U.S. patent application number 11/452591 was filed with the patent office on 2007-08-02 for epitaxial thin films.
Invention is credited to Girish Deshpande, Andrew Tye Hunt, Tzyy-Jiuan Jan Hwang, Wen-Yi Lin.
Application Number | 20070178227 11/452591 |
Document ID | / |
Family ID | 34082578 |
Filed Date | 2007-08-02 |
United States Patent
Application |
20070178227 |
Kind Code |
A1 |
Hunt; Andrew Tye ; et
al. |
August 2, 2007 |
Epitaxial thin films
Abstract
Epitaxial thin films are formed on textured substrates. An
electrode is formed on the exposed surface of the thin film; the
textured substrate removed, and second electrode is formed on the
thin film on the side opposite the first electrode. A capacitor is
thereby formed.
Inventors: |
Hunt; Andrew Tye; (Atlanta,
GA) ; Deshpande; Girish; (Atlanta, GA) ; Lin;
Wen-Yi; (Ellington, CT) ; Hwang; Tzyy-Jiuan Jan;
(Alpharetta, GA) |
Correspondence
Address: |
nGimatCo.;MICROCOATING TECHNOLOGIES, INC.
5315 PEACHTREE INDUSTRIAL BLVD
ATLANTA
GA
30341-2107
US
|
Family ID: |
34082578 |
Appl. No.: |
11/452591 |
Filed: |
June 15, 2006 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
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10862605 |
Jun 7, 2004 |
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11452591 |
Jun 15, 2006 |
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09889237 |
Jul 10, 2001 |
7033637 |
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PCT/US00/00824 |
Jan 12, 2000 |
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11452591 |
Jun 15, 2006 |
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60115519 |
Jan 12, 1999 |
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Current U.S.
Class: |
427/79 ;
427/126.3 |
Current CPC
Class: |
B01D 67/0072 20130101;
Y10T 29/49115 20150115; H01G 4/1209 20130101; Y02P 70/50 20151101;
H01G 4/33 20130101; Y10T 29/53204 20150115; Y02P 70/56 20151101;
Y02E 60/50 20130101; B01D 2256/12 20130101; Y10T 29/5313 20150115;
C23C 16/453 20130101; Y02E 60/525 20130101; H01M 8/0687 20130101;
Y10T 29/532 20150115; H01M 8/1253 20130101; B01D 2325/26 20130101;
B01D 71/024 20130101; B01D 53/228 20130101; Y10T 29/53135 20150115;
B01D 2325/22 20130101; H01M 8/124 20130101 |
Class at
Publication: |
427/079 ;
427/126.3 |
International
Class: |
B05D 5/12 20060101
B05D005/12 |
Goverment Interests
GOVERNMENT CONTRACT
[0002] The United States Government has rights in this invention
pursuant to Contract No. F33615-98-C-5418 awarded by the United
States Department of Defense, and Contract Nos. DE-FG02-97ER82345,
ACQ-9-29612-01 and 4500011833 awarded by the United States
Department of Energy.
Claims
1. A method of making a high permittivity dielectric layer between
a pair of opposing electrodes comprising the steps of: forming, as
said high permittivity dielectric layer, an epitaxial thin film on
a textured substrate; forming one of said electrodes on an exposed
surface of said thin film; wholly or partially removing said
textured substrate; and forming an electrical connection to access
said high permittivity dielectric layer on the side of said
textured substrate.
2. The method of claim 1, wherein at least one of said electrodes
is formed by being directly deposited on the surface of said thin
film.
3. The method of claim 1, wherein an insulator is formed onto parts
of the side of the textured substrate.
4. The method of claim 1, further comprising the step of forming
the dielectric layer as part of a discrete capacitor.
5. The method of claim 1 further comprising forming the dielectric
layer as part of a tunable filter.
6. The method of claim 1 further comprising forming the dielectric
layer as part of a phase shifter.
7. A method of making a dielectric layer between a pair of opposing
electrodes comprising the steps of: forming, as said dielectric
layer, an epitaxial cerate or zirconate thin film on a textured
substrate; forming one of said electrodes on an exposed surface of
said cerate or zirconate thin film; wholly or partially removing
said textured substrate; and forming an electrical connection to
access said dielectric layer on the side of said textured
substrate.
8. The method of claim 7 wherein said dielectric can transmit
oxygen.
9. The method of claim 7, wherein at least one of said electrodes
is formed by being directly deposited on the surface of said thin
film.
10. The method of claim 7, wherein an insulator is formed onto
parts of the side of the textured substrate.
11. The method of claim 7, further comprising the step of forming
the dielectric layer as part of a discrete capacitor.
12. The method of claim 7 further comprising forming the dielectric
layer as part of a tunable filter.
13. The method of claim 7 further comprising forming the dielectric
layer as part of a phase shifter.
14. A method of making a conductive oxide dielectric layer between
a pair of opposing electrodes comprising the steps of: forming, as
said conductive oxide dielectric layer, an epitaxial thin film on a
textured substrate; forming one of said electrodes on an exposed
surface of said thin film; wholly or partially removing said
textured substrate; and forming an electrical connection to access
said conductive oxide dielectric layer on the side of said textured
substrate.
15. The method of claim 14, wherein at least one of said electrodes
is formed by being directly deposited on the surface of said thin
film.
16. The method of claim 14, wherein at least one electrode is a
cermet.
17. The method of claim 14, wherein an insulator is formed onto
parts of the side of the textured substrate.
18. The method of claim 14, further comprising the step of forming
the dielectric layer as part of a discrete capacitor.
19. The method of claim 14 further comprising forming the
dielectric layer as part of a tunable filter.
20. The method of claim 14 further comprising forming the
dielectric layer as part of a phase shifter.
Description
RELATED CASES
[0001] This application is a divisional of U.S. Utility patent
application Ser. No. 09/889,237, filed Jul. 10, 2001, which is a
U.S. National filing of International Application No.
PCT/US00/00824, filed Jan. 12, 2000 and claiming priority to U.S.
Provisional Patent Application Ser. No. 60/115,519, filed Jan. 12,
1999.
FIELD OF THE INVENTION
[0003] The invention relates to epitaxial thin films, and more
particularly to epitaxial thin films for use as, inter alia, buffer
layers for high temperature superconductors, electrolytes in solid
oxide fuel cells (SOFC), gas separation membranes or dielectric
material in electronic devices.
