U.S. patent application number 16/415198 was filed with the patent office on 2019-09-12 for fuel cell device and system.
The applicant listed for this patent is Alan Devoe, Lambert Devoe. Invention is credited to Alan Devoe, Lambert Devoe.
Application Number | 20190280313 16/415198 |
Document ID | / |
Family ID | 39689527 |
Filed Date | 2019-09-12 |
![](/patent/app/20190280313/US20190280313A1-20190912-D00000.png)
![](/patent/app/20190280313/US20190280313A1-20190912-D00001.png)
![](/patent/app/20190280313/US20190280313A1-20190912-D00002.png)
![](/patent/app/20190280313/US20190280313A1-20190912-D00003.png)
![](/patent/app/20190280313/US20190280313A1-20190912-D00004.png)
![](/patent/app/20190280313/US20190280313A1-20190912-D00005.png)
![](/patent/app/20190280313/US20190280313A1-20190912-D00006.png)
![](/patent/app/20190280313/US20190280313A1-20190912-D00007.png)
![](/patent/app/20190280313/US20190280313A1-20190912-D00008.png)
![](/patent/app/20190280313/US20190280313A1-20190912-D00009.png)
![](/patent/app/20190280313/US20190280313A1-20190912-D00010.png)
View All Diagrams
United States Patent
Application |
20190280313 |
Kind Code |
A1 |
Devoe; Alan ; et
al. |
September 12, 2019 |
FUEL CELL DEVICE AND SYSTEM
Abstract
A fuel cell device is provided having an active central portion
with an anode, a cathode, and an electrolyte therebetween. At least
three elongate portions extend from the active central portion,
each having a length substantially greater than a width transverse
thereto such that the elongate portions each have a coefficient of
thermal expansion having a dominant axis that is coextensive with
its length. A fuel passage extends from a fuel inlet in a first
elongate portion into the active central portion in association
with the anode, and an oxidizer passage extends from an oxidizer
inlet in a second elongate portion into the active central portion
in association with the cathode. A gas passage extends between an
opening in the third elongate portion and the active central
portion. For example, the passage in the third elongate portion may
be an exhaust passage for the spent fuel and/or oxidizer
gasses.
Inventors: |
Devoe; Alan; (La Jolla,
CA) ; Devoe; Lambert; (San Diego, CA) |
|
Applicant: |
Name |
City |
State |
Country |
Type |
Devoe; Alan
Devoe; Lambert |
La Jolla
San Diego |
CA
CA |
US
US |
|
|
Family ID: |
39689527 |
Appl. No.: |
16/415198 |
Filed: |
May 17, 2019 |
Related U.S. Patent Documents
|
|
|
|
|
|
Application
Number |
Filing Date |
Patent Number |
|
|
15174076 |
Jun 6, 2016 |
10312530 |
|
|
16415198 |
|
|
|
|
14270787 |
May 6, 2014 |
9362572 |
|
|
15174076 |
|
|
|
|
13832382 |
Mar 15, 2013 |
8715879 |
|
|
14270787 |
|
|
|
|
13236223 |
Sep 19, 2011 |
8409764 |
|
|
13832382 |
|
|
|
|
12117622 |
May 8, 2008 |
8278013 |
|
|
13236223 |
|
|
|
|
60917262 |
May 10, 2007 |
|
|
|
Current U.S.
Class: |
1/1 |
Current CPC
Class: |
H01M 8/124 20130101;
H01M 8/2435 20130101; H01M 8/2404 20160201; H01M 8/1213 20130101;
H01M 8/002 20130101; H01M 8/0258 20130101; Y10T 156/10 20150115;
H01M 8/243 20130101; H01M 8/1231 20160201; H01M 8/0202 20130101;
H01M 8/0271 20130101; H01M 8/0297 20130101; H01M 8/2457 20160201;
H01M 2008/1293 20130101; H01M 8/04067 20130101; Y02P 70/50
20151101; H01M 8/2425 20130101; H01M 8/04007 20130101; H01M 8/2432
20160201; Y02P 70/56 20151101 |
International
Class: |
H01M 8/04007 20060101
H01M008/04007; H01M 8/2404 20060101 H01M008/2404; H01M 8/2432
20060101 H01M008/2432; H01M 8/2425 20060101 H01M008/2425; H01M
8/243 20060101 H01M008/243; H01M 8/2457 20060101 H01M008/2457; H01M
8/0271 20060101 H01M008/0271; H01M 8/0258 20060101 H01M008/0258;
H01M 8/00 20060101 H01M008/00; H01M 8/1231 20060101 H01M008/1231;
H01M 8/124 20060101 H01M008/124; H01M 8/1213 20060101 H01M008/1213;
H01M 8/0202 20060101 H01M008/0202; H01M 8/0297 20060101
H01M008/0297; H01M 8/2435 20060101 H01M008/2435 |
Claims
1. A fuel cell device comprising: an elongate ceramic substrate
having an exterior surface, an interior solid ceramic support
structure, and a length that is the greatest dimension whereby the
elongate ceramic substrate exhibits thermal expansion along a
dominant axis that is coextensive with the length, a reaction zone
along a first portion of the length configured to be exposed to a
heat source to heat the reaction zone to an operating reaction
temperature, and at least one cold zone along a second portion of
the length configured to be shielded from the heat source to remain
at a temperature below the operating reaction temperature when the
reaction zone is heated; an electrolyte disposed between a porous
anode and a porous cathode in the reaction zone, the electrolyte,
anode and cathode extending within the interior solid ceramic
support structure, the electrolyte being monolithic with the
interior solid ceramic support structure; a fuel passage associated
with the porous anode and extending within the interior solid
ceramic support structure from the at least one cold zone through
the reaction zone; an oxidizer passage associated with the porous
cathode and extending within the interior solid ceramic support
structure from the at least one cold zone through the reaction
zone; and a high-density current collector positioned at least
partially recessed into a surface portion of each of the porous
anode and porous cathode and exposed in the respective fuel and
oxidizer passages.
2. The fuel cell device of claim 1 wherein the porous anode and its
high-density current collector and the porous cathode and its
high-density current collector each have an electrical pathway
extending to the exterior surface in the at least one cold zone for
electrical connection at the temperature below the operating
reaction temperature.
3. The fuel cell device of claim 2 further comprising a negative
voltage connection to the exterior surface in the at least one cold
zone in electrical contact with the electrical pathway of the anode
and its high-density current collector; and a positive voltage
connection to the exterior surface in the at least one cold zone in
electrical contact with the electrical pathway of the cathode and
its high-density current collector.
4. The fuel cell device of claim 3 wherein the electrical pathways
each extend to the exterior surface in the reaction zone and
exterior surface metallizations are positioned from the exterior
surface in the reaction zone to the exterior surface in the at
least one cold zone.
5. The fuel cell device of claim 1 wherein the high-density current
collectors have a hatch pattern of intersecting lines with open
spaces between lines.
6. The fuel cell device of claim 5 wherein the high-density current
collectors are fully recessed into the surface portions of the
respective porous anode and porous cathode to form a planar surface
exposed within each of the respective fuel and oxidizer
passages.
7. The fuel cell device of claim 5 wherein the high-density current
collectors are only partially recessed into the surface portions of
the respective porous anode and porous cathode such that a first
portion of each of the high-density current collectors are
positioned within the respective porous anode and porous cathode
and a second portion of each of the high-density current collectors
protrude into the respective fuel and oxidizer passages.
8. The fuel cell device of claim 1 wherein at least one cold zone
includes first and second cold zones positioned at respective first
and second ends of the elongate ceramic substrate with the reaction
zone positioned between the first and second cold zones.
Description
CROSS-REFERENCE TO RELATED APPLICATIONS
[0001] This application is a divisional of U.S. patent application
Ser. No. 15/174,076 (Attorney Docket No. DEVOFC-05US2), filed Jun.
6, 2016, which is a continuation of U.S. Pat. No. 9,362,572
(Attorney Docket No. DEVOFC-05CO2), issued Jun. 7, 2016, which is a
continuation of U.S. Pat. No. 8,715,879 (Attorney Docket No.
DEVOFC-05C0) issued May 6, 2014, which is a continuation of U.S.
Patent U.S. Pat. No. 8,409,764 (Attorney Docket No. DEVOFC-05DV3)
issued Apr. 2, 2013, which is a divisional of U.S. Pat. No.
8,278,013 (Attorney Docket No. DEVOFC-05US1) issued Oct. 2, 2012,
which claims the benefit of and priority to Provisional Application
Ser. No. 60/917,262 (Attorney Docket No. DEVOFC-05P) filed on May
10, 2007. All matters referenced are entitled FUEL CELL DEVICE AND
SYSTEM, the disclosures of which are incorporated herein by
reference in their entirety as if completely set forth herein
below.
FIELD OF THE INVENTION
[0002] This invention relates to fuel cell devices and systems, and
methods of manufacturing the devices, and more particularly, to a
fuel cell device in the form of a multi-layer monolithic Fuel Cell
Stick.TM..
BACKGROUND OF INVENTION
[0003] Ceramic tubes have found a use in the manufacture of Solid
Oxide Fuel Cells (SOFCs). There are several types of fuel cells,
each offering a different mechanism of converting fuel and air to
produce electricity without combustion. In SOFCs, the barrier layer
(the "electrolyte") between the fuel and the air is a ceramic
layer, which allows oxygen atoms to migrate through the layer to
complete a chemical reaction. Because ceramic is a poor conductor
of oxygen atoms at room temperature, the fuel cell is operated at
700.degree. C. to 1000.degree. C., and the ceramic layer is made as
thin as possible.
[0004] Early tubular SOFCs were produced by the Westinghouse
Corporation using long, fairly large diameter, extruded tubes of
zirconia ceramic. Typical tube lengths were several feet long, with
tube diameters ranging from 1/4 inch to 1/2 inch. A complete
structure for a fuel cell typically contained roughly ten tubes.
Over time, researchers and industry groups settled on a formula for
the zirconia ceramic which contains 8 mol % Y.sub.2O.sub.3. This
material is made by, among others, Tosoh of Japan as product
TZ-8Y.
[0005] Another method of making SOFCs makes use of flat plates of
zirconia, stacked together with other anodes and cathodes, to
achieve the fuel cell structure. Compared to the tall, narrow
devices envisioned by Westinghouse, these flat plate structures can
be cube shaped, 6 to 8 inches on an edge, with a clamping mechanism
to hold the entire stack together.
[0006] A still newer method envisions using larger quantities of
small diameter tubes having very thin walls. The use of thin walled
ceramic is important in SOFCs because the transfer rate of oxygen
ions is limited by distance and temperature. If a thinner layer of
zirconia is used, the final device can be operated at a lower
temperature while maintaining the same efficiency. Literature
describes the need to make ceramic tubes at 150 .mu.m or less wall
thickness.
[0007] There are several main technical problems that have stymied
the successful implementation of SOFCs. One problem is the need to
prevent cracking of the ceramic elements during heating. For this,
the tubular SOFC approach is better than the competing "stack" type
(made from large, flat ceramic plates) because the tube is
essentially one-dimensional. The tube can get hot in the middle,
for example, and expand but not crack. For example, a tube furnace
can heat a 36'' long alumina tube, 4'' in diameter, and it will
become red hot in the center, and cold enough to touch at the ends.
Because the tube is heated evenly in the center section, that
center section expands, making the tube become longer, but it does
not crack. A ceramic plate heated in the center only would quickly
break into pieces because the center expands while the outside
remains the same size. The key property of the tube is that it is
uniaxial, or one-dimensional.
[0008] A second key challenge is to make contact to the SOFC. The
SOFC ideally operates at high temperature (typically
700-1000.degree. C.), yet it also needs to be connected to the
outside world for air and fuel, and also to make electrical
connection. Ideally, one would like to connect at room temperature.
Connecting at high temperature is problematic because organic
material cannot be used, so one must use glass seals or mechanical
seals. These are unreliable, in part, because of expansion
problems. They can also be expensive.
[0009] Thus, previous SOFC systems have difficulty with at least
the two problems cited above. The plate technology also has
difficulty with the edges of the plates in terms of sealing the gas
ports, and has difficulty with fast heating, as well as cracking.
The tube approach resolves the cracking issue but still has other
problems. An SOFC tube is useful as a gas container only. To work
it must be used inside a larger air container. This is bulky. A key
challenge of using tubes is that you must apply both heat and air
to the outside of the tube; air to provide the O.sub.2 for the
reaction, and heat to accelerate the reaction. Usually, the heat
would be applied by burning fuel, so instead of applying air with
20% O.sub.2 (typical), the air is actually partially reduced
(partially burned to provide the heat) and this lowers the driving
potential of the cell.
[0010] An SOFC tube is also limited in its scalability. To achieve
greater kV output, more tubes must be added. Each tube is a single
electrolyte layer, such that increases are bulky. The solid
electrolyte tube technology is further limited in terms of
achievable electrolyte thinness. A thinner electrolyte is more
efficient. Electrolyte thickness of 2 .mu.m or even 1 .mu.m would
be optimal for high power, but is very difficult to achieve in
solid electrolyte tubes. It is noted that a single fuel cell area
produces about 0.5 to 1 volt (this is inherent due to the driving
force of the chemical reaction, in the same way that a battery
gives off 1.2 volts), but the current, and therefore the power,
depend on several factors. Higher current will result from factors
that make more oxygen ions migrate across the electrolyte in a
given time. These factors are higher temperature, thinner
electrolyte, and larger area.
SUMMARY OF THE INVENTION
[0011] The present invention relates to a fuel cell system having a
hot zone chamber with a chamber wall of thickness T. One or more
fuel cell devices each comprise an elongate rectangular or tubular
substrate having a length that is the greatest dimension whereby
thermal expansion is exhibited along a dominant axis that is
coextensive with the length, a reaction zone along a first portion
of the length positioned in the hot zone chamber for exposure to an
operating reaction temperature, at least one cold zone along a
second portion of the length extending outside the hot zone chamber
and shielded by the chamber wall so as to remain at a temperature
below the operating reaction temperature, and an electrolyte
disposed between an anode and a cathode in the reaction zone. A
third portion of the length of each fuel cell device equal to
thickness T is positioned within the chamber wall, the third
portion having a maximum dimension L in a plane transverse to the
direction of the length wherein T.gtoreq.1/2 L. A heat source is
coupled to the hot zone chamber for heating the reaction zone to
the operating reaction temperature within the hot zone chamber.
BRIEF DESCRIPTION OF THE DRAWINGS
[0012] The accompanying drawings, which are incorporated in and
constitute a part of this specification, illustrate embodiments of
the invention and, together with a general description of the
invention given above, and the detailed description given below,
serve to explain the invention.
[0013] FIGS. 1 and 1A depict, in side cross-sectional view and top
cross-sectional view, respectively, one embodiment of a basic Fuel
Cell Stick.TM. device of the invention, having a single anode
layer, cathode layer and electrolyte layer, and a hot zone between
two end cold zones.
[0014] FIG. 2 depicts in perspective view a first end of one
embodiment of a Fuel Cell Stick.TM. device of the invention with a
fuel supply tube connected thereto.
[0015] FIG. 3A depicts in perspective view a Fuel Cell Stick.TM.
device according to one embodiment of the invention, but having
modified ends.
[0016] FIG. 3B depicts in perspective view a fuel supply tube
connected to one modified end of the device of FIG. 3A.
[0017] FIG. 4A depicts in perspective view a metallurgical bonding
attachment means to a plurality of Fuel Cell Stick.TM. devices to
make electrical connection to positive and negative voltage nodes
according to one embodiment of the invention.
[0018] FIG. 4B depicts in schematic end view a connection between
multiple Fuel Cell Stick.TM. devices according to one embodiment of
the invention, where each Fuel Cell Stick.TM. device includes a
plurality of anodes and cathodes.
[0019] FIG. 5 depicts in schematic end view a mechanical attachment
means for making the electrical connection to positive and negative
voltage nodes according to one embodiment of the invention.
[0020] FIGS. 6A and 6B depict in perspective views an alternative
embodiment having a single cold zone at one end of a Fuel Cell
Stick.TM. device to which fuel and air supply tubes are attached,
with the other end being in the hot zone.
[0021] FIGS. 7A and 7B are cross-sectional side and top views,
respectively, illustrating a plurality of support pillars in the
air and fuel passages according to one embodiment of the
invention.
[0022] FIGS. 7C and 7D are micrographs depicting the use of
spherical balls in the fuel and air passages as the support pillars
according to another embodiment of the invention.
[0023] FIG. 8A depicts in cross-section one embodiment of the
invention containing two fuel cells connected externally in
parallel.
[0024] FIG. 8B depicts in cross-sectional view another embodiment
of the invention similar to FIG. 8A, but having the two fuel cells
connected internally in parallel through the use of vias.
[0025] FIGS. 9A and 9B depict in cross-sectional views a multi-fuel
cell design according to an embodiment of the invention having
shared anodes and cathodes, where FIG. 9A depicts three fuel cell
layers connected in parallel and FIG. 9B depicts three fuel cells
connected in series.
[0026] FIG. 10 depicts in schematic side view a Fuel Cell Stick.TM.
device according to one embodiment of the invention having a fuel
supply tube connected to a cold end of the device and a side of the
device open in the hot zone to an air passage for supply of heated
air to the device in the hot zone.
[0027] FIG. 10A depicts in schematic side view a variation of the
embodiment of FIG. 10, where the hot zone is positioned between
opposing cold ends.
[0028] FIG. 10B depicts the Fuel Cell Stick.TM. device of FIG. 10A
in top cross-sectional view taken along line 10B-10B.
