JP2007149509A - Fuel battery cell, and fuel cell - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide fuel battery cell and a fuel cell capable of suppressing deformations. <P>SOLUTION: This fuel battery cell, which on one-side main face of porous support substrates 31 where gas flow passages 31a are formed in the inner part has solid electrolyte layers 33, and which on the other-side main face of the supporting substrates 31, has interconnectors 35. The fuel battery cell is comprises, forming dense layers 38 having a plurality of through-holes on the other-side face of the support substrates 31, and forming, respectively, interconnectors 35 in the through-holes of the dense layers 38. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

  The present invention relates to a fuel cell and a fuel cell, and in particular, a fuel cell and a fuel cell having a solid electrolyte layer on one side of a porous support having a gas flow path formed therein and an interconnector on the other side. It is about.

  In recent years, various fuel cells in which a stack of fuel cells is accommodated in a storage container have been proposed as next-generation energy.

  FIG. 5 shows a cell stack of a conventional hollow plate type solid oxide fuel cell. This cell stack is composed of a plurality of fuel cells 23 (23a, 23b) and one fuel cell 23a. A current collecting member 25 made of metal felt or the like is interposed between the other fuel cell 23b, and an inner electrode (oxygen side electrode) 27 of one fuel cell 23a and an outer electrode (fuel) of the other fuel cell 23b. Side electrode) 28 is electrically connected.

  The fuel battery cell 23 (23a, 23b) is configured by sequentially providing a solid electrolyte layer 29 and an outer electrode 28 on the outer peripheral surface of the flat inner electrode 27, and is exposed from the solid electrolyte layer 29 and the outer electrode 28. An interconnector 30 is provided on the inner electrode 27 so as not to be connected to the outer electrode 28. In the inner electrode 27, a plurality of gas passage holes 32 constituting a gas flow path are formed.

The electrical connection between one fuel battery cell 23a and the other fuel battery cell 23b is achieved by connecting the inner electrode 27 of one fuel battery cell 23a via the interconnector 30 and the current collecting member 25 provided on the inner electrode 27. This is done by connecting to the outer electrode 28 of the other fuel cell 23b (see, for example, Patent Documents 1 and 2).
JP-A-1-169878 JP-A-2005-243334

  However, in the fuel cell 23, the solid electrolyte 29 is formed continuously on the one side main surface of the inner electrode 27 in the gas flow path formation direction, and the other side main surface is opposed to the solid electrolyte 29. In addition, since the interconnector 30 is continuously formed in the gas flow path forming direction, there is a problem that the fuel cell warps during power generation so that the interconnector 30 side is back.

That is, the fuel cell is usually produced by sintering in the atmosphere, and the interior is exposed to a reducing gas during power generation, but it is an interconnector made of LaCrO ₃ system (lanthanum chromi system composition) that is usually used. The material is known to cause a dimensional change in a reducing atmosphere, and there is a problem that the fuel cell is deformed due to the dimensional change in the reducing atmosphere.

That is, the solid electrolyte 29 made of ZrO ₂ , CeO ₂ , lanthanum gallate, or the like formed on one main surface of the inner electrode 27 has a small dimensional change in a reducing atmosphere, but is provided on the other main surface. Since the interconnector 30 thus obtained has a large dimensional change in a reducing atmosphere, as shown in FIG. 4 (a), the fuel cell is warped with the interconnector side facing away (so that the interconnector side is convex). was there. This warpage of the fuel cell occurs not only in the case of bowing in the length direction but also in the width direction. In particular, in order to increase the amount of power generation per cell, the length of the fuel cell is increased. Then, as shown in FIG. 4 (a-2), it tends to warp in a bow direction in the length direction, and when the width of the fuel cell is increased, there is a problem that it tends to warp in the width direction as shown in FIG. 4 (a-3). there were.

  The cell stack is produced by electrically connecting a plurality of fuel cells 23 by the current collecting member 25, but when the fuel cells 23 are warped as described above, the current collection of the plurality of fuel cells 23 is performed. There is a fear that the electrical connection by the member 25 is released, and it is impossible to collect current from the plurality of fuel cells 23.

  An object of this invention is to provide the fuel cell and fuel cell which can suppress a deformation | transformation.

  The fuel cell of the present invention has a solid electrolyte layer on one side of a porous support having a gas flow path formed therein, and an interconnector on the other side facing the one side of the support. In the fuel cell, a dense layer having a plurality of through holes is formed on the other side surface of the support, and the interconnector is formed in each through hole of the dense layer. .

