JP4606081B2 - Solid oxide fuel cell - Google Patents

Description

The present invention relates to a solid oxide fuel cell (SOFC) using a solid electrolyte.

Conventionally, a flat plate type, a cylindrical type, and the like have been proposed as cell designs for solid oxide fuel cells.

  In the flat plate-type cell, a fuel electrode and an air electrode are respectively disposed on the front and back surfaces of a plate-like electrolyte, and a plurality of cells formed in this manner are used in a state where they are stacked via separators. The separator plays the role which completely isolate | separates the fuel gas and oxidant gas which are supplied to each cell, and the gas seal is given between each cell and the separator (for example, patent document 1). However, this flat cell has a drawback in that it is vulnerable to vibration, thermal cycle, etc. because it applies a gas seal by applying pressure to the cell. Yes.

  On the other hand, a cylindrical cell has a fuel electrode and an air electrode arranged on the outer peripheral surface and inner peripheral surface of a cylindrical electrolyte, and a cylindrical vertical stripe type, a cylindrical horizontal stripe type, and the like have been proposed (for example, Patent Documents). 2). However, the cylindrical cell has an advantage of excellent gas sealing properties, but has a disadvantage that the manufacturing process is complicated and the manufacturing cost is high because the structure is more complicated than that of the flat plate cell.

  In addition, there are the following problems. In order to improve the performance of both the flat cell and the cylindrical cell, it is required to reduce the thickness of the electrolyte, and it is necessary to reduce the ohmic resistance of the electrolyte material, but if the electrolyte is too thin, it becomes brittle. There was a problem that the vibration resistance and durability deteriorated.

  Therefore, as a fuel cell instead of the flat plate type and the cylindrical type described above, the fuel electrode and the air electrode are arranged on the same surface of the substrate made of a solid electrolyte, and power is generated by supplying a mixed gas of fuel gas and oxidant gas. A possible non-membrane type solid oxide fuel cell has been proposed (for example, Patent Document 3). According to this fuel cell, since it is not necessary to separate the fuel gas and the oxidant gas, the separator and the gas seal are not required, and the structure and the manufacturing process can be greatly simplified.

In this non-membrane type solid oxide fuel cell, the fuel electrode and the air electrode are formed close to each other on the same surface of the solid electrolyte, and the conduction of oxygen ions occurs mainly near the surface layer of the solid electrolyte. Therefore, the thickness of the electrolyte does not directly affect the performance of the battery unlike the flat plate type and the cylindrical type. Therefore, the thickness of the electrolyte can be increased while maintaining the performance of the battery, thereby improving the vulnerability.
JP-A-5-3045 (first page, FIG. 6) Japanese Patent Laid-Open No. 5-94830 (first page, FIG. 1) JP-A-8-264195 (page 2-3, FIG. 1)

  As described above, in the conventional solid oxide fuel cell, the vulnerability is improved by increasing the thickness of the electrolyte. However, since it is often the vicinity of the surface layer of the electrolyte that contributes to the battery reaction, even if the thickness of the electrolyte is increased in this way, the performance as a battery is not greatly improved, but the thickness of the electrolyte is increased. On the contrary, there is a problem that the manufacturing cost becomes high.

  There are also the following problems. In the fuel cell of Patent Document 3, a pair of fuel electrodes and air electrodes are considered as single battery cells, and a plurality of single battery cells are arranged on an electrolyte. The fuel electrode and the air electrode between adjacent unit cells are connected by an interconnector. However, in this structure, since an electrolyte exists between adjacent unit cells, this electrolyte can be a path for oxygen ions to move during power generation. As a result, the original electromotive force of the single battery cell and the electromotive force of the battery formed between the single battery cells cancel each other, resulting in an internal short-circuit state, so that the electromotive force of the entire fuel cell is lowered and the battery performance is lowered. There was a problem to do.

  The present invention has been made to solve the above-described problems, and provides a solid oxide fuel cell that can improve vulnerability, reduce costs, and obtain high power output. The purpose is to do.

