Solid oxide electrolysis cells and their uses

Abstract

To provide a technology capable of suppressing occurrence of cracking at a peripheral edge of an air electrode.SOLUTION: A solid oxide electrolyzer cell comprises: an air electrode; a fuel electrode; and a solid electrolyte layer disposed between the air electrode and the fuel electrode. A peripheral edge of the air electrode includes, in part or in entirety, an irregular part where projections and recesses are alternately repeated, and in the irregular part, each of top and bottom portions has an arc shape. A ratio (R1 / R2) of an arc radius R1 of the top portion to an arc radius R2 of the bottom portion is 3.0 or more.SELECTED DRAWING: Figure 5

Description

[Technical Field]

[0001] The present disclosure relates to solid oxide electrolysis cells and their uses. [Background technology]

[0002] Solid oxide fuel cells (hereinafter referred to as "SOFCs") are known that generate electricity by utilizing an electrochemical reaction between hydrogen and oxygen. For example, a single fuel cell, which is a constituent unit of an SOFC described in Patent Document 1, includes an electrolyte layer containing a solid oxide, an air electrode disposed on one side of the electrolyte layer, and an anode electrode disposed on the other side of the electrolyte layer. Oxygen ions dissociated from oxygen supplied to the air electrode migrate to the anode electrode based on the oxygen conductivity of the solid electrolyte, and react with hydrogen contained in the fuel gas supplied to the anode electrode to generate water vapor and electricity.

[0003] The SOFC can be used as a solid oxide electrolysis cell (hereinafter simply referred to as "SOEC") by passing current in the reverse direction, and is known to be used as an energy storage technology that converts water vapor into hydrogen using surplus electricity, which is an issue in the process of introducing renewable energy. When water vapor is supplied to the anode and an electric current is passed between the cathode and anode, the water vapor is electrolyzed, generating hydrogen from the anode, and oxygen ions generated at the anode migrate to the cathode due to the oxygen conductivity of the solid electrolyte, generating oxygen from the cathode. [Prior art documents] [Patent documents]

[0004] [Patent Document 1] Japanese Patent Publication No. 2023-080459 Summary of the Invention [Problem to be solved by the invention]

[0005] SOFCs generate heat during the reaction, which causes their temperature to rise. In contrast, SOECs sometimes experience a temperature drop between the start of operation and the thermal neutral point. This means that while SOFCs are susceptible to cracks due to expansion of the air electrode caused by temperature rise, SOECs are susceptible to cracks due to contraction of the air electrode caused by temperature drop. [Means for solving the problem]

[0006] The present disclosure can be realized in the following forms.

[0007] (1) According to one aspect of the present disclosure, there is provided a solid oxide electrolysis cell. The solid oxide electrolysis cell includes an air electrode, an anode, and a solid electrolyte layer disposed between the air electrode and the anode. The air electrode has a peripheral edge having an uneven portion with alternating concave and convex portions along a portion or the entire circumference, the top and bottom of the uneven portion both having an arc shape, and the ratio (R1 / R2) of the arc radius R1 of the top to the arc radius R2 of the bottom is 3.0 or greater. The solid oxide electrolysis cell of this aspect can suppress the occurrence of cracks on the peripheral edge of the air electrode.

[0008] (2) In the solid oxide electrolysis cell described in (1) above, the uneven portion may be present on at least one side of the air electrode. The solid oxide electrolysis cell of this configuration can efficiently suppress the occurrence of cracks on the periphery of the air electrode.

[0009] (3) In the solid oxide electrolysis cell described in (2) above, the uneven portion may be present in two or more locations on one side. The solid oxide electrolysis cell of this configuration can efficiently suppress the occurrence of cracks on the periphery of the air electrode.

[0010] (4) In the solid oxide electrolysis cell according to any one of (1) to (3) above, the uneven portion may be present on at least one side on the upstream side with respect to the flow of oxygen-containing gas. The solid oxide electrolysis cell of this configuration can efficiently suppress the occurrence of cracks on the periphery of the air electrode.

[0011] (5) In the solid oxide electrolysis cell according to any one of (1) to (4) above, the fuel electrode is supplied with a fuel gas containing water vapor at a rate of 100 to 130 liters / (min cm 2 ) may be supplied at a flow rate of 0.1 to 1.0 MPa. The solid oxide electrolysis cell of this configuration can efficiently prevent cracks from occurring on the periphery of the air electrode.

[0012] (6) In the solid oxide electrolysis cell according to any one of (1) to (5) above, the air electrode is supplied with an oxygen-containing gas at a rate of 30 to 50 liters / (min cm 2 ) may be supplied at a flow rate of 0.1 to 1.0 MPa. The solid oxide electrolysis cell of this configuration can efficiently prevent cracks from occurring on the periphery of the air electrode.

[0013] (7) In the solid oxide electrolysis cell according to any one of (1) to (6) above, the volume of the air chamber facing the air electrode is 9 cm 3 ~11cm 3 According to the solid oxide electrolysis cell of this configuration, it is possible to efficiently suppress the occurrence of cracks on the periphery of the air electrode.

[0014] (8) According to another aspect of the present disclosure, there is provided a separator-equipped cell including the solid oxide electrolysis cell according to any one of (1) to (7) above and a separator with a central opening disposed on the solid electrolyte layer. This aspect of the separator-equipped cell can efficiently suppress the occurrence of cracks on the periphery of the air electrode.

[0015] (9) According to another aspect of the present disclosure, there is provided an electrolysis stack including a plurality of stacked solid oxide electrolysis cells according to any one of (1) to (7) above. The electrolysis stack of this aspect can efficiently suppress the occurrence of cracks on the periphery of the air electrode. When stacking a plurality of solid oxide electrolysis cells according to any one of (1) to (7) above, all of the solid oxide electrolysis cells may be used, or some may be used in areas where cracks are relatively likely to occur depending on the usage environment of the electrolysis stack, etc.