  In such a fuel cell, the support has a solid electrolyte layer on one surface and an interconnector on the other surface, and the interconnector formed on the other surface is divided into a plurality of parts. Therefore, even if the interconnector is exposed to a reducing atmosphere during power generation, the divided interconnector deforms to some extent in the reducing atmosphere, but the interconnector is not continuously formed, so the dimensions change in the reducing atmosphere. The amount of warpage due to can be reduced.

  In the fuel cell of the present invention, the dense layer is made of a solid electrolyte material. In such a fuel cell, a solid electrolyte material is formed on both main surfaces of the support, for example, the support substrate, and the material configuration on both main surfaces of the support substrate can be made closer, and on both sides of the support substrate. The deformation difference can be suppressed and the amount of warpage can be reduced.

  Further, in the fuel cell of the present invention, an interconnector material layer is formed on a surface of the dense layer, and the interconnector material layer is formed in a plurality of through holes of the dense layer. It is characterized by being electrically connected to. In such a fuel cell, for example, when the fuel cell is electrically connected by the current collecting member, the current collecting member needs to be electrically connected to the interconnector in the through hole of the dense layer. In the present invention, an interconnector material layer that is electrically connected to the interconnectors in the plurality of through holes and electrically connected to each other is formed on the surface of the dense layer. Therefore, by connecting the current collecting member to the interconnector material layer, the current collecting member and the interconnector in the through-hole can be electrically connected, and it becomes easy to take out electricity from the fuel cell and efficiently collect. Can be electrified.

  The fuel cell of the present invention is characterized in that the support has conductivity, and the solid electrolyte layer is formed on one side of the support via an electrode layer. The electrode layer formed on one side surface of the support is a fuel electrode layer. The case where the electrode layer formed on one surface of the conductive support is an air electrode layer is also included.

  In such a fuel cell, since a support body that requires gas permeability and an electrode layer that requires reactivity with gas are separately formed, materials and structures corresponding to the respective functions should be used. In addition, current collection can be easily performed, and an optimal fuel cell can be manufactured.

  Furthermore, the fuel battery cell of the present invention is characterized in that the support functions as a fuel electrode, and the solid electrolyte layer is formed on one side surface of the support. This is a so-called fuel electrode-supported fuel battery cell, and since the support can be used as a fuel electrode, it has a simple structure and is advantageous in production.

  In the fuel cell of the present invention, the support is in the form of a substrate, one side surface of the support is a main surface on one side, and the other side surface of the support is a main surface on the other side. And That is, the support is in the form of a substrate, and has the solid electrolyte layer on one main surface of the support and the interconnector on the other main surface of the support. This is a so-called hollow flat fuel cell. Such a hollow plate type fuel cell has a small thickness and is easily deformed, so that the present invention can be particularly preferably used.

  The fuel cell of the present invention is characterized in that a plurality of the above-described fuel cells are accommodated in a storage container. In such a fuel cell, since the warpage of the fuel cell can be suppressed, for example, one fuel cell and the other fuel cell can be reliably connected by the current collecting member, and the electrical connection reliability can be improved.

  In the fuel cell of the present invention, the stress due to the dimensional change due to the reduction of the interconnector is relieved, and the amount of warpage of the fuel cell can be reduced.

  In FIG. 1 showing a cross section of the fuel cell of the present invention, and in FIG. 2 showing a cross-sectional perspective view, the fuel cell indicated by 30 as a whole has a hollow flat plate shape, a flat cross section, and an elongated substrate as a whole. A porous support substrate (support) 31 is provided. Inside the support substrate 31, six fuel gas passages 31a (forming gas passages) are formed penetrating in the length direction (axial direction) at appropriate intervals. The support substrate 31 has a structure in which various members are provided. A plurality of such fuel cells 30 are connected to each other in series by a current collecting member 40 as shown in FIG. 3, thereby forming a cell stack constituting the fuel cell.

  As is understood from the shapes shown in FIGS. 1 and 2, the support substrate 31 includes a flat portion A and arc-shaped portions B at both ends in the width direction of the flat portion A. The flat portion A has a main surface. Constitute. Both main surfaces of the flat portion A are formed substantially parallel to each other, and a porous fuel electrode layer 32 is provided so as to cover one main surface of the flat portion A and the arc-shaped portions B on both sides. A dense solid electrolyte layer 33 is laminated so as to cover the fuel electrode layer 32, and one main portion of the flat portion A is disposed on the solid electrolyte layer 33 so as to face the fuel electrode layer 32. An oxygen electrode layer 34 is laminated on the surface. The fuel electrode layer 32 and the solid electrolyte layer 33 are formed continuously on one side main surface of the flat portion A in the gas flow path forming direction G.

