special ceremic materials
TRANSCRIPT
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SPECIAL CERAMIC MATERIALS FOR SOFC-IT TYPE FUEL CELLS
Mircea GHITULESCU, Georgeta VELCIU, Lelian CIOROIANU,
Gabriela CIOROIANU, Gela PROROCU
ENERGETIC RESEARCH AND MODERNIZING INSTITUTE ICEMENERG S.A.
Energeticienilor Bvd., no. 8, district 3, Bucharest, phone: +4021 3462772, fax 4021 3465310
e-mail: [email protected]
AbstractFuel cells are, in the time being, the cleanest electrical energy production technology. Solid electrolyte
fuel cells suffered, lately, an intensive development. The actual tendency is to produce solid electrolyte fuel cells,
which function at intermediate temperatures (650-8500C) SOFC-IT.
The present paper shows the stage and functionality of a SOFC-IT type fuel cell. Types of ceramic
materials and the best compositions used in construction of fuel cell elements are also shown, as well as the
corresponding obtaining technologies.
1. INTRODUCTION
The European Union policy and the Kyoto Protocol impose important demands to the
energetic systems: reduction of the pollutant emissions and the rational use of energetic
resources.
Reduction of pollutant emissions is an essential condition, in regards to the fact that
over half of the noxes emitted in the environment are the result on electrical and thermal
energy production processes in classical thermal plants (SO2, NO2, CO2, slag, ash and thermal
pollution). [1]
The energetic resources are very important, being influenced by the uncertainties
accounted in insuring the supply, by the exploitation and conservation of superior fuels
resources for their use as raw materials or fuels for transport.
In present, there are researched alternative routes for electrical energy production
through using some maximum yield technologies, increased reliability, and minimum
pollution. From this point of view, the fuel cells are considered the most clean technologies
for obtaining of electrical energy.
For the period 2000-2030, studies done in the European Union show an increase of the
global energy needs with 33% and a double of the CO2 emissions 9from 6.3 to 13 mil. tones).
[1] There are known numerous possibilities of saving fuels and energy, as well as of using
some clean energy sources, which allow the accomplishment of the Kyoto objectives in
regards to reducing the gas emissions.
In the collaboration in the European Research Area frame, the efficient coordination
and support of European Union organizations are the key factors for accelerating the activities
in the fuel cells field until the commercial stage.
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2. ACTUAL STAGE OF DEVELOPMENT
IN THE SOFC-IT TYPE FUEL CELLS FIELD
Solid electrolyte fuel cells (SOFC) represent a potential alternative to energy
producing conventional technologies, offering the possibility of combined production of
electrical energy and heat with very high efficiency.
SOFC are energetic installations which produce energy through the direct conversion
of gas fuels, natural gas, coal gas, ethanol, methanol etc.), reducing the pollutant emissions of
NOx, SOx and gases with green house effect, CO2.
In the last period, the SOFC technology has encountered major progresses in regards
to the power density, as well as the life time.
Solving some technical, economical and ecological problems, allowed the fast
development of solid electrolyte fuel cells.
Fuel cells can be used in stationary decentralized power plants as energetic generators
having the possibility of cogeneration, capitalizing the heat from exhaust worm gases.
In compared to other types of fuel cells (MAFC, PAFC), the solid electrolyte fuel cells
(SOFC) have the following advantages:
clean conversion technology (the level of pollutant emissions NOx, SOx, CO2, under 10mg/m
3consumed gas)
net electrical yield of 55-60% low phonic pollution level (without noise, vibrations) different areas of applications (industry, domestic)
In present, there are in development three principal configurations (monolithic, tubular,
and planar). There are differences in opinions on the configuration to be adopted in order to
obtain the most advantageous solutions.
The planar type SOFC is still in the laboratory stage, while the tubular construction is
produced and tested.
Companies like Westinghouse E.C. Arfgone National Laboratories-USA, Dornier
GmbH-Germany have studied and developed the SOFC tubular configuration.
Westinghouse Electric Corp, Pittsburgh PA (USA) designed some pilot stations with
an over 40,000 hours functioning. The company has distributed two demonstrative units of 25
kW for two Japanese public services units and a Californian public service similar one.
