JP2010140895A - Solid oxide fuel cell, and fuel cell module having the same - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To materialize a solid oxide fuel cell wherein its initial power-generating performance is high and its initial power-generating durability is also good, by using its air-electrode current collecting body containing Ag and a perovskite type oxide within a specific ratio, in the solid oxide fuel cell which is formed so that its current flows in its axial direction. <P>SOLUTION: The solid oxide fuel cell includes a fuel electrode 6, an electrolyte 18 disposed in the fuel electrode, an air electrode 20 disposed in the electrolyte, and a current collecting portion 44a disposed in the air electrode, and is formed so that its current flows in its axial direction. Further, the current collecting portion has Ag and a perovskite type oxide. Moreover, the perovskite type oxide is contained in the current collecting portion, within a quantitative scope wherein its weight ratio to Ag exceeds zero and is smaller than 0.114. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

  The present invention relates to a solid oxide fuel cell and a fuel cell module including the same.

  Conventionally, a fuel cell having a tubular fuel cell is known (see, for example, Japanese Patent Application Laid-Open No. 2007-95442 (Patent Document 1)). The air electrode of this conventionally known solid oxide fuel cell is formed by applying a silver paste, and the silver is exposed to the air.

  Japanese Patent Laying-Open No. 2005-50636 (Patent Document 2) describes a flat solid oxide fuel cell, and an air electrode contact material inside the solid oxide fuel cell is a separator. It is sandwiched between air electrodes. The air electrode contact material comprises at least silver powder or silver alloy powder and perovskite oxide powder. The mixing ratio is preferably silver powder or silver alloy powder: perovskite oxide powder = 90: 10 wt% to 30:70 wt%, more preferably silver powder or silver alloy powder. : Perovskite-type oxide powder = 70: 30 wt% to 50:50 wt%, and according to this air electrode contact material, the air cell's original power generation performance is not greatly impaired, and it can be used in an air environment. It is described that it has excellent power generation performance and can suppress the destruction of a single cell.

  However, according to the knowledge obtained by the present inventors, the air electrode contact material described in the prior art, that is, a composition containing at least a silver powder or a silver alloy powder and a perovskite oxide powder is solid. When applied to the current collector of an oxide fuel cell, the amount of perovskite oxide added was large, resulting in increased electrical resistance and poor power generation performance. Furthermore, when the content of the perovskite type oxide powder is low, the porosity of the air electrode contact layer is lost, and the performance in the air atmosphere tends to deteriorate, and the single cell tends to be easily broken due to fixation. It was. There was a tendency for the power generation durability to decrease due to the loss of the porosity of the air electrode contact layer.

  Japanese Patent Application Laid-Open No. 2002-216807 (Patent Document 3) describes a flat solid oxide fuel cell, and an air current collector inside the solid oxide fuel cell is a separator. And is sandwiched between air electrodes. The air electrode current collector of the solid oxide fuel cell is composed of a dispersion-strengthened silver porous body in which an oxide is dispersed in a silver substrate.

  However, although this prior art discloses an air electrode current collector containing silver and oxide in a specific abundance ratio, current flows through the current collector in the adjacent direction of the cell, and the axis of the cell There is no disclosure when current flows in the direction.

JP 2007-95442 A JP-A-2005-50636 JP 2002-216807 A

  The present inventors have recently applied an air electrode current collector containing silver and a perovskite oxide in a specific abundance ratio to a solid oxide fuel cell in the case where a current flows in the axial direction of the cell. The inventors have obtained knowledge that a solid oxide fuel cell having high initial power generation performance and good power generation durability performance can be realized. The present invention is based on such knowledge.

  Accordingly, an object of the present invention is to provide a solid oxide fuel cell having high initial power generation performance and good power generation durability performance.

  The solid oxide fuel cell according to the present invention includes a fuel electrode, an electrolyte disposed on the fuel electrode, an air electrode disposed on the electrolyte, a current collector disposed on the air electrode, A solid oxide fuel cell, wherein the solid oxide fuel cell is formed such that current flows in an axial direction of the solid oxide fuel cell, and the current collector is Ag and A current collector comprising a perovskite oxide, wherein the amount of the perovskite oxide in the current collector is greater than 0 and less than 0.114 by weight with respect to Ag. Is.