The present invention is a solid oxide fuel cell having a plurality of unit cells each having an electrolyte, a fuel electrode, and an air electrode, and is made to achieve the above object. supporting the cell, comprising a substrate to have a one surface and the other surface, the electrolyte of each single cell is formed on one surface of the substrate at a predetermined interval, the fuel electrode and the air electrode They are arranged on the same surface of the electrolyte with a predetermined interval.

  According to this configuration, since the electrolyte is supported by the substrate, high durability against vibration and thermal cycle can be maintained even when a thin film electrolyte is formed. In particular, in this type of fuel cell, many of the parts that contribute to the cell reaction are in the vicinity of the surface layer of the electrolyte. Therefore, even if the electrolyte is thinned, the battery performance is not greatly affected, and the cost is reduced by thinning the electrolyte. be able to. As a method for reducing the thickness of the electrolyte, for example, there is a method in which an electrolyte is formed by printing, a method in which a sheet-like electrolyte is attached to a substrate, and the like.

  In the fuel cell, a plurality of electrode bodies are arranged. However, the interconnector may be arranged on the battery to connect the electrode bodies, or the interconnector is not arranged on the battery. An interconnector may be arranged on the device side where the battery is set, and the electrode body may be connected by the interconnector on the device side when the battery is set in the device.

  Further, in this fuel cell, since the electrolyte of each single battery cell is arranged at a predetermined interval, the following effects can also be obtained. That is, in the fuel cell, each single battery cell is arranged separately. Therefore, since there is no electrolyte between the single battery cells as in the conventional example, the oxygen ion path can be cut off, and an internal short circuit state can be prevented. As a result, it is possible to prevent the electromotive force of the fuel cell from being lowered, and a high power generation output can be obtained.

  Although the single battery cell of the above structure can be arrange | positioned only on one side of a board | substrate, it can also be arrange | positioned on both surfaces of a board | substrate. By doing so, a large number of unit cells can be formed on one substrate, and a high power generation output can be obtained while keeping the fuel cell compact.

  In addition, the fuel cell preferably further includes an insulating film disposed between the electrolytes. If it does in this way, since the said electrolyte is insulated, it can prevent more reliably that a fuel cell is formed between single battery cells like a prior art example, and, as a result, obtains high electric power generation output. Can do.

  Further, the substrate is preferably made of a ceramic material from the viewpoint of heat resistance.

  According to the fuel cell of the present invention, the fragility can be improved, the cost can be reduced, and a high power generation output can be obtained.

  Hereinafter, an embodiment of a solid oxide fuel cell according to the present invention will be described with reference to the drawings. FIG. 1 is a partial cross-sectional view of a fuel cell according to this embodiment, and FIG. 2 is a schematic plan view of the fuel cell.

As shown in FIGS. 1 and 2, this fuel cell includes a sheet-like substrate 1 and a plurality of unit cells C disposed on one surface thereof (here, two are indicated as C ₁ and C ₂ ). The single battery cells C are connected in series by an interconnector 9.

  Each single cell C includes a rectangular electrolyte 3 disposed on one surface of the substrate 1 and a pair of fuel electrode 5 and air electrode 7 disposed on the same surface of the electrolyte 3. The electrolyte 3 of each single battery cell C is disposed so as to form a gap S with a predetermined interval from the electrolyte 3 of the adjacent single battery cell C, and the interval is preferably 10 to 5000 μm, for example. More preferably, the thickness is 10 to 500 μm. Further, the fuel electrode 5 and the air electrode 7 on each electrolyte 3 are formed in a band shape and are arranged at a predetermined interval. At this time, the distance L between the fuel electrode 5 and the air electrode 7 is preferably, for example, 1 to 5000 μm, and more preferably 10 to 500 μm. For example, when the electrodes are formed by a general pattern printing method such as screen printing, the different polarities may be short-circuited due to the collapse of the electrode pattern, and the interval L is preferably 10 μm or more. When the gap L is formed by post-processing such as blasting or laser processing after forming the electrodes in a state where the different polarities are in contact with each other, processing of about 1 μm is possible from the viewpoint of processing accuracy.