The RISO research center, in Denmark, has the most recent results in the planar SOFC
field, succeeding in constructing and testing a 70 cells module, each with a 50 cm2
surface.
The maximum obtained power was 507 W for a functioning temperature of 10000C.
Promoting SOFC with intermediate temperature functioning (IT-SOFC)
The new generations of fuel cells have solid electrolyte and function at intermediate
temperatures, below 8000C (SOFC-IT).
The investment and exploitation costs for solid electrolyte fuel cells remain increased
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because of the high temperature of the functioning (about 10000C). There are researched
superalloys and ceramic materials with electroconductive properties for these properties.
Also, the high functioning temperature leads to gas leaking, cracks and other functioning and
maintenance problems for the SOFC assembly. This is the reason why the elimination of
these setbacks is pursued through the reduction of the functioning temperature.
The optimum functioning temperature is between 6500C and 800
0C, a sufficient
temperature for fuel internal reforming, reducing the investment, functioning and maintenance
costs.
At the temperature 8000C or lower, there can be used classical stainless steel instead of
special materials used at high temperature and also, the lower temperature allows the increase
of the life time of the fuel cells.
The quantity of electricity produced and the temperature for which the efficiency is
maximum highly depend on the electrolyte potential to allow conduction through oxygen
ions.
In conventional SOFCs, the inherent problem is the functioning of yttrium stabilized
zirconia (YSZ) at the temperature of 10000C. At lower temperatures, the electrical resistance
of YSZ increases, lowering the performances at an economical level. To overcome these
difficulties, a new alternative of electrode or a new fuel cell model is necessary.
Different institutions and companies (Royal Institute of Technology, EPRI, Sulzer
HEXIS Ltd. etc.) directed the research to lower the functioning temperature of SOFC. An
approach of the study of some very thin electrolytes or the use of some alternative electrolytematerials.
The decrease of the electrolyte thickness is the most direct approach of to maintain the
SOFC performances at lower temperature. In this case, the oxygen ions have traveled a
smaller distance through the electrolyte, the total resistance of the cell being able to be
decreased, even if the resistance per electrolyte unit increases due to the decreasing of the
temperature. This approach allows the use of YSZ as electrolyte.
To maintain the performances, the thickness of the electrolyte must be smaller than 10
m. the obtianing of this thickness is difficult to accomplish because of the cracks that can
appear, not wanted in the electrolyte structure. To obtain thin layers of YSZ, chemical
methods were applied, as the layers in colloidal suspension technique, obtaining layers of 4-
10 m thickness.
In laboratory tests of a solid electrolyte fuel cell, in which the electrolyte is a thin
layer, with functioning at 700-8000C, there were obtained very good results.
The development of some ceramic oxides composite materials will allow the
intermediate temperature (
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The increased performances of IT-SOFCs and the extremely high conductivity of
ceramic composite electrolytes imposes the development of the fuel cells field.
Through lowering the functioning temperature of the SOFC system, the fabrication
costs of components is expected to be reduced with 30-40%.
General functioning concept for solid electrolyte fuel cells SOFC-IT
A fuel cell is based on an electrochemical energy conversion process. The energy
conversion inside the fuel cell is clean and silent.
The solid electrolyte fuel cell, SOFC-IT, is comprised of two different compartments
for the fuel and oxidant continuous access. The compartments are separated by a component
of ceramic conductive material through oxygen ions that functions as electrolyte, which is
applied on each of the two component surfaces with electrode function: anode or fuel
electrode and cathode or oxygen electrode (fig. 1).
Figure 1. Ceramic solid electrolyte fuel cell structure
At the fuel cell function base is the possibility of production of some electrochemical
reactions at high temperatures. The process starts from the cathode electrode where a
reduction reaction of the oxygen form air takes place with the formation of oxygen ions,
followed by their diffusion through the electrolyte structure towards the anode and the fuel
oxidation reaction (H2 and/or CO). As a result, the cathode is positively charged and the
anode negatively, between the two electrodes setting an electrical tension, E1 (fig. 2). [2, 3, 4]
Current
direction
Interconnect
Anode
Electrolyte
Cathode
Air
Interconnect
Fuel
Repeating
cell unit
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Figure 2. Solid electrolyte fuel cell functioning principle
3. COMPOSITE MATERIALS AND TECHNOLOGIES
USED IN THE SOFC-IT OBTAINING
Fuel cell components
A fuel cell has three component parts: solid electrolyte, electrodes (cathode and
anode), and interconnect.