Moreover, according to this invention, the fuel cell module provided with the solid oxide fuel cell by the said this invention is provided.

  According to the present invention, it is possible to provide a solid oxide fuel cell having high initial power generation performance and good power generation durability performance.

1 is a diagram showing a solid oxide fuel cell according to one embodiment of the present invention. It is a figure which shows the solid oxide fuel cell unit by another aspect of this invention. It is a figure which shows the example of the fuel electrode terminal in FIG. It is a figure which shows the example of the air electrode terminal in FIG. The present invention is a diagram showing a solid oxide fuel cell unit according to another embodiment.

  In the industry, the fuel cell according to the present invention includes at least a fuel electrode, an electrolyte, and an air electrode, except that the current collector disposed in the air electrode satisfies the requirements described later. Usually means the same as those classified or understood as solid oxide fuel cells.

In the present invention, the current collector disposed in the air electrode contains Ag and a perovskite oxide. In the present invention, the perovskite oxide is contained in a weight ratio with respect to Ag in a range of more than 0 and less than 0.114, preferably more than 0 and 0.095 or less, More preferably, it is more than 0 and 0.090 or less. Here, the ratio can be determined by electron beam microanalyzer (EPMA) analysis of the current collector surface or cross section.

In the present invention, the perovskite oxide is preferably La0.6Sr0.4Co0.2Fe0.8O3. Further, according to a preferred aspect of the present invention, the oxide constituting the current collector has the same composition as the air electrode, and specific examples thereof include lanthanum manganes doped with at least one selected from Sr and Ca. Examples thereof include lanthanum ferrite doped with at least one selected from knight, Sr, Co, Ni, and Cu, or samarium cobalt or silver doped with at least one selected from Sr, Fe, Ni, and Cu.

In the present invention, the current collector is porous, and air is taken in through the holes and used for power generation. Oxygen that has passed through the current collector is supplied to the air electrode, and good power generation performance is obtained. Moreover, in this invention, the electrical conductivity of a current collection part is higher than an air electrode, As a result, current collection performance can be improved. In the present invention, the porosity of the current collector is about 20 to 80% in terms of porosity. The porosity can be obtained, for example, by embedding and polishing a cross section of a sample to be measured, photographing the sample cross section surface having a mirror surface with an SEM, and analyzing the photographed image.

The present invention will be described below with reference to the accompanying drawings. In order to facilitate understanding of the description, the same reference numerals denote the same components unless otherwise specified in the drawings.

  FIG. 1 is a cross-sectional view of a solid oxide fuel cell according to this embodiment.

  In FIG. 1, the fuel cell unit 1 includes a solid oxide fuel cell 6 and a fuel electrode terminal 24 and an air electrode terminal 26 disposed at both ends thereof. In this aspect, the solid oxide fuel cell is composed of one solid oxide fuel cell 6 (tubular body), and the solid oxide fuel cell 6 is cylindrical.

  The solid oxide fuel cell 6 has a stacked structure of a current collector 44 a, an air electrode 20, an electrolyte 18, and a fuel electrode 16 from the surface exposed to the oxidant gas. It has a through-flow passage 15 serving as a fuel gas passage. The current collector 44 a is connected to the air electrode terminal 26 fixed to the other end 6 b of the solid oxide fuel cell 6. The whole or a part of the air electrode 20 is covered with a current collector 44 a, and electricity generated at the air electrode flows in the axial direction of the cell of the current collector 44 a and takes out electricity from the air electrode terminal 26. The axial direction of the cell indicates the same direction as the direction of the fuel gas flowing through the through passage 15. That is, the direction of arrow A in the figure is shown.

  On the other hand, the fuel electrode terminal 24 fixed to one end 6 a of the solid oxide fuel cell 6 is in contact with the fuel electrode 16, and electricity generated at the fuel electrode 16 is taken out from the fuel electrode terminal 24.