[0016] (10) According to another aspect of the present disclosure, there is provided a hot module including the electrolytic stack according to (9), a vaporizer that generates water vapor to be supplied to the electrolytic stack, a heat exchanger that exchanges heat with a gas supplied to the electrolytic stack, a heater that heats the electrolytic stack, and a thermal insulator in which the electrolytic stack, the vaporizer, the heat exchanger, and the heater are disposed. The hot module of this aspect can efficiently suppress the occurrence of cracks on the periphery of the air electrode.

[0017] (11) According to another aspect of the present disclosure, there is provided a hydrogen production device including the hot module described above in (10). The hydrogen production device of this aspect can efficiently suppress the occurrence of cracks on the periphery of the air electrode.

[0018] The present invention can be realized in various forms, for example, in the form of a method for manufacturing a solid oxide electrolysis cell. [Brief explanation of the drawings]

[0019] [Figure 1] 1 is a perspective view showing an external configuration of an electrolysis stack according to an embodiment of the present disclosure; [Figure 2] FIG. 2 is an exploded schematic diagram of the electrolysis stack taken along line II-II in FIG. 1. [Figure 3] Schematic top view of a cell with a separator. [Figure 4] Block diagram of a hydrogen production device. [Figure 5] FIG. 4 is a schematic diagram for explaining a concave-convex portion. [Figure 6] FIG. 4 is a schematic diagram for explaining the shape of the concave and convex portions. [Figure 7] FIG. 10 is a schematic diagram for explaining another example of the concave-convex portion. [Figure 8] FIG. 10 is a schematic diagram for explaining another example of the concave-convex portion. DETAILED DESCRIPTION OF THE INVENTION

[0020] Fig. 1 is a perspective view showing the external configuration of an electrolysis stack 10 according to one embodiment of the present disclosure. The electrolysis stack 10 in this embodiment is a stack of solid oxide electrolysis cells (SOECs). Fig. 1 shows an example of the configuration of the electrolysis stack 10.

[0021] The electrolysis stack 10 includes a plurality of rectangular reaction units 11 stacked in the thickness direction, and approximately rectangular end plates 12 and 13 sandwiching the reaction units 11 in the thickness direction. Bolts 14 are arranged at the four corners of the periphery of the electrolysis stack 10, penetrating the end plates 12, the reaction units 11, and the end plates 13 in the thickness direction. The reaction units 11 and the end plates 12 and 13 are fastened together by the bolts 14.

[0022] The electrolysis stack 10 includes a terminal plate 52 disposed between the end plate 12 and the reaction unit 11, and a terminal plate 53 disposed between the end plate 13 and the reaction unit 11. The reaction units 11 are connected in series between the terminal plates 52 and 53. The protruding portions of the terminal plates 52 and 53 function as terminals. It is of course possible to omit the terminal plates 52 and 53 and electrically connect the reaction units 11 to the end plates 12 and 13, thereby using the end plates 12 and 13 as terminals of the electrolysis stack 10.

[0023] Four spaces penetrating the electrolysis stack 10 in the thickness direction are formed at the periphery of the electrolysis stack 10. These four spaces function as a passage 15a through which gas enters the electrolysis stack 10 from the outside to a fuel chamber 33 (described later) of the reaction unit 11, a passage 15b through which gas exits the electrolysis stack 10 from the fuel chamber 33, a passage 15c through which gas enters the electrolysis stack 10 from the outside to an air chamber 35 (described later) of the reaction unit 11, and a passage 15d through which gas exits the electrolysis stack 10 from the air chamber 35.

[0024] FIG. 2 is an exploded schematic diagram of the electrolysis stack 10 cut along line II-II in FIG. 1, which passes through the passages 15a and 15b. FIG. 2 shows a schematic cross-sectional view along line II-II, in which components constituting one reaction unit 11 are separated in the thickness direction. The reaction unit 11 includes, in order in the thickness direction, an interconnector 16, an anode frame 17, a separator-equipped cell 47, and an air electrode frame 19. Note that the thickness of each part is exaggerated in FIG. 2. Holes (passages 15a, 15b, 15c, and 15d) penetrate the interconnector 16, the anode frame 17, the separator 30, and the air electrode frame 19. The separator 30 is hermetically joined to the surface 24a of the solid electrolyte layer 24 (described later) with a brazing material 31, avoiding the air electrode 29.

[0025] 3 is a schematic top view of a separator-equipped cell 47. The separator-equipped cell 47 includes an electrolysis cell 20 and a separator 30 disposed in the electrolysis cell 20. The electrolysis cell 20 will be described later.

[0026] The separator 30 is a substantially rectangular frame-shaped member provided with an opening 37 that is larger than the air electrode 29 (described later). The separator 30 can be made of stainless steel, for example.

[0027] The interconnectors 16 are disposed at both ends of the electrolysis cell 20 in the thickness direction. The interconnectors 16 are formed of conductive, substantially rectangular plate-like members. The interconnectors 16 electrically connect the reaction units 11 adjacent to each other in the thickness direction. Stainless steel is exemplified as a material for the interconnectors 16.

[0028] The fuel electrode frame 17 is a substantially rectangular frame-shaped member disposed between the interconnector 16 and the separator 30. Stainless steel is an example of the material for the fuel electrode frame 17. The fuel electrode frame 17 surrounds the electrolysis cell 20 and a current collector 32 provided in the center of the interconnector 16.

[0029] The current collector 32 electrically connects the fuel electrode 21 and the interconnector 16. An example of a material for the current collector 32 is a porous body made of a gas-permeable metal such as Ni. Inside the fuel electrode frame 17, a fuel chamber 33 is formed which is surrounded by the interconnector 16, the fuel electrode frame 17, and the separator 30.

[0030] The air electrode frame 19 is a substantially rectangular frame-shaped member disposed between the interconnector 16 and the separator 30. An example of the material of the air electrode frame 19 is an insulator such as mica. The air electrode frame 19 surrounds a current collector 34 provided in the center of the interconnector 16. The current collector 34 electrically connects the air electrode 29 and the interconnector 16. In this embodiment, the current collector 34 is formed integrally with the interconnector 16, but this is not limiting. It is of course possible for the current collector 34 to be a member separate from the interconnector 16.