  The fuel battery cell 30 requires gas permeability by forming the solid electrolyte layer 33 via the fuel electrode layer 32 on the one side main surface of the conductive support substrate 31 while the support substrate 31 has conductivity. Since the support substrate 31 and the fuel electrode layer 32 required to react with the gas are separately formed, it is possible to use a material, a structure, or the like corresponding to each function, and to collect current easily. And an optimal fuel cell can be produced.

  In addition, a large number of dense divided interconnectors 35 to be described later are formed on the other main surface of the flat portion A where the fuel electrode layer 32 and the solid electrode layer 33 are not stacked. As is clear from FIG. 1, the fuel electrode layer 32 and the solid electrolyte layer 33 are configured such that the surface of the support substrate 31 is not exposed to the outside.

  In the present invention, a dense layer 38 having a large number of through-holes is formed on the other main surface of the support substrate 31. As shown in FIGS. Dense interconnectors 35 are respectively formed in the through-holes of the material layer 38, and each interconnector 35 is electrically connected to the fuel electrode layer 32 via the conductive support substrate 31. Thus, since the interconnector 35 is divided into a plurality of parts and is formed in the through hole of the dense layer 38, the dimensional change due to the reduction of the interconnector material is dispersed even if it is exposed to a reducing atmosphere during power generation. The stress due to the dimensional change is relieved, and the amount of warpage of the fuel cell can be reduced. In addition, deformation due to a difference in thermal expansion can be reduced even when the fuel cell is manufactured.

  In addition, the outer peripheral surface of the support substrate 31 is densely covered with the solid electrolyte layer 33, the dense layer 38, and the interconnector 35, whereby a reducing gas (for example, hydrogen) and an oxygen-containing gas (for example, air) are coated. Thus, the gas can be reliably shut off, and the gas leakage from the inside of the support substrate 31 is effectively prevented.

  As shown in FIG. 4B, the through holes of the dense layer 38 have a circular shape in plan view, and three columns formed in the width direction and two columns formed alternately form a matrix. There is no. In FIG. 4B, an example in which circular through holes are formed is described. However, as shown in FIG. 4A, a conventional interconnector formed continuously in the length direction may be divided. For example, the through hole may have any shape.

  The dense layer 38 is preferably made of a solid electrolyte material that forms the solid electrolyte layer 33. Thereby, solid electrolyte materials are formed on both main surfaces of the support substrate 31, the layer structure becomes substantially the same, the deformation difference between both main surfaces of the support substrate 31 is eliminated, and the warpage of the fuel cell can be further suppressed. . For the dense layer 38, forsterite material can be used, for example.

  Furthermore, in this invention, as shown to FIG.4 (c-1) (c-2), the interconnector material layer 47 is formed in the dense material 38 surface by the same material as the material which forms the interconnector 35, The interconnector material layer 47 can be electrically connected to the interconnector 35 in the plurality of through holes. In this case, as shown in FIG. 3, when the fuel cell stack is configured, the fuel cells are electrically connected to each other by the current collecting member 40, but the current collecting member 40 is connected to the interconnector material layer 47. This makes it easier to improve the connection reliability. Moreover, since the P-type semiconductor layer 39 can be formed on the interconnector material layer 47 as shown in FIG. 4C-2, the formation is easy. Since the interconnector material layer 47 is formed on the dense layer 38, the interconnector material layer 47 is not exposed to the reducing atmosphere, so that there is almost no dimensional deformation in the reducing atmosphere. 1 and 2 show a case where the interconnector material layer 47 is not provided. In this case, the P-type semiconductor layer 39 is formed only on the surface of the circular interconnector 35.

  The interconnector material layer 47 is formed on the surface of the dense layer 38 with the same material as that forming the interconnector 35. However, in the present invention, a conductive material different from the interconnector 35 is formed on the surface of the dense layer 38. A coating layer made of may be formed, and the plurality of interconnectors 35 may be electrically connected by this coating layer. For example, when the dense layer 38 is formed of a material other than the solid electrolyte material, a coating layer is formed on the surface of the dense layer 38 with an oxygen electrode material, and the interconnectors 35 can be electrically connected to each other. The covering layer may be formed from a noble metal, for example, an Ag-containing conductive material.