  The current collector 44a is assumed to satisfy the above requirements. According to the preferable aspect of this invention, it is preferable that the thickness of the current collection part 44a is 0.1-50 micrometers, More preferably, it is 0.5-30 micrometers.

  The fuel electrode 16 is, for example, a mixture of Ni and zirconia doped with at least one selected from rare earth elements such as Ca, Y, and Sc, and a mixture of Ni and ceria doped with at least one selected from rare earth elements. And a mixture of Ni and lanthanum gallate doped with at least one selected from Sr, Mg, Co, Fe, and Cu.

  The electrolyte 18 is, for example, zirconia doped with at least one selected from rare earth elements such as Y and Sc, ceria doped with at least one selected from rare earth elements, and lanthanum gallate doped with at least one selected from Sr and Mg. It is formed from at least one kind.

  The air electrode 20 is selected from, for example, lanthanum manganite doped with at least one selected from Sr and Ca, lanthanum ferrite doped with at least one selected from Sr, Co, Ni, and Cu, Sr, Fe, Ni, and Cu. It is formed from at least one of samarium cobalt, silver, etc. doped with at least one.

The thickness of the fuel electrode 16 is usually about 1 to 5 mm, the thickness of the electrolyte 18 is usually about 1 to 100 μm, and the thickness of the air electrode 20 is usually about 1 to 50 μm.

  A fuel electrode protruding peripheral surface 16a in which the fuel electrode 16 protrudes from the electrolyte 18 and the air electrode 20 and an electrolyte 18 protrudes from the air electrode 20 at one end 6a of the solid oxide fuel cell 6. An electrolyte protruding peripheral surface 18 a is provided, and the fuel electrode protruding peripheral surface 16 a and the electrolyte protruding peripheral surface 18 a constitute an outer peripheral surface of the solid oxide fuel cell 6. The air electrode 20 is covered with a current collector 44 a on the remaining outer peripheral surface including the other end 6 b of the solid oxide fuel cell 6. In this embodiment, the fuel electrode protruding peripheral surface 16 a is also the fuel electrode outer peripheral surface 21 that is in electrical communication with the fuel electrode 16.

  The fuel electrode terminal 24 is disposed so as to cover the outer peripheral surface 21 of the fuel electrode from the outside over the entire circumference and is electrically connected to the main body portion 24 a, and the solid oxide so as to be away from the solid oxide fuel cell 6. The tubular fuel cell 6 has a tubular portion 24b extending in the longitudinal direction. Preferably, the body portion 24a and the tubular portion 24b are cylindrical and arranged concentrically, and the tube diameter of the tubular portion 24b is smaller than the tube diameter of the body portion 24a. The main body portion 24a and the tubular portion 24b have a connection channel 24c that communicates with the through channel 15 and communicates with the outside. A step portion 24 d between the main body portion 24 a and the tubular portion 24 b is in contact with the end face 16 b of the fuel electrode 16.

  In this embodiment, the air electrode terminal 26 is disposed so as to cover the outer peripheral surface 22 of the air electrode from the outside over the entire circumference and is electrically connected to the body portion 26a, and the solid oxide fuel cell. And a tubular portion 26 b extending in the longitudinal direction of the solid oxide fuel cell 6 so as to be away from the fuel cell 6. Preferably, the body portion 26a and the tubular portion 26b are cylindrical and concentric, and the tube diameter of the tubular portion 26b is smaller than the tube diameter of the body portion 26a. The main body portion 26a and the tubular portion 26b have a connection channel 26c that communicates with the through channel 15 and communicates with the outside. A step portion 26 d between the main body portion 26 a and the tubular portion 26 b is in contact with the current collector 44 a, the air electrode 20, the electrolyte 18, and the end surface 16 c of the fuel electrode 16 via the annular insulating member 28.