BACKGROUND OF THE INVENTION
[0004] While the ability to deposit epitaxial coatings on textured
substrates has been demonstrated in the past, the methods to
produce these coatings have several disadvantages such as being
relatively slow as well as requiring expensive vacuum and other
extensive equipment. Furthermore, the use of epitaxial coatings has
been limited to only a few applications in the past. With the
advent of combustion chemical vapor deposition (CCVD), a new,
quicker and less expensive method of producing these coatings has
been realized. In addition to the cost savings and reduced
environmental impact achieved by using the CCVD method, the use of
epitaxial coatings has been expanded to several other fields.
[0005] The chemical vapor deposition processes that have been so
successful include the combustion chemical vapor deposition (CCVD)
processes described in U.S. Pat. Nos. 5,652,021; 5,858,465; and
5,863,604, and issued to Hunt et al. These patents, which are
hereby incorporated by reference, disclose methods and apparatus
for CCVD of films and coatings wherein a reagent and a carrier
medium are mixed together to form a reagent mixture. The mixture is
then ignited to create a flame or the mixture is fed to a plasma
torch. The energy of the flame or torch vaporizes the reagent
mixture and heats the substrate as well. These CCVD techniques have
enabled a broad range of new applications and provided new types of
coatings, with novel compositions and improved properties. In
addition to these three patents, U.S. Pat. No. 5,997,956, also
issued to Hunt et al. describes a further method of CVD involving
the use of a thermal spray with near supercritical and
supercritical fluid solutions. The coating processes disclosed in
this patent are also useful for forming the epitaxial coatings of
the present invention, and this patent is incorporated by reference
as well.
[0006] U.S. Pat. Nos. 5,739,086, issued on Apr. 14, 1998 and
5,741,377 issued on Apr. 21, 1998, both to Goyal et al. teach
textured articles having a rolled and annealed, biaxially textured
metal substrate and an epitaxial coating deposited thereon. The
articles are manufactured by rolling and annealing a metal base
preform to create a biaxially textured substrate with a
face-centered cubic, body-centered cubic or hexagonal closed-packed
crystalline structure. Onto the surface of the substrate, an
epitaxial layer is deposited to form a biaxially textured laminate.
A buffer layer in the form of an epitaxial barrier layer may first
be deposited, followed by an epitaxial superconducting layer
deposited thereon. A pulsed laser technique, as well as several
other techniques may be used to deposit the superconducting and
buffer layers.
[0007] U.S. Pat. No. 5,523,587 issued on Jun. 4, 1996 to Kwo is
drawn toward a method for low temperature growth of epitaxial
silicon, and devices produced using this method. The thin layer of
epitaxial silicon is grown at temperatures at or below 300.degree.
C. by first providing a substrate, forming a dielectric buffer
layer and then growing the epitaxial silicon on the buffer layer. A
directed ion beam bombards the buffer layer while it is being
deposited to provide the desired orientation. The low temperatures
used in this deposition process allow for the use of light-weight
substances such as glass coated plastics to reduce the weight of
displays in hand held and lap-top electronic equipment. These
deposition methods, however, require vacuum and other limiting
deposition parameters.
[0008] U.S. Pat. No. 5,968,877, issued on Oct. 19, 1999 to Budai et
al. discloses high T.sub.c YBCO superconductor deposited on a
biaxially textured Ni substrate. One or more epitaxial buffer
layers are deposited on the Ni substrate prior to the deposition of
the c-axis oriented YBCO top layer. The epitaxial buffer layers
include CeO.sub.2, yttria-stabilized ZrO.sub.2 and palladium, while
the superconducting layer is YBa.sub.2Cu.sub.3O.sub.7-.delta.. The
buffer layers are deposited by pulsed-laser, electron beam
evaporation, or sputtering methods.
[0009] International Patent Application, Publication No. WO
99/15333, published on Apr. 1, 1999 to Fritzemeier et al. is drawn
to superconducting articles with epitaxial layers. The articles are
produced in a partial vacuum environment using a gas phase method.
The epitaxial or buffer layers may include CeO.sub.2,
yttria-stabilized ZrO.sub.2, LaAlO.sub.3, SrTiO.sub.3, LaNiO.sub.3,
LaCuO.sub.3, SrRuO.sub.3, CaRuO.sub.3, NdGaO.sub.3 and NdAlO.sub.3.
By using the gas phase method, the epitaxial buffer layers are
formed with a surface having a pore density of less than about 500
pores per mm.sup.2.
[0010] U.S. Pat. No. 5,741,406, issued on Apr. 21, 1998 to Barnett
et al. discloses solid oxide fuel cells having dense
yttria-stabilized zirconia (YSZ) electrolyte films and a method of
depositing these electrolyte films. The YSZ electrolyte thin films
are deposited on a lanthanum strontium manganite (LSM) substrate
using an ion-assisted deposition technique such as sputtering. By
applying a DC bias voltage to the LSM substrate, ion bombardment of
the YSZ film is provided during deposition. The ion bombardment
leads to removal of material from protrusions, re-deposition into
pores and a more planar film surface.
[0011] None of the above references and patents, taken either
singly or in combination, is seen to provide an epitaxial thin
film, suitable for use as a buffer layer in applications requiring,
inter alai, low-loss dielectric substrates with high
permittivity.
SUMMARY OF THE INVENTION
[0012] The developed CCVD processes described herein have proved
advantageous for forming many types of thin films, thick films and
other coatings. When used to deposit epitaxial films on lattice
matching substrates, the CCVD processes produce very dense, and in
some cases, single crystal coatings. These epitaxial coatings are
not only useful for producing buffer layers in the field of high
temperature superconductors, but can also provide superior coatings
in several other fields such as solid oxide fuel cells (SOFC), gas
separation systems and microelectronics. Several different CCVD
processes have been developed as disclosed in the above-identified
U.S. Pat. Nos. 5,652,021; 5,858,465; 5,863,604, and 5,997,956, the
specifications of which are hereby incorporated by reference in
their entirety. It should be noted that one or more of these CCVD
processes may be used to produce the epitaxial coatings of the
present invention, depending on the requirements of the
application. These requirements include, but are not limited to,
speed of deposition, temperature limitations and oxidation
reduction or enhancement.