  The hollow flat plate fuel cell of the present invention can be suitably used when the length is 120 mm or more, the thickness is 8 mm or less, and the width is 20 mm or more. That is, in a hollow flat plate type fuel cell, when the length is long, as shown in FIG. 4 (a-2), when the cell is viewed in the length direction, it tends to warp like a bow with the interconnector side as the back. Therefore, the present invention can be used effectively, and when the width is widened, as shown in FIG. 4A-3, when the fuel cell is viewed in the width direction, that is, in the width direction. In addition, the present invention can be used effectively because it tends to warp in a crescent shape with the interconnector side as the back.

  In addition, when the thickness of the fuel cell is 8 mm or less, the distance between the main surfaces facing each other is small, so that the fuel cell tends to warp in the length direction and the width direction, so that the present invention can be used effectively.

  In the fuel cell having the above structure, the portion of the fuel electrode layer 32 facing the oxygen electrode layer 34 operates as a fuel electrode to generate electric power. That is, an oxygen-containing gas such as air is allowed to flow outside the oxygen electrode layer 34, and a fuel gas (hydrogen) is supplied to the gas passage 31 a in the support substrate 31, and the oxygen electrode layer 34 is heated to a predetermined operating temperature. Then, an electrode reaction of the following formula (1) is generated, and power is generated by generating an electrode reaction of the following formula (2), for example, in the portion that becomes the fuel electrode of the fuel electrode layer 32.

Oxygen electrode: 1 / 2O ₂ + 2e ⁻ → O ²⁻ (solid electrolyte) (1)
Fuel electrode: O ²⁻ (solid electrolyte) + H ₂ → H ₂ O + 2e ⁻ (2)
The current generated by the power generation is collected through the interconnector 35 attached to the support substrate 31.

(Support substrate 31)
In the fuel cell 30 having the structure as described above, the support substrate 31 is gas permeable to allow the fuel gas to permeate to the fuel electrode layer, and to collect current through the interconnector 35. It is required to be electrically conductive and to be free from cracks and peeling of the solid electrolyte layer due to a difference in thermal expansion during simultaneous firing. At the same time, the volume of the support substrate 31 in the reduction / oxidation cycle is satisfied. For the purpose of suppressing cracks in the solid electrolyte layer and the like caused by expansion, an inorganic aggregate that does not generate a reaction product between the catalytic active metal and its oxide and the catalytic metal and its oxide, such as a metal oxide. A solid electrolyte or a rare earth element oxide containing at least one rare earth element is included.

  As the catalyst metal, there are iron group components such as Fe, Co, and Ni, which may be a single metal, or an oxide, an alloy, or an alloy oxide. In the present invention, any of them can be used, but it is preferable that Ni and / or NiO are contained because they are inexpensive and stable in fuel gas.

Further, as the inorganic aggregate, the solid electrolyte layer 33 is formed in order to increase the so-called three-phase interface (electrolyte / catalyst metal / gas phase interface) in order to promote the electrode reaction of (2). A material equivalent to zirconia bromide, a lanthanum gallate-based perovskite type composition, or the like may be used, or a rare earth oxide may be used to lower the thermal expansion coefficient and approximate the solid electrolyte layer 33. In particular, an oxide containing at least one rare earth element selected from the group consisting of Sc, Y, Lu, Yb, Tm, Er, Ho, Dy, Gd, Sm, and Pr is used for the latter. Specific examples of such rare earth _{oxides, Sc 2 O 3, Y 2} O 3, Lu 2 O 3, Yb 2 O 3, Tm 2 O 3, Er 2 O 3, Ho 2 O 3, Dy 2 O ₃ , Gd ₂ O ₃ , Sm ₂ O ₃ , Pr ₂ O ₃ can be exemplified, and Y ₂ O _3, Yb ₂ O ₃ , and Y ₂ O ₃ are preferable in that they are particularly inexpensive. is there.

  The support substrate 31 may contain other metal components and oxide components as long as required characteristics are not impaired.

  Since the support substrate 31 as described above needs to have fuel gas permeability, it is usually preferable that the open porosity is 30% or more, particularly 35 to 50%. Further, the conductivity of the support substrate 31 is preferably 300 S / cm or more, and particularly preferably 440 S / cm or more.

  Further, the length of the flat portion A of the support substrate 31 is usually 20 to 35 mm, the length of the arc-shaped portion B (arc length) is about 3 to 8 mm, and the thickness of the support substrate 31 is (flat portion). The distance between both surfaces of A) is preferably about 2.5 to 8 mm.

(Fuel electrode layer 32)
In the present invention, the fuel electrode layer 32 causes the electrode reaction of the above-described formula (2), and is formed of a known porous conductive ceramic. For example, it is formed from ZrO ₂ in which a rare earth element is dissolved, and Ni and / or NiO. As ZrO ₂ (stabilized zirconia) in which the rare earth element is dissolved, the same one used for forming the solid electrolyte layer 33 described below is preferably used.