  The tubular portions 24b and 26b of the fuel electrode terminal 24 and the air electrode terminal 26 preferably have the same outer contour cross-sectional shape. More preferably, the fuel electrode terminal 24 and the air electrode terminal 26 have the same overall shape. The fuel electrode terminal 24 and the air electrode terminal 26 are heat-resistant metals such as Ag, stainless steel, nickel-base alloy, and chromium-base alloy.

  The fuel electrode terminal 24 and the solid oxide fuel cell 6, and the air electrode terminal 26 and the fuel cell 6 are sealed and fixed by a conductive sealing material 32 over the entire circumference.

  At one end 6a, the fuel electrode protruding peripheral surface 16a and the electrolyte protruding peripheral surface 18a extend over the entire circumference of the solid oxide fuel cell 6 and are adjacent to each other in the longitudinal direction A. Further, the fuel electrode protruding peripheral surface 16 a is located at the front end portion 6 c of the solid oxide fuel cell 6. A boundary 34 between the fuel electrode protruding peripheral surface 16a and the electrolyte protruding peripheral surface 18a is inside the main body portion 24a of the fuel electrode terminal 24, and between the electrolyte protruding peripheral surface 18 and the current collector protruding peripheral surface 44. The boundary 36 is located outside the main body portion 24a. The electrolyte projecting peripheral surface 18a has a tapered portion 18b that becomes thinner toward the fuel electrode projecting peripheral surface 16a.

  At one end 6a, the sealing material 32 extends over the entire circumference across the fuel electrode protruding peripheral surface 16a and the electrolyte protruding peripheral surface 18a, and is filled in the main body portion 24a of the fuel electrode terminal 24. It is spaced from the air electrode 20 via 18a. At the other end 6b, the sealing material 32 extends over the entire circumference of the air electrode protruding peripheral surface 20a and fills the space between the main body portion 26a of the air electrode terminal 26 and the insulating member 28. . The sealing material 32 is provided so as to partition the gas region acting with the fuel electrode 16, that is, the gas flow region acting with the air electrode 20 from the through flow channel 15 and the connection flow channels 24 c and 26 c. The sealing material 32 is various brazing materials including, for example, silver, a mixture of silver and glass, gold, nickel, copper, and titanium.

Here, the operation principle of the solid oxide fuel cell will be described. When oxidant gas is flowed to the air electrode side and fuel gas (H2, CO, etc.) is flowed to the fuel electrode side, oxygen in the oxidant gas changes to oxygen ions near the interface between the air electrode and the solid electrolyte. Ions reach the fuel electrode through the solid electrolyte. The fuel gas and oxygen ions react to form water and carbon dioxide. These reactions are represented by the formulas (1), (2) and (3). The generated electrons move to the air electrode or the fuel electrode and are collected at the terminal, so that the current flows in the long axis direction of the tubular cell. By connecting the air electrode and the fuel electrode with an external circuit, electricity can be taken out to the outside.
H 2 + O 2-→ H 2 O + 2 e-(1)
C O + O 2-→ CO 2 + 2 e-(2)
1/2 O2 + 2 e-→ O 2-(3)

  More specifically, the gas (fuel gas) that acts on the fuel electrode 16 in FIG. 1 is passed through the through passage 15 and the connection passages 24c and 26c. In addition, a gas (oxidant gas) that acts on the air electrode 20 flows around the air electrode 20. Thereby, the solid oxide fuel cell 6 operates. Further, the electricity of the fuel electrode 16 is taken out via the sealing material 32 and the fuel electrode terminal 24, and the electricity of the air electrode 20 is taken out via the sealing material 32 and the air electrode terminal 26.