[0031] An air chamber 35 is formed inside the air electrode frame 19 and is surrounded by the interconnector 16, the air electrode frame 19, and the separator 30. The separator 30 separates the fuel chamber 33 from the air chamber 35, preventing the fuel gas in the fuel chamber 33 and the oxidant gas (oxygen, air, etc.) in the air chamber 35 from mixing.

[0032] A hydrogen production device 60 including an electrolysis stack 10 and a hot module 61 will be described with reference to Fig. 4. Fig. 4 is a block diagram of the hydrogen production device 60. The hydrogen production device 60 is a device that produces hydrogen from water, and includes a hot module 61.

[0033] The hot module 61 includes the electrolysis stack 10, a vaporizer 62 that generates steam to be supplied to the electrolysis stack 10, a heat exchanger 63 that exchanges heat between the gas supplied to the electrolysis stack 10 and the gas generated by the electrolysis stack 10, and a heater 64 that heats the electrolysis stack 10. In the hot module 61, the electrolysis stack 10, the vaporizer 62, the heat exchanger 63, and the heater 64 are arranged inside a thermal insulator 65 to reduce heat radiation.

[0034] The vaporizer 62 includes a heat exchanger that exchanges heat with high-temperature gas containing oxygen produced by the electrolysis stack 10, and heats water to produce water vapor. The water vapor produced by the vaporizer 62 contains hydrogen, which reduces oxidation of the catalyst contained in the anode 21. The hydrogen-containing water vapor exchanges heat with hydrogen and oxygen produced by the electrolysis stack 10 in a heat exchanger 63, is heated to the operating temperature of the electrolysis stack 10 by a heater 64, and is supplied to the fuel chamber 33 of the electrolysis stack 10. The air exchanges heat with hydrogen and oxygen produced by the electrolysis stack 10 in the heat exchanger 63, is heated to the operating temperature of the electrolysis stack 10 by a heater 64, and is supplied to the air chamber 35 of the electrolysis stack 10.

[0035] Examples of the heat insulating material 65 include heat-resistant fibers such as ceramic wool, refractory ceramic fiber (RCF), and biosoluble fiber (AES), and a heat-resistant container made of heat-resistant fibers. The heat-resistant fibers fill gaps between the electrolysis stack 10, the vaporizer 62, the heat exchanger 63, and the heater 64. The condenser 66 is a device that cools the hydrogen gas, and liquefied water is supplied to the vaporizer 62 as raw water.

[0036] (Electrolytic cell) As shown in FIG. 2 , the electrolysis cell 20 includes an air electrode 29, an anode 21, and a solid electrolyte layer 24 disposed between the air electrode 29 and the anode 21. The electrolysis cell 20 of this embodiment includes a reaction prevention layer 25 between the solid electrolyte layer 24 and the air electrode 29, although the reaction prevention layer 25 may be omitted. Furthermore, in this embodiment, the air electrode 29 includes, in order from the side closest to the solid electrolyte layer 24, an air electrode functional layer 26 and an air electrode current collecting layer 27. The thickness of the electrolysis cell 20 is not particularly limited, but may be, for example, 300 μm to 3 mm. The shape of the electrolysis cell 20 viewed from above is not particularly limited, but examples include a square with sides measuring 1 to 10 cm, a rectangle with long sides measuring 5 to 30 cm and short sides measuring 3 to 15 cm, or a circle with a diameter of 10 cm. A plurality of electrolysis cells 20 are connected in series by interconnectors 16 to form an electrolysis stack 10.

[0037] The fuel electrode 21 is formed using nickel oxide and oxygen-ion conductive ceramic particles as materials. Nickel oxide (NiO) used as the material of the fuel electrode 21 is converted into nickel through a reduction process described below. The fuel electrode 21 of this embodiment is a porous, thin-plate-shaped sintered body composed of nickel and YSZ (yttria-stabilized zirconia). Examples of ceramic materials having oxygen ion conductivity include YSZ (yttria-stabilized zirconia), ScSZ (scandia-stabilized zirconia), (Gd,Ce)O2, i.e., GDC (gadolinium-doped ceria), (Sm,Ce)O2, i.e., SDC (samarium-doped ceria), and LaGaO3 (lanthanum gallate). The ceramic material contained in the fuel electrode 21 may be one type or two or more types. The thickness of the fuel electrode 21 is not particularly limited, but is, for example, 0.3 to 3 mm. In this embodiment, the fuel electrode 21 has the greatest thickness among the thicknesses of the components of the electrolysis cell 20, and functions as a support (support substrate, the member with the highest rigidity) for the electrolysis cell 20.

[0038] The anode 21 functions as the cathode of the electrolysis cell 20. The anode 21 includes, in order from the solid electrolyte layer 24 side, an anode functional layer 23 and an anode substrate layer 22. In this embodiment, the anode 21 includes, in order from the solid electrolyte layer 24 side, the anode functional layer 23 and the anode substrate layer 22, which has a porosity greater than that of the anode functional layer 23. This ensures the strength of the anode functional layer 23. The thickness of the anode substrate layer 22 is preferably greater than that of the anode functional layer 23. The porosity of the anode functional layer 23 is not particularly limited, but is, for example, preferably 30% or less, more preferably 25% or less, and preferably 5% or more, and more preferably 10% or more. The porosity of the anode substrate layer 22 is not particularly limited, but is, for example, preferably 50% or less, more preferably 40% or less, and preferably 10% or more, and more preferably 20% or more. The anode 21 may be formed of a single layer instead of the anode functional layer 23 and the anode substrate layer 22.

[0039] The anode substrate layer 22 is a porous, plate-shaped sintered body containing a transition metal and an oxygen ion conductive material. The anode substrate layer 22 may contain nickel (Ni) as the transition metal. The anode substrate layer 22 may contain, as the oxygen ion conductive material, a zirconia-based material such as yttria-stabilized zirconia (8YSZ, 10YSZ, etc.) or scandia-stabilized zirconia (ScSZ), a ceria-based material such as gadolinium-doped ceria (GDC:(Ce,Gd)O) or samarium-doped ceria (SDC:(Ce,Sm)O), or yttria (YO).