  The stabilized zirconia content in the fuel electrode layer 32 is preferably in the range of 35 to 65% by volume, and the Ni or NiO content is preferably 65 to 35% by volume. Further, the open porosity of the fuel electrode layer 32 is preferably 15% or more, particularly preferably in the range of 20 to 40%, and the thickness is preferably 1 to 30 μm. For example, if the thickness of the fuel electrode layer 32 is too thin, the performance may be deteriorated, and if it is too thick, there is a risk of peeling due to a difference in thermal expansion between the solid electrolyte layer 33 and the fuel electrode layer 32. .

Further, since the fuel electrode layer 32 only needs to be present at a position facing the oxygen electrode layer 34 and the fuel electrode is formed, for example, the fuel electrode layer 32 has a fuel only in the flat portion A on the side where the oxygen electrode layer 34 is provided. The polar layer 32 may be formed. (Solid electrolyte layer 33)
The solid electrolyte layer 33 provided on the fuel electrode layer 32 is generally formed of a dense ceramic called ZrO ₂ (usually stabilized zirconia) in which 3 to 15 mol% of a rare earth element is dissolved. . Examples of rare earth elements include Sc, Y, La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, and Lu, but they are inexpensive. From the point, Y and Yb are desirable.

  The stabilized zirconia ceramics forming the solid electrolyte layer 33 is desirably a dense material having a relative density (according to Archimedes method) of 93% or more, particularly 95% or more from the viewpoint of preventing gas permeation. It is desirable that the thickness is 10 to 100 μm. The solid electrolyte layer 3 may be composed of a lanthanum gallate perovskite type composition in addition to the stabilized zirconia.

(Oxygen electrode layer 34)
The oxygen electrode layer 34 is formed of a conductive ceramic made of a so-called ABO ₃ type perovskite oxide. As such a perovskite oxide, at least one of transition metal perovskite oxides, particularly LaMnO ₃ oxides, LaFeO ₃ oxides, and LaCoO ₃ oxides having La at the A site is preferable. LaFeO ₃ -based oxides are particularly suitable because they have high electrical conductivity at an operating temperature of about 1000 ° C. In the perovskite oxide, Sr and the like may exist together with La at the A site, and Co and Mn may exist together with Fe at the B site.

  The oxygen electrode layer 34 must have gas permeability. Therefore, the conductive ceramic (perovskite oxide) forming the oxygen electrode layer 34 has an open porosity of 20% or more, particularly 30. It is desirable to be in the range of ˜50%.

  The thickness of the oxygen electrode layer 34 is preferably 30 to 100 μm from the viewpoint of current collection.

(Interconnector 35)
The interconnector 35 provided on the support substrate 31 at the position facing the oxygen electrode layer 34 is made of conductive ceramics, but is in contact with the fuel gas (hydrogen) and the oxygen-containing gas. It is necessary to have oxidation resistance. For this reason, lanthanum chromite perovskite oxides (LaCrO ₃ oxides) are generally used as the conductive ceramics. Further, in order to prevent leakage of the fuel gas passing through the inside of the support substrate 31 and the oxygen-containing gas passing through the outside of the support substrate 31, such conductive ceramics must be dense, for example, 93% or more, particularly 95%. It is preferable to have the above relative density.

  The interconnector 35 is desirably 10 to 200 μm from the viewpoint of preventing gas leakage and electrical resistance. That is, if the thickness is smaller than this range, gas leakage is likely to occur, and if the thickness is larger than this range, the electric resistance is large, and the current collecting function may be reduced due to a potential drop. .

  A P-type semiconductor layer 39 is provided on the outer surface (upper surface) of the interconnector 35. By connecting the current collecting member 40 to the interconnector 35 via the P-type semiconductor layer 39, the contact between the two becomes an ohmic contact, the potential drop can be reduced, and the deterioration of the current collecting performance can be effectively avoided. Thus, for example, the current from the oxygen electrode layer 34 of one fuel battery cell 30 can be efficiently transmitted to the support substrate 31 of the other fuel battery cell 30. As such a P-type semiconductor, a transition metal perovskite oxide can be exemplified.

Specifically, those having higher electronic conductivity than LaCrO ₃ oxides constituting the interconnector 35, for example, LaMnO ₃ oxides and LaFeO ₃ oxides in which Mn, Fe, Co, etc. exist at the B site P-type semiconductor ceramics made of at least one of LaCoO ₃ -based oxides can be used. In general, the thickness of the P-type semiconductor layer 39 is preferably in the range of 30 to 100 μm.