[0029] FIGS. 11-24 schematically depict various embodiments of the
invention, where FIG. 11 provides a key for the components depicted
in FIGS. 12-24.
[0030] FIGS. 25A and 27A depict in schematic top plan view and FIG.
27B depicts in schematic side view a Fuel Cell Stick.TM. device
according to one embodiment of the invention having a panhandle
design with an elongate section at one cold end and a large surface
area section at the opposing hot end.
[0031] FIGS. 25B and 26A depict in schematic top plan view and FIG.
26B depicts in schematic side view an alternative embodiment of the
panhandle design having two elongate sections at opposing cold ends
with a center large surface area section in a central hot zone.
[0032] FIGS. 28A-28D depict a Fuel Cell Stick.TM. device according
to one embodiment of the invention, having a spiral or rolled,
tubular configuration, where FIGS. 28A-28C depict the unrolled
structure in schematic top view, end view and side view,
respectively, and FIG. 28D depicts the spiral or rolled, tubular
configuration in schematic perspective view.
[0033] FIGS. 29A-29G depict another alternative embodiment of the
invention wherein the Fuel Cell Stick.TM. device has a tubular
concentric form, and where FIG. 29A depicts the device in schematic
isometric view, FIGS. 29B-29E depict cross-sectional views taken
from FIG. 29A, FIG. 29F depicts an end view at the air input end,
and FIG. 29G depicts an end view at the fuel input end.
[0034] FIG. 30A depicts in schematic cross-sectional side view an
embodiment of a Fuel Cell Stick.TM. device of the invention having
an integrated pre-heat zone preceding an active zone in the hot
zone, and FIGS. 30B and 30C depict the device of FIG. 30A in
schematic cross-sectional view taken along lines 30B-30B and
30C-30C, respectively.
[0035] FIGS. 31A-31C are similar to FIGS. 30A-30C, but depict two
cold zones with a central hot zone.
[0036] FIGS. 32A-32B depict in schematic cross-sectional side view
and schematic cross-sectional top view taken along line 32B-32B of
FIG. 32A, respectively, an embodiment similar to that depicted in
FIGS. 31A-31C, but further including pre-heat chambers extending
between the fuel inlet and the fuel passage and between the air
inlet and the air passage, each pre-heat chamber extending from the
cold zone into the pre-heat zone of the hot zone.
[0037] FIGS. 33A-33C depict another embodiment of the invention for
pre-heating the air and fuel, where FIG. 33A is a schematic
cross-sectional side view through the longitudinal center of the
Fuel Cell Stick.TM. device, FIG. 33B is a schematic cross-sectional
top view taken along line 33B-33B of FIG. 33A, and FIG. 33C is a
schematic cross-sectional bottom view taken along line 33C-33C of
FIG. 33A.
[0038] FIGS. 34A and 34B depict in schematic oblique front view and
schematic side view, respectively, an embodiment of the invention
having multiple anodes and cathodes interconnected externally in
series.
[0039] FIG. 35 depicts in schematic side view the structure of FIG.
34B doubled with the two structures connected externally by metal
stripes to provide a series-parallel design.
[0040] FIGS. 36A and 36B depict in schematic side view and
perspective view another embodiment of the invention including
metal stripes to connect anodes and cathodes in series and/or
parallel in the hot zone and long metal stripes extending from the
hot zone to the cold zone for making low temperature connection in
the cold zones to the positive and negative voltage nodes.
[0041] FIG. 37 depicts in schematic isometric view an embodiment
similar to that of FIG. 36B, but having a single cold zone for the
air and fuel supply connections and for the voltage node
connection.
[0042] FIGS. 38A and 38B depict in schematic cross-sectional side
view an embodiment of the invention having multiple exit gaps along
the sides of the device for bake-out of organic material used to
form passages within the structure.
[0043] FIG. 39 depicts in schematic cross-sectional end view
another embodiment of the invention in which anode material is used
as the supporting structure, referred to as an anode-supported
version of a Fuel Cell Stick.TM. device.
[0044] FIGS. 40A and 40B depict in schematic cross-sectional end
view and schematic cross-sectional side view, respectively, an
anode-supported version according to another embodiment of a Fuel
Cell Stick.TM. device of the invention in which an open fuel
passage is eliminated in favor of a porous anode that serves the
function of conveying the fuel through the device.
[0045] FIGS. 41A and 41B depict in schematic cross-sectional end
view and schematic cross-sectional top view, respectively, another
embodiment of an anode-supported version of a Fuel Cell Stick.TM.
device of the invention, in which multiple air passages are
provided within the anode-supporting structure, and a single fuel
passage is provided normal to the multiple air passages.
[0046] FIGS. 42A-42C depict in schematic cross-sectional view a
method for forming an electrode layer in a passage of a Fuel Cell
Stick.TM. device of the invention, according to one embodiment.
[0047] FIG. 43 depicts in schematic cross-sectional side view
another embodiment of the invention in which the electrolyte layer
is provided with an uneven topography to increase the surface area
available to receive an electrode layer.
[0048] FIG. 44 depicts in schematic cross-sectional side view an
alternative embodiment of the invention for providing uneven
topography on the electrolyte layer.
[0049] FIG. 45A depicts in schematic top view and FIG. 45B depicts
in cross-sectional view through the hot zone an embodiment of a
Fuel Cell Stick.TM. device of the invention having a plurality of
fuel cells on each of a left and right side of the device, with a
bridging portion therebetween.
[0050] FIGS. 46A and 46B depict in schematic perspective view and
schematic cross-sectional view, respectively, another embodiment of
a Fuel Cell Stick.TM. device of the invention having large exterior
contact pads to provide a large or wide path of low resistance for
electrons to travel to the cold end of the device.
[0051] FIG. 47 depicts in schematic cross-sectional side view a
Fuel Cell Stick.TM. device according to another embodiment of the
invention having a single exhaust passage for both spent fuel and
air.
[0052] FIGS. 48A-48C depict an alternative embodiment referred to
as an "end-rolled Fuel Cell Stick.TM. device" having a thick
portion and a thin rolled portion, wherein FIG. 48A depicts the
unrolled device in perspective view, FIG. 48B depicts the rolled
device in cross-sectional side view, and FIG. 48C depicts the
rolled device in perspective view.
[0053] FIGS. 49A depicts in schematic cross sectional side view an
embodiment for building a Fuel Cell Stick.TM. device using a wire
between two ceramic layers.
[0054] FIG. 49B depicts in schematic perspective view the device of
FIG. 49A after lamination.
[0055] FIG. 49C depicts in schematic perspective view the device of
FIG. 49B after the wire has been removed.
[0056] FIGS. 50A-50C depict in schematic cross sectional view
another embodiment for building a Fuel Cell Stick.TM. device using
a combination of wire and gap-forming tape.
[0057] FIGS. 51 and 52A depict in schematic perspective view a Fuel
Cell Stick.TM. device passing through a furnace wall.
[0058] FIG. 52B depicts in schematic perspective view the portion
of the Fuel Cell Stick.TM. device of 52B within the bounds of the
furnace wall.
[0059] FIG. 52C depicts in schematic perspective view a portion of
a tubular Fuel Cell Stick.TM. device where it would pass through a
furnace wall.
[0060] FIG. 53 depicts in schematic perspective view a Fuel Cell
Stick.TM. device passing through a furnace wall made up of multiple
layers.
[0061] FIG. 54 depicts in schematic perspective view a Fuel Cell
Stick.TM. device passing through a furnace wall made up of multiple
layers and an air gap.
[0062] FIGS. 55A-55E depict in schematic cross sectional view the
assembly of a Fuel Cell Stick.TM. device having a floating current
collector.
[0063] FIGS. 56A and 56B are micrographs depicting zirconia balls
supporting a floating current collector.
[0064] FIGS. 57A and 57B depict in schematic cross sectional view
the backfilling of the structure of FIG. 55D with anode or cathode
particles suspended in a viscous liquid to form an anode or
cathode.
[0065] FIGS. 58A, 58B, and 58C are micrographs depicting a current
collector nearly causing a blockage of a passage.
[0066] FIG. 59 depicts in schematic cross sectional view current
collectors on the surface of the anode and the cathode.
[0067] FIG. 60 depicts in schematic cross sectional view current
collectors buried in the surface of the anode and the cathode.
[0068] FIGS. 61A-61C depict a method of burying a current collector
in an anode or cathode.
[0069] FIG. 62 is a schematic cross sectional view depicting a
method of achieving an individual layer of electrolyte having two
thicknesses.
[0070] FIG. 62A is a detailed view of FIG. 62.
[0071] FIG. 63 is a micrograph depicting a top view of a current
collector in a hatch pattern.
[0072] FIGS. 64 and 65 are micrographs depicting side and angled
cross-sectional views of a current collector over a porous anode or
cathode.
[0073] FIG. 66A is a schematic cross-sectional view of a tube
slipped over the end of a Fuel Cell Stick.TM. device.
[0074] FIG. 66B is a schematic perspective view of the end of a
Fuel Cell Stick.TM. device of FIG. 66A.
[0075] FIG. 67A is a schematic cross-sectional view of a connector,
including spring electrical contacts, positioned on the end of a
Fuel Cell Stick.TM. device.
[0076] FIG. 67B is a schematic perspective view of the connector of
FIG. 67A.
[0077] FIGS. 68A and 68B are schematic perspective views depicting
Fuel Cell Stick.TM. devices having four points of exit.
[0078] FIG. 69 is a micrograph depicting a current collector trace
that has been recessed into a porous anode or cathode.
[0079] FIG. 70 is a micrograph image depicting a gap left after
removing a carbon-wax sacrificial material.
DETAILED DESCRIPTION
[0080] In one embodiment, the invention provides a SOFC device and
system in which the fuel port and the air port are made in one
monolithic structure. In one embodiment, the SOFC device is an
elongate structure, essentially a relatively flat or rectangular
stick (and thus, referred to as a Fuel Cell Stick.TM. device), in
which the length is considerably greater than the width or
thickness. The Fuel Cell Stick.TM. devices are capable of having
cold ends while the center is hot (cold ends being <300.degree.
C.; hot center being >400.degree. C., and most likely
>700.degree. C.). Slow heat conduction of ceramic can prevent
the hot center from fully heating the colder ends. In addition, the
ends are quickly radiating away any heat that arrives there. The
invention includes the realization that by having cold ends for
connection, it is possible to make easier connection to the anode,
cathode, fuel inlet and H.sub.2O CO.sub.2 outlet, and air inlet and
air outlet. While tubular fuel cell constructions are also capable
of having cold ends with a hot center, the prior art does not take
advantage of this benefit of ceramic tubes, but instead, places the
entire tube in the furnace, or the hot zone, such that high
temperature connections have been required. The prior art
recognizes the complexity and cost of making high temperature
brazed connections for the fuel input, but has not recognized the
solution presented herein. The Fuel Cell Stick.TM. device of the
invention is long and skinny so that it has the thermal property
advantages discussed above that allow it to be heated in the center
and still have cool ends. This makes it structurally sound with
temperature, and makes it relatively easy to connect fuel, air and
electrodes. The Fuel Cell Stick.TM. device is essentially a
stand-alone system, needing only heat, fuel, and air to be added in
order to make electricity. The structure is designed so that these
things can be readily attached.
[0081] The Fuel Cell Stick.TM. device of the invention is a
multi-layer structure and may be made using a multi-layer co-fired
approach, which offers several other advantages. First, the device
is monolithic, which helps to make it structurally sound. Second,
the device lends itself to traditional high volume manufacturing
techniques such as those used in MLCC (multi-layer co-fired
ceramic) production of capacitor chips. (It is believed that
multi-layer capacitor production is the largest volume use of
technical ceramics, and the technology is proven for high volume
manufacturing.) Third, thin electrolyte layers can be achieved
within the structure at no additional cost or complexity.
Electrolyte layers of 2 .mu.m thicknesses are possible using the
MLCC approach, whereas it is hard to imagine a SOFC tube with less
than a 60 .mu.m electrolyte wall thickness. Hence, the Fuel Cell
Stick.TM. device of the invention can be about 30 times more
efficient than a SOFC tube. Finally, the multi-layer Fuel Cell
Stick.TM. devices of the invention could each have many hundreds,
or thousands, of layers, which would offer the largest area and
greatest density.
[0082] Consider the surface area of a SOFC tube of the prior art
versus a Fuel Cell Stick.TM. device of the invention. For example,
consider a 0.25'' diameter tube versus a 0.25''.times.0.25'' Fuel
Cell Stick.TM. device. In the tube, the circumference is
3.14.times.D, or 0.785''. In the 0.25'' Fuel Cell Stick.TM. device,
the usable width of one layer is about 0.2 inch. Therefore, it
takes about 4 layers to give the same area as one tube. These
figures are dramatically different than those for capacitor
technology. The state of the art for Japanese multi-layer
capacitors is currently 600 layers of 2 .mu.m thicknesses. The
Japanese will likely soon launch 1000 layer parts in production,
and they make them now in the laboratory. These chip capacitors
with 600 layers are only 0.060'' (1500 .mu.m). Applying this
manufacturing technology to a Fuel Cell Stick.TM. device of the
invention, in a 0.25'' device having a 2 .mu.m electrolyte
thickness and air/fuel passages with respective cathodes/anodes of
10 .mu.m thickness, it would be feasible to produce a single device
with 529 layers. That would be the equivalent of 132 tubes. Prior
art strategies either add more tubes, increase diameter, and/or
increase tube length to get more power, with result being very
large structures for high power output. The invention, on the other
hand, either adds more layers to a single Fuel Cell Stick.TM.
device to get more power and/or uses thinner layers or passages in
the device, thereby enabling miniaturization for SOFC technology.
Moreover, the benefit in the present invention is a squared effect,
just like in capacitors. When the electrolyte layers are made half
as thick, the power doubles, and then you can fit more layers in
the device so power doubles again.
[0083] Another key feature of the invention is that it would be
easy to link layers internally to increase the output voltage of
the Fuel Cell Stick.TM. device. Assuming 1 volt per layer, 12 volts
output may be obtained by the Fuel Cell Stick.TM. devices of the
invention using via holes to link groups of 12 together. After
that, further connections may link groups of 12 in parallel to
achieve higher current. This can be done with existing methods used
in capacitor chip technology. The critical difference is that the
invention overcomes the brazing and complex wiring that other
technologies must use.
[0084] The invention also provides a greater variety of electrode
options compared to the prior art. Precious metals will work for
both the anodes and cathodes. Silver is cheaper, but for higher
temperature, a blend with Pd, Pt, or Au would be needed, with Pd
possibly being the lowest priced of the three. Much research has
focused on non-precious metal conductors. On the fuel side,
attempts have been made to use nickel, but any exposure to oxygen
will oxidize the metal at high temperature. Conductive ceramics are
also known, and can be used in the invention. In short, the present
invention may utilize any sort of anode/cathode/electrolyte system
that can be sintered.
[0085] In an embodiment of the invention, it is possible that when
a large area of 2 .mu.m tape is unsupported, with air/gas on both
sides, the layer might become fragile. It is envisioned to leave
pillars across the gap. These would look something like pillars in
caves where a stalactite and stalagmite meet. They could be spaced
evenly and frequently, giving much better strength to the
structure.
[0086] For attachment of the gas and air supply, it is envisioned
that the end temperature is below 300.degree. C., for example,
below 150.degree. C., such that high temperature flexible silicone
tubes or latex rubber tubes, for example, may be used to attach to
the Fuel Cell Stick.TM. devices. These flexible tubes can simply
stretch over the end of the device, and thereby form a seal. These
materials are available in the standard McMaster catalog. Silicone
is commonly used at 150.degree. C. or above as an oven gasket,
without losing its properties. The many silicone or latex rubber
tubes of a multi-stick Fuel Cell Stick.TM. system could be
connected to a supply with barb connections.
[0087] The anode material or the cathode material, or both
electrode materials, may be a metal or alloy. Suitable metals and
alloys for anodes and cathodes are known to those of ordinary skill
in the art. Alternatively, one or both electrode materials may be
an electronically conductive green ceramic, which ceramics are also
known to those of ordinary skill in the art. For example, the anode
material may be a partially sintered metallic nickel coated with
yttria-stabilized zirconia, and the cathode material may be a
modified lanthanum manganite, which has a perovskite structure.
[0088] In another embodiment, one or both of the electrode
materials may be a composite of a green ceramic and a conductive
metal present in an amount sufficient to render the composite
conductive. In general, a ceramic matrix becomes electronically
conductive when the metal particles start to touch. The amount of
metal sufficient to render the composite matrix conductive will
vary depending mainly on the metal particle morphology. For
example, the amount of metal will generally need to be higher for
spherical powder metal than for metal flakes. In an exemplary
embodiment, the composite comprises a matrix of the green ceramic
with about 40-90% conductive metal particles dispersed therein. The
green ceramic matrix may be the same or different than the green
ceramic material used for the electrolyte layer.
[0089] In the embodiments in which one or both electrode materials
include a ceramic, i.e., the electronically conductive green
ceramic or the composite, the green ceramic in the electrode
materials and the green ceramic material for the electrolyte may
contain cross-linkable organic binders, such that during
lamination, the pressure is sufficient to cross-link the organic
binder within the layers as well as to link polymer molecular
chains between the layers.
