph of at most 4 and combinations thereof.

107. The method of claim 106, wherein said electrolyte is deposited in said distinct channels by a method comprising a member of the group: pressure injection, vacuum forming, hot embossing, and combinations thereof.

108. The method of claim 85, wherein said first and second catalyst layers are deposited to a minimum thickness to cause catalytic activity.

109. The method of claim 85, wherein said step of depositing first and second catalyst layers on the channel walls is replaced with the step of forming the first and second catalyst layers in the channel walls.

110. The method of claim 85, wherein the step of forming said anodes and said cathodes from said first and second catalyst layers comprises using a member of the group: noble metals, alloys comprising noble metals, platinum, alloys of platinum, ruthenium, alloys of ruthenium and combinations thereof.

111. The method of claim 85, wherein each said distinct channel is a member of the group comprising: an undulating channel, a straight channel, and irregular channel.

112. The method of claim 111, wherein at least one of said undulating channels is of a sinusoidal shape.

113. The method of claim 111, wherein at least one of said straight channels is of a shape that follows a straight line.

114. The method of claim 111, wherein at least one of said irregular channels is of a shape that is in at least three planes.

115. The method of claim 85, wherein said step of forming said porous substrate comprises using a material selected from the group: metal foam, graphite, graphite composite, at least one silicon wafer, sintered polytetrafluroethylene, crystalline polymers, composites of crystalline polymers, reinforced phenolic resin, carbon cloth, carbon foam, carbon aerogel, ceramic, ceramic composites, composites of carbon and polymers, ceramic and glass composites, recycled organic material, and combinations thereof.

116. The method of claim 85, wherein said fuel cell positive electrical connections and said fuel cell negative electrical connections of said independent fuel cells in the fuel cell layer are connected in series.

117. The method of claim 85, wherein said fuel cell positive electrical connections and said fuel cell negative electrical connections of said fuel cells in the fuel cell layer are connected in parallel.

118. The method of claim 85, wherein said fuel cell positive electrical connections and said fuel cell negative electrical connections of said fuel cells in the fuel cell layer are connected a combination of in series and in parallel.

119. A micro structured fuel cell system comprising: a fuel cell layer comprising an anode side and a cathode side, a positive end and a negative end, and at least one surface disposed between the positive end and the negative end, and at least one electronic system mounted on said at least one surface.

120. The system of claim 119, wherein said electronic system is a cellular phone.

121. The system of claim 119, wherein said electronic system is selected from the group comprising: a PDA, a satellite phone, a laptop computer, portable DVD, portable CD player, portable personal care electronics, portable boom boxes, portable televisions, radar, radio transmitters, radar detectors, and combinations thereof.

122. The system of claim 119, wherein said electronic system is powered by the electricity produced by the fuel cell layer on which the system is mounted.

123. The system of claim 119, wherein said electronic system serves an ancillary function for fuel cell operation.

124. The system of claim 123, wherein said ancillary function is a member of the group comprising: fuel cell performance monitoring, fuel cell control, fuel cell fault diagnostics, fuel cell performance optimization, fuel cell performance recording and combinations thereof.

125. The system of claim 119, wherein a plurality of fuel cell layers comprises said system.

126. The system of claim 125, wherein at least two electronic systems are mounted, one on each side of said fuel cell layer.

127. A multiple fuel cell layer structure comprising:
a. a plurality of fuel cell layers, each fuel cell layer comprising an anode side and a cathode side, a positive end and a negative end, and wherein a first fuel cell layer is stacked on top of a second fuel cell layer such that the anode side of the first fuel cell layer and the anode side of the second fuel cell layer adjoin, a third fuel cell layer is stacked on the second fuel cell layer such that the third fuel cell layer cathode side adjoins the second fuel cell layer cathode side forming a stack with adjacent fuel cell layers, additional fuel cell layers can then be disposed on said first, second and third fuel cell layers in a like manner;
b. at least one seal disposed between said adjacent fuel cell layers forming at least one plenum;
c. a positive connector for connecting said stack to an outside load; and d. a negative connector for connecting said stack to said outside load;
such that when fuel is presented to the anode sides of the plurality of fuel cell layers, and oxidant is presented to the cathode sides of the plurality of fuel cell layers current is produced to drive said outside load.

128. The multiple fuel cell layer structure of claim 127, wherein said at least one plenum is a member of the group: fuel plenum, an oxidant plenum and combinations thereof.

129. The multiple fuel cell layer structure of claim 127, wherein said at least one plenum is a permeable material.

130. The multiple fuel cell layer structure of claim 127, wherein said at least one plenum is a solid material with a flow field.

131. The multiple fuel cell layer structure of claim 127, wherein said at least one plenum is open to an ambient environment.

132. The multiple fuel cell layer structure of claim 127, wherein said positive and negative ends are connected in series between the positive and negative connectors.

133. The multiple fuel cell layer structure of claim 127, wherein said positive ends and negative ends are connected in parallel to the positive and negative connectors.

134. The multiple fuel cell layer structure of claim 127, wherein said positive ends and said negative ends are connected in a combination of in series and in parallel between the positive and negative connectors.