[0013] To produce some of the various epitaxial coatings of the
present invention, a rolled, textured nickel substrate is coated
with the desired material using CCVD. Although other materials with
a similar lattice parameter may be used depending on the thin film,
Nickel is a preferred material. Nickel is preferred as it is
relatively inexpensive, has a high melting temperature, is easily
roll textured and can be etched using inexpensive and commercially
available materials. In addition, Nickel's lattice parameter
facilitate alignment with the lattice of many other materials in
the formation of an epitaxial film. Thus Nickel is well suited as a
substrate for many applications. However, it will be understood
that the methods described herein may employ other substrate
materials, depending upon the application, such as where cost is
less of an issue, to develop epitaxial films according to the
invention. It is also to be noted that the substrate used in the
deposition process is not necessarily (and oftentimes is not) a
component of the final product. After depositing the epitaxial
layer(s) on the textured substrate, the substrate is often etched
away, leaving the deposited layer or layers having the preferred
epitaxial orientation. Should additional layers be required, they
may be deposited prior to or after etching away the textured metal
substrate. Of course, for some applications, it may be desirable to
leave the original textured substrate as part of the final product.
The details of the specific construction and coating process of
each epitaxial thin film are further described below, with respect
to their particular application.
[0014] In the field of high-temperature superconductors, second
generation superconducting wire is typically made up of four
components, a flexible metal substrate, a buffer layer, a
superconducting layer such as YBa.sub.2Cu.sub.3O.sub.7-x (YBCO),
and a final layer in the form of an insulating or conducting layer.
Buffer layers are employed to protect the metal substrate from
oxidizing during the superconductor application as well as to
prevent diffusion of the metal substrate into the superconducting
layer. Buffer layers must also impart the desired crystallographic
texture to the superconducting layer. High temperature
superconductors (HTSC) have enormous potential for electric power
applications such as current leads, motors, transmission cables,
generators, transformers and current limiters, however, the cost of
HTSC wire must be reduced to levels comparable to copper to enable
most practical applications. Even the most promising forecasts for
mass production cost of state-of-the-art HTSC powder-in-tube wire
are well in excess of this target; this wire also suffers from
performance limitations. Therefore, processes amenable to scale-up
that will facilitate YBCO and associated buffer layer deposition at
a low cost with good control of stoichiometry are required for high
volume, low cost manufacturing of HTSC wires. The atmospheric
pressure combustion chemical vapor deposition (CCVD) process and
the controlled atmosphere chemical vapor deposition (CACVD)
technique use inexpensive chemical precursors and low cost
equipment, and can be configured for continuous, uninterrupted
processing of wires and tapes. Prior methods and products cannot
compare to the reduced expense and the flexibility of the CCVD
methods and high quality epitaxial buffer layers produced
thereby.
[0015] Since the discovery of high temperature superconductivity by
Bednorz and Muller, significant effort has been focused on the
manufacturing of flexible, long length conductors with high
critical current density for power equipment and other large-scale
electrical applications. The above-described YBCO is one such
liquid-nitrogen-cooled superconductor with good potential for these
applications. However, "weak link" or dissipative behavior at grain
boundaries within the current path for YBCO has been this
material's major limitation. To overcome this limitation and to
obtain high critical current density (J.sub.c) values
(.about.10.sup.5 to 10.sup.6 A/cm.sup.2 at 77 K), it is essential
that the crystallographic orientation of the superconducting wire
or tape possess a high degree of in-plane and out-of-plane
alignment over the entire length of the conductor. Recent
innovations in both ion-beam-assisted deposition (IBAD) and in
rolling-assisted, biaxially-textured-substrate (RABiTS)
technologies have resulted in high J.sub.c values and alleviation
of the problems of brittleness and weak links. As these innovations
show promise to enable fabrication of long length YBCO wires, both
are applicable to the present innovation. Several other methods
such as physical vapor deposition techniques, conventional chemical
vapor techniques including metal-organic chemical vapor deposition
(MOCVD), and the solution techniques, including sol-gel and
metal-organic deposition, are available to deposit the above
multi-layer oxides. However, all of these methods have expense and
scalability limitations. Therefore it is essential to develop
inexpensive, easily scalable process for the production of buffer
layer oxides with epitaxial or preferred orientation and good
stoichiometry control. The previously discussed CCVD processes are
capable of doing this.
[0016] One type of epitaxial coating of the present invention is
the use of selected perovskite oxides, such as SrTiO.sub.3,
LaAlO.sub.3, and SrLaAlO.sub.4, as buffer layers for these high
temperature superconductors. At this time, it is understood that,
selected perovskite oxides such as SrTiO.sub.3, LaAlO.sub.3, and
SrLaAlO.sub.4 have not been deposited epitaxially onto textured
metal substrates with the entire film exhibiting the desired cube
orientation. Deposition conditions and results described herein
include results for the CCVD deposition of SrTiO.sub.3 on Ni.
Conditions for the CCVD deposition of SrTiO.sub.3 on other textured
metal substrates and LaAlO.sub.3 and SrLaAlO.sub.4 on Ni and other
textured metal substrates would be understood to be similar.
[0017] Another type of epitaxial coating described herein involves
electrolytes and electrodes for use in solid oxide fuel cells
(SOFC). Fuel cells are a fundamentally novel way of generating
electrical power from a variety of fuels. It has long been
recognized that the successful development and commercialization of
fuel cells will offer significant environmental advantage and
greatly reduce global pollution. The key advantage of a fuel cell
is the high-energy conversion efficiency. Without the intermediate
thermal energy, the fuel cell directly converts the electrochemical
energy to electrical energy. Other advantages include simpler
construction, high efficiency at part load, potential for
co-generation, and much lower production pollutants. Currently, the
commercial market for fuel cells is limited to spacecraft and other
specialty uses, due to the expense of the required chemical
precursors and deposition equipment. A fabrication process to
deposit low-cost and high quality SOFC thin films without complex
post-deposition treatment/sintering is essential for the widespread
commercialization of fuel cells. Furthermore, for widespread use,
the performance/efficiency of SOFCs must be improved. The present
invention provides epitaxial and in some cases single crystal thin
films, resulting in the microstructures needed in both the
electrolytes and electrodes for improving SOFC performance. In
addition, with its open-atmosphere capabilities, the CCVD process
enables continuous depositions of these layers with at least 50%
capital cost reduction and with 75% in operational costs compared
with the other CVD processes, and hence offers significant
commercial advantages for the SOFC industry.
[0018] Current processes for fabricating oxide electrolytes are
limited by the availability of desired powder stoichiometry and
characteristics, the film thickness (a result of both raw material
availability and process limitation), and the densification for
pore-free and ideal grain boundary/interface microstructure. These
limitations thus hinder the development and possible improvements
of SOFC performance and efficiency. Recently, it has been shown
that by fully densifying and greatly reducing the YSZ electrolyte
thickness to 4-5 .mu.m, the power density of YSZ-based fuel cell
can be increased to 1.6 W/cm.sup.2. This indicates that a technique
to fabricate an epitaxial electrolyte layer results in a very thin
and fully dense electrolyte layer without relying on the
availability of raw materials greatly improves the possibility of
the commercialization of SOFCs.