Further, as shown in FIG. 2, takes out the current to the fuel electrode disposed at both ends in the battery, i.e. one of the fuel electrode 5 of the single-battery cells C _1, and the other of the air electrode 7 of the single-battery cells C ₂ Current collectors 8 are formed respectively.

The interconnector 9 connects the adjacent unit cells C as described above, and specifically, the air electrode 7 of _{one unit} cell C ₁ and the fuel electrode 5 of the other unit cell C _2. Is connected. At this time, the interconnector 9 is formed on the electrolyte 3 and is disposed on the substrate 1 so as to cross the gap S between adjacent unit cells C.

  Next, the material of the fuel cell configured as described above will be described. The substrate 1 is preferably formed of a material excellent in adhesiveness with the electrolyte 3, and specifically, SUS, or a ceramic material such as an alumina material, a silica material, or a titanium material is preferably used. Can do. In particular, it is preferable to use a ceramic material excellent in heat resistance of 1000 ° C. or higher. In addition, it is preferable that the thickness of the board | substrate 1 shall be 50 micrometers or more from a viewpoint of intensity | strength.

  As the material of the electrolyte 3, those known as electrolytes for solid oxide fuel cells can be used. For example, ceria oxide doped with samarium or gadolinium, lanthanum galade doped with strontium or magnesium Oxygen ion conductive ceramic materials such as oxides, zirconia-based oxides containing scandium and yttrium can be used.

  As the fuel electrode 5, for example, a mixture of a metal catalyst and a ceramic powder material made of an oxide ion conductor can be used. As the metal catalyst used at this time, a material that is stable in a reducing atmosphere, such as nickel, iron, cobalt, or a noble metal (platinum, ruthenium, palladium, etc.) and has hydrogen oxidation activity can be used. In addition, as the oxide ion conductor, one having a fluorite structure or a perovskite structure can be preferably used. Examples of those having a fluorite structure include ceria-based oxides doped with samarium, gadolinium, and the like, and zirconia-based oxides containing scandium and yttrium. In addition, examples of those having a perovskite structure include lanthanum galide oxides doped with strontium and magnesium. Among the materials described above, the fuel electrode 5 is preferably formed of a mixture of an oxide ion conductor and nickel. The mixed form of the ceramic material made of the oxide ion conductor and nickel may be a physical mixed form or a form of powder modification to nickel. Moreover, the ceramic material mentioned above can be used individually by 1 type or in mixture of 2 or more types. Moreover, the fuel electrode 5 can also be comprised using a metal catalyst alone.

As the ceramic powder material forming the air electrode 7, for example, a metal oxide made of Co, Fe, Ni, Cr, Mn or the like having a perovskite structure or the like can be used. Specifically, (Sm, Sr) CoO ₃ , (La, Sr) MnO ₃ , (La, Sr) CoO ₃ , (La, Sr) (Fe, Co) O ₃ , (La, Sr) (Fe, Co , Ni) O _{3 and the} like, and (La, Sr) MnO ₃ is preferable. The ceramic material mentioned above can be used individually by 1 type or in mixture of 2 or more types.

  The electrolyte 3, the fuel electrode 5 and the air electrode 7 can be formed of a ceramic powder material. The average particle size of the powder used at this time is preferably 10 nm to 100 μm, more preferably 50 nm to 50 μm, and particularly preferably 100 nm to 10 μm. In addition, an average particle diameter can be measured according to JISZ8901, for example.

Further, the interconnector 9 and the current collector 8 are made of conductive metal such as Pt, Au, Ag, Ni, Cu, SUS, or a metal material, or La (Cr, Mg) O ₃ , (La, Ca) CrO. ₃ , (La, Sr) CrO ₃ and other conductive ceramic materials such as lanthanum and chromite. One of these may be used alone, or two or more may be mixed. May be used.