  FIG. 2 is an example of a solid oxide fuel cell unit according to another aspect of the present invention. The cell unit 2 includes a cell 7 and two terminals. The cell is composed of a solid electrolyte disposed outside a fuel electrode support having a through-flow passage inside, and an air electrode disposed outside the solid electrolyte. The electric part is arranged. The solid oxide fuel cell 7 is provided with one end 56a and the other end 56b. The fuel electrode terminal 104 is provided inside the other end 56b, and two terminals, the air electrode terminal 106, are provided outside. It has been. FIG. 3 shows the inner fuel electrode terminal 104. The fuel electrode terminal 104 is inserted into the through-flow passage of the fuel electrode and is in contact with the fuel electrode. The fuel electrode terminal 104 has a substantially cylindrical shape in order to increase the contact area with the solid oxide fuel cell 7 at the center. FIG. 4 shows the outer cathode terminal 106. The air electrode terminal 106 is in contact with the current collector 144a covered outside the air electrode. The air electrode terminal 106 has a substantially cylindrical shape so that the solid oxide fuel cell 7 can be inserted into the center thereof. Each terminal is made of a heat-resistant metal such as Ag, stainless steel, nickel-base alloy, or chromium-base alloy, and the terminal and the cell are fixed by the spring force of the metal. As with the specifications in Fig. 1, when an oxidant gas is flowed to the air electrode side and a fuel gas (H2, CO, etc.) is flowed to the fuel electrode side, electricity is generated at the air electrode and the fuel electrode and collected at each terminal. As it is energized, current will flow in the axial direction of the tubular cell.

  FIG. 5 shows a solid oxide fuel cell unit 3 according to another embodiment of the present invention. The cell is composed of a solid electrolyte disposed outside a fuel electrode support having a through-flow passage inside, and an air electrode disposed outside the solid electrolyte. The electric part is arranged. The solid oxide fuel cell 8 has one end portion 66a and the other end portion 66b, and one end portion 66a includes an electrolyte protrusion 214 in which an electrolyte protrudes from the air electrode. The Ag wire that is the air electrode terminal 206 is wound around the outer periphery of the current collector 244 a and is formed near the center of the solid oxide fuel cell 8. The position wound around the outer periphery is not limited to the vicinity of the center, and may be the other end 66b of the solid oxide fuel cell 8. The fuel electrode terminal 204 includes a cylindrical Ag mesh larger than the inner diameter of the through channel. The fuel electrode terminal 204 is inserted into the solid oxide fuel cell 8 to a depth of 10 to 100 mm from one end 66a, and is in contact with the fuel electrode by the spring force of Ag mesh. As with the specifications in Fig. 1, when an oxidant gas is flowed to the air electrode side and a fuel gas (H2, CO, etc.) is flowed to the fuel electrode side, electricity is generated at the air electrode and the fuel electrode and collected at each terminal As it is energized, current will flow in the axial direction of the tubular cell.

  What has been described so far is a solid oxide fuel cell, but the solid oxide fuel cell module includes a solid oxide fuel cell that is surrounded by a heat insulating container and exposed to an oxidant gas. May be applied.

  In the present invention, the solid oxide fuel cell is not limited to a cylindrical shape, and may be applied to a flat shape or the like as long as a current flows in the axial direction of the cell.

The solid oxide fuel cell according to the present invention can be appropriately manufactured according to a known method. Although the current collection part arrange | positioned at an air electrode may be formed by the method similar to a well-known method, the preferable manufacturing method is as follows. First, silver and oxide powders are prepared, and an amount that is the same as the final composition of the current collector is weighed. This is a coating liquid mixed with a resin in a solvent. This coating solution is applied to the air electrode, dried, and baked to form a current collector. The coating liquid can be applied to the air electrode by using a rally coating method, a tape casting method, a doctor blade method, a screen printing method, a spin coating method, a spray method, a flow coating method, a roll coating method, or a combination thereof. . In addition, examples of the resin include urethane resin, acrylic resin, epoxy resin, and phenol resin. Examples of the solvent include ethanol, methanol, α-terpineol, dihydroterpineol, n-methyl-2-pyrrolidone, benzyl alcohol, toluene, acetonitrile, 2-phenoxyethanol, and mixed solvents thereof. The amount of coating liquid applied to the air electrode may be appropriately determined in consideration of the final thickness of the current collector. The drying is preferably performed at about 50 to 150 ° C. for 0.5 to 5 hours, and the firing is preferably performed at about 400 to 800 ° C. for 0.5 to 5 hours.