From the electrolyte configuration point of view, the solid electrolyte fuel cells are:
tubular (fig.3) and planar (fig.4).
Figure 3. Tubular SOFC fuel cell
Ni-ZrO2 - Anode
YSZ - electrolyte
LaMnO3 - Cathode
Fuel: CO, H2Combustion
Products: CO2, H2O
Usablepower
Anode
Interconnector
Electrolyte
Cathode
Air
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Figure 4. Planar SOFC fuel cell
Materials and compositions used for their obtianing
In the low temperature solid electrolyte fuel cells domain, the materials used for
obtaining the cell components play an important role.
Electrolyte
The solid electrolyte must posses a very good ionic conductivity and, as much as
possible, the electronic conductivity to be missing.
The temperature dependence of the electric conductivity of a ceramic material
constitutes the criteria on which their use as electrolytes is based upon.
In a ceramic oxidic compound, MO, comprising cations M2+
and anions O2-
, the
electrical charge carriers are represented by the ionic and electronic crystalline lattice defects
formed at structural level. The defects quantity at the crystalline lattice level is created by
substitution processes of the cation M2+
with another cation having a close atomic radius and
a different valance, in general, smaller than of the replaced cation. Under the influence of
temperature, the possibility of migration of defects in the material structure determines the
electrical conductivity of the electrolyte material.
The obtaining of a ceramic material requires a certain technology to obtain the
structure necessary for the electrolyte function. Therefore, because must be defined
temperature and oxygen partial pressure intervals specific for the working media in which the
electrolyte can function.
For the high temperature cell electrolyte, the use of stabilized zirconia ceramic
materials (electric conductivity in the order 2.5 10-2
S/cm at 10000C) is recommended and
for low temperature cell electrolyte, 700-8000C, there are recommended materials included in
a greater number of ceramic oxides groups as:
cerium based materials in binary systems with alkaline metals (CaO, MgO, BaO) or rareearth oxides (La2O3, Y2O3, Gd2O3, Sm2O3, Nd2O3)
Cathode
Electrolyte
Anode
Fuel
Interconnector
Air
Interconnector
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perovskite-type materials (lanthanum oxide based materials in bianry systems with CaO,BaO, SrO oxides, strontium or barium cerates or with rare earth doping etc.)
composite type materials (bismuth oxide based materials with different rare earth dopants:Y, Er, Nd)
Cerium oxide based oxidic compounds group represented an interest as electrolytesbecause of the fluorite type structure resembling stabilized zirconia, having oxygen ions with
a high degree of mobility in network and with the possibility to increase the structural defects
through doping processes.
The ceria oxide is instable in the higher temperature area of 10000C due to the cerium
ion valance state change from Ce4+
to Ce3+
, process that leads to the increase of stability,
especially in the presence of reducing atmosphere.
The CeO2 forming process in solid solution systems through rare earth oxides doping
(La2O3, Y2O3, Gd2O3) shown the possibility to increase the structural stability and obtaining
of some good quality electrolytes.
The conductivity studies on cerium oxide binary systems materials with 15 mol %
La2O3 have shown a behaviour of electric conductors comparable with the one exhibited by
the zirconia stabilized with CaO and values even greater in the lower temperature domain
(under 8000C).
A special electrolyte behaviour was still observed at cerium oxide compositions doped
with gadolinium oxide (4 and 8 mol %). Conductivity studies done through impedance
spectroscopy have shown conductivity values of the order 10
-2
10
-1
S/cm at 800
0
C, samevalues being presented for stabilized zirconia at 1000
0C. It was observed, also, an important
influence of the working atmosphere for the composition with 8 mol %, the ionic conduction
domain being dependent on the decrease of oxygen partial pressure and increase of
temperature, an electronic contribution on the conduction process in the air atmosphere being
expected only above 10000C, exemplified in figure 5. [5]
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Figure 5. Binary system CeO-Gd (8 mol % Gd2O3) electric conductivity
Neodymium oxide doping (8 and 16 mol %) at 7000C also showed a predominant
ionic conduction in the air atmosphere (figure 6).