[0090] Reference will now be made to the drawings in which like
numerals are used throughout to refer to like components. Reference
numbers used in the Figures are as follows:
[0091] 10 Full Cell Stick.TM. device
[0092] 11a First end
[0093] 11b Second end
[0094] 12 Fuel inlet
[0095] 13 Fuel pre-heat chamber
[0096] 14 Fuel passage
[0097] 16 Fuel outlet
[0098] 18 Air inlet
[0099] 19 Air pre-heat chamber
[0100] 20 Air passage
[0101] 21 Exhaust passage
[0102] 22 Air outlet
[0103] 24 Anode layer
[0104] 25 Exposed anode portion
[0105] 26 Cathode layer
[0106] 27 Exposed cathode portion
[0107] 28 Electrolyte layer
[0108] 29 Ceramic
[0109] 30 Cold zone (or second temperature)
[0110] 31 Transition zone
[0111] 32 Hot zone (or heated zone or first temperature zone)
[0112] 33a Pre-heat zone
[0113] 33b Active zone
[0114] 34 Fuel supply
[0115] 36 Air supply
[0116] 38 Negative voltage node
[0117] 40 Positive voltage node
[0118] 42 Wire
[0119] 44 Contact pad
[0120] 46 Solder connection
[0121] 48 Spring clip
[0122] 50 Supply tube
[0123] 52 Tie wrap
[0124] 54 Support pillars
[0125] 56 First via
[0126] 58 Second via
[0127] 60 Barrier coating
[0128] 62 Surface particles
[0129] 64 Textured surface layer
[0130] 66 Anode suspension
[0131] 70 Openings
[0132] 72(a,b) Organic material/sacrificial layer
[0133] 80 Left side
[0134] 82 Right side
[0135] 84 Bridging portion
[0136] 90 Bridge
[0137] 92 Wire (physical) Structure
[0138] 94 Gap-forming tape
[0139] 96 Furnace wall
[0140] 96' Multiple-layer furnace wall
[0141] 96'' Multiple-layer furnace wall with air gap
[0142] 98a,b,c Insulation
[0143] 100 Fuel Cell Stick.TM. device
[0144] 102 Elongate section
[0145] 104 Large surface area section
[0146] 106 Elongate section
[0147] 120 Air gap
[0148] 122 Current collector
[0149] 123 Gap
[0150] 124 Electrode particles
[0151] 126 Viscous fluid
[0152] 128 Temporary substrate
[0153] 130 Ceramic tape
[0154] 132 Indentations
[0155] 134 Connector
[0156] 136 Electrical contacts
[0157] 138 Gas flow pathway
[0158] 140 O-ring
[0159] 200 Spiral Tubular Fuel Cell Stick.TM. device
[0160] 300 Concentric Tubular Fuel Cell Stick.TM. device
[0161] 400 End-rolled Fuel Cell Stick.TM. device
[0162] 402 Thick portion
[0163] 404 Thin portion
[0164] 500 Fuel Cell Stick.TM. device
[0165] The terms "zone," "area," and "region" may be used
interchangeably throughout, and are intended to have the same
meaning. Similarly, the terms "passage," "channel," and "path" may
be used interchangeably throughout and the terms "outlet" and
"exit" may be used interchangeably throughout.
[0166] FIGS. 1 and 1A depict, in side cross-sectional view and top
cross-sectional view, respectively, one embodiment of a basic Fuel
Cell Stick.TM. device 10 of the invention, having a single anode
layer 24, cathode layer 26 and electrolyte layer 28, wherein the
device 10 is monolithic. The Fuel Cell Stick.TM. device 10 includes
a fuel inlet 12, a fuel outlet 16 and a fuel passage 14
therebetween. Device 10 further includes an air inlet 18, an air
outlet 22 and an air passage 20 therebetween. The fuel passage 14
and the air passage 20 are in an opposing and parallel relation,
and the flow of fuel from fuel supply 34 through the fuel passage
14 is in a direction opposite to the flow of air from air supply 36
through air passage 20. The electrolyte layer 28 is disposed
between the fuel passage 14 and the air passage 20. The anode layer
24 is disposed between the fuel passage 14 and the electrolyte
layer 28. Similarly, the cathode layer 26 is disposed between the
air passage 20 and the electrolyte layer 28. The remainder of the
Fuel Cell Stick.TM. device 10 comprises ceramic 29, which may be of
the same material as the electrolyte layer 28 or may be a different
but compatible ceramic material. The electrolyte layer 28 is
considered to be that portion of the ceramic lying between opposing
areas of the anode 24 and cathode 26, as indicated by dashed lines.
It is in the electrolyte layer 28 that oxygen ions pass from the
air passage 20 to the fuel passage 14. As shown in FIG. 1, O.sub.2
from the air supply 36 travels through the air passage 20 and is
ionized by the cathode layer 26 to form 2O.sup.-, which travels
through the electrolyte layer 28 and through the anode 24 into the
fuel passage 14 where it reacts with fuel, for example, a
hydrocarbon, from the fuel supply 34 to first form CO and H.sub.2
and then to form H.sub.2O and CO.sub.2. While FIG. 1 depicts the
reaction using a hydrocarbon as the fuel, the invention is not so
limited. Any type of fuel commonly used in SOFCs may be used in the
present invention. Fuel supply 34 may be any hydrocarbon source or
hydrogen source, for example. Methane (CH.sub.4), propane
(C.sub.3H.sub.8) and butane (C.sub.4H.sub.10) are examples of
hydrocarbon fuels.
[0167] For the reaction to occur, heat must be applied to the Fuel
Cell Stick.TM. device 10. In accordance with the invention, the
length of the Fuel Cell Stick.TM. device 10 is long enough that the
device can be divided into a hot zone 32 (or heated zone) in the
center of the device 10 and cold zones 30 at each end 11a and 11b
of the device 10. Between the hot zone 32 and the cold zones 30, a
transition zone 31 exists. The hot zone 32 will typically operate
above 400.degree. C. In exemplary embodiments, the hot zone 32 will
operate at temperatures >600.degree. C., for example
>700.degree. C. The cold zones 30 are not exposed to a heat
source, and due to the length of the Fuel Cell Stick.TM. device 10
and the thermal property advantages of the ceramic materials, heat
dissipates outside the hot zone 32, such that the cold zones 30
have a temperature <300.degree. C. It is believed that heat
transfer from the hot zone 32 down the length of the ceramic to the
end of the cold zone 30 is slow, whereas the heat transfer from the
ceramic material outside the hot zone 32 into the air is relatively
faster. Thus, most of the heat inputted in the hot zone 32 is lost
to the air (mainly in the transition zone 31) before it can reach
the end of the cold zone 30. In exemplary embodiments of the
invention, the cold zones 30 have a temperature <150.degree. C.
In a further exemplary embodiment, the cold zones 30 are at room
temperature. The transition zones 31 have temperatures between the
operating temperature of the hot zone 32 and the temperature of the
cold zones 30, and it is within the transition zones 31 that the
significant amount of heat dissipation occurs.
[0168] Because the dominant coefficient of thermal expansion (CTE)
is along the length of the Fuel Cell Stick.TM. device 10, and is
therefore essentially one-dimensional, fast heating of the center
is permitted without cracking. In exemplary embodiments, the length
of the device 10 is at least 5 times greater than the width and
thickness of the device. In further exemplary embodiments, the
length of the device 10 is at least 10 times greater than the width
and thickness of the device. In yet further exemplary embodiments,
the length of the device 10 is at least 15 times greater than the
width and thickness of the device. In addition, in exemplary
embodiments, the width is greater than the thickness, which
provides for greater area. For example, the width may be at least
twice the thickness. By way of further example, a 0.2 inch thick
Fuel Cell Stick.TM. device 10 may have a width of 0.5 inch. It may
be appreciated that the drawings are not shown to scale, but merely
give a general idea of the relative dimensions.
[0169] In accordance with the invention, electrical connections to
the anode 24 and cathode 26 are made in the cold zones 30 of the
Fuel Cell Stick.TM. device 10. In an exemplary embodiment, the
anode 24 and the cathode 26 will each be exposed to an outer
surface of the Fuel Cell Stick.TM. device 10 in a cold zone 30 to
allow an electrical connection to be made. A negative voltage node
38 is connected via a wire 42, for example, to the exposed anode
portion 25 and a positive voltage node 40 is connected via a wire
42, for example, to the exposed cathode portion 27. Because the
Fuel Cell Stick.TM. device 10 has cold zones 30 at each end 11a,
11b of the device, low temperature rigid electrical connections can
be made, which is a significant advantage over the prior art, which
generally requires high temperature brazing methods to make the
electrical connections.
[0170] FIG. 2 depicts in perspective view a first end 11a of Fuel
Cell Stick.TM. device 10 with a supply tube 50 attached over the
end 11a and secured with a tie wrap 52. Fuel from fuel supply 34
will then be fed through the supply tube 50 and into the fuel inlet
12. As a result of first end 11a being in the cold zone 30,
flexible plastic tubing or other low temperature type connection
material may be used to connect the fuel supply 34 to the fuel
inlet 12. The need for high temperature brazing to make the fuel
connection is eliminated by the invention.
[0171] FIG. 3A depicts in perspective view a Fuel Cell Stick.TM.
device 10 similar to that depicted in FIG. 1, but having modified
first and second ends 11a, 11b. Ends 11a, 11b have been machined to
form cylindrical end portions to facilitate connection of the fuel
supply 34 and air supply 36. FIG. 3B depicts in perspective view a
supply tube 50 connected to the first end 11a for feeding fuel from
fuel supply 34 to the fuel inlet 12. By way of example, supply tube
50 can be a silicone or latex rubber tube that forms a tight seal
by virtue of its elasticity to the first end 11a. It may be
appreciated that the flexibility and elasticity of the supply tubes
50 can provide a shock-absorbing holder for the Fuel Cell Stick.TM.
devices 10 when the use is in a mobile device subject to
vibrations. In the prior art, the tubes or plates were rigidly
brazed, and thus subject to crack failure if used in a dynamic
environment. Therefore, the additional function of the supply tubes
50 as vibration dampers offers a unique advantage compared to the
prior art.
[0172] Referring back to FIG. 3A, contact pads 44 are provided on
the outer surface of the Fuel Cell Stick.TM. device 10 so as to
make contact with the exposed anode portion 25 and the exposed
cathode portion 27. Material for the contact pads 44 should be
electrically conductive so as to electrically connect the voltage
nodes 38, 40 to their respective anode 24 and cathode 26. It may be
appreciated that any suitable method may be used for forming the
contact pads 44. For example, metal pads may be printed onto the
outer surface of a sintered Fuel Cell Stick.TM. device 10. The
wires 42 are secured to the contact pads 44 by a solder connection
46, for example, to establish a reliable connection. Solders are a
low temperature material, which can be used by virtue of being
located in the cold zones 30 of the Fuel Cell Stick.TM. device 10.
For example, a common 10Sn88Pb2Ag solder can be used. The present
invention eliminates the need for high temperature voltage
connections, thereby expanding the possibilities to any low
temperature connection material or means.
[0173] Also depicted in FIG. 3A, in perspective view, are the fuel
outlet 16 and the air outlet 22. The fuel enters through the fuel
inlet 12 at first end 11a, which is in one cold zone 30, and exits
out the side of Fuel Cell Stick.TM. device 10 through outlet 16
adjacent the second end 11b. Air enters through air inlet 18
located in the second end 11b, which is in the cold zone 30, and
exits from the air outlet 22 in the side of the Fuel Cell Stick.TM.
device 10 adjacent the first end 11a. While the outlets 16 and 22
are depicted as being on the same side of the Fuel Cell Stick.TM.
device 10, it may be appreciated that they may be positioned at
opposing sides, for example, as depicted below in FIG. 4A.
[0174] By having air outlet 22 close to fuel inlet 12 (and
similarly fuel outlet 16 close to air inlet 18), and through the
close proximity of the overlapping layers (anode, cathode,
electrolyte), the air outlet 22 functions as a heat exchanger,
usefully pre-heating the fuel that enters the device 10 through
fuel inlet 12 (and similarly, fuel outlet 16 pre-heats air entering
through air inlet 18). Heat exchangers improve the efficiency of
the system. The transition zones 31 have overlapping areas of spent
air and fresh fuel (and spent fuel and fresh air), such that heat
is transferred before the fresh fuel (fresh air) reaches the hot
zone 32. Thus, the Fuel Cell Stick.TM. device 10 of the invention
is a monolithic structure that includes a built-in heat
exchanger.
[0175] With respect to FIG. 4A, there is depicted in perspective
view the connection of a plurality of Fuel Cell Stick.TM. devices
10, in this case two Fuel Cell Stick.TM. devices 10, by aligning
each contact pad 44 connected to the exposed anode portions 25 and
soldering (at 46) a wire 42 connected to the negative voltage node
38 to each of the contact pads 44. Similarly, the contact pads 44
that are connected to the exposed cathode portions 27 are aligned
and a wire 42 connecting the positive voltage node 40 is soldered
(at 46) to each of those aligned contact pads 44, as shown
partially in phantom. As may be appreciated, because the connection
is in the cold zone 30, and is a relatively simple connection, if
one Fuel Cell Stick.TM. device 10 in a multi-Fuel Cell Stick.TM.
system or assembly needs replacing, it is only necessary to break
the solder connections to that one device 10, replace the device
with a new device 10, and re-solder the wires 42 to the contact
pads 44 of the new Fuel Cell Stick.TM. device 10.
[0176] FIG. 4B depicts in an end view the connection between
multiple Fuel Cell Stick.TM. devices 10, where each Fuel Cell
Stick.TM. device 10 includes a plurality of anodes 24 and cathodes
26. For example, the specific embodiment depicted in FIG. 4B
includes three sets of opposing anodes 24 and cathodes 26, with
each anode 24 exposed at the right side of the Fuel Cell Stick.TM.
device 10 and each cathode 26 exposed at the left side of the Fuel
Cell Stick.TM. device 10. A contact pad 44 is then placed on each
side of the Fuel Cell Stick.TM. device 10 to contact the respective
exposed anode portions 25 and exposed cathode portions 27. On the
right side, where the anodes 24 are exposed, the negative voltage
node 38 is connected to the exposed anode portions 25 by securing
wire 42 to the contact pad 44 via a solder connection 46.
Similarly, positive voltage node 40 is connected electrically to
the exposed cathode portions 27 on the left side of the Fuel Cell
Stick.TM. device 10 by securing wire 42 to contact pad 44 via the
solder connection 46. Thus, while FIGS. 1-4A depicted a single
anode 24 opposing a single cathode 26, it may be appreciated, as
shown in FIG. 4B, that each Fuel Cell Stick.TM. device 10 may
include multiple anodes 24 and cathodes 26, with each being exposed
to an outer surface of the Fuel Cell Stick.TM. device 10 for
electrical connection by means of a contact pad 44 applied to the
outer surface for connection to the respective voltage node 38 or
40. The number of opposing anodes 24 and cathodes 26 in the
structure may be tens, hundreds and even thousands.
[0177] FIG. 5 depicts in an end view a mechanical attachment for
making the electrical connection between wire 42 and the contact
pad 44. In this embodiment, the Fuel Cell Stick.TM. devices 10 are
oriented such that one set of electrodes is exposed at the top
surface of each Fuel Cell Stick.TM. device 10. The contact pad 44
has been applied to each top surface at one end (e.g., 11a or 11b)
in the cold zone 30. Spring clips 48 may then be used to removably
secure the wire 42 to the contact pads 44. Thus, metallurgical
bonding may be used to make the electrical connections, such as
depicted in FIGS. 3A, 4A and 4B, or mechanical connection means may
be used, as depicted in FIG. 5. The flexibility in selecting an
appropriate attachment means is enabled by virtue of the cold zones
30 in the Fuel Cell Stick.TM. devices 10 of the invention. Use of
spring clips 48 or other mechanical attachment means further
simplifies the process of replacing a single Fuel Cell Stick.TM.
device 10 in a multi-stick assembly.
[0178] FIGS. 6A and 6B depict in perspective views an alternative
embodiment having a single cold zone 30 at the first end 11a of
Fuel Cell Stick.TM. device 10, with the second end 11b being in the
hot zone 32. In FIG. 6A, the Fuel Cell Stick.TM. device 10 includes
three fuel cells in parallel, whereas the Fuel Cell Stick.TM.
device 10 of FIG. 6B includes a single fuel cell. Thus, embodiments
of the invention may include a single cell design or a multi-cell
design. To enable the single end input of both the fuel and the
air, the air inlet 18 is reoriented to be adjacent the first end
11a at the side surface of the Fuel Cell Stick.TM. device 10. The
air passage 20 (not shown) again runs parallel to the fuel passage
14, but in this embodiment, the flow of air is in the same
direction as the flow of fuel through the length of the Fuel Cell
Stick.TM. device 10. At the second end 11b of the device 10, the
air outlet 22 is positioned adjacent the fuel outlet 16. It may be
appreciated that either the fuel outlet 16 or the air outlet 22, or
both, can exit from a side surface of the Fuel Cell Stick.TM.
device 10, rather than both exiting at the end surface.
[0179] As depicted in FIG. 6B, the supply tube 50 for the air
supply 36 is formed by making holes through the side of the supply
tube 50 and sliding the device 10 through the side holes so that
the supply tube 50 for the air supply 36 is perpendicular to the
supply tube 50 for the fuel supply 34. Again, a silicone rubber
tube or the like may be used in this embodiment. A bonding material
may be applied around the joint between the supply tube 50 and the
device 10 to form a seal. The electrical connections are also made
adjacent the first end 11a in the cold zone 30. FIGS. 6A and 6B
each depict the positive voltage connection being made on one side
of the Fuel Cell Stick.TM. device 10 and the negative voltage
connection being made on the opposing side of the Fuel Cell
Stick.TM. device 10. However, it may be appreciated that the
invention is not so limited. An advantage of the single end input
Fuel Cell Stick.TM. device 10 is that there is only one cold-to-hot
transition instead of two transition zones 31, such that the Fuel
Cell Stick.TM. device 10 could be made shorter.