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

Example 1
First, a fuel electrode support was manufactured as follows. That is, a mixture of NiO powder and (ZrO2) 0.90 (Y2O3) 0.10 (hereinafter abbreviated as YSZ) powder was prepared by a wet mixing method, followed by heat treatment and pulverization to obtain a fuel electrode support raw material powder. The mixing ratio of NiO powder and YSZ powder was 65/35 by weight. A cylindrical molded body was produced by extruding the powder. The molded body was heat-treated at 900 ° C. to obtain a calcined body of the fuel electrode support.

  A solid electrolyte film was formed on the surface of the fuel electrode support by a slurry coating method and fired at 1300 ° C. The fuel electrode support on which the solid electrolyte was formed had dimensions after firing, an outer diameter of 10.4 mm, a wall thickness of 1.5 mm, and an effective cell length of 100 mm.

  Next, an air electrode was formed on the surface of the solid electrolyte by a slurry coating method and fired at 1100 ° C. As shown in Table 1, La0.6Sr0.4Co0.2Fe0.8O3 (hereinafter abbreviated as LSCF) was used as the air electrode. The area of the air electrode was 25.2 cm2.

Next, the following coating liquid was applied on the air electrode to form a current collector. A coating liquid containing a resin, a solvent and a metal powder was prepared. Specifically, urethane resin as a resin, n-methyl-2-pyrrolidone (NMP) and benzyl alcohol as a solvent in a 50:50 mixed solvent, Ag as a metal powder as a conductive metal, air as an oxide La0.6Sr0.4Co0.2Fe0.8O3 (LSCF), which is the same as the electrode material, was prepared. When the total amount of the metal powder and the oxide was 100% by weight, it was weighed so as to be the weight% shown in Table 1 (Ag 92.0% by weight, LSCF 8.0% by weight). Resin, solvent, metal powder, and oxide powder were mixed and stirred. Here, the weight% of the additive material in Table 1 represents the weight% of the metal powder (Ag) and oxide (LSCF) contained when the current collector is 100% by weight. The ratio of the perovskite oxide in the current collector was 0.087 by weight with respect to Ag.

  The obtained coating solution is applied to a solid oxide fuel cell by screen printing, then dried at 80 ° C. for 30 minutes, cooled at room temperature and baked at 700 ° C. for 1 hour, outside the air electrode. A solid oxide fuel cell having a current collector was obtained. Therefore, the current collector was a film comprising Ag and LSCF. More specifically, the current collector became a film of Ag 92.0% by weight and LSCF 8.0% by weight.

  The ratio of the alloy containing Ag and LSCF in the obtained current collector was determined by EPMA analysis of the surface and cross section of this cell current collector. This ratio was as shown in Table 1.

(Example 2)
As shown in Table 1, the current collector was placed outside the air electrode in the same manner as in Example 1 except that the metal powder and oxide powder of the current collector were Ag 98.0 wt% and LSCF 2.0 wt%. A solid oxide fuel cell was obtained. The ratio of the perovskite oxide in the current collector was 0.020 by weight with respect to Ag.

(Example 3)
As shown in Table 1, the current collector was placed outside the air electrode in the same manner as in Example 1 except that the metal powder and oxide powder in the current collector were Ag 99.5 wt% and LSCF 0.5 wt%. A solid oxide fuel cell was obtained. The ratio of the perovskite oxide in the current collector was 0.005 by weight with respect to Ag.

Example 4
As shown in Table 1, the outside of the air electrode was the same as in Example 1 except that the metal powder and oxide powder of the current collector were Ag 90.0 wt%, Pd 2.0 wt%, and LSCF 8.0 wt%. Thus, a solid oxide fuel cell having a current collector disposed therein was obtained. The ratio of the perovskite oxide in the current collector was 0.089 by weight with respect to Ag.