[0019] The CCVD processes produce dense and epitaxial electrolyte
thin films, porous and adherent electrodes, and may be combined
with other coating techniques to construct a superior, solid oxide
fuel cell with reduced manufacturing time and costs. By operating
in the open atmosphere with inexpensive precursors, CCVD provides
continuous coating of epitaxial electrolyte layers, which will
increase the ionic conductivity at lower temperatures. The
CCVD-based process may also provide for better fuel cell
performance by minimizing grain boundary/interface resistance and
reducing polarizations. In addition, the CCVD system capitalization
requirement is reduced at least ten times compared to a
vacuum-based system, and the throughput is far greater than with
other technologies. The CCVD process generally uses solutions with
all the necessary elemental constituents dissolved in a solvent
that also acts as the combustible fuel. The ease of controlling and
changing dopants and stoichiometries enables the deposition of
multi-layered and multi-compound films in one process, which
further increases throughput and reduces production costs.
Depositions can be performed at atmospheric pressure and
temperature in an exhaust hood, a clean room or outdoors.
[0020] Gas separation membranes in accordance with the present
invention can also be formed. One application of gas separation
membranes is in the production of oxygen. Mixed-conducting oxide
membranes could produce oxygen with lower costs then the present
commercial means of oxygen production, namely cryogenics, pressure
swing adsorption (PSA) and polymeric membranes. Developing these
oxygen semipermeable membranes requires the fabrication of a hybrid
membrane comprising a thin film of mixed-conducting oxides
supported on a porous substrate, preferably of the same material.
CCVD can be used to deposit high-quality, dense, gas-tight, pinhole
free sub-micron scale layers of mixed-conducting oxides onto porous
ceramic substrates. Such hybrid membranes will offer both high
permselectivity and high transport rates for oxygen, thereby
enabling its widespread use as a semipermeable membrane for
commercial oxygen production. By reducing the costs of producing
pure oxygen, the membranes of the present invention can greatly
enhance several industries. Natural gas, comprising mostly methane,
can be converted to clean burning transportation fuels, by using
pure oxygen for conversion of methane to syngas. Commercial
production of such fuels has been hindered by the high cost of
oxygen production, which to date is primarily from expensive and
energy-intensive cryogenic processing. An alternative is the use of
dense ceramic membranes, based on mixed-conducting perovskite
ceramic oxides that exhibit high ionic and electronic conductivity
for oxygen. These types of membranes have become of great interest
as a potentially economical, clean and efficient means of producing
pure oxygen by separation from air or other oxygen-containing gas
mixtures. Other applications of oxygen-separating membranes range
from small-scale oxygen pumps for medical applications to
large-scale usage in combustion processes, e.g. coal gasification.
Another application of mixed-conducting oxide membranes is to be
found in the field of chemical processing, including the partial
oxidation of light hydrocarbons, such as natural gas to value-added
products including ethane-ethene mixtures, syngas production, waste
reduction and recovery.
[0021] The desired perovskite structure (ABO.sub.3) consists of a
cubic array of corner-sharing BO.sub.6 octahedra, where B is a
transition metal cation. The A-site ion, interstitial between the
BO.sub.6 octahedra, may be occupied by either an alkali, an
alkaline earth, or a rare earth ion. In many cases, the BO.sub.6
octahedra are distorted, tilted due to the presence of A ion, which
is generally larger than the B cation. The onset of electronic
conductivity mainly depends on the nature of the B-site cation. The
total electrical conductivity can be either predominantly ionic as
in the acceptor-doped rare earth aluminates or predominantly
electronic, as in the late transition metal containing perovskites.
Some perovskite oxides (ABO.sub.3) containing a transition metal at
B sites are found to be good mixed-conducting materials, exhibiting
both ionic and electronic conductivities. Due to their high
electronic and ionic conductivity, these materials can be used as
oxygen semipermeable membranes without electrodes and external
circuits. Oxygen conductive ceramic materials include
yttria-stabilized zirconia doped with either titania and ceria.
Conducted on acceptor-doped perovskite oxides include those with
the generic formula
La.sub.1-xA.sub.xCo.sub.1-yB.sub.yO.sub.3-.delta., wherein A=Sr, Ba
or Ca and B.dbd.Fe, Cu or Ni).
[0022] Another application of gas separation membranes is in the
production of hydrogen. Generation of pure hydrogen is required for
various large-scale industrial applications such as
hydrodesulfurization and hydrotreating processes in refineries. The
increase of hydrogen to carbon ratios in transportation fuels and
the burgeoning field of hydrogen fuel cells are expected to greatly
increase the demand for hydrogen gas. Hydrogen can be extracted
from raw fuels such as natural gas as well as from process streams
such as the catalytic gasification of coal, non-oxidative methane
conversion and steam reforming. Membrane-based separation processes
are cost-effective and environmentally friendly alternatives for
separating hydrogen when compared with other more energy intensive
processes such as distillation and pressure swing adsorption. To be
useful in industrial processes these separation membranes must be
stable at high temperatures (up to 1000.degree. C.) and pressures
(up to 600 psi). Industrial membranes must also have reasonably
high tolerances to corrosion or poisoning by the effluent streams
commonly encountered in industrial processes.
[0023] Ultrahigh purity hydrogen can be produced from gaseous
mixtures containing hydrogen by the use of three types of membranes
including polymeric membranes, inorganic (non-metal porous or
nonporous) membranes and dense (metal) membranes. Polymeric
membranes suffer from limited selectivity and resistance to high
temperatures and reactive chemicals that may be present in typical
feed streams. Porous inorganic membranes exhibit very high hydrogen
permeability, but suffer from brittleness and very low hydrogen
selectivity. Inorganic membranes derived from proton conducting
solid-oxide ceramic materials exhibit lower permeability, are
brittle, and require an electric current to be applied through
electrodes at each surface of the membrane to induce the proton
conduction. Examples of proton conducting membranes that do not
require the application of electric fields include the perovskites
such as yttria-stabilized strontium zirconate and yttria-stabilized
strontium cerate.
[0024] Palladium and palladium alloy membranes have generated much
interest in their applications to membrane reactors. Membrane
reactors function as both separator and reactor in a single unit.