  The fuel electrode 5 and the air electrode 7 are formed by adding appropriate amounts of a binder resin, an organic solvent, and the like with the above-described material as a main component. More specifically, it is preferable to add a binder resin or the like so that the main component is 50 to 95% by weight in the mixing of the main component and the binder resin. Similarly to the fuel electrode 5 and the air electrode 7, the electrolyte 3 is also formed by adding an appropriate amount of a binder resin, an organic solvent, or the like with the above-described material as a main component. In the mixing, it is preferable to mix so that the ratio of the main component is 80% by weight or more. Furthermore, the interconnector 9 is also formed by adding the above additive to the above-described material. The film thicknesses of the air electrode 3, the fuel electrode 5 and the interconnector 9 are formed so as to be 1 μm to 500 μm after sintering, but preferably 10 μm to 100 μm. The thickness of the electrolyte 3 is preferably 10 to 5000 μm, and more preferably 50 to 2000 μm.

  The fuel cell configured as described above generates power as follows. First, a mixed gas of a fuel gas composed of a hydrocarbon-based gas such as methane and ethane and an oxidant gas composed of air or the like is placed on one surface of the substrate 1 on which the unit cell C is formed at a high temperature (for example, 400-1000 ° C). Thereby, ion conduction occurs near the surface layer of the electrolyte 3 between the fuel electrode 5 and the air electrode 7 to generate power.

  Thus, in the fuel cell according to this embodiment, since the electrolyte 3 is supported by the substrate 1, high durability against vibration and thermal cycle can be maintained even if the electrolyte 3 is thinned. In particular, in a fuel cell of the type described above, the portion other than the vicinity of the surface layer of the electrolyte 3 hardly contributes to the cell reaction. Therefore, even if the thin-film electrolyte 3 is formed by printing, the performance is not greatly affected. Therefore, the effect of cost reduction can be obtained by thinning the film.

  Further, a high voltage can be taken out by connecting a plurality of unit cells C in series with the interconnector 9 as described above.

  Furthermore, in the fuel cell according to the present embodiment, the electrolyte of each single battery cell is arranged at a predetermined interval, and therefore has the following effects. That is, in the fuel cell, each single battery cell is arranged separately via a gap and connected by an interconnector. Therefore, since there is no electrolyte between the single battery cells as in the conventional example, oxygen ions can be prevented from moving between the single battery cells, and an internal short circuit state can be prevented. As a result, it is possible to prevent the electromotive force of the fuel cell from being lowered, and a high power generation output can be obtained.

Next, an example of the fuel cell manufacturing method described above will be described with reference to FIG. First, the powder materials for the electrolyte 3, fuel electrode 5 and air electrode 7 described above are used as main components, and an appropriate amount of a binder resin, an organic solvent, etc. are added and kneaded to each of them, and the electrolyte paste, fuel electrode paste, air electrode paste Are respectively prepared. The viscosity of each paste is preferably about 10 ³ to 10 ⁶ mPa · s so as to be compatible with the screen printing method described below. Similarly, the interconnector paste is prepared by adding an additive such as a binder resin to the powder material described above. The viscosity of this paste is the same as described above.

  Next, after applying an electrolyte paste to a plurality of positions on the substrate 1 by screen printing, drying is performed at a predetermined time and temperature, whereby a plurality of rectangular electrolytes 3 arranged at predetermined intervals S are performed. Is formed (FIG. 3A). Subsequently, the fuel electrode paste is applied in a strip shape on each electrolyte 3 by a screen printing method, and then dried and sintered at a predetermined time and temperature to form the fuel electrode 5 (FIG. 3B). Following this, an air electrode paste is applied to each position facing the fuel electrode 5 on each electrolyte 3 by screen printing, and dried and sintered at a predetermined time and temperature to form the air electrode 7. . Thus, a plurality of single battery cells C are formed (FIG. 3C). Finally, the interconnector 9 is formed by applying an interconnector paste in a line shape between the single cells C by screen printing so that the plurality of single cells C are connected in series. At this time, the interconnector 9 is formed so as to cross the gap S between the electrolytes 3 and pass over the substrate 1. Through the above steps, a fuel cell as shown in FIGS. 1 and 2 is completed.