[0180] One benefit of the invention is the ability to make the
active layers very thin, thereby enabling a Fuel Cell Stick.TM.
device 10 to incorporate multiple fuel cells within a single
device. The thinner the active layers are, the greater the chance
of an air passage 20 or fuel passage 14 caving in during
manufacture of the Fuel Cell Stick.TM. device 10, thereby
obstructing flow through the passage 14 and/or 20. Therefore, in
one embodiment of the invention, depicted in FIGS. 7A and 7B, a
plurality of support pillars 54, for example ceramic support
pillars, are provided in the passages 14 and 20 to prevent
distortion of the electrolyte layer 28 and obstruction of the
passages 14, 20. FIG. 7A is a cross-sectional side view, whereas
FIG. 7B is a cross-sectional top view through the air passage 20.
According to one method of the invention, using the tape casting
method, a sacrificial tape layer may be used, with a plurality of
holes formed in the sacrificial layer, such as by means of laser
removal of the material. A ceramic material is then used to fill
the holes, such as by spreading a ceramic slurry over the
sacrificial tape layer to penetrate the holes. After the various
layers are assembled together, the sacrificial material of the
sacrificial layer is removed, such as by use of a solvent, leaving
the support pillars 54 remaining.
[0181] In another embodiment for forming the support pillars 54,
large particles of a pre-sintered ceramic can be added to an
organic vehicle, such as plastic dissolved in a solvent, and
stirred to form a random mixture. By way of example and not
limitation, the large particles may be spheres, such as 0.002 in.
diameter balls. The random mixture is then applied to the green
structure, such as by printing in the areas where the fuel and air
passages 14 and 20 are to be located. During the sintering
(bake/fire) process, the organic vehicle leaves the structure (e.g.
is burned out), thereby forming the passages 14, 20, and the
ceramic particles remain to form the support pillars 54 that
physically hold open the passages 14, 20. The resultant structure
is shown in the micrographs of FIGS. 7C and 7D. The support pillars
54 are randomly positioned, with the average distance being a
function of the loading of the ceramic particles in the organic
vehicle.
[0182] FIG. 8A depicts in cross-section one embodiment of the
invention containing two fuel cells in parallel. Each active
electrolyte layer 28 has an air passage 20 and cathode layer 26a or
26b on one side and a fuel passage 14 and anode layer 24a or 24b on
the opposing side. The air passage 20 of one fuel cell is separated
from the fuel passage 14 of the second fuel cell by ceramic
material 29. The exposed anode portions 25 are each connected via
wire 42 to the negative voltage node 38 and the exposed cathode
portions 27 are each connected via a wire 42 to the positive
voltage node 40. A single air supply 36 can then be used to supply
each of the multiple air passages 20 and a single fuel supply 34
may be used to supply each of the multiple fuel passages 14. The
electrical circuit established by this arrangement of the active
layers is depicted at the right side of the figure.
[0183] In the cross-sectional view of FIG. 8B, the Fuel Cell
Stick.TM. device 10 is similar to that depicted in FIG. 8A, but
instead of having multiple exposed anode portions 25 and multiple
exposed cathode portions 27, only anode layer 24a is exposed at 25
and only one cathode layer 26a is exposed at 27. A first via 56
connects cathode layer 26a to cathode layer 26b and a second via 58
connects anode layer 24a to anode layer 24b. By way of example,
laser methods may be used during formation of the green layers to
create open vias, which are then subsequently filled with
electrically conductive material to form the via connections. As
shown by the circuit at the right of FIG. 8B, the same electrical
path is formed in the Fuel Cell Stick.TM. device 10 of FIG. 8B as
in the Fuel Cell Stick.TM. device 10 of FIG. 8A.
[0184] FIGS. 9A and 9B also depict, in cross-sectional views,
multi-fuel cell designs, but with shared anodes and cathodes. In
the embodiment of FIG. 9A, the Fuel Cell Stick.TM. device 10
includes two fuel passages 14 and two air passages 20, but rather
than having two fuel cells, this structure includes three fuel
cells. The first fuel cell is formed between anode layer 24a and
cathode layer 26a with intermediate electrolyte layer 28. Anode
layer 24a is on one side of a fuel passage 14, and on the opposing
side of that fuel passage 14 is a second anode layer 24b. Second
anode layer 24b opposes a second cathode layer 26b with another
electrolyte layer 28 there between, thereby forming a second fuel
cell. The second cathode layer 26b is on one side of an air passage
20 and a third cathode layer 26c is on the opposing side of that
air passage 20. Third cathode layer 26c opposes a third anode layer
24c with an electrolyte layer 28 therebetween, thus providing the
third fuel cell. The portion of the device 10 from anode layer 24a
to cathode layer 26c could be repeated numerous times within the
device 10 to provide the shared anodes and cathodes thereby
multiplying the number of fuel cells within a single Fuel Cell
Stick.TM. device 10. Each anode layer 24a, 24b, 24c includes an
exposed anode portion 25 to which electrical connections can be
made at the outer surface of the Fuel Cell Stick.TM. device 10 to
connect to a negative voltage node 38 via a wire 42, for example.
Similarly, each cathode layer 26a, 26b, 26c includes an exposed
cathode portion 27 to the outside surface for connection to a
positive voltage node 40 via a wire 42, for example. A single air
supply 36 may be provided at one cold end to supply each of the air
passages 20 and a single fuel supply 34 may be provided at the
opposite cold end to supply each of the fuel passages 14. The
electrical circuit formed by this structure is provided at the
right side of FIG. 9A. This Fuel Cell Stick.TM. device 10 contains
three fuel cell layers in parallel trebling the available power.
For example, if each layer produces 1 volt and 1 amp, then each
fuel cell layer produces 1 watt of power output
(volt.times.amp=watt). Therefore, this three-layer layout would
then produce 1 volt and 3 amps for a total of 3 watts of power
output.
[0185] In FIG. 9B, the structure of FIG. 9A is modified to provide
a single electrical connection to each of the voltage nodes to
create three fuel cells in series, as shown by the circuit at the
right side of FIG. 9B. The positive voltage node 40 is connected to
cathode layer 26a at exposed cathode portion 27. Anode layer 24a is
connected to cathode layer 26b by via 58. Anode layer 24b is
connected to cathode layer 26c by via 56. Anode layer 24c is then
connected at exposed anode portion 25 to the negative voltage node
38. Thus, using the same 1 amp/1 volt per layer assumption, this
three cell structure would produce 3 volts and 1 amp for a total of
3 watts of power output.
[0186] Another embodiment of the invention is depicted in side view
in FIG. 10. In this embodiment, the Fuel Cell Stick.TM. device 10
has a single cold zone 30 at the first end 11a with the second end
11b being in the hot zone 32. As in other embodiments, the fuel
inlets 12 are at the first end 11a and connected to a fuel supply
34 by a supply tube 50. In this embodiment, the fuel passages 14
extend the length of the Fuel Cell Stick.TM. device 10 with the
fuel outlet 16 being at second end 11b. Thus, the fuel supply
connection is made in the cold zone 30 and the outlet for the fuel
reactants (e.g., CO.sub.2 and H.sub.2O) is in the hot zone 32.
Similarly, the anodes have an exposed anode portion 25 in the cold
zone 30 for connecting to the negative voltage node 38 via a wire
42.
[0187] In the embodiment of FIG. 10, the Fuel Cell Stick.TM. device
10 is open at least at one side, and potentially at both opposing
sides, to provide both air inlets 18 and air passages 20 in the hot
zone 32. The use of support pillars 54 may be particularly useful
in this embodiment within the air passages 20. The air outlet can
be at the second end 11b, as depicted. Alternatively, although not
shown, the air outlet may be at an opposing side from the air inlet
side if the passages 20 extend through the width and the air supply
is directed only toward the input side, or if the passages 20 do
not extend through the width. Instead of providing only heat to the
hot zone 32, in this embodiment, air is also provided. In other
words, the sides of the device 10 in the hot zone 32 are open to
heated air instead of supplying air through a forced air tube.
[0188] FIG. 10A shows in side view a variation of the embodiment
depicted in FIG. 10. In FIG. 10A, the Fuel Cell Stick.TM. device 10
includes opposing cold zones 30 with a central heated zone 32
separated from the cold zones 30 by transition zones 31. The air
inlet 18 is provided in the central heated zone 32, in at least a
portion thereof, to receive the heated air. However, in this
embodiment, the air passage 20 is not completely open to the side
of the Fuel Cell Stick.TM. device 10 for an appreciable length as
in FIG. 10. Rather, as shown more clearly in FIG. 10B, air passage
20 is open in a portion of the hot zone 32 and then is close to the
sides for the remainder of the length and then exits at air outlet
22 at second end 11b of the Fuel Cell Stick.TM. device 10. This
embodiment allows heated air to be supplied in the hot zone 32
rather than a forced air supply tube, but also allows for the fuel
and air to exit at one end 11b of the device 10 in a cold zone
30.
[0189] While specific embodiments have been depicted and described
in detail, the scope of the invention should not be so limited.
More general embodiments of the invention are described below and
may be understood more fully with reference to the schematic views
depicted in FIGS. 11-24. FIG. 11 provides a key for the components
depicted schematically in FIGS. 12-24. Where fuel (F) or air (A) is
shown by an arrow going into the Fuel Cell Stick.TM. device (e.g.,
SOFC Stick) that indicates forced flow, such as through a tube
connected to the input access point. Where air input is not
depicted, that indicates that heated air is supplied in the hot
zone by means other than a forced flow connection and the Fuel Cell
Stick.TM. device is open to the air passage at an access point
within the hot zone.
[0190] One embodiment of the invention is a Fuel Cell Stick.TM.
device that includes at least one fuel passage and associated
anode, at least one oxidant pathway and associated cathode, and an
electrolyte therebetween, where the cell is substantially longer
than it is wide or thick so as to have a CTE in one dominant axis
and operating with a portion thereof in a heated zone having a
temperature of greater than about 400.degree. C. In this
embodiment, the Fuel Cell Stick.TM. device has integrated access
points for both air and fuel input at one end of the device
according to the dominant CTE direction, or air input at one end
and fuel input at the other end according to the dominant CTE
direction, and air and fuel inputs being located outside the heated
zone. For example, see FIGS. 20 and 24.
[0191] In another embodiment of the invention, the fuel cell has a
first temperature zone and a second temperature zone, wherein the
first temperature zone is the hot zone, which operates at a
temperature sufficient to carry out the fuel cell reaction, and the
second temperature zone is outside the heated zone and operates at
a lower temperature than the first temperature zone. The
temperature of the second temperature zone is sufficiently low to
allow low temperature connections to be made to the electrodes and
a low temperature connection for at least the fuel supply. The fuel
cell structure extends partially into the first temperature zone
and partially into the second temperature zone. For example, see
FIGS. 12, 13 and 17.
[0192] In one embodiment of the invention, the fuel cell includes a
first temperature zone that is the heated zone and a second
temperature zone operating at a temperature below 300.degree. C.
The air and fuel connections are made in the second temperature
zone using rubber tubing or the like as a low temperature
connection. Low temperature solder connections or spring clips are
used to make the electrical connections to the anode and cathode
for connecting them to the respective negative and positive voltage
nodes. Further, the fuel outlet for carbon dioxide and water and
the air outlet for depleted oxygen are located in the first
temperature zone, i.e., the heated zone. For example, see FIG.
17.
[0193] In another embodiment, the fuel cell structure has a central
first temperature zone that is the heated zone, and each end of the
fuel cell is located outside the first temperature zone in a second
temperature zone operating below 300.degree. C. Fuel and air inputs
are located in the second temperature zone, as are solder
connections or spring clips for electrical connection to the anode
and cathode. Finally, output for the carbon dioxide, water and
depleted oxygen are located in the second temperature zone. For
example, see FIGS. 19, 20 and 24.
[0194] In another embodiment of the invention, fuel inputs may be
provided at each end according to the dominant CTE direction in a
second temperature zone operating below 300.degree. C. with a first
temperature zone being the heated zone provided in the center
between the opposing second temperature zones. The output for the
carbon dioxide, water, and depleted oxygen may be located in the
central heated zone. For example, see FIGS. 15 and 18.
Alternatively, the output for the carbon dioxide, water and
depleted oxygen may be located in the second temperature zone,
i.e., outside of the heated zone. For example, see FIGS. 16 and
19.
[0195] In another embodiment, both the fuel and air input access
points are located outside the first temperature zone, which is the
heated zone, in a second temperature zone operating below
300.degree. C. thereby allowing use of low temperature connections,
such as rubber tubing for air and fuel supply. In addition, solder
connections or spring clips are used in the second temperature zone
for connecting the voltage nodes to anodes and cathodes. In one
embodiment, the fuel and air input are both at one end according to
the dominate CTE direction, with the other end of the Fuel Cell
Stick.TM. device being in the first heated temperature zone with
the outputs of carbon dioxide, water and depleted oxygen being in
the heated zone. For example, see FIG. 17. Thus, the Fuel Cell
Stick.TM. device has one heated end and one non-heated end.
[0196] In another embodiment, fuel and air are inputted into one
end according to the dominant CTE direction outside the heated zone
and exit at the opposite end also outside the heated zone, such
that the heated zone is between two opposing second temperature
zones. For example, see FIG. 20. In yet another alternative, fuel
and air are inputted into both of opposing ends located in second
temperature zones with the fuel and air outputs being in the
central heated zone. For example, see FIG. 18.
[0197] In yet another alternative, fuel and air are inputted into
both of opposing ends located in second temperature zones with the
respective outputs being in the second temperature zone at the
opposite end from the input. For example, see FIG. 19. Thus, the
fuel cell has a central heated zone and opposing ends outside the
heated zone, with fuel and air both inputted into the first end
with the respective reaction outputs exiting adjacent the second
end, and both fuel and air being inputted into the second end and
the reaction outputs exiting adjacent the first end.
[0198] In yet another embodiment, fuel input may be at one end
outside the heated zone and air input may be at the opposite end
outside the heat zone. For example, see FIGS. 21-24. In this
embodiment, the reaction outputs from both the air and fuel may be
within the heated zone (see FIG. 21), or they both may be outside
the heated zone adjacent the opposite end from the respective input
(see FIG. 24). Alternatively, the carbon dioxide and water output
may be in the hot zone while the depleted oxygen output is outside
the hot zone (see FIG. 22), or conversely, the depleted oxygen
output may be in the heated zone and the carbon dioxide and water
output outside the heated zone (see FIG. 23). The variations with
respect to fuel and air output depicted in FIGS. 22 and 23 could
also be applied in the embodiments depicted in FIGS. 18-20, for
example.
[0199] In another embodiment of the invention, depicted in top plan
view in FIGS. 25A and 27A and in side view in FIG. 27B, a Fuel Cell
Stick.TM. device 100 is provided having what may be referred to as
a panhandle design. The Fuel Cell Stick.TM. device 100 has an
elongate section 102, which may be similar in dimension to the Fuel
Cell Stick.TM. devices 10 depicted in prior embodiments, that has a
CTE in one dominant axis, i.e., it is substantially longer than it
is wide or thick. The Fuel Cell Stick.TM. device 100 further has a
large surface area section 104 having a width that more closely
matches the length. Section 104 may have a square surface area or a
rectangular surface area, but the width is not substantially less
than the length, such that the CTE does not have a single dominant
axis in section 104, but rather has a CTE axis in the length
direction and the width direction. The large surface area section
104 is located in the hot zone 32, whereas the elongate section 102
is at least partially located in the cold zone 30 and the
transition zone 31. In an exemplary embodiment, a portion of the
elongate section 102 extends into the hot zone 32, but this is not
essential. By way of example, the fuel and air supplies 34, 36 may
be connected to the elongate section 102 in the manner depicted in
FIG. 6B, as well as the electrical connections.
[0200] In FIGS. 25B and 26A, a top plan view is provided and in
FIG. 26B a side view is provided of an alternative embodiment
similar to that shown in FIGS. 25A, 27A and 27B but further having
a second elongate section 106 opposite the elongate section 102 so
as to position the large surface area section 104 between the two
elongate sections 102 and 106. Elongate section 106 is also at
least partially located in a cold zone 30 and a transition zone 31.
In this embodiment, fuel may be inputted into elongate section 102
and air inputted into elongate section 106. By way of example, the
air supply 36 and the fuel supply 34 could then be connected to the
elongate sections 106 and 102, respectively, in the manner depicted
in FIG. 2 or FIG. 3B. As depicted in FIG. 25B, the air output may
be located in the elongate section 102 adjacent the fuel input, and
the fuel output may be located in elongate section 106 adjacent the
air input. Alternatively, one or both of the air and fuel outputs
may be located in the large surface area section 104 in the hot
zone 32, as depicted in FIGS. 26A and 26B in top and side views,
respectively. It may be appreciated that in the embodiments of
FIGS. 25A and 25B, the surface area of the opposing anode 24 and
cathode 26 with intervening electrolyte 28 may be increased in the
hot zone 32 to increase the reaction area, thereby increasing the
power generated by the Fuel Cell Stick.TM. device 100.