These membranes are superior to polymeric membranes and to
inorganic (non-metal) membranes in that they exhibit excellent
selectivity for hydrogen and can be operated at high temperatures
(up to 1000.degree. C.). Palladium-based membranes are easily
poisoned by sulfur containing gas contaminants such as hydrogen
sulfide. To overcome the deficiencies associated with
sulfur-deactivation, palladium metal is coated with a thin layer of
yttria-stabilized strontium zirconate, which is not affected by
sulfur containing compounds.
[0025] Another practical application of epitaxial thin films is as
dielectric material in capacitors. Capacitors are used in almost
every electronic product, as they are one of the key passive
components in electronic circuits. They are utilized according to
their capacitance values which are dependent on their physical
structure and dielectric permittivity. The current invention
utilizes the CCVD process to deposit low-loss, epitaxial perovskite
films to produce dielectric layers with extremely high
permittivity. This produces capacitors with a greater capacitance
to size ratio, resulting in a reduction in the required size and
weight of individual capacitors and the overall circuit. This
advantage can be utilized in discrete components as well as
embedded devices.
[0026] Once a capacitor is formed, its thickness and dimension are
fixed and therefore, the only adjustable factor for modifying
capacitance is its permittivity. The epitaxial dielectrics of the
current invention, allow the application of a DC bias to adjust the
capacitance of capacitors made of high-permittivity, low-loss
ferroelectric materials. These electrically tunable capacitors can
be used in a wide variety of applications. For example, a signal
filter circuit, normally composed of a capacitor and a resistor,
will be able to function as a multiple frequency filter by
electrically adjusting the permittivity and hence, the capacitance.
Capacitors embedded in printed circuit boards can also take
advantages of this multiple frequency capability. In wireless
communication, electrical adjustment of permittivity will induce
phase shifts that are highly desired for phase array radar. In
addition, these tunable devices can also be used as filters and
oscillators for telecommunication at variable frequencies. Prior
art capacitors are not able to achieve the desired properties using
a practical material processing approach. Thin disks of dielectric
materials, sliced from bulk materials, require a voltage in the
order of 1000V to achieve practical adjustability. In addition
previously deposited dielectric films have been too lossy to render
practical utilization of this effect.
[0027] Accordingly, it is a first object of the invention to
provide thin film, epitaxial buffer layers for high temperature
superconductors, that provide protection and insulation of the
superconductor.
[0028] It is another object of the invention to provide dense and
pore-free electrolytes for solid oxide fuel cells.
[0029] It is a further object of the invention to provide dense and
pore-free membranes for separating oxygen or hydrogen from mixed
gas streams.
[0030] It is yet another object of the invention to provide
dielectric layers with high permittivity and low loss for use in
capacitors.
[0031] It is still another object of the invention to provide
electrically adjustable capacitors by using dielectric layers with
high permittivity and low loss.
[0032] These and other objects of the present invention will become
readily apparent upon further review of the following specification
and drawings.
BRIEF DESCRIPTION OF THE DRAWINGS
[0033] The foregoing and other objects and advantages of the
invention will be appreciated more fully from the following further
description thereof, with reference to the accompanying drawings
wherein;
[0034] FIG. 1 is a side plane view of an apparatus used to deposit
the epitaxial thin films of the present invention.
[0035] FIG. 2 is a front view of the apparatus of FIG. 1.
[0036] FIG. 3 is a pole figure showing the desired single
orientation of SrTiO3 on textured Ni.
[0037] FIG. 4 is a typical nanostructure of SrTiO3 on textured
Ni.
[0038] FIG. 5 is a plot of the conductivity vs. temperature for two
samples A, B, and YSZ from a reference.
[0039] FIG. 6 depicts pictorially one fuel cell having an epitaxial
layer according to the invention.
[0040] FIG. 7 depicts pictorially one process for forming the fuel
cell of FIG. 6.
[0041] FIG. 8 depicts an SEM micrograph of LSM on sapphire showing
a porous and columnar microstructure.
DETAILED DESCRIPTION OF THE CERTAIN ILLUSTRATED EMBODIMENTS
[0042] The present invention may be understood more readily by
reference to the following detailed description of certain
embodiments of the invention and the Figures. While the epitaxial
thin films of the present invention can be deposited using a number
of suitable techniques, the preferred method of deposition is CCVD
as described in the above-mentioned U.S. patents. Furthermore when
a reducing atmosphere is required to avoid oxidation of the
substrate or for other reasons, it may be desired to use a
controlled atmosphere chemical vapor deposition (CACVD) technique.
Other deposition techniques that provide a reducing atmosphere or a
vacuum environment may also be used, however as is well documented
in the CCVD patents, the numerous advantages of the CCVD and CACVD
processes are understood to make them the preferred methods.
[0043] One deposition method for growing epitaxial thin films on
nickel employs CACVD to avoid, or reduce, oxidation of the nickel
during the deposition process. FIGS. 1 and 2 illustrate a CCVD and
CACVD apparatus 100 that may be used to deposit the epitaxial thin
films of the present invention, and reference to these figures
should be made with respect to the examples described below. The
needle 101 is supplied with the precursor at a supply end 102 and
includes a delivery orifice 103 that can be swaged to form a
restriction, or may be non-swaged. Electrodes 104 and 105 are
attached to the ends of the needle 101 to provide a DC or AC
current for heating the precursor in the needle when required. Tip
oxygen is supplied to supply port 106 and is routed around the
needle 101 through conduits 107 and out of orifices 200. The
hydrogen pilot gas is supplied to supply port 108 and is routed
around the tip oxygen through conduits 109 and out of delivery
ports 201. The delivery orifice 103 and substrate S are located in
a localized reducing atmosphere provided by the pilot gas hydrogen.
To avoid oxidation of some coatings and/or substrates, a shield 110
may be attached to the body 111 of the apparatus, thereby allowing
a controlled atmosphere deposition process. The shield gas is an
inert gas such as argon, and is supplied through the shield 110 and
around the pilot hydrogen. Should further oxidation protection be
required, the entire apparatus 100 and substrate S may be placed in
a chamber and additional argon may be supplied around the
deposition area during deposition and while cooling the substrate
after the deposition. It should be noted that apparatus 100 is only
an example and other types of devices, including devices for other
methods of deposition, may be used to produce the thin films
described herein.
[0044] Methods for employing the apparatus 100 for forming films on
a substrate include those described in the above referenced U.S.
Pat. No. 5,997,956, issued to Hunt et al. As discussed therein
chemical vapor deposition and powder formation may be achieved
using thermal spray with fluid solutions including near
supercritical and supercritical fluid solutions, to produce very
fine atomization, nebulization, vaporization or gasification. The
dissolved chemical precursors need not have high vapor pressure,
but high vapor pressure precursors can work well or better than
lower vapor pressure precursors. By heating the solution fluid just
prior to or at the end of the nozzle or restriction tube, the
available time for precursor chemical reaction or dissolution prior
to atomization is understood to be minimized. This method can be
used to deposit coatings from various metalorganics and inorganic
precursors.