Figure 6. Binary system CeO-NdO electric conductivity
The obtaining of some materials with cerium oxide in binary and ternary systems with
ZrO2 and Y2O3 was experimented and observed the fact that only compositions with
tetragonal monophase compositions have stable electrolyte properties under 10000
C for amaximum content of 12 mol % CeO2. In compositions with a high content of CeO2 more than
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25 mol %, the electronic conductivity becomes predominant due to the chemical instability of
the cerium ion through valance change from 4+ to 3+, with the release of electrons.
Another conductor material group with electrolyte characteristics is comprised by thematerial group based on lanthanum oxide in binary systems with CaO, SrO and MgO type
oxides. The process of forming as solid solutions resembles the stabilized zirconia systems,
the La3+
ions being substituted by Ca2+
ions with the formation of anionic vacancies or
interstitial cations.
Some older experiments indicated an ionic conductivity for a doping with 15 mol %
CaO between 400-11000C and a conductivity of the order 10
-2S/cm at 900
0C and low oxygen
partial pressures. The importance of the ion radius that substitutes the lanthanum ion
determined the best qualities as ionic conductors in these binary systems. Therefore, for
temperatures between 500-8000C, doping with 1 mol % SrO or BaO, has lead to increased
conductivities of the order 10-2 10-3 S/cm at 8000C and, also, a majoritary ionic type
conductivity with similar values and low oxygen partial pressures, below 10-7
atm, only a
maximum 15 mol % content was obtained.
Another class of used materials to function as electrolyte are ceramic composite materialsbased on bismuth oxide.
This type of ceramic electrolyte is a composite having an exterior layer rich in zirconia
and yttrium with a minor quantity of bismuth oxideand another layer rich in bismuth oxide
and poorer in zirconia and yittria, presenting high electric conductivities at the operating
temperatures of 700-800
0
C.These can be used to function as eelctrolyte and the materials from the system Bi2O3-
Re (where Re is the rare earth oxide). Bi2O3 doped with Al2O3 (Bi2Al4O9) at 8000C has a
conductivity of the order 7 9 10-2
S/cm.
Materials with perovskite-type structure (AxByO3-) presents a mixed conductivity (ionicas well as protonic) where A ca be one of the elements Al, Zr, Nb, Bi and B can be Y, La, Nd,
Sm, Gd, and Yb. The perovskite-type structure of these materials determines their electrolyte
quality through the possibility of maintaining, in the crystalline lattice, a considerable quantity
of ions which can contribute to the formation of structural defects as charge carriers of anionic
nature (O2-
) as well as protonic (H+) or electronic (electron holes) nature. [6, 7]
Electrodes (cathodes, anodes)
Besides the electrolyte, SOFC cell performances are also influenced by the electrodes.
The electrodes actually represent the support and activators for the electrochemical reactions.
They insure also the charge carriers transport, totally for electrons and partially for ions.
Electrodes form, together with the electrolyte, a triple phase gas electronic solid
ionic solid boundary, at which level, the conduction mechanism is suddenly changed from
ionic to electronic (figure 7).
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TPB
4e-O2
2O2-
YSZ
4e-
O2
2O2-
YSZ
O2
4e-
2O2-
Figure 7. Triple phase boundary formed at the solid electrolyte electrode interphase
The use of ceramic materials as SOFC-IT cell electrodes represented the most
advantageous solution currently accepted by these energetic systems constructors. These
oxidic compounds meant a material which, at the temperature of functioning of the cell (800-
10000C) have electrical conduction properties of the electronic preponderant type. As in the
case of electrolytic materials, the electric conductivity characteristic is generated at the
network structure of defects called electron holes.