[0201] Another benefit of the Fuel Cell Stick.TM. devices 10, 100
of the invention is low weight. Typical combustion engines weigh on
the order of 18-30 lbs per kW of power. A Fuel Cell Stick.TM.
device 10, 100 of the invention can be made with a weight on the
order of 0.5 lbs per kW of power. FIGS. 28A-28D depict an
alternative embodiment of a Tubular Fuel Cell Stick.TM. device 200
of the invention, having a spiral or rolled, tubular configuration.
FIG. 28A is a schematic top view of device 200, in the unrolled
position. The unrolled structure of device 200 has a first end 202
and a second end 204 of equal length L that will correspond to the
length of the rolled or spiral Tubular Fuel Cell Stick.TM. device
200. Fuel inlet 12 and air inlet 18 are shown on opposing sides
adjacent first end 202. Fuel passage 14 and air passage 20 then
extend along the width of the unrolled structure of device 200 to
the second end 204 such that the fuel outlet 16 and air outlet 22
are at the second end 204, as further shown in the schematic end
view of the unrolled structure of device 200 in FIG. 28B and the
schematic side view of the unrolled structure of device 200 in FIG.
28C. The fuel passage 14 and air passage 20 are shown as extending
nearly the length L of the unrolled structure of device 200 so as
to maximize fuel and air flow, but the invention is not so limited.
To form the spiral Tubular Fuel Cell Stick.TM. device 200, first
end 202 is then rolled toward second end 204 to form the spiral
tube structure of device 200 depicted in the schematic perspective
view of FIG. 28D. Air supply 36 may then be positioned at one end
of the spiral Tubular Fuel Cell Stick.TM. device 200 for input into
air inlet 18, while the fuel supply 34 may be positioned at the
opposite end of the spiral Tubular Fuel Cell Stick.TM. device 200
to input fuel into the fuel inlet 12. The air and the fuel will
then exit the spiral Tubular Fuel Cell Stick.TM. device 200 along
the length L of the device 200 through fuel outlet 16 and air
outlet 22. The voltage nodes 38, 40 can be soldered to contact pads
44 formed on or adjacent to opposing ends of the spiral Tubular
Fuel Cell Stick.TM. device 200.
[0202] FIGS. 29A-29G depict an alternative embodiment of the
invention wherein the Fuel Cell Stick.TM. device is in a tubular
concentric form. FIG. 29A depicts in schematic isometric view a
concentric Tubular Fuel Cell Stick.TM. device 300. FIGS. 29B-29E
depict cross-sectional views of the concentric device 300 of FIG.
29A. FIG. 29F depicts an end view at the air input end of the
device 300, and FIG. 29G depicts an end view at the fuel input end
of device 300. The particular embodiment shown includes three air
passages 20, one being in the center of the tubular structure and
the other two being spaced from and concentric therewith. The
concentric Tubular Fuel Cell Stick.TM. device 300 also has two fuel
passages 14 between and concentric with the air passages 20. As
shown in FIGS. 29A-29D, the concentric Tubular Fuel Cell Stick.TM.
device 300 includes a fuel outlet 16 connecting the fuel passages
14 at one end and an air outlet 22 connecting the air passages 20
at the other end opposite their respective inlets 12, 18. Each air
passage 20 is lined with cathodes 26 and each fuel passage 14 is
lined with anodes 24, with electrolyte 28 separating opposing
anodes and cathodes. As shown in FIGS. 29A-29B and 29F-29G,
electrical connection may be made to the exposed anodes 25 and
exposed cathodes 27 at opposing ends of the concentric Tubular Fuel
Cell Stick.TM. device 300. Contact pads 44 may be applied to the
ends to connect the exposed anodes 25 and exposed cathodes 27, and
although not shown, the contact pads 44 can be run along the
outside of the device 300 to permit the electrical connection to be
made at a point along the length of the device 300 rather than at
the ends. Concentric Tubular Fuel Cell Stick.TM. device 300 may
include support pillars 54 positioned within the air and fuel
passages 14, 20 for structural support.
[0203] In the embodiments of the invention having two cold zones 30
at opposing ends 11a, 11b, with air input and fuel output at one
end and fuel input and air output at the opposing end, the spent
fuel or air is in a heated state as it exits the central hot zone
32. The heated air and fuel cool as they travel through the
transition zones 31 to the cold zones 30. Thin layers of electrodes
and/or ceramic/electrolyte separate an air passage 20 from a
parallel fuel passage 14, and vice-versa. In one passage, heated
air is exiting the hot zone 32, and in an adjacent parallel
passage, fuel is entering the hot zone 32, and vice-versa. The
heated air, through heat exchange principles, will heat up the
incoming fuel in the adjacent parallel passage, and vice-versa.
Thus, there is some pre-heating of the air and fuel through heat
exchange. However, due to the rapid loss of heat outside the hot
zone 32, as discussed above, heat exchange may not be sufficient to
pre-heat the air and fuel to the optimal reaction temperature
before it enters the active region in the hot zone 32. In addition,
in embodiments where the Fuel Cell Stick.TM. device 10 includes one
cold end (cold zone 30) and one hot end (hot zone 32), fuel and air
are inputted into the same cold end 30 and exit through the same
opposing hot end 32, such that there is no cross-flow of fuel and
air for heat-exchange to occur. Only limited heat exchange to the
incoming fuel and air is available from the electrode and ceramic
materials of the Fuel Cell Stick.TM. device 10.
[0204] FIGS. 30A-33C depict various embodiments of a Fuel Cell
Stick.TM. device 10 having integrated pre-heat zones 33a for
heating the fuel and air before it enters an active zone 33b in
which the anodes 24 and cathodes 26 are in opposing relation. These
embodiments include Fuel Cell Stick.TM. devices 10 in which there
are two cold ends 30 with an intermediate hot zone 32 and fuel and
air input at opposing cold ends 30, and Fuel Cell Stick.TM. devices
10 in which there is one hot end 32 and one cold end 30 with fuel
and air input both at the single cold end 30. In these embodiments,
the amount of electrode material used can be limited to the active
zone 33b with only a small amount leading to the cold zone 30 for
the external connection to the voltage nodes 38, 40. Another
benefit in these embodiments, which will be described in more
detail later, is that the electrons have the shortest possible path
to travel to the external voltage connection, which provides a low
resistance.
[0205] FIG. 30A depicts a schematic cross-sectional side view of a
first embodiment of a Fuel Cell Stick.TM. device 10 having one cold
zone 30 and one opposing hot zone 32 with an integrated pre-heat
zone 33a. FIG. 30B depicts in cross-section a view through the
anode 24 looking up toward the fuel passage 14, and FIG. 30C
depicts in cross-section a view through the cathode 26 looking down
toward the air passage 20. As shown in FIGS. 30A and 30B, the fuel
from fuel supply 34 enters through fuel inlet 12 and extends along
the length of the device 10 through fuel passage 14 and exits from
the opposite end of the device 10 through fuel outlet 16. The cold
zone 30 is at the first end 11a of Fuel Cell Stick.TM. device 10
and the hot zone 32 is at the opposing second end 11b. Between the
hot and cold zones is the transition zone 31. The hot zone 32
includes an initial pre-heat zone 33a through which the fuel first
travels, and an active zone 33b that includes the anode 24 adjacent
the fuel passage 14. As shown in FIG. 30B, the cross-sectional area
of the anode 24 is large in the active zone 33b. The anode 24
extends to one edge of the Fuel Cell Stick.TM. device 10 and an
external contact pad 44 extends along the outside of the device 10
to the cold zone 30 for connection to the negative voltage node
38.
[0206] Similarly, as shown in FIGS. 30A and 30C, the air from air
supply 36 enters through the air inlet 18 positioned in the cold
zone 30 and the air extends along the length of the Fuel Cell
Stick.TM. device 10 through air passage 20 and exits from the hot
zone 32 through the air outlet 22. Because the air and fuel are
entering at the same end and traveling along the length of the Fuel
Cell Stick.TM. device 10 in the same direction, there is limited
pre-heating of the air and fuel by heat exchange prior to the hot
zone 32. The cathode 26 is positioned in the active zone 33b in
opposing relation to the anode 24 and extends to the opposite side
of the Fuel Cell Stick.TM. device 10 where it is exposed and
connected to an external contact pad 44 that extends from the
active hot zone 33b to the cold zone 30 for connection to the
positive voltage node 40. It is not necessary, however, that the
exposed cathode 27 be on an opposite side of the device 10 as the
exposed anode 25. The exposed anode 25 and exposed cathode 27 could
be on the same side of the device 10 and the contact pads 44 could
be formed as stripes down the side of the Fuel Cell Stick.TM.
device 10. By this structure, the air and fuel are first heated in
the pre-heat zone 33a, where no reaction is taking place, and the
majority of the anode and cathode material is limited to the active
zone 33b where the heated air and fuel enter and react by virtue of
the opposed anode and cathode layers 24, 26.
[0207] The embodiment depicted in FIGS. 31A-31C is similar to that
depicted in FIGS. 30A-30C, but rather than having one hot end 32
and one cold end 30, the embodiment of FIGS. 31A-C includes
opposing cold zones 30 with a central hot zone 32. Fuel from fuel
supply 34 enters through the first end 11a of device 10 through
fuel inlet 12 in the cold zone 30 and exits from the opposite
second end 11b through fuel outlet 16 positioned in the opposing
cold zone 30. Similarly, air from air supply 36 enters through the
opposite cold zone 30 through air inlet 18 and exits at the first
cold zone 30 through air outlet 22. The fuel enters the hot zone 32
and is pre-heated in pre-heat zone 33a, while the air enters at the
opposite side of the hot zone 32 and is pre-heated in another
pre-heat zone 33a. There is thus a cross-flow of fuel and air. The
anode 24 opposes the cathode 26 in an active zone 33b of hot zone
32 and the reaction occurs in the active zone 33b involving the
pre-heated fuel and air. Again, the majority of electrode material
is limited to the active zone 33b. The anode 24 is exposed at one
edge of the Fuel Cell Stick.TM. device 10, and the cathode 26 is
exposed at the other side of device 10. An external contact pad 44
contacts the exposed anode 25 in the hot zone 32 and extends toward
the first cold end 11a for connection to negative voltage node 38.
Similarly, an external contact pad 44 contacts the exposed cathode
27 in hot zone 32 and extends toward the second cold end 11b for
connection to positive voltage node 40.
[0208] The pre-heat zones 33a provide the advantage of fully
heating the gas to the optimal reaction temperature before it
reaches the active region. If the fuel is colder than the optimum
temperature, the efficiency of the SOFC system will be lower. As
the air and fuel continue on their paths, they warm up. As they
warm up, the efficiency of the electrolyte 28 increases in that
region. When the fuel, air and electrolyte 28 reach the full
temperature of the furnace, then the electrolyte 28 is working
under its optimal efficiency. To save money on the anode 24 and
cathode 26, which may be made out of precious metal, the metal can
be eliminated in those areas that are still below the optimal
temperature. The amount of the pre-heat zone 33a, in terms of
length or other dimensions, depends on the amount of heat transfer
from the furnace to the Fuel Cell Stick.TM. device 10, and from the
Fuel Cell Stick.TM. device 10 to the fuel and air, as well as
whether any heat exchange is occurring due to cross-flow of the
fuel and air. The dimensions further depend on the rate of flow of
fuel and air; if the fuel or air is moving quickly down the length
of the Fuel Cell Stick.TM. device 10, a longer pre-heat zone 33a
will be advantageous, whereas if the flow rate is slow, the
pre-heat zone 33a may be shorter.
[0209] FIGS. 32A and 32B depict an embodiment similar to that shown
in FIGS. 31A-31C, but the Fuel Cell Stick.TM. device 10 includes a
pre-heat chamber 13 between the fuel inlet 12 and fuel passage 14
that extends into the hot zone 32 for pre-heating in the pre-heat
zone 33a a large volume of fuel before it passes through the more
narrow fuel passage 14 into the active zone 33b. The Fuel Cell
Stick.TM. device 10 similarly includes a pre-heat chamber 19
between the air inlet 18 and the air passage 20 that extends into
the hot zone 32 for pre-heating a large volume of air in the
pre-heat zone 33a before it passes through the more narrow air
passage 20 to the active zone 33b. As disclosed in embodiments
above, the Fuel Cell Stick.TM. device 10 may include multiple fuel
passages 14 and air passages 20, each of which would receive flow
from a respective pre-heat chamber 13, 19.
[0210] With respect to a high-volume pre-heat chamber 13, 19
instead of a pre-heat channel, it may be imagined, by way of
example only, that if it takes 5 seconds for a molecule of air to
heat up to the optimal temperature, then if the molecules of air
are traveling down the Fuel Cell Stick.TM. device 10 at 1 inch per
second, the Fuel Cell Stick.TM. device 10 would need a pre-heat
channel that is 5 inches in length before the air enters the active
zone 33b. If, however, a large volume chamber is provided instead
of a channel, the volume permits the molecules to spend additional
time in the cavity before entering the more narrow channel to the
active zone 33b, such that the air molecules are heated in the
chamber and then a short length of channel may be used for feeding
the heated air molecules to the active zone 33b. Such a cavity or
pre-heat chamber 13, 19 could be prepared in a number of different
ways, including taking a green (i.e., before sintering) assembly
and drilling into the end of the assembly to form the chamber, or
by incorporating a large mass of organic material within the green
stack as it is formed, whereby the organic material is baked out of
the Fuel Cell Stick.TM. device during sintering.
[0211] FIGS. 33A-33C depict yet another embodiment for pre-heating
the air and fuel prior to the air and fuel reaching the active zone
33b. FIG. 33A is a schematic cross-sectional side view, essentially
through the longitudinal center of the Fuel Cell Stick.TM. device
10. FIG. 33B is a cross-sectional top view taken along the line
33B-33B where the fuel passage 14 and anode 24 intersect, while
FIG. 33C is a cross-sectional bottom view taken along the line
33C-33C where the air passage 20 intersects the cathode 26. The
Fuel Cell Stick.TM. device 10 has two opposing cold zones 30 and a
central hot zone 32, with a transition zone 31 between each cold
zone 30 and the hot zone 32. Fuel from fuel supply 34 enters the
first end 11a of Fuel Cell Stick.TM. device 10 through fuel inlet
12 and travels through the fuel passage 14, which extends toward
the opposite end of the hot zone 32, where it makes a U-turn and
travels back to the cold zone 30 of first end 11a, where the spent
fuel exits through fuel outlet 16. Similarly, air from air supply
36 enters the second end 11b of Fuel Cell Stick.TM. device 10
through the air inlet 18 and travels through the air passage 20,
which extends toward the opposing end of the hot zone 32, where it
makes a U-turn and travels back to the second end 11b, where the
air exits from the cold zone 30 through air outlet 22. By means of
these U-turned passages, the portion of the fuel passage 14 and air
passage 20 from the initial entry into the hot zone 32 through the
bend (U-turn) constitute a pre-heat zone for heating the fuel and
air. After the bends, or U-turns, in the passages 14, 20, the
passages are lined with a respective anode 24 or cathode 26, which
are in opposing relation with an electrolyte 28 therebetween, which
region constitutes the active zone 33b in hot zone 32. Thus, the
fuel and air are heated in the pre-heat zone 33a prior to entry
into the active zone 33b to increase the efficiency of the Fuel
Cell Stick.TM. device 10, and to minimize the usage of electrode
material. The anode 24 is extended to the exterior of the device 10
in the cold zone 30 for connection to negative voltage node 38.
Similarly, cathode 26 is extended to the exterior of the device 10
for electrical connection to positive voltage node 40. The fuel and
air outlets 16 and 22 also may exit from the cold zones 30.
[0212] In many of the embodiments shown and described above, the
anodes 24 and cathodes 26 travel within the layers of the Fuel Cell
Stick.TM. device 10, essentially in the center area of each layer,
i.e., internal to the device, until they reach the end of the
device. At that point, the anodes 24 and cathodes 26 are tabbed to
the outside of the Fuel Cell Stick.TM. device 10 where the exposed
anode 25 and exposed cathode 27 are metallized with a contact pad
44, such as by applying a silver paste, and then a wire is soldered
to the contact pad 44. For example, see FIGS. 4A-4B. It may be
desirable, however, to build up the layers in the Fuel Cell
Stick.TM. device 10 into higher voltage combinations, for example
as shown in FIGS. 8A-9B. If it is desired to make a Fuel Cell
Stick.TM. device 10 that produces 1 KW of power, the power is
divided between the voltage and the current. One standard is to use
12 volts, such that 83 amps would be needed to create the total 1
KW of power. In FIGS. 8B and 9B, vias were used to interconnect the
electrode layers to form parallel or series combinations.
[0213] Alternative embodiments for interconnecting the electrode
layers are depicted in FIGS. 34A to 37. Rather than interconnecting
the electrode layers in the interior of the Fuel Cell Stick.TM.
device 10, these alternative embodiments use exterior stripes
(narrow contact pads), for example of silver paste, along the sides
of the Fuel Cell Stick.TM. device 10, in particular, multiple small
stripes. Using the striping technique, a simple structure is formed
that can provide series and/or parallel combinations to achieve any
current/voltage ratios needed. Moreover, the external stripes will
have loose mechanical tolerances compared to the internal vias,
thereby simplifying manufacturing. Also, the external stripes will
likely have a lower resistance (or equivalent series resistance)
than the vias. Lower resistance in a conductor path will result in
lower power loss along that path, such that the external stripes
provide the ability to remove the power from the Fuel Cell
Stick.TM. device 10 with a lower loss of power.