[0040] The thickness of the anode substrate layer 22 can be, for example, 0.2 mm to 5.0 mm. When the anode substrate layer 22 functions as a substrate, the thickness of the anode substrate layer 22 may be the largest among the components of the electrolysis cell 20. In the anode substrate layer 22, the volume ratio of Ni can be, for example, 20 to 50 volume %, and the volume ratio of the oxygen ion conductive material can be, for example, 30 to 60 volume %.

[0041] The anode functional layer 23 is disposed between the anode substrate layer 22 and the solid electrolyte layer 24. The anode functional layer 23 is a porous, sintered plate containing a transition metal and an oxygen ion conductive material. The anode functional layer 23 contains at least Ni as a transition metal. The anode functional layer 23 may further contain Fe or Cu as a transition metal. The anode functional layer 23 contains, as an oxygen ion conductive material, a zirconia-based material such as yttria-stabilized zirconia (8YSZ, 10YSZ, etc.) or scandia-stabilized zirconia (ScSZ), or a ceria-based material such as gadolinium-doped ceria (GDC:(Ce,Gd)O2) or samarium-doped ceria (SDC:(Ce,Sm)O2).

[0042] The thickness of the anode functional layer 23 can be, for example, 1.0 μm to 30 μm. In the anode functional layer 23, the volume ratio of Ni can be, for example, 30 to 60 volume %, and the volume ratio of the oxygen ion conductive material can be, for example, 40 to 70 volume %.

[0043] The solid electrolyte layer 24 is a dense, thin-plate-like sintered body. The solid electrolyte layer 24 is formed of a solid oxide such as YSZ (yttria-stabilized zirconia), ScSZ (scandia-stabilized zirconia), SDC (samarium-doped ceria), GDC (gadolinium-doped ceria), or a perovskite-type oxide. Examples of perovskite-type oxides include lanthanum gallate-based oxides having a perovskite-type structure. The porosity of the solid electrolyte layer 24 is not particularly limited, but is, for example, 0 to 10%. The thickness of the solid electrolyte layer 24 is not particularly limited, but is, for example, 0.5 to 30 μm.

[0044] In this embodiment, the solid electrolyte layer 24 is disposed between the anode 21 and the reaction prevention layer 25. The solid electrolyte layer 24 has a function of allowing oxygen ions generated in the cathode 29 to pass therethrough. The solid electrolyte layer 24 may contain zirconium (Zr), or the solid electrolyte layer 24 may contain Zr as zirconia (ZrO2). The solid electrolyte layer 24 may contain ZrO2 as a main component. The solid electrolyte layer 24 may also contain additives such as Y2O3 and / or Sc2O3 in addition to ZrO2. These additives function as stabilizers. In the solid electrolyte layer 24, the molar composition ratio of the stabilizer to ZrO2 (stabilizer:ZrO2) is preferably approximately 3:97 to 20:80. That is, examples of materials for the solid electrolyte layer 24 include yttria-stabilized zirconia such as 3YSZ, 8YSZ, and 10YSZ, and zirconia-based materials such as ScSZ.

[0045] The air electrode 29 is disposed on the reaction prevention layer 25. The air electrode 29 functions as the anode of the electrolysis cell 20. The air electrode 29 may contain, for example, a lanthanum-containing perovskite complex oxide as a main component. Examples of lanthanum-containing perovskite complex oxides include LSCF (lanthanum strontium cobalt ferrite), lanthanum manganite, lanthanum cobaltite, and lanthanum ferrite. The lanthanum-containing perovskite complex oxide may be doped with strontium, calcium, chromium, cobalt, iron, nickel, aluminum, or the like. The thickness of the air electrode 29 may be, for example, 5 μm to 300 μm.

[0046] The air electrode 29 contains a complex oxide having a perovskite structure. The composition of the complex oxide is expressed by the general formula ABO3. However, the ratio of A, B, and O is not required to be strictly 1:1:3. The ideal unit cell of a complex oxide having a perovskite structure expressed by the general formula ABO3 is a cube, with the A element located at the corner of the unit cell, the B element located at the body center of the unit cell, and the oxygen element located at the face center of the unit cell. In this disclosure, the corner of the unit cell where the A element is located is referred to as the "A site," and the body center of the unit cell where the B element is located is referred to as the "B site."

[0047] The A site preferably contains at least one of La and Sr atoms. The B site preferably contains at least one of Co and Fe atoms. Specific examples of such complex oxides, for example, in the case of the material of the air electrode 29, include materials such as LSCF (i.e., (La,Sr)(Co,Fe)O3), LSF (i.e., (La,Sr)FeO3), LSC (i.e., (La,Sr)CoO3), LNF (i.e., La(Ni,Fe)O3), and SSC (i.e., (Sm,Sr)CoO3). These complex oxides are substances that have both oxygen ion conductivity and electronic conductivity, and are also called mixed conductive materials. In this embodiment, the air electrode 29 is made of lanthanum strontium cobalt ferrite LSCF (La 0.6 Sr 0.4 Co 0.2 Fe 0.8 O3) is a porous, thin, fired body formed from a material containing

[0048] The air electrode 29 can contain a composite oxide as a "main component." The phrase "composition X contains substance Y as a "main component"" means that substance Y preferably accounts for 60 mass % or more, more preferably 70 mass % or more, and even more preferably 90 mass % or more of the entire composition X. The air electrode 29 may contain components other than the composite oxide. The material of the air electrode 29 may be a powder (for example, with an average particle size of about 0.1 μm to 5 μm) or a crushed material (for example, with an average particle size of about 5 μm to 500 μm), or may be a lump larger than the crushed material.

[0049] The cathode current collecting layer 27 contains a complex oxide having a perovskite structure represented by the general formula ABO3. Examples of such complex oxides include, but are not limited to, LSCF, LSF, LSC, LNF, and SSC. The cathode functional layer 26 may contain a component other than the complex oxide contained in the cathode current collecting layer 27. For example, the cathode functional layer 26 may be composited with the material of the solid electrolyte layer 24 (e.g., ceria or zirconia), which will be described later. The thickness of the cathode current collecting layer 27 is not particularly limited, but may be, for example, 5 to 300 μm. The thickness of the cathode functional layer 26 is not particularly limited, but may be, for example, 5 to 30 μm. The cathode functional layer 26 may not be provided, and the cathode functional layer 26 may not contain Ce. The porosity of the cathode current collecting layer 27 is not particularly limited, but may be, for example, 35 to 45%. The porosity of the cathode functional layer 26 is not particularly limited, but may be, for example, 35 to 45%. The electrical conductivity of the material that constitutes the air electrode current collecting layer 27 may be greater than the electrical conductivity of the material that constitutes the air electrode functional layer 26 .