The cathode materials are, generally, MO or MO2 oxides and ABO3 oxidic compounds
having a perovskite-type phase structure. The formation of defects takes place through a
doping process with cations having different valance, resulting a valance state transition for
the cation being replaced through doping. [8] For instance, in the NiO compounds case,
through Li doping, it takes place the valence transition from Ni2+ to Ni3+ with the liberation of
one electron. By increasing the temperature, these electrons receive a sufficient energy to pass
from the valance band in the conduction band. The electric conductivity characteristic of the
material in function of the corresponding temperature for a conduction mechanism through
electron holes is expressed by the following relation:
)/(exp kTEg
T
A =
where: A constant dependent on material structure and charge carrier concentrationEg activation energy
Pursuing researches for new types of electronic conductor oxidic compounds at high
temperatures has lead to the obtaining of perovskite material groups based on Ca, Sr, Zn
doped lanthanum chromites and manganites. For these compounds, the partial substitution
process of La with Ca or Sr leads to the increase of the electronic defects quantity and, in the
same time, also has as result an increase of the chemical stability of the material.
The most known obtained composition are of the La1-xSrxMnO3, La1-xSrxCrO3, La1-
xSrxCoO3, La1-xCaCrO3 type.
With the same electronic predominant conductor quantity, there were obtained
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materials and from solid solutions in binary and ternary systems of the cerium oxide with rare
earth oxides (Nd2O3, La2O3, Yb2O3, Gd2O3) or with Ta2O5 and Pr6O11, the conductive
phenomena being caused by the Ce4+
to Ce3+
transition.
Selecting the materials for the SOFC-IT anodes has imposed less problems in regards
of the criteria for electronic conductors with chemical stability in reducing conditions of the
working environment for high temperatures and moderate costs.
The studies of the anodic material recommended SOFC-IT cells indicated the
following groups of materials:
cermets based on cerium oxide ceramic composite materials cerium oxide based materialsThe cermets compositions, Ni-YSZ, seem to be the best anodic materials for
electrochemical installations of the SOFC type.
To accomplish an efficient electrode, an optimum mixture of the two phases and a
good physical contact between the both materials are necessary in order to attain the high
electrochemical performances and, in the same time, a high chemical stability and durability.
[9, 10]
Other compositions for anodes of the composite type are also the ones obtained from
NiO as electrolyte material of the gadolinium type doped with ceria (GDC) and samarium
doped with ceria (SDC). These anodic NiO/SDC and NiO/GSC materials have the best
electric conductivity when the eelctrolyte is based on cerium oxide.There are, also, other materials for anodes such as in the cerium oxide based CeO2
doped form or Ce0.6La0.4O1.8 and Ce0.6Y0.4O1.8 compounds. Their electronic type conduction is
predominant for a content greater than 50 mol % CeO2 and is due to the Ce4+
to Ce3+
transition.
Recent studies indicated the accomplishment of other compositions in the structure of
some solid solutions with rare earth oxides, SmO1.5, GdO1.5, NbO2.5 or in binary compositions
with ZrO2 and Y2O3 at a content between 50 90 mol % CeO2. [11]
In order to diminish the polarisation penomena at anodes and to improve the decreased
conversion yield of the cell, problems remain unsolved in the case of regular Ni/ZrO2 cermite
type anode materials, new materials as cermites Ru/ZrO2 or Ru/Al2O3 were developed, which
have an increased activity in all the SOFC-IT cell processes, even in the case of methane gas
fuel use.
Recent informations recommend the successful use of some oxidic compounds with
ZrO2 stabilized Y2O3 and admixture of TiO2, materials with a mixed electric, ionic and
electronic, conductivity and with a very good compatibility towards the cell electrolyte.
Technological ceramic materials processing solutions
To obtain the ceramic materials used in the components of a fuel cell, classical
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ceramic technologies, as well as special unconventional technologies can be applied.
Each of these technologies allows the first stage to be preparing the material under the
ceramic powder shape having the stoechiometric composition specific for the oxidic
compound with electrolyte or electrodes qualities at temperatures below 8000C.
Classical processing technology
In this case, the starting point is the highly pure chemical reactives (oxides and
carbonates). The technological flux stages are: wet homogenizing, drying, chemical synthesis
treatment (roasting), grounding after which is obtained the ceramic powder with structural
characteristics specific for the oxidic compound and the particle sizes required for shaping
under the form of necessary ceramic piece.