[0214] Referring now specifically to FIGS. 34A and 34B, an external
anode/cathode interconnect in series is depicted. FIG. 34A provides
a schematic oblique front view of the alternating anodes 24a, 24b,
24c and cathodes 26a, 26b, 26c. Along the length of the Fuel Cell
Stick.TM. device 10, the anodes 24a, 24b, 24c and cathodes 26a,
26b, 26c include a tab out to the edge of the device 10 to provide
the exposed anodes 25 and exposed cathodes 27. An external contact
pad 44 (or stripe) is then provided on the outside of the Fuel Cell
Stick.TM. device 10 over the exposed anodes 25 and cathodes 27, as
best shown in the schematic side view of FIG. 34B. By connecting
the three pairs of opposed anodes 24a, 24b, 24c and cathodes 26a,
26b, 26c in series, the Fuel Cell Stick.TM. device 10 provides 3
volts and 1 amp. In FIG. 35, the structure is doubled and the two
structures are connected by long stripes down the sides of the
device 10, thereby providing an external anode/cathode interconnect
in a series parallel design that provides 3 volts and 2 amps.
[0215] FIGS. 36A and 36B provide an embodiment for a low equivalent
series resistance path for providing low power loss. In this
embodiment, the hot zone 32 is in the center of the Fuel Cell
Stick.TM. device 10 with the first end 11a and second end 11b being
in cold zones 30. Fuel is inputted through fuel inlets 12 in first
end 11a and air is inputted through air inlets 18 in second end
11b. Within the hot zone 32, which is the active area of the Fuel
Cell Stick.TM. device 10, the anodes 24 and cathodes 26 are exposed
to the sides of the device 10, with the anodes 24 exposed to one
side, and the cathodes 26 exposed to the opposite side. Contact
pads 44 (or stripes) are applied over the exposed anodes 25 and
cathodes 27. Then, the edges of the Fuel Cell Stick.TM. device 10
are metallized along the length of the sides of the device 10 until
the metallization reaches the cold zones 30, where the low
temperature solder connection 46 is made to the negative voltage
node 38 and the positive voltage node 40. The anodes 24 and
cathodes 26 cannot be optimized only for low resistance because
they have other functions. For example, the electrodes must be
porous to allow the air or fuel to pass through to the electrolyte
28, and porosity increases resistance. Further, the electrodes must
be thin to allow for good layer density in a multi-layer Fuel Cell
Stick.TM. device 10, and the thinner the electrode, the higher the
resistance. By adding thicker contact pads 44 to the edges (sides)
of the Fuel Cell Stick.TM. device 10, it is possible to provide a
low resistance path toward the solder connection 46. The thicker
the contact pad 44, the lower the resistance. If an electron must
travel 10 inches, for example, down the electrode within the Fuel
Cell Stick.TM. device 10, past all the voids in the electrode
layer, the path of least resistance would be to travel 0.5 inch,
for example, to the side edge of the device 10, and then travel the
10 inches down the external non-porous contact pad 44. Thus, the
long contact pads 44 along the exterior of the Fuel Cell Stick.TM.
device 10 that extend to the cold zones 30 allow for the power to
be removed from the Fuel Cell Stick.TM. device 10 with a lower loss
by providing a lower resistance conductor path. Thus, the striping
technique may be used in the active area (hot zone 32) of the Fuel
Cell Stick.TM. device 10 for making series and parallel connections
to increase power, and a long stripe down the side of the device 10
to the cold ends 30 allows that power to be efficiently removed
from the Fuel Cell Stick.TM. device 10.
[0216] FIG. 37 depicts, in schematic isometric view, an embodiment
similar to that depicted in FIG. 36B, but having a single cold zone
30 at the first end 11a of the Fuel Cell Stick.TM. device 10, with
the hot zone 32 being at the second end 11b of device 10. Multiple
vertical stripes or contact pads 44 are provided within the hot
zone 32 to make the series and/or parallel connections, and the
horizontal long stripes or contact pads 44 down the sides of the
device 10 are provided from the hot zone 32 to the cold zone 30 for
making the low temperature solder connections 46 to the positive
voltage node 40 and negative voltage node 38.
[0217] One method for forming the fuel passages 14 and air passages
20 is to place an organic material as a sacrificial layer within
the green, layered structure that can then bake out during a later
sintering step. To build individual Fuel Cell Stick.TM. devices 10
having high power output, such as 1 KW or 10 KW output, the Fuel
Cell Stick.TM. device 10 must be long, wide and have a high layer
count. By way of example, the Fuel Cell Stick.TM. devices may be on
the order of 12 inches to 18 inches long. When baking the green
structure to sinter the ceramic and remove the sacrificial organic
material, the organic material used to form the fuel passage 14
must exit through openings 12 and 16 that form the fuel inlet and
fuel outlet, respectively. Similarly, the organic material used to
form the air passage 20 must bake out through the openings 18 and
22 that form the air inlet and air outlet, respectively. The longer
and wider the devices, the more difficult it is for the organic
material to exit through these openings. If the device is heated
too fast during bake-out, the various layers can delaminate because
the decomposition of the organic material occurs faster than the
material can exit the structure.
[0218] FIGS. 38A and 38B depict, in schematic cross-sectional top
view, an alternative embodiment that provides multiple exit gaps
for bake-out of the organic material (sacrificial layer) 72. As
shown in FIG. 38A, multiple openings 70 are provided on one side of
the Fuel Cell Stick.TM. device 10 to provide multiple bake-out
paths for the organic material 72 to exit the structure. As
depicted in FIG. 38B, after bake-out, the multiple openings 70 are
then closed by applying a barrier coating 60 to the side of the
Fuel Cell Stick.TM. device 10. By way of example, the barrier
coating 60 may be a glass coating. In another example, the barrier
coating 60 may be a glass containing a ceramic filler. In yet
another embodiment, the barrier coating 60 may be a contact pad 44,
for example filled with paste, which would then also serve as the
low resistance path for the generated power. The silver paste may
also contain glass for increased adhesion. In an exemplary
embodiment, the bake-out paths for the cathode 26 are vented to one
side of the Fuel Cell Stick.TM. device 10 and the bake-out paths
for the anode 24 are vented to the opposing side of the device 10
to avoid shorting between opposite electrodes.
[0219] In an alternative embodiment for a Fuel Cell Stick.TM.
device 10, 100, 200, 300, rather than having an open air passage 20
and fuel passage 14 lined with a cathode 26 or anode 24,
respectively, the cathode and air channel may be combined and the
anode and fuel channel may be combined through use of porous
electrode materials that permit flow of the air or fuel. The
cathodes and anodes must be porous anyway to permit the reaction to
occur, so in combination with forced air and fuel input, sufficient
flow could be achieved through the Fuel Cell Stick.TM. device to
permit the power generating reaction to occur.
[0220] Another embodiment of the present invention is depicted in
schematic cross-sectional end view in FIG. 39. This embodiment is
essentially an anode-supported version of a Fuel Cell Stick.TM.
device 10. As with other embodiments, the Fuel Cell Stick.TM.
device 10 may have a hot end 32 and a cold end 30, or two cold ends
30 with an intermediate hot zone 32. Rather than having the device
10 supported by ceramic 29, the anode-supported version uses the
anode material as the supporting structure. Within the anode
structure, a fuel passage 14 and an air passage 20 are provided in
opposing relation. The air passage 20 is lined with an electrolyte
layer 28, and then with a cathode layer 26. Chemical vapor
deposition could be used to deposit the internal layers, or by
using solutions of viscous pastes.
[0221] In FIGS. 40A and 40B, a further embodiment is shown for an
anode-supported version of the Fuel Cell Stick.TM. device 10. In
this embodiment, the separate open fuel passage 14 is eliminated,
such that the porous anode 24 also serves as the fuel passage 14.
In addition, the Fuel Cell Stick.TM. device 10 is coated with a
barrier coating 60, such as a glass coating or a ceramic coating,
to prevent the fuel from exiting out the sides of the device 10.
The Fuel Cell Stick.TM. device 10 may have as many air passages 14
with associated electrolyte 28 and cathode 26 in the anode
structure as desired. As depicted in FIG. 40B, the fuel from fuel
supply 34 is forced into first end 11a through the porous anode 24,
which serves as the fuel passage 14, and passes through the
electrolyte layers 28 and the cathodes 26 to react with air from
air supply 36, and the spent air and fuel can then exit out the air
outlet 22.
[0222] In another embodiment depicted in a schematic
cross-sectional end view in FIG. 41A and a schematic
cross-sectional top view in FIG. 41B, the Fuel Cell Stick.TM.
device 10 may include a plurality of air passages 20 provided
within the anode-supporting structure, and a single fuel passage 14
normal to the multiple air passages 20 for feeding fuel from the
fuel supply 34 through the single fuel inlet 12 to multiple air
passages 20. Again, the air passages 20 are lined first with an
electrolyte layer 28 and then with a cathode 26. The fuel passes
from the single fuel passage 14 through the anode structure 24,
through the electrolyte 28, and through the cathode 26 to react
with the air in the air passage 20, and the spent fuel and air exit
from the air outlet 22. The spent fuel can also seep out the side
of the Fuel Cell Stick.TM. device 10 that does not include the
barrier coating 60, which uncoated side would be located on the
opposing side of the device 10 from the orientation of the single
fuel passage 14.
[0223] In the embodiments pertaining to an anode-supported
structure, it may be appreciated that the structure may be
essentially reversed to be a cathode-supported structure. Fuel
passages 14 coated with an electrolyte layer 28 and an anode layer
24 would then be provided within the cathode structure. A separate
air passage 20 or multiple air passages 20 could also be provided,
or the porosity of the cathode 26 could be used for the air
flow.
[0224] FIGS. 42A-42C depict a method for forming the electrodes
within the air passages 20 and fuel passages 14. Taking the fuel
passage 14 and anode 24 as an example, rather than building up a
green structure layer by layer using layers of green ceramic and
metal tape layers, or printing metallizations, in the present
embodiment, the Fuel Cell Stick.TM. device 10 is first built
without the electrodes. In other words, green ceramic material is
used to form the electrolyte 28 and ceramic supporting portions 29
of the Fuel Cell Stick.TM. device 10 and the organic material is
used to form the passages, such as fuel passage 14. After the Fuel
Cell Stick.TM. device 10 has been sintered, the fuel passage 14 is
filled with an anode paste or solution. The paste may be thick like
that of a printing ink, or runny like that of a high-content water
solution. The anode material can be filled into the fuel passage 14
by any desired means, such as sucking it in via a vacuum, by
capillary forces, or forcing it in via air pressure.
[0225] Alternatively, as shown in FIGS. 42A-42C, the anode material
is dissolved in solution, flowed into the fuel passage 14, and then
precipitated. For example, through a change of pH, the anode
particles can be precipitated and the solution drawn out. In
another alternative, the anode particles can be simply allowed to
settle, and then the liquid dried or baked out of the fuel passage
14. This settling can be accomplished by creating an ink or liquid
carrier that will not keep the particles in suspension for any
extended period of time, for example, due to low viscosity. A
centrifuge could also be used to force the settling. The centrifuge
can easily allow preferential settling of most particles onto one
surface of the fuel passage 14 to thereby conserve electrode
material and to ensure that only one surface of the fuel passage 14
acts as an electrolyte.
[0226] As shown in FIG. 42A, the anode particle-containing solution
66 is pulled into the fuel passage 14 until the passage 14 is
completely filled, as shown in FIG. 42B. The particles then settle
to the bottom of the passage 14 to form an anode layer 24, as shown
in FIG. 42C. Flooding in of the solution 66 can be accelerated by
gravity, vacuum, or centrifuge, as compared to normal capillary
forces. Of course, while the anode 24 and fuel passage 14 were used
as an example, any of these alternative embodiments may also be
used with a cathode paste or solution to create a cathode layer 26
in an air passage 20.
[0227] In another alternative, a ceramic electrode material (anode
or cathode) could be infused into the passage (fuel or air) in a
liquid sol-gel state, and then deposited inside the passage. It is
also possible to repeat the filling operation multiple times, such
as in the case where the concentration of the desired electrode
material in the liquid is low, or to provide a gradient of
properties in the electrode (such as to provide a different amount
of YSZ in the electrode close to the electrolyte versus the amount
of YSZ in the electrode farther from the electrolyte), or if there
is a desire to put multiple layers of dissimilar materials together
(such as a cathode made of LSM near the electrolyte, and then
silver over the top of the LSM for better conductivity).
[0228] Referring back to FIGS. 7C and 7D, in which ceramic spheres
or balls were used to provide structural support to the air and
fuel passages 20, 14, ceramic particles may also be used to
increase the effective surface area for a greater reaction area,
thus giving a higher output. Very fine-sized ceramic balls or
particles can be used inside the fuel passage 14 and the air
passage 20 prior to applying the electrode layer. As shown in FIG.
43 in schematic cross-sectional side view, surface particles 62
line the passage 14 to provide the electrolyte layer 28 with an
uneven topography that increases the surface area available to
receive the electrode layer. The anode 24 is then applied over the
uneven topography with the anode material coating all around the
surface particles 62 thereby increasing the reaction area.
[0229] In an alternative embodiment, depicted in schematic
cross-sectional side view in FIG. 44, the electrolyte layer 28 may
be laminated so as to provide the uneven topography or textured
surface layer 64, such as by pressing the green electrolyte layer
against a fine grading having a V-shaped pattern, which pattern is
then imparted to the electrolyte layer 28. After the electrolyte
layer 28 is sintered to solidify the ceramic and the textured
surface layer 64, the anode layer 24 may then be applied, such as
by using the backfill process described above in FIGS. 42A-42C, to
provide an anode with a high reaction area.
[0230] Yet another embodiment of the invention is depicted in FIGS.
45A and 45B. FIG. 45A is a schematic top view depicting the air and
fuel flow through air and fuel passages and the arrangement of the
electrodes, and FIG. 45B is a cross-sectional view through the hot
zone 32. Along the length of Fuel Cell Stick.TM. device 10, the
device is divided into a left side 80 and a right side 82 with an
intermediate or bridging portion 84 therebetween. A plurality of
air passages 20L extend from the first end 11a of Fuel Cell
Stick.TM. device 10 along the length through the left side 80 and
exit out the left side 80 adjacent second end 11b, and a plurality
of air passages 20R extend from first end 11a along the length
through the right side 82 and exit the Fuel Cell Stick.TM. device
10 on the right side 82 adjacent the second end 11b. The air
passages 20L are offset from the air passages 20R, as best shown in
FIG. 45B. A plurality of fuel passages 14L extend from the second
end 11b of Fuel Cell Stick.TM. device 10 along the length through
the left side 80 and exit on the left side 80 adjacent first end
11a, and a plurality of fuel passages 14R extend from second end
11b along the length through the right side 82 and exit the right
side 82 adjacent first end 11a. The fuel passages 14L are offset
from the fuel passages 14R. In addition, with the exception of one
fuel passage and one air passage, each fuel passage 14L is paired
with and slightly offset from an air passage 20R and each air
passage 20L is paired with and slightly offset from a fuel passage
14R. For each offset pair of fuel passages 14L and air passages
20R, a metallization extends along each fuel passage 14L from the
left side 80 to the right side 82, where it then extends along the
slightly offset air passage 20R. Similarly, for each offset pair of
fuel passages 14R and air passages 20L, a metallization extends
along each air passage 20L from the left side 80 to the right side
82, where it then extends along the slightly offset fuel passage
14R. The metallization serves as an anode 24L or 24R when the
metallization extends along a fuel passage 14L or 14R, and the
metallization serves as a cathode 26L or 26R when the metallization
extends along an air passage 20L or 20R. In the bridging portion 84
of the Fuel Cell Stick.TM. device 10, where the metallizations do
not extend along any air or fuel passage, the metallization simply
serves as a bridge 90 between an anode and a cathode. In one
embodiment of the present invention, the metallization may comprise
the same material along its length, such that the anode 24L or 24R,
the bridge 90 and the cathode 26L or 26R each comprise the same
material. For example, the metallizations may each comprise
platinum metal, which functions well as either an anode or a
cathode. Alternatively, the metallization may comprise different
materials. For example, the cathodes 26R or 26L may comprise
lanthanum strontium manganite (LSM), while the anodes 24R or 24L
comprise nickel, NiO, or NiO+YSZ. The bridges 90 may comprise
palladium, platinum, LSM, nickel, NiO, or NiO+YSZ. The present
invention contemplates any combination or type of materials
suitable for use as a cathode or an anode, or a bridging material
therebetween, and the invention is not limited to the specific
materials identified above.
[0231] On one side of the Fuel Cell Stick.TM. device 10, shown here
at the right side 82, a fuel passage 14R is provided with an
associated anode 24R that extends to the right edge of the Fuel
Cell Stick.TM. device 10 to provide the external exposed anode 25.
There is no offset air passage 20L associated with this fuel
passage 14R, and the anode 24R need not extend into the left side
80. As depicted in FIG. 45A, an external contact pad 44 is applied
over the exposed anode 25 and extends along the length of the Fuel
Cell Stick.TM. device 10 into the cold zone 30. Negative voltage
node 38 can then be connected by wire 42 and solder connection 46
to the contact pad 44. The anode 24R could extend, as shown, to the
right edge throughout the hot zone 32, or could just extend in a
small tab portion to reduce the amount of electrode material used.
Also, the anode 24R could extend to the right edge of the Fuel Cell
Stick.TM. device 10 along the length of the fuel passage 14R,
although such embodiment would involve an unnecessary use of
electrode material.