  The interconnector 35 can also be provided directly on the flat portion A of the support substrate 31 on the side where the solid electrolyte layer 33 is not provided, but this portion is also provided with a fuel electrode material, and this fuel electrode material layer. An interconnector 35 can be provided thereon. In this case, it is advantageous in that the potential drop at the interface between the support substrate 31 and the interconnector 35 can be suppressed.

(Manufacture of fuel cells)
The fuel battery cell having the above structure is manufactured as follows. First, an iron group metal such as Ni or its oxide powder, for example, Y ₂ O ₃ powder, an organic binder, and a solvent are mixed to prepare a clay, and by extrusion molding using this clay, A support substrate molding is produced and dried.

  Next, a fuel electrode forming material (Ni or NiO powder and stabilized zirconia powder), an organic binder, and a solvent are mixed to prepare a slurry. Using this slurry, a sheet for the fuel electrode is prepared, and is placed in a predetermined position. Laminate. Further, instead of producing a sheet for the fuel electrode, a paste in which a material for forming a fuel electrode is dispersed in a solvent is applied to a predetermined position of the support substrate molded body formed as described above, and dried. A coating layer may be formed.

  This is calcined to produce a support substrate calcined body on which the fuel electrode calcined body is formed, and the open pores of the fuel electrode calcined body are impregnated with a resin material. As the resin material, an acrylic resin or the like is used. For impregnation, the resin material may be immersed in an organic solvent in which the resin is dissolved. On the other hand, the portion of the support substrate calcined body on which the interconnector is formed is masked so that the solid electrolyte is not formed.

Thereafter, a solid electrolyte is formed on the surface of the fuel electrode calcined body by a dip coating method. First, an immersion liquid containing a solid electrolyte material is prepared, and the support substrate calcined body is immersed in the immersion liquid. As the solid electrolyte material, for example, ZrO ₂ powder in which a rare earth element is dissolved is used, and in addition, an acrylic binder as an organic binder and toluene as a solvent are added and mixed in the immersion liquid. The immersion liquid has an organic component adjusted so as to have a predetermined viscosity.

  The dipping direction is preferably dipped in the width direction of the support substrate calcined body rather than dipping in the length direction of the support substrate calcined body in the dipping solution. When the substrate is immersed and then pulled up, the support substrate calcined body is deposited on the fuel electrode calcined body to form a solid electrolyte molded body, and the support substrate calcined body is also deposited on the surface of the dense calcined layer molded body. Form.

  That is, a porous fuel electrode calcined body is formed on the surface of the porous support substrate calcined body, and the open pores of the fuel electrode calcined body are filled with a resin material. A solid electrolyte molded body is formed on the surface, and a dense layer molded body is formed on the surface of the support substrate calcined body on which the interconnector is formed. The open pores of the fuel electrode calcined body are not impregnated with the solid electrolyte material. By removing the mask, through holes are formed in the dense layer molded body made of the solid electrolyte material.

The support substrate calcined body is composed of iron group metal such as Ni or its oxide particles and Y ₂ O ₃ particles, and the fuel electrode calcined body is composed of Ni or NiO particles and stabilized zirconia particles. The solid electrolyte molded body and the dense layer molded body are composed of a stabilized zirconia powder and an organic component.

Thereafter, a material for an interconnector (for example, LaCrO ₃ oxide powder), an organic binder, and a solvent are mixed to prepare a slurry, and an interconnector sheet is prepared. This interconnector sheet is laminated in the through hole of the dense layer molded body to produce a fired laminate. When forming an interconnector material layer molded body on the dense layer molded body, for example, an immersion liquid containing the interconnector material is prepared, and the dense layer molded body is penetrated into the immersion liquid. The support substrate calcined body in which the holes are formed can be immersed to form an interconnector material layer on the dense layer surface, and the interconnector material can be filled into the through holes of the dense layer.

Next, the above laminate for firing is subjected to a binder removal treatment, and co-fired at 1300 to 1600 ° C. in an oxygen-containing atmosphere, and an oxygen electrode forming material (for example, LaFeO ₃₎ is placed at a predetermined position of the obtained sintered body. And paste containing a P-type semiconductor layer forming material (for example, LaFeO ₃ -based oxide powder) and a solvent by dipping or the like, if necessary. The fuel cell 30 of the present invention having the structure shown in FIG. 1 can be manufactured by baking.