[0050] Due to the difference in thermal expansion coefficients, the air electrode 29 may peel off from the solid electrolyte layer 24. To address this issue, a technique exists in which a composite material, in which an electrolyte is mixed with the air electrode 29, is provided between the air electrode 29 and the solid electrolyte layer 24. However, when a Zr-based material is used as the electrolyte material, the presence of Sr in the air electrode 29 can lead to the generation of SrZrO3 (SZO). In this case, the electrolyte material to be mixed is, for example, gadolinium-doped ceria (GDC) or samarium-doped ceria (SDC). Preferably, an intermediate layer containing a mixture of an electrolyte and a composite oxide can be disposed between the air electrode 29 and the solid electrolyte layer 24, and this intermediate layer serves as the air electrode functional layer 26. However, the air electrode 29 may include the air electrode current collecting layer 27 but not the air electrode functional layer 26. Depending on the actual usage environment, the air electrode 29 may include the air electrode functional layer 26 but not the air electrode current collecting layer 27.

[0051] When Sr (strontium) contained in the air electrode 29 diffuses toward the solid electrolyte layer 24 and reacts with Zr (zirconium) contained in the solid electrolyte layer 24, a highly resistive substance called SrZrO3 (hereinafter also referred to as "SZO") is generated. If SZO is generated in a layer in the region between the air electrode 29 and the solid electrolyte layer 24, electrolysis performance deteriorates. To suppress the generation of SZO, it is preferable to dispose a reaction prevention layer 25 containing, for example, gadolinium-doped ceria (GDC) between the air electrode 29 and the solid electrolyte layer 24. This effectively suppresses the reaction of Sr diffused from the air electrode 29 with Zr contained in the solid electrolyte layer 24 to generate SZO. However, the electrolysis cell 20 does not necessarily have to include the reaction prevention layer 25. Examples of materials for the reaction prevention layer 25 include ceria-based materials containing cerium (Ce) and rare earth metal oxides dissolved in Ce. The reaction prevention layer 25 is preferably, but not limited to, a dense, thin-plate-shaped sintered body made of ceria. Examples of ceria include, but are not limited to, GDC (gadolinium-doped ceria) and SDC (samarium-doped ceria).

[0052] In this embodiment, the reaction prevention layer 25 is disposed between the solid electrolyte layer 24 and the air electrode 29. The reaction prevention layer 25 has the function of preventing a high-resistance layer from being formed between the solid electrolyte layer 24 and the air electrode 29. The thickness of the reaction prevention layer 25 can be set to, for example, 3 μm to 20 μm.

[0053] In this embodiment, the periphery of the air electrode 29 has an uneven portion V in which unevenness is repeated alternately over a part or the entire periphery.

[0054] Fig. 5 is a schematic diagram illustrating the uneven portion V. In Fig. 5, the periphery of the air electrode 29 has the uneven portion V in part. In this embodiment, the uneven portion V exists on at least one side of the air electrode 29, and there are sides where the uneven portion V exists in two or more places and sides where the uneven portion V exists in one place.

[0055] In Figure 5, the oxygen-containing gas flows from the left side of the page to the right side. This flow is in a fixed direction. In this embodiment, the uneven portion V is present on at least one side upstream of the flow of the oxygen-containing gas. This can efficiently prevent cracks from occurring in the upstream air electrode 29, where the temperature is prone to change.

[0056] FIG. 6 is a schematic diagram illustrating the shape of the uneven portion V. In this specification, the apex T of the uneven portion V refers to a portion that is far from the center of the air electrode 29. Furthermore, the bottom B of the uneven portion V refers to a portion that is close to the center of the air electrode 29. In the uneven portion V, both the apex T and the bottom B are arc-shaped. The ratio (R1 / R2) of the arc radius R1 of the apex T to the arc radius R2 of the bottom B is 3.0 or more. The inventors have found that there is a strong correlation between the occurrence of cracks in the air electrode 29 and the ratio (R1 / R2) of the arc radius R1 of the apex T to the arc radius R2 of the bottom B. The ratio (R1 / R2) is not particularly limited as long as it is 3.0 or more, but the upper limit is preferably 20 or less, more preferably 18 or less, and even more preferably 17 or less. Specifically, the ratio (R1 / R2) increases as R1 increases (the convexity decreases), as R2 decreases (if there are extremely concave portions), or as a combination of these. The pitch P of the concave-convex portion V refers to the distance between adjacent bottoms B. The pitch P of the concave-convex portion is not particularly limited, but may be, for example, 0.2 to 2 mm. The height difference H refers to the height difference from the point on the top T that is farthest from the center to the point on the bottom B that is closest to the center. The height difference H is not particularly limited, but is, for example, preferably 0.1 to 4, more preferably 0.2 to 3, and even more preferably 0.25 to 2.5.

[0057] In this SOEC electrolysis cell 20, water vapor is supplied to the fuel electrode 21, and a gas containing oxygen is supplied to the air electrode 29. At the same time, a current is passed between the fuel electrode 21 and the air electrode 29, causing the chemical reactions shown in the following formulas (1) and (2). As a result, hydrogen is generated from the fuel electrode 21, and oxygen is generated from the air electrode 29. H2O+2e - →H2+O 2- (At: Fuel electrode 21) …(1) O 2- →(1 / 2)·O2+2e - (At: Air electrode 29) ... (2)

[0058] In this SOEC electrolysis cell 20, conductive connecting members (interconnectors 16) for collecting current are usually joined and fixed to each of the fuel electrode 21 and the air electrode 29 with a bonding agent, and a potential difference is applied via each interconnector 16 to allow current to flow. Then, hydrogen gas generated from the fuel electrode 21 is collected.