(Example 5)
As shown in Table 1, the outside of the air electrode was the same as in Example 1 except that the metal powder and oxide powder of the current collector were Ag 92.0 wt%, Pd 2.0 wt%, and LSCF 6.0 wt%. Thus, a solid oxide fuel cell having a current collector disposed therein was obtained. The ratio of the perovskite oxide in the current collector was 0.065 by weight with respect to Ag.

(Example 6)
As shown in Table 1, the outside of the air electrode was the same as in Example 1 except that the metal powder and oxide powder of the current collector were Ag 94.0 wt%, Pd 2.0 wt%, and LSCF 4.0 wt%. Thus, a solid oxide fuel cell having a current collector disposed therein was obtained. The ratio of the perovskite oxide in the current collector was 0.043 by weight with respect to Ag.

(Example 7)
As shown in Table 1, the outside of the air electrode was the same as in Example 1 except that the metal powder and oxide powder of the current collector were Ag 96.0 wt%, Pd 2.0 wt%, and LSCF 2.0 wt%. Thus, a solid oxide fuel cell having a current collector disposed therein was obtained. The ratio of the perovskite oxide in the current collector was 0.021 by weight with respect to Ag.

(Example 8)
As shown in Table 1, the outside of the air electrode was the same as in Example 1 except that the metal powder and oxide powder of the current collector were Ag 97.0 wt%, Pd 2.0 wt%, and LSCF 1.0 wt%. Thus, a solid oxide fuel cell having a current collector disposed therein was obtained. The ratio of the perovskite oxide in the current collector was 0.010 by weight with respect to Ag.

Example 9
As shown in Table 1, the outside of the air electrode was the same as in Example 1 except that the metal powder and oxide powder in the current collector were 97.5 wt% Ag, 2.0 wt% Pd, and 0.5 wt% LSCF. Thus, a solid oxide fuel cell having a current collector disposed therein was obtained. The ratio of the perovskite oxide in the current collector was 0.005 by weight with respect to Ag.

(Comparative Example 1)
As shown in Table 1, a solid oxide fuel cell having a current collector disposed outside the air electrode in the same manner as in Example 1 except that the metal powder and oxide powder in the current collector were 100% by weight Ag. Got. The ratio of the perovskite oxide in the current collector was 0.000 by weight with respect to Ag.

(Comparative Example 2)
As shown in Table 1, the outside of the air electrode was the same as in Example 1 except that the metal powder and oxide powder in the current collector were Ag88.0 wt%, Pd2.0 wt%, and LSCF10.0 wt%. Thus, a solid oxide fuel cell having a current collector disposed therein was obtained. The ratio of the perovskite oxide in the current collector was 0.114 by weight with respect to Ag.

(Comparative Example 3)
As shown in Table 1, the outside of the air electrode was the same as in Example 1 except that the metal powder and oxide powder of the current collector were Ag68.0 wt%, Pd2.0 wt%, and LSCF30.0 wt%. Thus, a solid oxide fuel cell having a current collector disposed therein was obtained. The ratio of the perovskite oxide in the current collector was 0.441 by weight with respect to Ag.

(Comparative Example 4)
As shown in Table 1, the metal powder and oxide powder of the current collector were prepared. Specifically, Ag was 98.0% by weight, and it was the same as Example 1 except that NiO was changed to 2.0% by weight so that NiO corresponds to 2.0% by weight with respect to Ag. A solid oxide fuel cell having a current collector disposed outside the air electrode was obtained. The ratio of the perovskite oxide in the current collector was 0.000 by weight with respect to Ag.

(Evaluation methods)
1. Evaluation of power generation durability performance of solid oxide fuel cells Power was generated using a mixed gas of H2 and N2. The fuel utilization rate was 75%. The oxidant gas was air. The power generation potential was measured at a measurement temperature of 700 ° C. and a current density of 0.3 A / cm 2. The rate of change from the initial power generation potential was taken as the potential drop rate. The potential decrease rate after 100 hours of durability indicates the power generation performance maintaining performance of the solid oxide fuel cell, and the lower the potential decrease rate, the better the solid oxide fuel cell performance.