[0045] The above described type of device was employed to form
epitaxial thin films suitable for use as buffer layers in
applications including high temperature superconductors,
electrolytes in solid oxide fuel cells (SOFC), gas separation
membranes and dielectric material in electronic devices. By using
CCVD, CACVD or any other suitable deposition process, epitaxial
films having pore-free, or substantially pore-free, grain
boundaries, and dense structure can be formed. Several different
types of materials are disclosed for use as buffer layers in high
temperature superconductors. For purposes of describing the
epitaxial thin films of the invention, certain examples are
provided below, however, it will be understood that the examples
below are merely representative of the films of the invention, and
are not to be deemed limiting, or an exhaustive list of such
films.
EXAMPLE 1
[0046] In this example, SrTiO.sub.3 (STO) was deposited on roll
textured Ni. The precursor solution included 1.26 g of
Sr-2-ethylhexanoate (2eh) (diluted with toluene to 1.5 wt % Sr),
1.11 g of Ti-di-I-propoxide bis acetylacetonate (diluted with
isopropanol to 0.94 wt % Ti), 51 ml denatured ethanol and 300 g of
propane. This solution was fed to the needle at a rate of 3
ml/min., while supplying 1.75 amps of heating current to the
needle. Tip oxygen at 80 psi was supplied at a rate of 3 lpm, pilot
hydrogen at 15 psi was supplied at a rate of 18 lpm and argon at 50
psi was used as the shield gas at a rate of 32 lpm. The deposition
was conducted for 10 minutes with a substrate temperature of
950.degree. C.
[0047] The deposited buffer layer was highly epitaxial and
exhibited a single cube in-plane orientation as shown in FIG. 3.
FIG. 3 is a pole figure of a YBa2Cu3Ox (YBCO) superconductor
deposited on top of the CCVD deposited SrTiO3 buffer layer on Ni.
The pole figure of the YBCO layer is exhibiting the same single
in-plane orientation of the buffer layer which is necessary for the
superconductor to exhibit high critical current densities. Typical
in-plane measurements of the STO were determined to be 8.89.degree.
full-width-at-half-maximum (FWHM) for the (111) plane. Typical
out-of-plane measurements were 7.53.degree. FWHM for the (002)
plane. FIG. 4 is a typical microstructure of SrTiO.sub.3 on Ni. The
film is dense and continuous which allows the film to act as a
template for a superconductor that exhibits a high critical current
density. For use in superconductor applications, the thickness of
the perovskite buffer layer should be between 50-1000 nm. Initial
Auger experiments show that these thicknesses prevent significant
diffusion of the metal substrate and any oxide that may form. A
YBCO film was successfully deposited onto a CCVD deposited
SrTiO.sub.3 film on Ni. While the length of the coated specimen is
approximately 2 cm, this length can be increased to useful
parameters using a reel-to-reel system.
[0048] In the formation of fuel cells, such as the Fuel Cell 600
depicted in FIG. 6, single crystal or epitaxial YSZ is deposited
using CCVD or CACVD on a roll textured single crystal Ni substrate
to form a YSZ electrolyte. On top of the electrolyte layer, a
cathode such as LaSrMnO (LSM) is deposited. The cathode can be
deposited completely by CCVD or CACVD, or an interface layer from
50-200 nm can be deposited using the CCVD or CACVD process and
other deposition processes such as sol-gel can be used to deposit
the bulk of the cathode. After deposition of the cathode, the Ni
can be etched off of the electrolyte, as the cathode will provide
the necessary support layer. The anode is then deposited on the
electrolyte to complete the fuel cell. FIG. 7 depicts one process
for forming such a fuel cell.
[0049] It is important to note that several different variations of
the above method can be used to form the fuel cell. Additionally,
other electrolytes may be used such as BaCeO.sub.3, and any single
crystal substrate can be used. Any suitable electrode materials may
be used as well. The epitaxial and near single crystal electrolyte
provides increased performance over polycrystalline electrolytes by
minimizing grain boundary effects. The etching step can be avoided
by directly depositing the electrolyte to an electrode. For
example, NiO and YSZ powders can be pressed into pellets and
sintered to yield dense discs for the anode. The electrolyte is
then directly deposited onto these dense discs using CCVD or CACVD.
Heat treatment of the coated discs in a reducing atmosphere reduces
the NiO to Ni and creates porosity in the anode. Cathode (e.g. Ag)
paste is then applied to the electrolyte by screen printing or
brushing and heat treatment is used to remove the organic portion
of the paste leaving a porous metal layer for the cathode. The
anode discs can be dip coated with additional anode material prior
to CCVD coating of the electrolyte.
[0050] Fuel cells will be constructed with electrolyte thin film
and porous electrodes on each side of the electrolyte layer. The
process may involve not only the CCVD technique but also other
coating/forming methods. In general, the electrolyte material, for
example YSZ, will be deposited onto a smooth lattice-compatible,
large-grained (>1 cm) substrate. A dense, pore/grain-boundary
free, epitaxial YSZ film of one-five micron neighborhood is then
deposited. Consequently, the cathode, for example LSM, will be
applied onto the YSZ layer via CCVD or by screen printing etc. The
substrate will then be removed by etching or simply melting away
depending on the property of the substrate. Finally, the anode,
perhaps Ni-YSZ, is formed on the exposed YSZ surface by the CCVD
process or by depositing porous YSZ via the CCVD technique and
filtrating with Ni (or NiO) slurry. Steps in this process
development may also involve the use of bi-layer electrolyte
(ceria/YSZ), or creating a rougher microstructure of YSZ on top of
the dense YSZ layer. Porous LSM layer can be deposited first by
growing a thin LSM layer (in nanometer range) on YSZ via CCVD and
then build up the thickness by other coating method, in order to
further reduce interface resistance. A strong LSM layer is
typically employed because after the removal of the substrate it
acts as a supporting layer during the processing. After the removal
of the substrate, porous Ni-YSZ layer of 10-30 .mu.m thickness will
be deposited onto the exposed surface. This anode layer will be
thin to maximize efficiency and minimize the polarization.