[0232] Similarly, on the other side of the Fuel Cell Stick.TM.
device 10, shown as the left side 80, a single air passage 20L is
provided with an associated cathode 26L that extends to the left
side of the Fuel Cell Stick.TM. device 10 to form the exposed
cathode 27. This air passage 20L is not associated with an offset
fuel passage 14R, and it is not necessary that the cathode 26L
extend to the right side 82. A contact pad 44 may be applied along
the exterior of the left side 80 of the Fuel Cell Stick.TM. device
10 from the exposed cathode 27 to a cold end 30, where a positive
voltage node 40 may be connected via wire 42 and solder connection
46 to the contact pad 44.
[0233] In FIG. 45B, the single fuel passage 14R and associated
anode 24R are shown at the top of the right side 82, while the
single air passage 20L and associated cathode 26L are shown at the
bottom of the left side 80 of the Fuel Cell Stick.TM. device 10.
However, the invention is not limited to that arrangement. For
example, air passage 20L and associated cathode 26L could be
provided also at the top of device 10 on the left side 80, in a
similar offset manner to the single fuel passage 14R and its
associated anode 24R, but the metallization would not run from the
left side 80 through the bridging portion 84 to the right side 82.
Rather, the bridge 90 would be absent such that the anode 24R is
electrically separated from the cathode 26L. Additional
arrangements are contemplated in which a Fuel Cell Stick.TM. device
10 may be provided with two unique air pathway stacks and two
unique fuel pathway stacks within a single Fuel Cell Stick.TM.
device 10, with the cells connected in series. The embodiment
depicted in FIGS. 45A and 45B has an advantage of raising the
voltage without raising the current, and while maintaining a low
resistance. Further, this embodiment provides a high density within
the Fuel Cell Stick.TM. device 10.
[0234] In FIGS. 46A and 46B, an alternative embodiment is depicted
in schematic perspective view and schematic cross-sectional view,
respectively. Previous embodiments (e.g., FIG. 37) provided
external stripes along the exterior sides or edges of the Fuel Cell
Stick.TM. device 10 from the hot zone 32 to the cold zone(s) 30 to
provide a path of low resistance for the electrons to travel to the
cold-end. In the embodiment of FIGS. 46A and 46B, instead of
stripes down the sides or edges of the device 10, a contact pad 44
is applied along one side and one of the top and bottom surfaces
for the external connection to the anode 24 and another contact pad
44 is applied along the opposing side and the other of the top and
bottom surfaces for the external connection to the cathode 26.
Thus, the electrons have a large or wide path along which to
travel, thereby providing an even lower resistance. These large
contact pads 44 that are applied on two adjacent surfaces could be
used in any of the embodiments disclosed herein.
[0235] In FIG. 47, yet another embodiment is depicted, in schematic
cross-sectional side view, of a Fuel Cell Stick.TM. device 10 that
takes advantage of heat exchange principles. After the heated air
and fuel pass through the active zone 33b of the hot zone 32 (i.e.,
the portion of the hot zone 32 where the anode 24 is in opposing
relation to the cathode 26 with an electrolyte 28 therebetween),
the fuel passage 14 and air passage 20 are joined into a single
exhaust passage 21. Any un-reacted fuel will burn when combined
with the heated air, thus producing additional heat. The exhaust
passage 21 travels back toward the cold zone 30 adjacent the active
zone 33b, with the direction of flow of the exhaust (spent fuel and
air) being opposite that of the incoming fuel and air in the
adjacent fuel and air passages 14, 20. The additional heat
generated in the exhaust passage 21 is transferred to the adjacent
passages 14, 20 to heat the incoming fuel and air.
[0236] FIGS. 48A-48C depict an "end-rolled Fuel Cell Stick.TM.
device" 400 having a thick portion 402 having a greater thickness
than a thin portion 404, as depicted in FIG. 48A. The fuel and air
inlets 12, 18 are positioned adjacent first end 11a, which is at
the end of thick portion 402, and while not shown, the air and fuel
outlets (16, 22) may be provided at the sides of the device 400
adjacent opposing second end 11b, which is at the end of the thin
portion 404. The thick portion 402 should be thick enough to
provide mechanical strength. This may be achieved by providing
thick ceramic 29 around the adjacent fuel and air inlets 12, 18.
The thin portion 404 will include the active zone 33b (not shown)
that includes an anode (not shown) in opposing relation to a
cathode (not shown) with an electrolyte (not shown) therebetween
(as in prior embodiments). The thin portion 404 should be thin
enough to permit it to be rolled while in the green (unfired)
state, as shown in FIG. 48B. After the thin portion 404 is rolled
to a desired tightness, the device 400 is fired. The rolled thin
portion 404 can then be heated to cause the reaction, while the
thick portion 402 is a cold end, as discussed in other embodiments.
The end-rolled Fuel Cell Stick.TM. device 400 is a large surface
area device that can fit in a small space by virtue of rolling the
thin portion 404. Moreover, the thin cross-section of the active
zone (33b) in the thin portion 404 reduces the heat transfer out
along the ceramic and allows good temperature cycle
performance.
[0237] In embodiments in which the anode 24 and cathode 26 are
exposed at the edges (sides) of the Fuel Cell Stick.TM. device 10
in the active (reaction) zone 32 and/or 33b, the ceramic 29 at the
top of the device 10 may be recessed in the area of the active zone
32 and/or 33b. This allows access to both the cathode 26 and anode
24 from the top for making the electrical connections. Contact pads
44 (e.g., metallization stripes) may then be applied along the top
surface of the Fuel Cell Stick.TM. device 10 from the active zone
32 and/or 33b to the cold zone(s) 30 to provide connections to
outside of the hot zone chamber/furnace.
[0238] In another embodiment in which the Fuel Cell Stick.TM.
device 10 includes two cold zones 30 at the opposing ends 11a, 11b
and the hot zone 32 in the middle, contact pad(s) 44 (e.g.,
metallization stripes) for the anode(s) 24 and/or the cathode(s) 26
can go from the hot zone 32 out toward both ends 11a, 11b of the
Fuel Cell Stick.TM. device 10, for example, as shown in FIG. 36B.
Two separate electrical connections can then be made to each of the
anode(s) 24 and cathode(s) 26. By way of example and not
limitation, one set of connections can be used to monitor voltage
output from the cell, while the other set of connections can
connect the load and allow the current flow. The ability to measure
voltage separately, at the cell itself, has the advantage of giving
a better idea of the total power output from the cell.
[0239] For the contact pads 44 (e.g., metallization stripes), any
suitable conducting material known to those of ordinary skill in
the art may be used. Examples include silver, LSM and NiO.
Combinations of materials may also be used. In one embodiment,
non-precious metal materials may be used along the surface of the
Fuel Cell Stick.TM. device 10 in the hot zone 32. LSM, for example,
may be used where the atmosphere of the hot zone chamber/furnace is
oxidizing. NiO, for example, may be used where the atmosphere of
the hot zone chamber/furnace is reducing. In either case, however,
the non-precious metal materials lose conductivity if the material
extends outside the hot zone chamber/furnace such that the
metallization material must be transitioned to a precious metal or
corrosion resistant material just before the Fuel Cell Stick.TM.
device 10 exits the hot zone chamber/furnace. Silver paste is a
convenient precious metal material. By way of further explanation,
certain materials such as LSM will become non-conducting as the
temperature drops from the reaction temperature to room
temperature, and other materials such as nickel will become
non-conducting when exposed to air at the cold end 30 of the device
10. Thus, the metallization material for the contact pads 44 in the
cold end regions 30 of the Fuel Cell Stick.TM. device 10 must be
conductive in air (i.e., no protective atmosphere) and at low
temperature. Precious metals such as silver work across the
temperature/atmosphere transition area, such that the metallization
material can be transitioned to the precious metal before the Fuel
Cell Stick.TM. device 10 exits the hot zone chamber/furnace. The
use of a combination of materials allows for material selection
based on the particular needs of conductance in a hot zone 32
versus a cold zone 30, and allows for reducing cost by reducing the
amount of expensive precious metals used.
[0240] As depicted in FIGS. 49A-49C, wire 92 or other physical
structure is placed into the device during the process of building
up the green layers (FIG. 49A), the layers are then laminated with
the wire 92 in place (FIG. 49B), and then the wire 92 is removed
after lamination (FIG. 49C). This is useful, for example, at the
entrance point of fuel or air, where the Fuel Cell Stick.TM. device
10 may have a length of several inches before the gas flow passage
14, 20 enters the hot zone 32 (reaction region) of the Fuel Cell
Stick.TM. device 10. Instead of printing a polymer that must bake
out slowly in the process to form the passage, the wire process may
be used to remove the bake-out challenge from that part of the Fuel
Cell Stick.TM. device 10. By way of example and not limitation, a
wire 92 with a 0.010 inch diameter may be used, which will pull out
easily. The wire 92 may also be rolled flat, to form a ribbon-like
physical structure that has a similar volume as the wire, but is
shorter in cross section. Because the ribbon has more surface area,
a release agent may be applied to the surfaces thereof to keep it
from sticking to the ceramic layers during lamination. Thus, the
term "wire" is intended to broadly include various physical
structures that are long and then narrow, whether circular, oval,
square, rectangular, etc. in cross-section.
[0241] FIGS. 50A-50C depict an example of forming entrance channels
for a 1 layer Fuel Cell Stick.TM. device 10. In this example,
rather than using a gap-forming tape 94 (e.g., polymer or wax tape)
to form the entire fuel and oxidizer passages 14, 20, the
gap-forming tape 94 is only used in the active zone 33b, i.e., in
the regions where the anodes 24 and cathodes 26 are positioned in
opposing relation with electrolyte 28 therebetween. In the
non-active regions where the fuel and oxidizer passages 14, 20 do
not have an associated opposed anode 24 and cathode 26, wires 92
are used instead of the gap-forming tape 94. As shown, the wires 92
touch or overlap the gap-forming tape 94 so that the passages 14,
20 formed by the wire 92 and the gap-forming tape 94 are continuous
from the inlets 12, 18 to the outlets 16, 22 (not shown).
[0242] As Fuel Cell Stick.TM. devices 10 become more and more
complicated, it can be more and more useful to use this wire
concept, for example, the complex bake-out challenge of a
multi-layer Fuel Cell Stick.TM. device 10 (e.g., 50 layers) can be
simplified. This is in part because the challenge for binder
removal, especially in complicated structures, is that the binder
bake-out products must travel from the location that they are
generated (from the decomposition of polymer) to the outside of the
Fuel Cell Stick.TM. device 10. After a wire 92 is pulled out of the
structure, however, the path along this void is free and clear. If
wires 92 (or other suitable physical structure) can be put into a
complicated structure, and then pulled out, the voids created
thereby can allow many regions within the structure for bake-out
products to quickly find a path out of the structure.
[0243] Another useful purpose for the wire concept is to help with
pressure distribution within the Fuel Cell Stick.TM. device 10.
When a single tube is supplying air or fuel to the Fuel Cell
Stick.TM. device 10, then different flow rates may exist along the
many passages/channels within the Fuel Cell Stick.TM. device 10.
For example, if there are 50 air passages 20 in the Fuel Cell
Stick.TM. device 10, corresponding to 50 active layers, then there
may be one passage that has a slightly larger sectional area, and
one passage that has a slightly smaller sectional area. This can
arise from random variation in the dimensions of the gap-forming
materials. One solution is to limit the sectional area of the exit
from each layer. If the cross section of the exit point from each
layer can be precisely made, so that those sectional areas are
equal, and if the sectional area of the exit point is less than the
area of the flow channel, and if the area of all those exit points
is less that the sectional area of the input tube, then the flow
will be equal on each layer. This corresponds with the
practicalities of gas and fluid flow. The wire concept enables this
solution. At the exit point of each layer, a wire 92 is inserted to
make the final passage of the gas to the outside world. For 50
layers, 50 short wire pieces are inserted. When they are pulled
out, each layer has a precision exit dimension (for example, a 5
mil diameter passageway).
[0244] Thus, the present invention contemplates a multilayer Fuel
Cell Stick.TM. device 10 in which the exit points of each layer are
smaller in sectional area than the flow path sectional area itself.
The present invention further contemplates a multilayer Fuel Cell
Stick.TM. device 10 in which the exit points of each layer are
precision machined so that they have exactly the same cross
sectional area at some given location. The present invention yet
further contemplates a multilayer Fuel Cell Stick.TM. device 10
where all exit areas put together are smaller than the sectional
area of the input. In these embodiments, the sectional area of the
exit point is defined as being at some location in the flow path
that is beyond the end of the active portion of the layer, but
before the end output point of the Fuel Cell Stick.TM. device 10.
In other words, this neck-down point in the flow path does not have
to be exactly at the exit point from the Fuel Cell Stick.TM. device
10, just somewhere downstream from the active area.
[0245] In previous embodiments, the hot zone 32 and hot zone
chamber have been discussed. The hot zone chamber may also be
referred to as a furnace. The cold zone or cold end regions 30 are
positioned outside of the furnace. The transition zone 31 is a
region of the Fuel Cell Stick.TM. device 10 adjacent the region
inside the furnace. As depicted in FIG. 51, the furnace wall 96 has
a total thickness T. The Fuel Cell Stick.TM. device 10 passes
through this furnace wall 96. The length of the Fuel Cell Stick.TM.
device 10 in the wall 96 is the X dimension and is equal to
thickness T. The width of the Fuel Cell Stick.TM. device 10 as it
passes through the wall 96 is the Y dimension. The thickness of the
Fuel Cell Stick.TM. device 10 is the Z dimension. For purposes of
this embodiment, Z is less than or equal to Y.
[0246] According to an embodiment of the invention, for optimal
conditions, the furnace wall thickness T should be greater than the
width, Y, of the Fuel Cell Stick.TM. device 10 as it passes through
the wall 96. If T is less than Y, then the stress on the Fuel Cell
Stick.TM. device 10 as it passes through the wall 96 may be too
high, and the Fuel Cell Stick.TM. device 10 could crack.
[0247] In another embodiment, depicted in FIGS. 52A-52C, dimension
L is the maximum dimension in a plane transverse to the direction
of the length of the device 10 (i.e., in the Y-Z plane) of the Fuel
Cell Stick.TM. device 10, (100, 200, 300 or 400) at the portion
where it passes through the furnace wall 96. For a rectangular Fuel
Cell Stick.TM. device 10 (100, 400), the maximum dimension L may be
the diagonal, as shown in FIG. 52B. For a tubular Fuel Cell
Stick.TM. device 200, 300, the maximum dimension L may be the
diameter. For optimal conditions, the dimensions should be such
that T>1/2 L.
[0248] The wall thickness T may be made from one uniform material
(insulation) 98. Alternatively, as depicted in FIG. 53, the wall
thickness T may also be made from multiple, graded insulation
layers, such as three insulation layers 98a, 98b, 98c, such that
the heat transfer properties are optimized in each layer to give
the best possible temperature transition results. In the case of a
multiple-layer furnace wall 96', the total thickness T of all
layers put together should be greater than Y and/or greater than or
equal to 1/2 L, but the thickness of one layer of the wall 96'
could be less than Y and/or less than 1/2 L.
[0249] In another embodiment, depicted in FIG. 54, a multiple-layer
furnace wall 96'' is provided in which multiple layers of
insulation 98a, 98c may be separated by air gaps 120. In this
design, there could be a high-temperature insulation layer 98c
close to the hot zone 32, and a lower temperature insulation layer
98a close to the cold zone 30. An intermediate (medium) temperature
zone then lies between the two insulation layers 98a and 98c, for
example, corresponding to transition zone 31 or a preheat zone 33a.
This embodiment can enable a longer preheat area for the air that
is flowing into the Fuel Cell Stick.TM. device 10, while not having
to make the hottest area of the furnace larger. In this embodiment,
the thickness of one layer of wall 96'' could be made to be less
than the Y dimension of the Fuel Cell Stick.TM. device 10 and/or
less than 1/2 L as it passes through the wall 96''. But the total
dimension T of the wall 96'', including layers 98a and 98c, and the
air gap 120 would be larger than the Y dimension of the Fuel Cell
Stick.TM. device 10 and/or greater than or equal to 1/2 L. This
embodiment further contemplates more than two insulation
layers.
[0250] Discussed above is the idea of first making the Fuel Cell
Stick.TM. device 10 without the anode and cathode, and then
backfilling those elements later. The reason for doing this can be
that a certain anode or cathode material will densify too much at
the sintering temperature of Zr, and if it is too dense then it
will not allow a good reaction. Or, to say it more generically,
backfilling can be necessary if the different components of the
system do not want to sinter optimally with the same temperature
profile.
[0251] It is more difficult, however, to provide the current
collectors on the top portions of the anode or cathode. A current
collector 122, as shown in FIGS. 55A-55E discussed below, is known
to those skilled in the art to be a high-density electrode
positioned as a surface portion of an anode or cathode. It
generally is a highly electrically conductive layer or matrix, like
a fine wire, that can collect the electrons and move them where
they need to go. The current collector 122 may be made of NiO, or
LSM, or some other low cost material, or even precious electrodes.
Following a backfill process for forming the anodes and cathodes,
it is difficult to put on a precise current collector in a uniform
way. But the challenge of a current collector is different than
that of an anode or cathode. It is desirable for the anode and
cathode to be porous, which causes the danger of over-firing;
whereas the collector is desirably dense (for good conductivity),
so potentially, it can be co-fired with the Zr. While the current
collector 122 could be placed on the electrolyte 28 before
back-filling, such that the current collectors are under the anode
and cathode, touching the electrolyte 28, this arrangement blocks
active area on the electrolyte 28, which is needlessly wasteful of
active area.