Table 1 shows the evaluation results of Examples and Comparative Examples of the present invention.

Examples and comparative examples will be described with reference to Table 1. In Examples 1 to 3, as a result of adding LSCF to Ag of the current collector, durability was improved by 1% / 100 hr or more compared to 100% by weight of the current collector Ag of Comparative Example 1. When Example 1 to 3 which is a current collection part with favorable power generation durability performance was observed with a SEM (scanning electron microscope), many pores were observed on the surface and cross section of the current collection part. Oxygen that passed through the current collector provided sufficient oxygen to the air electrode by the current collector pores, and good power generation performance was obtained. Comparative Example 1 shows a high value of the potential drop rate of 1% / 100 hr or more, and when the microstructure was observed with an SEM (scanning electron microscope), many pores were found on the current collector surface and cross section. A state close to zero was observed. Due to the densification of the current collector, oxygen was not supplied to the air electrode, and the power generation durability decreased. Furthermore, in Examples 4 to 9, the power generation durability performance was good. In particular, Examples 6 to 8 showed good results with the potential drop rate indicating the power generation durability performance after 100 hours being on the order of 0.18%.
On the other hand, Comparative Examples 2 to 4 showed a high potential drop rate of 1.0% or more after 100 hours. In Comparative Examples 2 to 3, since the amount of LSCF added was large, the adhesion with the air electrode LSCF as the base material was impaired, and the potential decrease rate increased. Moreover, since the comparative example 4 did not use the perovskite oxide, the potential decrease rate increased.

  DESCRIPTION OF SYMBOLS 1 ... Fuel cell unit, 6 ... Solid oxide fuel cell (solid oxide fuel cell body), 6a ... One end, 6b ... The other end, 15 ... Through flow path, 16 ... Fuel Electrode, 16a ... Fuel electrode protruding peripheral surface, 18 ... Electrolyte, 20 ... Air electrode, 21 ... Fuel electrode outer peripheral surface, 22 ... Air electrode outer peripheral surface, 24 ... Fuel electrode terminal, 24b ... Tubular portion, 24c ... Connection flow path, 26 ... Air electrode terminal, 26b ... Tubular portion, 26c ... Connection flow path, 32 ... Sealing material, 44a ... Current collector, 2 ... Fuel cell unit, 7 ... Solid oxide fuel cell, 56a ... One end , 56b ... the other end, 144a ... the current collector, 104 ... the fuel electrode terminal, 106 ... the air electrode terminal, 3 ... the fuel cell unit, 8 ... the solid oxide fuel cell, 66a ... one end 66b ... the other end, 244a ... current collector, 204 ... fuel Electrode terminal, 206 ... Air electrode terminal, 214 ... Electrolyte protrusion

Claims (6)

A solid oxide fuel cell comprising: a fuel electrode; an electrolyte disposed on the fuel electrode; an air electrode disposed on the electrolyte; and a current collector disposed on the air electrode,
The solid oxide fuel cell is formed such that current flows in the axial direction of the solid oxide fuel cell,
Further, the current collector is a current collector comprising Ag and a perovskite oxide, and the amount of the perovskite oxide in the current collector is in a range of more than 0 and less than 0.114 by weight with respect to Ag. A solid oxide fuel cell characterized by comprising. The perovskite oxide is lanthanum manganite doped with at least one selected from Sr and Ca, lanthanum ferrite doped with at least one selected from Sr, Co, Ni, and Cu, or Sr, Fe, Ni, and Cu. The solid oxide fuel cell according to claim 1, which is samarium cobalt or silver doped with at least one selected from the group consisting of:   The solid oxide fuel cell according to claim 1, wherein the perovskite oxide is La0.6Sr0.4Co0.2Fe0.8O3.   The solid oxide fuel cell according to claim 1, wherein the oxide has the same composition as the air electrode.   2. The solid oxide fuel cell according to claim 1, wherein a ratio of the Ag and the oxide is in a range of more than 0 and 0.095 or less. A solid oxide fuel cell module comprising the solid oxide fuel cell according to claim 1.

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