  As mentioned above, although one Embodiment of this invention was described, this invention is not limited to this, A various change is possible unless it deviates from the meaning. For example, in the above embodiment, the electrolyte 3, the fuel electrode 5, and the air electrode 7 are formed only on one surface of the substrate 3, but these may be formed on the other surface of the substrate 3. As a manufacturing method at this time, for example, in each step of forming the electrolyte 3, the fuel electrode 5, and the air electrode 7 on one surface of the substrate 1, the electrolyte, the fuel electrode, and the air electrode are respectively disposed on the other surface of the substrate 1. The same battery is formed on both sides of the substrate 1 in the same manner. By doing so, a high power generation output can be obtained while keeping the fuel cell compact.

  Moreover, in the said embodiment, although the clearance gap is formed between the electrolytes 3 adjacent, the insulating film 10 can also be arrange | positioned in the clearance gap S between the electrolytes 3 as shown in FIG. Thereby, the adjacent electrolyte 3 is partitioned off by the insulating film 10, and the electrical separation between the unit cells C becomes more reliable. Therefore, it can prevent more reliably that a fuel cell is formed between the single cells C, and can obtain a high power generation output.

  In this case, the insulating film 10 is preferably formed of a ceramic material, and for example, an alumina-based or silica-based ceramic material can be used. The particle size of the ceramic material powder constituting the insulating film 10 is usually 10 nm to 100 μm, preferably 100 nm to 10 μm, like the electrolyte and the like. Further, the insulating film 10 is used with the ceramic material powder as a main component and an appropriate amount of a binder resin, an organic solvent, or the like. And it is preferable to make the film thickness after sintering the same as the film thickness of the electrolyte.

  In the manufacturing method described above, a screen printing method is used for applying each paste, but the present invention is not limited to this. The doctor blade method, the spray coating method, the lithography method, the spin coating method, the electrophoresis method, and the like. Other general printing methods such as a printing method such as a deposition method, a roll coating method, a gravure roll coating method, a dispenser coating method, a CVD method, an EVD method, a sputtering method, and a transfer method can be used. Moreover, as a post-process after printing, CIP (hydrostatic pressure press), HIP (hot isostatic press), hot press, and other general press processes can also be used. When the electrolyte is formed by printing, it is preferable to interpose a stress relaxation layer made of an adhesive material showing an intermediate value between the thermal expansion coefficients of the substrate and the electrolyte. By doing so, cracks can be prevented from occurring in the electrolyte of the thin film during sintering due to the difference in expansion coefficient between the two.

  Furthermore, in addition to forming the electrolyte by printing, a fuel cell can also be configured by preparing a plate-like or sheet-like electrolyte and attaching it to a substrate via an adhesive or the like. In this case, a fuel cell can be formed by attaching a plurality of electrolytes of a predetermined size to the substrate for each single battery cell. Alternatively, after attaching the electrolyte, the electrolyte can be separated for each unit cell by cutting.

  Further, in the fuel cell described above, the case where two unit cells are used has been described. Needless to say, however, more unit cells may be used, and further, unit cells may be connected in series. It may be connected in parallel.

  In addition, although the interconnector in the said embodiment is demonstrated so that it may contact the side surface of each electrode in each drawing, you may be comprised so that the edge part of an interconnector may be applied to the upper surface of each electrode It is.

  Hereinafter, the present invention will be described in more detail with reference to examples.