[0252] In accordance with an embodiment of the invention, and as
depicted in FIGS. 55A-55E, the current collectors 122 are
positioned and co-fired so as to have them floating in space within
the Fuel Cell Stick.TM. device 10. This may be accomplished by
printing the current collector 122 on top of a sacrificial first
organic layer 72a (e.g., polymer), and then coating a sacrificial
second organic layer 72b (e.g., polymer) over the top of the
current collector 122 as shown schematically in FIG. 55A. The
current collector 122 is thereby sandwiched between two sacrificial
organic layers 72a, 72b, as shown in FIG. 55B. The Fuel Cell
Stick.TM. device 10 is built, including placing the sacrificial
layers/current collector structure within a ceramic supporting
structure 29, as shown in FIG. 55C, and then sintered, whereby the
sacrificial organic layers 72a, 72b disappear to form a gap 123 and
the current collector 122 is left floating in space within the gap
123, as shown in FIG. 55D. It is then easy to backfill the porous
anode or cathode into the gap 123, to complete the anode or cathode
formation. The use of support pillars 54, as described above, may
also be used, such that the floating current collector 122 rests on
the support pillars 54, as shown in FIG. 55E, to provide mechanical
support or to standardize the location. To achieve this, periodic
via holes or small gaps may be created in the first sacrificial
layer 72a of polymer, so that the current collector material would
periodically print down into a hole. After binder removal, this
filled hole becomes a support pillar 54. Alternatively, zirconia
balls may be added into the sacrificial polymer gap material. As
the sacrificial polymer dissolves, the current collector 122 would
stick to those balls, and the balls would stick to the ceramic
supporting structure 29, as shown in FIGS. 56A and 56B, thus
providing the support. The porous anode 24 or cathode 26 then can
be backfilled into the space, as shown in FIGS. 57A and 57B, in
which the electrode particles 124 are held in viscous liquid 126
for the back-fill, then the device is dried and the particles
settle and are sintered to form the anode 24 or cathode 26. The
anode or cathode particles can be selectively deposited onto one
side, if that is useful (by gravity or by centrifuge).
[0253] With a current collector style that uses printed hatch
lines, there may be some variation in the gap dimension of the air
or fuel passage 14, 20 resulting in the passage becoming pinched or
blocked at the current collector 122. This variation occurs due to
random dimensional changes during sintering. FIGS. 58A-58C are
micrographs that show an example of a current collector 122 that is
nearly causing a blockage of a passage 14, 20. The goal for the
passage 14, 20 is to have clear flow. It is possible to make the
passages larger, but this will unnecessarily decrease the density
of the Fuel Cell Stick.TM. device 10 (thicker passages and thicker
layers lower the power density of the multi-layer device).
According to one embodiment of the invention, to reduce the
possibility of the passages 14, 20 being blocked at the current
collector 122, the current collector lines may be buried within the
porous anode 24 and cathode 26. As depicted in FIGS. 59 and 60, in
which FIG. 59 shows the current collectors 122 on the surfaces of
the anode 24 and cathode 26 and FIG. 60 shows the current
collectors 122 buried into the surfaces of the anode 24 and cathode
26, if the current collectors 122 are buried into the thickness of
the porous anode and cathode 24,26 (or substantially buried into
the anode/cathode) then the current collector 122 will be less
likely to block the path of gas flow. FIG. 69 shows an actual
current collector trace that has been recessed into the porous
anode or cathode.
[0254] A method of burying the current collector 122 is shown in
FIGS. 61A-61C. First, dispense or print the current collector 122
onto a temporary substrate 128. Then, cover this current collector
122 with the electrode material such as by printing a paste or
backfilling with a viscous liquid 126 containing electrode
particles 124 and drying. Finally, remove the temporary substrate
128. The temporary substrate 128 may be a piece of plastic with
only moderate adhesion to the electrode material after drying such
that the dried electrode-on-plastic can be turned over and the
plastic peeled off. The same or similar result may be achieved by
putting the current collector 122 and anode/cathode 24,26 onto the
gap-forming tape 94 that is inserted into the stack, and during
bake-out and sintering, the gap-forming tape 94 will disappear,
leaving the same end result.
[0255] When printing the anode 24 or cathode 26 over the top of the
current collector 122, if the current collector 122 tends to
dissolve a little and spread out, materials with different
solubilities may be used (in the extreme case, the current
collector 122 can contain resin material that is soluble in polar
solvents, and the porous electrode ink can have a resin material
soluble in non-polar solvents). It is desirable to limit this
spreading, because too much spreading of the current collector 122
will work to reduce the diffusion of gasses into the porous anode
24 or cathode 26. So, it is possible that some spreading of the
current collector 122 will happen, but at least a portion of the
current collector 122 is desirably buried in the porous material.
Thus, this invention contemplates a current collector path where
some portion of the current collector 122 is recessed into the
porous anode 24 or cathode 26 in order to reduce the protrusion of
the current collector 122 in to the fuel passage 14 or air passage
20.
[0256] In the active zone 33b of the multilayer Fuel Cell Stick.TM.
device 10, one would like to have the electrolyte 28 be as thin as
possible, for example, 10 .mu.m. But a super-thin electrolyte
increases the possibility of having a leak between the air and fuel
sides of the device. Thinner electrolyte can give higher power, but
too thin will allow a crack or leak, and give zero output from the
layer. According to one embodiment of this invention, a key to the
minimum allowable thickness of the electrolyte 28 in the active
zone 33b is that the anode and cathode thickness also contribute to
the total thickness, and therefore to the total strength. By way of
example only and not limitation, if 100 .mu.m of thickness is
desired to prevent cracking, and each anode 24 and cathode 26
measures 45 .mu.m, then a 10 .mu.m electrolyte thickness will work
well. (45+45+10=100).
[0257] In the passive area (areas without an opposing anode and
cathode) of a multilayer Fuel Cell Stick.TM. device 10, there is a
different thickness required. This passive area is responsible for
distribution of air and fuel. This has been shown in many of the
drawings as air and fuel distribution passages that overlap. The
requirement here is also to have a certain thickness to prevent
cracking, but without the anode 24 and cathode 26, the ceramic 29
here must be thicker than the ceramic electrolyte layer 28 in the
active zone 33b. So in the example above, the ceramic 29 in the
passive area must be 100 .mu.m while the ceramic electrolyte layer
28 in the active zone 33b can be thinner, such as 10 .mu.m.
[0258] According to an embodiment of the invention, a method is
provided for achieving an individual layer of ceramic electrolyte
28, 29 with two thicknesses: thicker ceramic 29 in the passive gas
passages area, and thinner ceramic electrolyte 28 in the active
zone 33b. The method, depicted in FIGS. 62-62A, uses three pieces
of ceramic tape 130 to create the ceramic 29 in the passive gas
flow region, where two of the tape pieces 130a, 130c end and only
the center layer 130b continues into the active zone 33b to serve
as ceramic electrolyte 28 between the opposing anode 24 and cathode
26.
[0259] Numerous ideas are presented above in the context of an
elongate structure that exits the furnace for low temperature
connections. However, many of the ideas also may be used in
multi-layer Fuel Cell devices that do not exit the furnace and/or
that have a plate shape or the like. The densities of the devices
achievable in the present invention may be achieved in other Fuel
Cell devices and systems where connections are made to the hot Fuel
Cell device in a furnace. For example, concepts disclosed herein
that may be used in other fuel cell devices include polymer tape,
polymer tape filled with round balls, a wire used to form exit or
entrance passages, one passage serving two electrodes, a
paddle-shaped device, drying the electrode suspension towards one
side by using gravity or centrifuge, side gaps for termination and
series design.
[0260] The current collector 122 has a purpose of allowing
electrons that are produced or consumed in the electrodes (anode 24
and cathode 26) to travel in a low-resistance path on their way to
the load (voltage nodes 38, 40). The optimal electrode design is
not very conductive because it must allow several things to happen
at once: there are pores to allow the gases to flow, there is
ceramic in the electrodes to allow the oxygen ions to flow toward
the electrolyte, and there are electronic conductors to let the
electrons flow. The presence of the pores and the ceramic means
that the electrode overall will have higher resistance than if it
was only made of electronic conductor.
[0261] Once the electron is liberated, it is important to allow it
to travel on a high conductivity path. Existing designs for current
collectors are based on removing the electrolyte ceramic from the
conductor, but still leaving the porosity. This creates a more
conductive layer. This is printed over the entire anode or cathode.
One disadvantage of this design in a multilayer structure is that
if the anode/cathode materials have to be added after sintering, it
can be difficult to create two distinct layers, as described. The
advantage of co-firing a current collector is described above.
[0262] According to an embodiment of the invention, a current
collector 122 may be used that comprises a high-density conductor
material (i.e., little or no porosity, such that if it was printed
over the entire anode 24 or cathode 26 it would inhibit the
reaction), which is printed in a hatch pattern. In one embodiment,
the collector is printed in a rectilinear pattern, also referred to
as a hatch pattern, leaving open space between the hatch marks for
the gas to penetrate. Gas permeability in the porous anode 24 and
cathode 26 is such that the gas that enters the porous material
between hatch lines will also flow under the hatch lines. By
varying the pitch from line to line, and the line width itself, it
is possible to find an optimal geometry. By way of example, a
0.006'' line width and a 0.030'' line pitch may be used. FIG. 63
depicts a top view of a current collector 122 with a hatch pattern.
FIG. 64 depicts a side view of the current collector 122 over
porous anode or cathode. FIG. 65 depicts an angled view, showing in
order from top to bottom: current collector hatch, top porous
electrode, electrolyte, and bottom electrode (sticking out from
electrolyte because of fracture). As the active area becomes
larger, it would also be possible to vary the line width in
different regions. Small conductor lines could feed into larger
conductor lines, and larger lines could feed into still larger
conductor lines.
[0263] Flexible supply tubes 50 have been described above for
connecting the fuel and air supplies 34,36 to the Fuel Cell
Stick.TM. device 10. By stretching the supply tube 50 open, it can
be slipped over one of the ends 11a, 11b of the Fuel Cell Stick.TM.
device 10. An adhesive can hold it in place. An alternative,
according to one embodiment of the invention, is to form the end
11a (and/or 11b) of the Fuel Cell Stick.TM. device 10 with
indentations 132 on the sides, as depicted in FIGS. 66A-66B, so
that the Fuel Cell Stick.TM. device 10 will mechanically hold the
supply tube 50 in place. This is achieved most conveniently in the
green state by machining the Fuel Cell Stick.TM. device 10 with a
router or end mill.
[0264] Based on this, a connector 134 may also be used that can
clamp on to the end 11a (and/or 11b) of the Fuel Cell Stick.TM.
device 10, as depicted in FIGS. 67A-67B in top schematic
cross-sectional and perspective view, respectively. The connector
134 may be a molded plastic with integrated electrical contacts 136
and a gas flow pathway 138, either one or two, depending on the
design of the Fuel Cell Stick.TM. device 10, and a gas-tight seal,
such as in the form of an O-ring 140, and either one or two
electrical contacts 136 for contacting the contact pad(s) 44. If
the Fuel Cell Stick.TM. device 10 is a two ended Fuel Cell
Stick.TM. device 10, such that one polarity is exiting the Fuel
Cell Stick.TM. device 10 at each end of the Fuel Cell Stick.TM.
device 10, then the connector 134 could still have two or more
electrical contacts 136 at each end of the Fuel Cell Stick.TM.
device 10 in order to give lower resistance contacts. The
electrical contacts 136 could be on the sides of the Fuel Cell
Stick.TM. device 10 or on the top and bottom of the Fuel Cell
Stick.TM. device 10, the latter of which would give lower
resistance because the contacts are wider.
[0265] Although not shown, the connector 134 could have two
O-rings, thereby providing two sections of sealing within the
connector 134: one for air, the other for fuel. Such a connector
could be used as a single connector on a single-ended Fuel Cell
Stick.TM. device 10, which provides positive and negative contacts,
and air and fuel delivery.
[0266] The embodiments described above included two opposing ends
11a, 11b for the device. However, the concepts of the Fuel Cell
Stick.TM. device 10 described above could be applied to a device
500 that has more than 2 ends or exit points leaving the furnace.
For example, FIGS. 68A-68B depict devices having 4 points of exit.
The four locations could provide the air inlet 18, air outlet 22,
fuel inlet 12, and fuel outlet 16. This could make it easier to
recycle unburned fuel into the furnace heating operation. Exit
points other than 2 and 4 may be used, such as 3 or 6.
[0267] The use of support balls (see FIGS. 7C-7D) may be used in
Fuel Cell devices other than Fuel Cell Stick.TM. devices 10, for
example, square plate devices. The support balls allow large areas
to be created in the multilayer structure, without having the
different layers collapse on each other. The device could have
large, open areas within a generic multilayer plate. Or, the device
could have paths that were 0.5 inch wide, but many inches long,
filling the area. In either case, the ball technology disclosed
herein would be advantageous.
[0268] A key idea of the balls is that they are rounded, which can
prevent puncture. Because there is a need to make the electrolytes,
anodes and cathodes thin (for density, and for higher performance),
it is possible for punctures to arise from the use of irregularly
shaped materials. Sand or grit could dig into the electrolyte and
cause a leak. On the other hand, the electrolyte can gently deform
around the balls without causing leaks or tears. Similarly, the
pillar concept of FIGS. 7A-7B can be used in a multilayer Fuel Cell
structure other than the Fuel Cell Stick.TM. device 10 form.
[0269] In FIGS. 38A-38B, we show the use of multiple bake-out ports
that can later be sealed over. This is an advantageous concept for
any multilayer approach to the SOFC or other fuel cell device.
Again, regarding the large plate, the designer will have large
areas of gas passages that are being created, and the need to
remove the organic material that fills those spaces. Typically,
however, there is only one fuel entrance point, and one fuel exit
point. The same is true of the air side. With such large areas of
organic material, but so few exit points, it is likely that one of
the largest manufacturing challenges will be to avoid
delaminations.
[0270] The solution to this is to create numerous bake-out points,
small openings that can allow bake-out gasses or liquids (in the
case that wax is used) to come out of the structure with minimum
stress on the entire structure. After the multilayer structure is
sintered, it is easy to come back later and fill in those small
bake-out points with a solid material to prevent leaks (such as a
glass-ceramic combination).
[0271] The wire 92 concept is a lot like the bake-out port concept
above, and very useful for a multilayer structure. Imagine making a
4 inch square plate, with 20 or 50 active layers in the plate. You
would like to create the bake-out ports for easier organic removal.
But it would be even better if these convenient bake-out ports
could reach into the center of the plate. By inserting the wire 92
and then pulling it out after lamination, this can be accomplished.
The wire 92 could cut across several areas that otherwise might
have very long distances to go between the middle of the plate and
the outside world. The concept does not have to be a wire exactly,
as discussed above. That is just the most convenient form, because
it has a low surface area. The physical piece could be flat, for
example 0.002'' thick by 0.200'' wide. In that case, it might need
to be covered with a release agent to prevent the layers from
sticking. Regardless, the idea is a physical piece that is inserted
into the structure and then removed in order to facilitate organic
removal.
[0272] In another embodiment, carbon tape with wax is used as a
gap-forming tape 94. A challenge is to have the gap-forming
material come out evenly without causing splitting or delamination
in the Fuel Cell Stick.TM. devices 10. It would be better if the
material could magically disappear at the right time, leaving open
channels so that the other polymer materials in the anode 24 and
cathode 26 and electrolyte 28 could bake out. One approach is to
use wax. The waxes that are used for investment casting (the
so-called lost wax method) work well melting at around 90.degree.
C., above the lamination temperature used to laminate the
multilayer structure, but below the binder burnout temperatures of
150-300.degree. C. But wax is not ideal because if you cast it into
a 2-mil thick sheet, it does not have desirable strength. It is
brittle to the touch. The wax should be stronger in the thin
section. The solution to this is to combine the wax with some kind
of fiber to give it strength. One choice is carbon fiber. The
carbon fiber can be purchased in a random fiber configuration,
called mat, or in a woven fiber configuration, that resembles
actual cloth. Other fibers may also be possible. By impregnating
the wax into carbon fiber, optimal properties can be obtained. The
carbon/wax composite can be put into the multilayer structure to
form a gap. After lamination, the temperature is raised to the
melting point of the wax, and the wax then turns to liquid and runs
out of the Fuel Cell Stick.TM. device 10. This leaves open-air
pathways within the carbon fibers, which allows easy bake-out of
the surrounding polymer materials inside the structure. The carbon
fiber does not volatilize (turn to CO.sub.2) until temperatures
near 750.degree. C. Thus, it is possible to make a structure where
one of the chief gap formation materials disappears before binder
burn-out occurs, thereby leaving clear paths for binder removal.
Then, at the mid temperatures, the polymer itself can volatilize.
Finally, at the high temperatures, the carbon fibers can disappear.
FIG. 70 is an image of the gap left once the wax and carbon fibers
are gone after sintering using this carbon-wax combination.
[0273] While the invention has been illustrated by the description
of one or more embodiments thereof, and while the embodiments have
been described in considerable detail, they are not intended to
restrict or in any way limit the scope of the appended claims to
such detail. Additional advantages and modifications will readily
appear to those skilled in the art. The invention in its broader
aspects is therefore not limited to the specific details,
representative apparatus and method and illustrative examples shown
and described. Accordingly, departures may be made from such
details without departing from the scope of the general inventive
concept.
* * * * *