135. A multiple fuel cell layer structure comprising:
a. a plurality of fuel cell layers, each fuel cell layer comprising an anode side and a cathode side, a positive end and a negative end, and wherein a first fuel cell layer is stacked on top of a second fuel cell layer such that the anode side of the first fuel cell layer and the anode side of the second fuel cell layer adjoin, a third fuel cell layer is stacked on the second fuel cell layer such that the third fuel cell layer cathode side adjoins the second fuel cell layer cathode side forming a stack with adjacent fuel cell layers, additional fuel cell layers can then be disposed on said first, second and third fuel cell layers in a like manner;

b. at least one seal disposed between said adjacent fuel cell layers forming at least one plenum;

c. at least one flow field is formed in at least one fuel cell layer of said stack;

d. a positive connector for connecting said stack to an outside load; and e. a negative connector for connecting said stack to said outside load;
such that when fuel is presented to the anode sides of the plurality of fuel cell layers, and oxidant is presented to the cathode sides of the plurality of fuel cell layers current is produced to drive said outside load.

136. The multiple fuel cell layer structure of claim 135, wherein said at least one plenum is a member of the group: fuel plenum, an oxidant plenum and combinations thereof.

137. The multiple fuel cell layer structure of claim 135, wherein said at least one plenum is a permeable material.

138. The multiple fuel cell layer structure of claim 135, wherein said at least one plenum is a solid material with a flow field.

139. The multiple fuel cell layer structure of claim 138, wherein said at least one plenum is open to an ambient environment.

140. The multiple fuel cell layer structure of claim 135, wherein said positive and negative ends are connected in series between the positive and negative connectors.

141. The multiple fuel cell layer structure of claim 135, wherein said positive ends and negative ends are connected in parallel to the positive and negative connectors.

142. The multiple fuel cell layer structure of claim 135, wherein said positive ends and said negative ends are connected in a combination of in series and in parallel between the positive and negative connectors.

143. The multiple fuel cell layer structure of claim 135, wherein said flow field is formed by a method selected from the group comprising: cutting, ablating, molding, embossing, etching, laminating, embedding, melting and combinations thereof.

144. A bi-level fuel cell layer structure comprising:

a. a first fuel cell layer and a second fuel cell layers, each fuel cell layer comprising an anode side and a cathode side, a positive end and a negative end, and wherein said first fuel cell layer is stacked on top of said second fuel cell layer such that the anode side of the first fuel cell layer and the anode side of the second fuel cell layer adjoin forming a bi-level stack;

b. a seal disposed between said first and second fuel cell layers forming a fuel plenum;

c. a positive connector for connecting said bi-level stack to an outside load; and d. a negative connector for connecting said bi-level stack to said outside load; such that when fuel is introduced to the fuel plenum and the cathode sides are exposed to an oxidant, current is produced to drive said outside load.

145. The bi-level fuel cell layer structure of claim 144, wherein said fuel plenum is a permeable material.

146. The bi-level fuel cell layer structure of claim 144, wherein said fuel plenum is a solid material with a flow field.

147. The bi-level fuel cell layer structure of claim 144, wherein said fuel plenum is open to an ambient environment.

148. The bi-level fuel cell layer structure of claim 144, wherein said positive and negative ends are connected in series between the positive and negative connectors.

149. The bi-level fuel cell layer structure of claim 144, wherein said positive ends and negative ends are connected in parallel to the positive and negative connectors.

150. The bi-level fuel cell layer structure of claim 144, wherein said fuel plenum comprises a volume comprising a hydrogen storage material.

151. The bi-level fuel cell layer structure of claim 144, further comprising at least one flow field formed in at least one fuel cell layer.

152. The bi-level fuel cell layer structure of claim 151, wherein said flow field is formed by a method selected from the group comprising: cutting, ablating, molding, embossing, etching, laminating, embedding, melting and combinations thereof.

153. A bi-level fuel cell layer structure comprising:
a. a first fuel cell layer and a second fuel cell layers, each fuel cell layer comprising an anode side and a cathode side, a positive end and a negative end, and wherein said first fuel cell layer is stacked on top of said second fuel cell layer such that the cathode side of the first fuel cell layer and the cathode side of the second fuel cell layer adjoin forming a bi-level stack;

b. a seal disposed between said first and second fuel cell layers forming a oxidant plenum;

c. a positive connector for connecting said bi-level stack to an outside load; and d. a negative connector for connecting said bi-level stack to said outside load; such that when oxidant is introduced to the oxidant plenum and the anode sides are exposed to a fuel, current is produced to drive said outside load.

154. The bi-level fuel cell layer structure of claim 153, wherein said oxidant plenum is a permeable material.

155. The bi-level fuel cell layer structure of claim 153, wherein said oxidant plenum is a solid material with a flow field.

156. The bi-level fuel cell layer structure of claim 153, wherein said oxidant plenum is open to an ambient environment.

157. The bi-level fuel cell layer structure of claim 153, wherein said positive and negative ends are connected in series between the positive and negative connectors.

158. The bi-level fuel cell layer structure of claim 153, wherein said positive ends and negative ends are connected in parallel to the positive and negative connectors.

159. The bi-level fuel cell layer structure of claim 153, further comprising at least one flow field formed in at least one fuel cell layer.

160. The bi-level fuel cell layer structure of claim 159, wherein said flow field is formed by a method selected from the group comprising: cutting, ablating, molding, embossing, etching, laminating, embedding, melting and combinations thereof.

161. The apparatus of claim 4, wherein said ball valve further comprises:

a. control means movably disposed within said annulus for controlling movement of the spherical ball;

b. a tubular piston movably mounted in said ball valve for longitudinal extension and retraction, said tubular piston being coupled to said control means for extending said tubular piston relative to said control means signals; and c. a fluid port through which pressurized fluid from a remote source above the tubing hanger may be alternately applied to or exhausted from in order to move the valve closure member between the open and closed positions.

162. The apparatus of claim 5, wherein the radius of curvature of the convex spherical segment is matched with the radius of curvature of the concave spherical segment to permit nesting engagement of the segments.