Example 1
As Example 1, a solid oxide fuel cell shown in FIG. GDC (Ce _0.9 Gd _0.1 O _1.9 ) powder (0.05-5 μm, average particle size 0.5 μm) is used as the electrolyte material, and a small amount of a cellulose-based binder resin is mixed therein. An electrolyte paste having a weight ratio of 5 was prepared. The electrolyte paste had a viscosity of about 5 × 10 ⁵ mPa · s suitable for the screen printing method by diluting with a solvent.

Further, as a fuel electrode material, NiO powder (0.01 to 10 μm, average particle size 1 μm), SDC (Ce _0.8 Sm _0.2 O _1.9 ) powder (particle size 0.01 to 10 μm, average particle size 0) 0.1 μm) was mixed to a weight ratio of 7: 3, and then a cellulose-based binder resin was added to prepare a fuel electrode paste in which the ratio of the mixture was 80% by weight. That is, the weight ratio of the mixture to the binder resin was set to 80:20. The viscosity of the fuel electrode paste was about 5 × 10 ⁵ mPa · s suitable for screen printing by diluting with a solvent.

Subsequently, SSC (Sm _0.5 Sr _0.5 CoO ₃ ) powder (0.1 to 10 μm, average particle size 1 μm) is used as an air electrode material, a cellulose binder resin is added, and the ratio of the powder The air electrode paste was prepared so that the ratio was 80%. That is, the weight ratio of the SSC powder to the binder resin was set to 80:20. As with the fuel electrode, the viscosity of the air electrode paste was about 5 × 10 ⁵ mPa · s which was diluted with a solvent and suitable for screen printing. The substrate 1 was an alumina substrate having a thickness of 1 mm and a 10 mm square.

In addition, as an interconnector for connecting the battery cells and a material for the current collector, Au powder (0.1 to 5 μm, average particle size 2.5 μm) is used, and this is mixed with a cellulose-based binder resin. Thus, pastes for interconnectors and current collectors were produced. The viscosity of the interconnector paste was 5 × 10 ⁵ mPa · s suitable for screen printing.

  Next, the electrolyte paste described above is applied onto the substrate 1 by screen printing to form a plurality of rectangular electrolytes. At this time, the electrolyte paste was patterned so that two electrolytes having a size of 9 × 4.2 mm square opened a gap of 0.6 mm and the distance from the edge of the substrate was 0.5 mm. Then, after drying for 15 minutes at 130 degreeC, it sintered for 10 hours at 1500 degreeC, and formed the electrolyte 3 whose thickness after sintering becomes 200 micrometers. Next, a fuel electrode paste was applied on each electrolyte 3 by screen printing. At this time, the fuel electrode paste was applied so that the fuel electrode 5 having a width of 500 μm, a length of 7 mm, and a coating thickness of 50 μm was formed on each electrolyte 3. And after drying for 15 minutes at 130 degreeC, it sintered at 1450 degreeC for 1 hour, and the thickness after sintering was 30 micrometers. Subsequently, an air electrode paste was applied on the same surface of each electrolyte 3 by a screen printing method. At this time, the air electrode paste was applied so that the air electrode 7 having a width of 500 μm, a length of 7 mm, a coating thickness of 50 μm, and an interval of 500 μm from the fuel electrode 5 was formed on each electrolyte 3. And like the fuel electrode 5, after drying for 15 minutes at 130 degreeC, it sintered at 1200 degreeC for 1 hour. The thickness after sintering was 30 μm.

  Subsequently, an interconnector paste was applied by a screen printing method (width 500 μm, thickness 50 μm), and the unit cells C were connected in series as shown in FIG. 1 and FIG. A current collector 8 was formed. Thus, the solid oxide fuel cell according to Example 1 was manufactured.

  Moreover, the comparative example 1 compared with this Example 1 was manufactured as follows. That is, in Comparative Example 1, an electrolyte having a size of 10 × 10 mm and a thickness of 1 mm was prepared and used as a substrate. Then, two fuel electrodes and two air electrodes were formed on the electrolyte with the same dimensions and intervals as in Example 1, and connected in series with an interconnector. Moreover, the comparative example 2 with one unit cell was also produced.