  In the case where Ni alone is used to form the support substrate 31 and the fuel electrode layer 32, Ni is oxidized to NiO by firing in an oxygen-containing atmosphere. , Ni can be returned.

(Cell stack)
As shown in FIG. 3, the cell stack includes a plurality of the fuel cells 30 described above, and a metal felt and / or between one fuel cell 30 and the other fuel cell 30 adjacent to each other in the vertical direction. A current collecting member 40 made of a metal plate is interposed, and both are connected in series with each other. That is, the support substrate 31 of one fuel battery cell 30 is electrically connected to the oxygen electrode 34 of the other fuel battery cell 30 via the interconnector 35, the P-type semiconductor layer 39, and the current collecting member 40. . Such cell stacks are arranged side by side as shown in FIG. 3, and adjacent cell stacks are connected in series by a conductive member 42. In FIG. 3, the description of the P-type semiconductor layer 39 is omitted.

  The fuel cell of the present invention is configured by accommodating the cell stack of FIG. 3 in a storage container. The storage container is provided with an introduction pipe for introducing a fuel gas such as hydrogen into the fuel battery cell 30 from the outside, and an introduction pipe for introducing an oxygen-containing gas such as air into the external space of the fuel battery cell 30. The fuel cell is heated to a predetermined temperature (for example, 600 to 900 ° C.) to generate electric power, and the used fuel gas and oxygen-containing gas are discharged out of the storage container.

  In addition, this invention is not limited to the said form, A various change is possible in the range which does not change the summary of invention. For example, in the above embodiment, the case where the fuel electrode layer 32 is formed on the support substrate 31 has been described. However, the support substrate itself is provided with a function as a fuel electrode, and a solid electrolyte and an oxygen electrode layer are formed on the support substrate. Also good. Moreover, although the case where the fuel electrode layer 32 was formed on the support substrate 31 was demonstrated in the said form, the cell which formed the air electrode layer in the support substrate may be sufficient.

  Furthermore, in the above embodiment, an example in which the present invention is applied to a hollow flat plate fuel cell has been described. However, the present invention is not limited to the above embodiment. For example, the present invention is applicable to a cylindrical fuel cell. The invention can be applied effectively.

NiO powder having an average particle size of 0.5 μm and Y ₂ O ₃ powder (average particle size is 0.6 to 0.9 μm), NiO is 48% by volume in terms of Ni, and Y ₂ O ₃ is 52% by volume. Then, the mixed powder is extruded to form a support substrate clay formed by mixing a pore agent, an organic binder (polyvinyl alcohol), and water (solvent), and then dried and debindered. It processed, the flat molded object for support substrates was produced, and this was dried. Then, it calcined at 1000 degreeC and produced the support substrate calcined body.

Next, a fuel electrode forming sheet using a slurry in which ZrO ₂ (YSZ) powder containing 8 mol% Y ₂ O ₃ , NiO powder, organic binder (acrylic resin), and solvent (toluene) is mixed. Was laminated at a predetermined position on the support substrate calcined body and calcined at 1000 ° C. to form a fuel electrode calcined body on the surface of the support substrate calcined body.

  Thereafter, masking was performed so that a through-hole could be formed at the interconnector formation position (surface of the electrode calcined body) in FIG. On the other hand, an immersion liquid in which the YSZ powder, an organic binder (acrylic resin), and a solvent made of toluene are mixed is prepared, and the support substrate calcined body is dipped in the immersion liquid and pulled up, whereby the fuel electrode is calcined. A coating film of a solid electrolyte material was formed on the surface of the body and the surface of the support substrate calcined body, and dried to form a solid electrolyte molded body and a dense layer molded body.

Next, using a slurry obtained by mixing LaCrO ₃ oxide powder having an average particle diameter of 2 μm, an organic binder (acrylic resin), and a solvent (toluene), a sheet for an interconnector is produced. Dense layer molding is performed by laminating the laminated sheet mask on the peeled portion, and further mixing a slurry of LaCrO ₃ oxide powder having an average particle diameter of 2 μm, an organic binder (acrylic resin), and a solvent (toluene). It apply | coated on the body and the interconnector material layer molded object was formed.

  A sintered laminated sheet consisting of a support substrate calcined body, a fuel electrode calcined body, an interconnector sheet, an interconnector material layer molded body, and a solid electrolyte molded body is produced, and the sintered laminated sheet is subjected to a binder removal treatment. And co-fired at 1500 ° C. in the air.