[0059] The fuel electrode 21 is supplied with a fuel gas containing water vapor at a rate of, for example, 90 to 140 liters / (min cm 2 ) and may be used at a flow rate of 100 to 130 liters / (min cm 2 ) may be supplied at a flow rate of 1000 kJ / s. In the case of co-electrolysis, a gas containing water vapor and CO2 may be supplied as the fuel gas. In a stack in which cells are stacked in multiple stages, the amount of fuel gas input by blowers, pumps, etc. naturally increases in proportion to the number of cells stacked.

[0060] The air electrode 29 is supplied with an oxygen-containing gas at a rate of, for example, 20 to 60 liters / (min cm 2 ) and may be used at a flow rate of 30 to 50 L / (min cm 2 ) may be supplied and used. As the oxygen-containing gas, oxygen gas or air may be used. In a stack in which cells are stacked in multiple stages, the amount of gas introduced into the air electrode side by a blower, pump, etc. naturally increases in proportion to the number of cells stacked.

[0061] The volume of the air chamber 35 facing the air electrode 29 is not particularly limited, but is preferably 8 cm 3 ~13cm 3 Preferably, 9cm 3 ~11cm 3Here, the volume of the air chamber 35 facing the air electrode 29 refers to the volume per cell, excluding the space occupied by current collecting members and the like.

[0062] (Manufacturing method) Next, an example of a method for manufacturing the electrolytic cell 20 will be described. Various conditions such as the materials, particle size, temperature, and application method described below can be changed as appropriate. In the following description, the term "molded body" refers to the state before firing.

[0063] (Preparation of green sheet for fuel electrode substrate layer) Organic beads as a pore former, butyral resin, DOP as a plasticizer, a dispersant, and a mixed solvent of toluene and ethanol are added to a mixed powder of NiO powder and YSZ powder, and the mixture is mixed in a ball mill to prepare a slurry. The organic beads are spherical particles formed from a polymer such as polymethyl methacrylate or polystyrene. The obtained slurry is thinned by a doctor blade method to prepare a green sheet for an anode substrate layer having a predetermined thickness (e.g., 200 μm to 300 μm). The mixing ratio of NiO powder and YSZ powder when preparing the anode green sheet can be appropriately set as long as the performance is satisfied. The mixing ratio of NiO powder and YSZ powder may be, for example, 20 to 50 volume % NiO and 30 to 60 volume % YSZ.

[0064] (Preparation of green sheet for fuel electrode functional layer) A butyral resin, DOP (a plasticizer), a dispersant, and a mixed solvent of toluene and ethanol are added to a mixed powder of NiO powder and YSZ powder, and the mixture is mixed in a ball mill to prepare a slurry. The resulting slurry is thinned by a doctor blade method to prepare a green sheet for an anode functional layer having a predetermined thickness (for example, 5 μm to 50 μm). The mixing ratio of the NiO powder and the YSZ powder when preparing the green sheet for an anode functional layer can be appropriately set as long as the performance is satisfied. The mixing ratio of the NiO powder and the YSZ powder may be, for example, 30 to 60 volume % NiO and 40 to 70 volume % YSZ.

[0065] (Preparation of green sheets for solid electrolyte layers) Butyral resin, DOP (a plasticizer), a dispersant, and a mixed solvent of toluene and ethanol are added to the YSZ powder and mixed in a ball mill to prepare a slurry. The resulting slurry is thinned by a doctor blade method to produce a green sheet for the solid electrolyte layer with a predetermined thickness (e.g., 10 μm).

[0066] (Fabrication of a Laminate of Solid Electrolyte Layer 24, Anode Functional Layer 23, and Anode Substrate Layer 22) The green sheet for the anode substrate layer, the green sheet for the anode functional layer, and the green sheet for the solid electrolyte layer are attached together and degreased at a predetermined temperature (e.g., about 280°C). The laminate of the degreased green sheets is then fired at a predetermined temperature (e.g., about 1350°C). This results in a laminate of the solid electrolyte layer 24, the anode functional layer 23, and the anode substrate layer 22. The maximum temperature during firing is preferably, for example, 1500°C or less, more preferably 1450°C or less, and even more preferably 1400°C or less. The maximum temperature during firing is preferably, for example, 1100°C or more, more preferably 1200°C or more, and even more preferably 1300°C or more. The holding time at high temperature is, for example, preferably 420 minutes or less, more preferably 360 minutes or less, and even more preferably 300 minutes or less. Furthermore, the retention time at high temperature is, for example, preferably 30 minutes or more, more preferably 40 minutes or more, and even more preferably 50 minutes or more. For example, the temperature increase rate is preferably 3°C / min or less, more preferably 2°C / min or less, even more preferably 1.5°C / min or less, and even more preferably 1.3°C / min or less. For example, the temperature increase rate is preferably 0.3°C / min or more, more preferably 0.5°C / min or more, even more preferably 0.8°C / min or more, and even more preferably 1.0°C / min or more. For example, the temperature decrease rate is preferably 2°C / min or less, more preferably 1.5°C / min or less, and even more preferably 1.3°C / min or less. For example, the temperature decrease rate is preferably 0.3°C / min or more, more preferably 0.5°C / min or more, and even more preferably 0.8°C / min or more.

[0067] The cell manufacturing method is not limited to this method, and the following method may also be used. A slurry is prepared by adding polyvinyl alcohol (PVA) as a binder to a mixture of NiO powder and YSZ powder. This slurry is then dried and granulated using a spray dryer, and a green body for the anode 21 is formed by die press molding. Next, water and a binder are added to the YSZ powder, and the mixture is mixed in a ball mill for 24 hours to prepare a slurry. This slurry is then applied and molded onto the green body for the anode 21, thereby forming a green body for the solid electrolyte layer 24. This green body stack is then co-sintered in air in an electric furnace (in an oxygen-containing atmosphere) at, for example, 1350°C, to form a stack of the anode 21 and the solid electrolyte layer 24. A tape lamination method, printing method, or the like may also be used to form a film that will later become the solid electrolyte layer 24 on the anode 21.