The following evaluation experiment was performed on the manufactured Example 1 and Comparative Example 1. That is, by introducing a mixed gas of methane and oxygen at 800 ° C. and causing a reaction of CH ₄ + 1 / 2O ₂ → 2H ₂ + CO, nickel oxide as the fuel electrode 5 is reduced, and current-voltage characteristics Was evaluated. In order to perform the reduction process, hydrogen gas may be introduced instead of the mixed gas.

  As a result, the electromotive force of one comparative cell 2 of the single battery cell was 610 mV, whereas the electromotive force of Example 1 having two single battery cells was 1190 mV. On the other hand, in Comparative Example 1 having two sets of electrodes, the electromotive force was 900 mV. From the above results, it can be seen that Comparative Example 1 is not twice the electromotive force obtained in Comparative Example 2 due to an internal short circuit. On the other hand, in Example 1, since electrolyte is arrange | positioned at predetermined intervals, it turns out that it will not be in an internal short circuit state, but an electromotive force of about 2 times of the comparative example 2 will be obtained.

(Example 2)
In Example 2, in the fuel cell shown in FIG. 5, an insulating film was disposed between each unit cell.

  The same electrolyte paste, fuel electrode paste, air electrode paste, interconnector paste and substrate as those in Example 1 were prepared. Further, an insulating film paste for forming an insulating film was produced. This was prepared by mixing a cellulose-based binder resin with alumina powder (particle size 0.1 to 10 μm).

  Next, an insulating film paste was applied to a predetermined position between the electrolytes 3 on the substrate 1, and the paste was sintered at 1800 ° C. to form an insulating film 10. Subsequently, the electrolyte 3, the fuel electrode 5, and the air electrode 7 were formed in the same manner as in Example 1. At this time, the electrolyte 3 was positioned so as to sandwich the insulating film paste. Finally, in the same manner as in Example 1, both single battery cells C were connected in series by the interconnector 9, and the current collectors 8 were formed on the electrodes at both ends of the battery. Thus, a solid oxide fuel cell according to Example 2 was manufactured.

  As a result of conducting the same experiment as Example 1 for Example 2, the same performance as that of Example 1 was shown.

1 is a partial cross-sectional view of an embodiment of a solid oxide fuel cell according to the present invention. FIG. 2 is a schematic plan view of the fuel cell shown in FIG. 1. It is a figure which shows an example of the manufacturing method of the fuel cell shown in FIG. FIG. 2 is a cross-sectional view (a) and a plan view (b) of another example of the fuel cell shown in FIG. 1. 1 is a plan view of a fuel cell according to Example 1. FIG.

Explanation of symbols

1 Substrate 3 Electrolyte 5 Fuel electrode 7 Air electrode 9 Interconnector 10 Insulating film C Single battery cell

Claims (6)

A solid oxide fuel cell comprising a plurality of unit cells each having an electrolyte, a fuel electrode, and an air electrode,
Supporting said plurality of single cells, comprising a substrate to have a one surface and the other surface,
The electrolyte of each single battery cell is formed on one surface of the substrate at a predetermined interval,
The solid oxide fuel cell, wherein the fuel electrode and the air electrode are arranged on the same surface of the electrolyte at a predetermined interval.   The solid oxide fuel cell according to claim 1, further comprising an interconnector that connects the plurality of unit cells.   The solid oxide fuel cell according to claim 1, wherein the electrolyte is formed on the substrate by printing.   4. The solid oxide fuel cell according to claim 1, wherein the plurality of unit cells are disposed on both surfaces of the substrate. 5.   The solid oxide fuel cell according to any one of claims 1 to 4, further comprising an insulating film disposed between the electrolytes.   The solid oxide fuel cell according to claim 1, wherein the substrate is made of a ceramic material.

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