[0051] It is generally recognized that increasing the TPB
(three-phase-boundary between the gas, electrode and electrolyte)
line length should increase the reaction rate in fuel cells. One
can increase the TPB line length by using a porous composite
electrode (cermet e.g. Ni-YSZ, Ru-YSZ). The electrode is required
to be porous and electronically conductive in order to facilitate
the transport of gaseous species or ions to the electrolyte while
allowing for the collection of electrons from the associated
electrochemical reactions at the interface. It is also preferred
because the contiguous electrode layer has fine pore sizes.
[0052] The use of CCVD to increase conductivity by reducing film
thickness and using highly epitaxial and single crystalline thin
films as the electrolyte in SOFCs has been accomplished. To test
the feasibility of producing these single crystal electrolytes, YSZ
films of 480 and 410 nm thickness were deposited onto sapphire
substrates via CCVD at .about.1050.degree. C. The YSZ films were
deposited onto sapphire substrates at a deposition rate as high as
10.8 .mu.m/hr at a 1400.degree. C. flame temperature and at 2.5
.mu.m/hour at a 1150.degree. C. deposition temperature. At these
flame temperatures, the substrate temperature is about
900-1100.degree. C. and below 800.degree. C., respectively. The
samples were tested for impedance spectroscopy. Fully stabilized
zirconia with 8 mole percent (m/o) yttria (8YSZ) may be used as the
main electrolyte material for deposition studies and process
development. It is the most common electrolyte in SOFCs for its
adequate level of oxygen-ion conductivity and its stability in both
oxidizing and reducing environments. The use of fully stabilized
phase is preferred to yield maximum conductivity and avoid the
problems of phase transformation associated with partially
stabilized zirconia.
[0053] After the electrodes consisting of Heraeus C-1000 silver
paste and silver lead wires were fired onto the samples at
800.degree. C. for 10 minutes, these two samples were placed in a
furnace with lead wires coming outside for applying a test signal.
The frequency was swept from 2.times.10.sup.7 Hz to 0.1 Hz while
acquiring the impedance spectra at 600, 675 and 730.degree. C. The
resistance associated with the YSZ films was then converted to
conductivity, and normalized for a standard geometry. The
calculated conductivity values are illustrated in FIG. 5 along with
the data from Reference 15. The figure is a Plot of the
Conductivity (in .OMEGA..sup.-1 cm.sup.-1) vs. Temperature (1000/T,
K.sup.-1) for Samples A, B, and YSZ from Reference 15. The
resulting high conductivity for CCVD deposited YSZ films can be
explained by the high degree of epitaxy and the absence of grain
boundary in the film. A high degree of epitaxy and the absence of
grain boundary greatly reduce the interface and boundary
resistance, and, hence, increase the conductivity. Sources of
deviation, which are minor, are the conduction across the surface
of the YSZ film instead of through the film, which should be minor
since sapphire is not conductive, and the inaccurate measurement of
the sample geometry. One should note that the configuration used
here for testing can yield data on the YSZ film but the
conductivity data is not directly applicable to fuel cell
application due to the substrate. After examination by SEM, the
films appeared to be dense and uniform with no observable grain
boundary or pores. The XRD pattern of the YSZ films on sapphire
showed a preferred orientation of (111). An XRD pole figure pattern
of the (111) peak was acquired for a YSZ film deposited onto a-axis
sapphire via CCVD. The intensities are less than one, which is less
than 0.5% of the maximum, except at the four 45 degree .phi.
locations (90.degree. to each other), and a very minor peak at the
origin of the pole figure. This pole figure indicates the high
degree of epitaxy in the YSZ film.
[0054] Oxide electrolyte materials including yttria-stabilized
zirconia (8 m/o yttria, 8YSZ), ceria (CeO.sub.2), yttria-doped
ceria (YDC), yttria-stabilized bismuth oxide (YSB) and
samaria-doped ceria (SDC), have been deposited on substrates using
CCVD processing. Strontium doped lanthanum manganite (LSM), a
commonly used cathode, has also been deposited by the CCVD
technique. Deposition parameters were adjusted to achieve porous,
columnar structure for LSM films. Yttria-stabilized zirconia-based
solid oxide fuel cells were constructed using Ni-YSZ cermet as the
anode, YSZ as the electrolyte and silver as the cathode. Ceria
films were deposited on both fused silica and sapphire substrates.
Highly crystalline films of cerianite phase were produced at as low
as 700.degree. C. flame temperature. The XRD patterns indicated a
(200) preferred orientation and the degree of epitaxy increased as
the deposition temperature increased. YDC, YSB and SDC thin films
were also deposited onto sapphire substrates to exploit the
feasibility of the CCVD process in producing ceria- and
bismuth-based electrolytes for SOFCs. Highly crystalline and dense
films were produced using CCVD. By adjusting the precursor solution
concentration, deposition temperature, and atomization settings,
adherent and columnar LSM cathode layers were deposited on sapphire
substrates. The film thickness of the deposited layers included
layers of approximately 420 nm. SEM micrographs of YSZ thin films
deposited by the CCVD processing at 1350.degree. C. showed dense
films with no grain boundary, however white spheres indicative of
foreign particles provided for contrast were identified. The films
had an undulating structure achieved by changing degree of
atomization, and a columnar structure was also achieved.
Additionally, YSZ (111) XRD pole figures indicated strong epitaxy
on a-plane sapphire; and CeO.sub.2 (111) XRD pole figures indicated
strong epitaxy on lanthanum aluminate (100).
[0055] The main candidate electrode materials will be Ni-YSZ and La
doped strontium manganate (LSM). The materials will be either
deposited onto electrolyte layer via CCVD or in combination with
other methods. An example of porous LSM is shown in FIG. 8. Another
example for combining coating techniques could involve an initial
deposition of a porous layer of electrolyte material over the dense
electrolyte using the CCVD process. After depositing the porous
layer, the next step is to infiltrate the electrode material into
the pores to form a contiguous porous electrode while maintaining a
long TPB line length.
EXAMPLE 2
[0056] In this example, LSM was deposited on a-plane sapphire using
CCVD. The precursor solution comprised 0.21 g Mn-2eh (diluted with
mineral spirits to 6 wt % Mn), 1.96 g La-2eh (diluted with mineral
spirits to 2 wt % La), 0.97 g Sr-2eh (10 wt % Sr in 2-ethylhexanoic
acid and further diluted with toluene to 1.25 wt % Sr). This
solution was added to toluene for a total volume of 10 ml, and then
added to 60 g propane. This solution was fed at a rate of 3 ml/min.
for a total deposition time of 30 min. 2.42 amps of current were
supplied to the needle with 3500 ml/min. of tip oxygen. Tip oxygen
was 60 psi (with no hydrogen or argon). The flame temperature was
maintained at 1200-1400 degrees C. In FIG. 8, the SEM micrograph of
LSM on sapphire shows a porous and columnar microstructure. The
porosity of the electrode layer must be sufficient for the
transport of gaseous species or ions to the electrolyte while
allowing for the collection of electrons from the associated
electrochemical reactions at the interface.