[0068] (Formation of reaction prevention layer 25) Next, the reaction prevention layer 25 is formed. Specifically, polyvinyl alcohol as an organic binder and butyl carbitol as an organic solvent are added to and mixed with GDC powder, and the viscosity is adjusted to prepare a paste for the reaction prevention layer. The obtained paste for the reaction prevention layer is applied by, for example, screen printing to the surface of the solid electrolyte layer 24 side of the laminate of the solid electrolyte layer 24 and the anode 21, and then fired at, for example, 1180°C. This forms the reaction prevention layer 25, and a laminate of the anode 21, solid electrolyte layer 24, and reaction prevention layer 25 (hereinafter referred to as the "intermediate laminate") is produced.

[0069] (Formation of the air electrode functional layer 26) Next, the air electrode functional layer 26 is formed. First, LSCF powder and GDC powder are mixed in a mass ratio of 1:1, and polyvinyl alcohol as an organic binder and butyl carbitol as an organic solvent are mixed. The viscosity is adjusted to prepare a paste for the air electrode functional layer. Next, the prepared paste for the air electrode functional layer is applied to the surface of the intermediate laminate on the side of the reaction prevention layer 25 by, for example, screen printing, and then dried. At this time, a screen mask is used that forms an uneven portion V around the periphery of the air electrode 29. Examples of the screen mask include a mesh mask and a metal mask.

[0070] (Formation of Air Electrode Current Collecting Layer 27) Next, the air electrode current collecting layer 27 is formed. First, LSCF powder, polyvinyl alcohol as an organic binder, butyl carbitol as an organic solvent, and organic beads as a pore-forming material are mixed, and the viscosity is adjusted to prepare an air electrode current collecting layer paste. Next, the prepared air electrode current collecting layer paste is applied to the surface of the intermediate laminate on the air electrode functional layer 26 side by, for example, screen printing, and then dried. At this time, a screen mask is used that forms an uneven portion V on the periphery of the air electrode 29. Examples of the screen mask include a mesh mask and a metal mask. Then, the intermediate laminate on which the current collecting layer paste is applied is fired at a predetermined firing temperature (for example, 1100°C). This firing process forms the air electrode current collecting layer 27, and a laminate of the anode 21, the solid electrolyte layer 24, the reaction prevention layer 25, the air electrode functional layer 26, and the air electrode current collecting layer 27, i.e., the single electrolysis cell 20, is produced.

[0071] Thereafter, a reduction step is performed to reduce the fuel electrode 21 (i.e., reduce NiO contained in the fuel electrode 21 to Ni) to enable the electrolysis cell 20 to operate for hydrogen production. The reduction step is achieved, for example, by exposing the fuel electrode 21 to a hydrogen atmosphere at a predetermined temperature for a predetermined time. The reducing gas used in the reduction step is not limited to hydrogen, but may be other gases such as methane gas, and the concentration of the reducing gas is also not limited. A reducing gas with a reducing agent concentration of less than 100% by volume may contain, for example, nitrogen gas in addition to hydrogen gas.

[0072] (Explanation of effect) As described above, the periphery of the air electrode 29 in the above configuration has an uneven portion V with alternating concave and convex portions. In the uneven portion V, both the top portion T and the bottom portion B are arc-shaped. The ratio (R1 / R2) of the arc radius R1 of the top portion T to the arc radius R2 of the bottom portion B is 3.0 or greater. When an SOEC is operated in a typical environment after reaching thermal neutrality, cracks rarely occur on the periphery of the air electrode. However, before reaching thermal neutrality, such as during startup of an SOEC, the electrolysis cell 20 operates in a harsh environment, which may cause cracks on the periphery of the air electrode 29. In other words, shrinkage due to a temperature drop generally occurs on the periphery of the air electrode 29, generating stress in the air electrode 29 and potentially causing cracks on the air electrode 29. However, because the air electrode 29 of the above configuration has the uneven portion V as described above, stress on the air electrode 29 is dispersed, suppressing stress concentration and thereby suppressing the occurrence of cracks in the air electrode 29. As a result, peeling of the air electrode 29 due to the occurrence of cracks in the air electrode 29 can be suppressed. Furthermore, the hot module 61 including the air electrode 29 of the above configuration has a heat source such as the heater 64 or the heat exchanger 63, and can therefore increase the temperature of the gas supplied to the electrolysis stack 10 and the electrolysis cell 20, thereby effectively suppressing the occurrence of cracks in the air electrode 29 when the temperature drops.

[0073] A test that confirmed that the occurrence of cracks in the air electrode 29 is suppressed by the air electrode 29 having the above configuration will be described below.

[0074] (test) In this test, for the SOEC (electrolysis cell 20) according to the above embodiment, multiple types of test specimens (sintered bodies) were used, each of which had different combinations of the material of the cathode current collecting layer 27, the height difference H of the unevenness V formed on the periphery of the cathode current collecting layer 27, the arc radius R1 of the top T, and the arc radius R2 of the bottom B. Specifically, as shown in Table 1, six levels were prepared, and 10 test specimens were produced for each level. The values ​​of H, R1, and R2 in Table 1 each represent an average value. In the evaluation results in parentheses, the denominator indicates the total number of test specimens, and the numerator indicates the number of test specimens that had cracks.

[0075] In these test samples, the thickness of the air electrode functional layer 26 was 5 to 30 μm, and the thickness of the air electrode current collecting layer 27 was 80 to 300 μm. The pitch P of the irregularities was 0.2 to 2 mm. The height difference H was 0.05 to 1 mm. The porosity of the air electrode functional layer 26 was 35 to 45%. The porosity of each layer was adjusted by the particle size of the powder in the slurry and the amount of pore-forming material added. The co-firing temperature of the air electrode 29 (air electrode functional layer 26 and air electrode current collecting layer 27) was adjusted within a range of 900 to 1100°C. The co-firing time was adjusted within a range of 1 to 10 hours. The reduction treatment temperature was adjusted within a range of 800 to 1000°C. The reduction treatment time was adjusted within a range of 1 to 10 hours.