Coprecipitation processing technology
The coprecipitation method is a chemical processing method. In this case, there are
used salt solutions of the components which coprecipitate at a certain pH value, after
coprecipitate filtration, taking place the synthesis through roasting of the compound as a
ceramic powder with submicronic particles.
Applying one of these methods implies a series of technological or economical factors,
which can influence the selection of the most advantageous methods.
The obtaining, under the form of components of electrolyte and electrode with a
certain configuration, requires the use of classical shaping ceramic technologies (pressing,
aqueous suspension pouring or pressure pouring from termoplastic slip, extrusion, lamination)or unconventional technologies of deposition in thin layer through serigraphy, spraying in
plasma, electrochemical deposition in vapour state (EDV) etc.
Serigraphy technology
The serigraphy technology is an easy to perform technology, which leads to the
obtaining of thin layers. Using this technology, an optimum contact between electrode,
support and electrolyte is accomplished, and controlled sizes can be obtained. The optimum
thickness of the deposed layers was not established, but is indicated to be in the range 50
100 m.
The obtaining stages of the thin layers, through the serigraphy technology, of the
ceramic components are:
obtaining of electrolyte, ceramic electrodes, interconnect, under the form of aserigraphic ink
serigraphy drying of the serigraphic layers sintering or cosintering the thin layer components
The serographic ink is obtained according to the stages:
dosing of the electrolyte, electrode or interconnect ceramic powders
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dosing the charges: binders plastifiers solvents dispersing agents thixotropic agents thickening agents
In order to be easily obtained, the serigraphic ink must have a good homogeneity and
adherence to the alumina support in the case of cathode and electrolyte, and the anode and
interconnect to adhere well to the electrolyte. Also, the serigraphic ink must have good
rheological properties to allow passing through the serigraphic sieve.
The cost, reproductibility, installations and even obtaining criteria of some
technological parameters have limited the use of some of these technologies, the most
economically convenient technologies being preferred in order to accomplish the solid
electrolyte fuel cell construction.
4. CONCLUSION
Through the development strategy in the field of Hydrogen and Fuel Cells at the
national level, the evolving of the main activity areas will be followed, in accordance with the
European strategy for hydrogen and combustion cells. The main research directions in the
field of solid electrolyte fuel cells are connected to the study of materials, in regards to: reduce the operating temperature increase the energetic efficiency improve the cells fiability internal reforming and direct use of methane use of some sealing materials resistant to high temperatures
5. BIBLIOGRAPHY
1. Philippe Busquin, Prospects for Fuek Cells in A European Resarch Area, Tervuren-Brussels, Belgium29
th
and 30th
of May 20002. L. Oniciu, Pile de combustie, Ed. stiintifica, Bucuresti, 19713. L. Oniciu, E. M. Rus, Surse electrochimice de putere", Ed. Dacia Cluj-Napoca, 19874. S.C. Singhal, Proceedings 2nd Internaional Symposium on SOFC, 2-5 July, 1991, pg. 31-355. P.Duran, J.R. Jurado s.a., Microstructural and electrical characterization of some ceria-gadolinia solid
electrolityes, High Tech Ceramics, 1987,pg.1943-1953
6. T.Ivers Tiffe and H.J. Oel, Electronic conductivity of ceria, High Tech Ceramics, 1987,pg.1933-19417. B.C.H. Steele, s.a., Solide State Ionics 40/41, 1990, pg. 3388. H.Iwahara, s.a., J. Electrochem. Soc., 135, 526, 19889. Kuo, J.H., s.a., Journal Solide State Chem., nr.83,199210. Marjan Marinsek, Andrej Degen and Jordan Macek, Key Engineering Materials, vol. 132-136,199611. Soren Prindahl, Bent F. Sorensen & Mogens Mogensen, Journal of the American Ceramics Society, vol.
3, nr.3, 2000
12. Suzuki. M., s.a., Proceedings 2nd Internaional Symposium on SOFC, 2-5 Yuly, 1991, Athens Greecee