EXAMPLE 3
[0057] In this example, YSB was deposited on a-plane sapphire using
CCVD. The precursor solution comprised 2.88 g Ba-2eh (8.5 wt % Ba
in xylene and further diluted with toluene to 2 wt % Ba), 0.08 g
Y-2eh (diluted with toluene to 0.69 wt % Y). This solution was
added to toluene for a total volume of 10 ml, and then added to 60
g propane. This solution was fed at a rate of 3 ml/min. for a total
deposition time of 29 min. 2.50 amps of current were supplied to
the needle with 3300 ml/min. of tip oxygen. The flame temperature
was maintained at 1200 degrees C. Tip oxygen was 60 psi (with no
hydrogen or argon).
EXAMPLE 4
[0058] In this example, YDC was deposited on a-plane sapphire using
CCVD. The precursor solution comprised 1.17 g Ce-2eh (12 wt % Ce in
2-ethylhexanoic acid and further diluted with toluene to 1.8 wt %
Ce), 0.22 g Y-2eh (diluted with toluene to 0.69 wt % Y). This
solution was added to toluene for a total volume of 14 ml, and then
added to 51 g propane. This solution was fed at a rate of 3 ml/min.
for a total deposition time of 21 min. 2.76 amps of current were
supplied to the needle with 3500 ml/min. of tip oxygen. The flame
temperature was maintained at 1350 degrees C. Tip oxygen was 60 psi
(with no hydrogen or argon).
[0059] In the field of gas separation membranes, specifically for
hydrogen selective membranes, hydrogen conducting pervoskite
ceramic oxide coatings such as SrZrO.sub.3 and SrCeO.sub.3 are
deposited onto palladium. These films are dense, homogeneous,
pinhole free and sub-micron thick. Hydrogen transport rates through
these composite membranes at 300.degree. C. are approximately 70
GPU's.
EXAMPLE 5
[0060] In this example, SrZrO3 was deposited on Pd using CCVD. The
precursor solution comprised 2.19 g Sr-2eh (10 wt % Sr in
2-ethylhexanoic acid and further diluted with toluene to 1.5 wt %
Sr), 0.912 g Zr-2eh (diluted with mineral spirits to 6 wt % Zr),
0.24 g Y-2eh (diluted with toluene to 0.7 wt % Y). This solution
was added to 160 ml ISP, and then added to 75 g propane. This
solution was fed at a rate of 3.13 ml/min. for a total deposition
time of 38 min. 3.0 amps of current were supplied to the needle
with 5930 ml/min. of tip oxygen (80 psi) and 1200 ml/min. of pilot
hydrogen. The flame temperature was maintained at 1150 degrees
C.
[0061] Epitaxial dielectrics for capacitors can be formed from a
wide range of dielectric materials. Using the CCVD process, single
phase, epitaxial (determined from XRD) SrTiO.sub.3,
Ba.sub.0.5Sr.sub.0.5TiO.sub.3, and Ba.sub.0.6Sr.sub.0.4TiO.sub.3
films were successfully coated on (100) MgO single crystal
substrates. Examples are described below.
EXAMPLE 6
[0062] In this example, SrTiO.sub.3 coatings were deposited onto
MgO using the CCVD process. The solution of the SrTiO.sub.3
precursor contained 0.0452 wt % of Sr in the form of strontium
2-ethylhexanoate, 0.0449 wt % Ti (di-1-propoxide) bis
(acetylacetonate), 13.3329 wt % toluene, 0.5828 wt % isoproponal,
and 85.9919 wt % propane. The constant flow rate for the solution
was at 2.0 ml/min and for the tip oxygen 4000 ml/min at 80 psi. The
deposition temperature as measured at the substrate front surface
varied from 900 to 1100.degree. C.
EXAMPLE 7
[0063] In this example, Ba.sub.0.5Sr.sub.0.5TiO.sub.3 coatings were
deposited onto MgO using the CCVD process. The solution of the
Ba.sub.0.5Sr.sub.0.5TiO.sub.3 precursor contained 0.0146 wt % of Sr
in the form of strontium 2-ethylhexanoate, 0.0420 wt % of Ba in the
form of barium 2-ethylhexanoate, 0.0311 wt % Ti (di-1-propoxide)
bis (acetylacetonate), 13.3774 wt % toluene, 0.0104 wt %
isoproponal, 0.5023 wt % 1-butanol, and 86.0404 wt % propane. The
constant flow rate for the solution was at 2.0 ml/min and for the
tip oxygen 4000 ml/min at 80 psi. The deposition temperature as
measured at the substrate front surface varied from 900 to
1100.degree. C.
EXAMPLE 8
[0064] In this example, Ba.sub.0.6Sr.sub.0.4TiO.sub.3 coatings were
deposited onto MgO using the CCVD process. The solution of the
Ba.sub.0.6Sr.sub.0.4TiO.sub.3 precursor contained 0.0143 wt % of Sr
in the form of strontium 2-ethylhexanoate, 0.0615 wt % of Ba in the
form of barium 2-ethylhexanoate, 0.0355 wt % Ti (di-1-propoxide)
bis (acetylacetonate), 12.6049 wt % toluene, 0.0118 wt %
isoproponal, 1.5333 wt % 1-butanol, and 85.7412 wt % propane. The
constant flow rate for the solution was at 2.0 ml/min and for the
tip oxygen 4000 ml/min at 80 psi. The temperature as measured at
the substrate front surface varied from 900 to 1100.degree. C.
[0065] It is to be understood that the terminology used herein is
for the purpose of describing particular embodiments only and is
not intended to be limiting. It must be noted that, as used in the
specification and the appended claims, the singular forms "a," "an"
and "the" include plural referents unless the context clearly
dictates otherwise.
[0066] Throughout this application, where publications are
referenced, the disclosures of these publications in their
entireties are hereby incorporated by reference into this
application in order to more fully describe the state of the art to
which this invention pertains.
[0067] It should be apparent to those skilled in the art that
various modifications or variations could be made to the present
invention without departing from the scope of the invention. Other
embodiments of the invention would be apparent to those skilled in
the art from review of the specification disclosed herein. It is
intended that the specification be considered as exemplary only,
with the true scope of the invention being indicated by the
following claims.
* * * * *