The obtained sintered body was immersed in a paste made of La _0.6 Sr _0.4 Co _0.2 Fe _0.8 O ₃ powder having an average particle diameter of 2 μm and a solvent (normal paraffin), and sintered. A coating layer for oxygen-side electrode is provided on the surface of the solid electrolyte layer formed on the body, and at the same time, the paste is applied to the outer surface of the interconnector material layer formed on the sintered body, and the coating layer for P-type semiconductor Was further baked at 1150 ° C. to produce a fuel cell as shown in FIG.

  The produced fuel cell has a length of 145 mm, a width of 26 mm, a thickness of 3.2 mm, a fuel electrode layer thickness of 10 μm, an oxygen electrode layer thickness of 50 μm, an interconnector thickness of 50 μm, and a P-type semiconductor layer thickness. Was 50 μm. Further, 40 interconnectors having a diameter of 6 mm were formed, and the interconnector material layer had a thickness of 50 μm.

  For the manufactured fuel cell, linear rulers are applied to the upper and lower ends of the surface opposite to the interconnector formation side, and the maximum distance between this ruler and the cell surface is obtained (FIG. 4 (a-2)). A straight ruler is applied to both ends in the width direction of the surface opposite to the interconnector formation side, and the maximum distance between this ruler and the cell surface is obtained (Fig. 4 (a-3)). The amount of warpage Lb in the width direction was set. As a result, the amount of warpage in the length direction after cell fabrication was 0.1 mm, and the amount of warpage in the width direction was 0.08 mm.

  Furthermore, hydrogen gas was supplied into the gas passage 31a at a temperature of 850 ° C. for 12 hours, and the obtained fuel cell was allowed to cool while flowing hydrogen gas. Then, when the amount of warpage in the length direction and the amount of warpage in the width direction were determined in the same manner as described above, the amount of warpage in the length direction was 0.3 mm, and the amount of warpage in the width direction was 0.1 mm.

  On the other hand, as a comparative example, a fuel cell as shown in FIG. 4 (a) without dividing the interconnector was prepared, and the amount of warpage after production and the amount of warpage after the reduction treatment were measured. The amount of warpage in the length direction is 0.5 mm and the amount of warpage in the width direction is 0.3 mm. After the reduction treatment, the amount of warpage in the length direction is 1.8 mm, and the amount of warpage in the width direction is 0.6 mm. It was. Therefore, it can be seen that the amount of warpage can be suppressed in the fuel battery cell of the present invention.

BRIEF DESCRIPTION OF THE DRAWINGS The fuel cell of this invention is shown, (a) is a cross-sectional view, (b) is a longitudinal cross-sectional view along the xx line of (a). It is a section perspective view of the fuel battery cell of the present invention. It is a cross-sectional view showing a stack of fuel cells of the present invention. It is explanatory drawing which shows the formation state of an interconnector, (a) is a conventional thing, (b) is the case where an interconnector is divided | segmented and formed in the through-hole of a dense membrane, respectively, (c) is a dense interconnector. It is connected by an interconnector material layer formed on the layer. It is a cross-sectional view showing a stack of conventional fuel cells.

Explanation of symbols

31 ... Support substrate (support)
31a ... Fuel gas passage (gas passage)
32 ... Fuel electrode layer 33 ... Solid electrolyte layer 34 ... Oxygen electrode layer 35 ... Interconnector 38 ... Dense layer 40 ... Current collecting member 47 ... Interconnector material layer

Claims (8)

A fuel cell having a solid electrolyte layer on one side of a porous support having a gas flow path formed therein and an interconnector on the other side facing the one side of the support, A fuel cell, wherein a dense layer having a plurality of through holes is formed on the other side surface of the support, and the interconnector is formed in each through hole of the dense layer. The fuel cell according to claim 1, wherein the dense layer is made of a solid electrolyte material. An interconnector material layer is formed on the surface of the dense layer, and the interconnector material layer is electrically connected to the interconnector formed in the plurality of through holes of the dense layer. The fuel cell according to claim 1 or 2, characterized in that: 4. The fuel cell according to claim 1, wherein the support has conductivity, and the solid electrolyte layer is formed on one side of the support via an electrode layer. cell. The fuel cell according to claim 4, wherein the electrode layer is a fuel electrode layer. The fuel cell according to any one of claims 1 to 3, wherein the support functions as a fuel electrode, and the solid electrolyte layer is formed on one side surface of the support. 7. The support according to claim 1, wherein the support is in the form of a substrate, one side of the support is a main surface on one side, and the other side of the support is a main surface on the other side. A fuel battery cell according to claim 1. A fuel cell comprising a plurality of the fuel cells according to claim 1 in a storage container.

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