[0076] The following thermal cycle electrolysis test was then performed on these test specimens. Specifically, for each test specimen, with a reducing fuel gas flowing through the anode 21, the ambient temperature was increased from room temperature (25°C) to 750°C over 8 hours, and then decreased from 750°C to room temperature (25°C) over 2 hours. This series of steps was repeated 10 times. The test specimens that underwent this thermal cycle electrolysis test were checked for the presence or absence of cracks on the periphery of the cathode current collecting layer 27 (i.e., the portion of the cathode current collecting layer 27 where irregularities were formed). This check was performed by visual inspection and microscopic observation.

[0077] (result) The evaluation results are shown in Table 1.

[0078] [Table 1]

[0079] This thermal cycle electrolysis test is a severe test in terms of thermal stress, but as shown in Table 1, when R1 / R2 is 3.0 or more, no cracks were observed, although the reason is unclear. On the other hand, when R1 / R2 is less than 3.0, cracks were observed. The inventors have separately confirmed that when the electrolytic cell 20 of this embodiment is used under typical usage conditions and environments, when R1 / R2 is 3.0 or more, no cracks occur on the periphery of the air electrode current collecting layer 27.

[0080] The present invention is not limited to the above-described embodiments and can be realized in various configurations without departing from the spirit of the present invention. For example, the technical features in the embodiments corresponding to the technical features in each aspect described in the Summary of the Invention section can be appropriately replaced or combined to solve some or all of the above-described problems or achieve some or all of the above-described effects. Furthermore, if a technical feature is not described as essential in this specification, it can be appropriately deleted.

[0081] The electrolysis cell 20 only needs to have the fuel electrode 21, the solid electrolyte layer 24, and the air electrode 29, and the presence or absence of other components, as well as the shape, material, dimensions, etc. of each component can be modified. For example, the configuration of the electrolysis cell 20 may be modified as follows. (1) The shape of the electrolysis cell 20 may be, for example, an anode-supported type, a flat type, a cylindrical type, a flat type, a vertically striped type, a horizontally striped type, a type for a single-end-supported stack, a type for a double-end-supported stack, etc. The cross section of the cell may also be elliptical. (2) The configurations listed as different forms can be combined with each other. (3) In the above embodiment, the periphery of the air electrode 29 has a concave-convex portion V in part. In the above embodiment, the concave-convex portion V is present on at least one side of the air electrode 29, with the concave-convex portion V being present in one or more locations on one side. However, this is not limited to this. The periphery of the air electrode 29 may have the concave-convex portion V along the entire periphery ( FIG. 7 ), or on two opposing sides ( FIG. 8 ), or may have the concave-convex portion V in three or more locations on one side, or may have the concave-convex portion V on a side downstream of the flow of the oxygen-containing gas, or may have the concave-convex portion V on a side parallel to the flow of the oxygen-containing gas.

[0082] Furthermore, in the above embodiment, the air electrode 29 has the unevenness V on the peripheries of both the air electrode functional layer 26 and the air electrode current collecting layer 27. However, the unevenness V may also be on the periphery of one of the air electrode functional layer 26 or the air electrode current collecting layer 27. If the air electrode current collecting layer 27 is larger than the air electrode functional layer 26 in a planar view, the unevenness V of the air electrode functional layer 26 may be omitted, and the unevenness V may only be on the periphery of the air electrode current collecting layer 27. On the other hand, if the air electrode functional layer 26 is larger than the air electrode current collecting layer 27 in a planar view, the unevenness V of the air electrode current collecting layer 27 may be omitted, and the unevenness V may only be on the periphery of the air electrode functional layer 26. In the above embodiment, the air electrode 29 has the air electrode functional layer 26 and the air electrode current collecting layer 27. However, this is not limited thereto, and the air electrode 29 may be formed of a single layer. Furthermore, in the above embodiment, the air electrode current collecting layer 27 is in contact only with the upper surface of the air electrode functional layer 26, but this is not limiting, and the air electrode current collecting layer 27 may cover the upper and side surfaces of the air electrode functional layer 26. In this case, the uneven portion V of the air electrode functional layer 26 may be omitted, and the uneven portion V may be formed only on the periphery of the air electrode current collecting layer 27. [Explanation of symbols]

[0083] 10...electrolysis stack, 11...reaction unit, 12, 13...end plate, 14...bolt, 15a, 15b, 15c, 15d...passage, 16...interconnector, 17...fuel electrode frame, 19...air electrode frame, 20...electrolysis cell, 21...fuel electrode, 22...fuel electrode substrate layer, 23...fuel electrode functional layer, 24...solid electrolyte layer, 24a...surface, 25...reaction prevention layer, 26...air electrode functional layer, 27...air electrode current collecting layer, 29...air electrode 30...Separator, 31...Brazing material, 32...Current collector, 33...Fuel chamber, 34...Current collector, 35...Air chamber, 37...Opening, 47...Cell with separator, 52, 53...Terminal plate, 60...Hydrogen production device, 61...Hot module, 62...Vaporizer, 63...Heat exchanger, 64...Heater, 65...Insulating material, 66...Condenser, B...Bottom, H...Height difference, P...Pitch, R1...Arc radius, R2...Arc radius, T...Top, V...Uneven portion

Claims

1. an air electrode; a fuel electrode; a solid electrolyte layer disposed between the air electrode and the fuel electrode; Equipped with The periphery of the air electrode has an uneven portion in which unevenness alternates over a part or the entire periphery, In the concave-convex portion, both the top and bottom are arc-shaped, a ratio (R1 / R2) of the arc radius R1 of the top portion to the arc radius R2 of the bottom portion is 3.0 or more; A fuel gas containing water vapor is supplied to the fuel electrode, The temperature drops from the start of operation until it reaches the thermal neutral point. Solid oxide electrolysis cell.

2. 2. The solid oxide electrolysis cell according to claim 1, The uneven portion is present on at least one side of the air electrode. Solid oxide electrolysis cell.

3. 3. The solid oxide electrolysis cell according to claim 2, The uneven portion is present at two or more locations on the one side. Solid oxide electrolysis cell.

4. The solid oxide electrolysis cell according to claim 1 or 2, The uneven portion is present on at least one side on the upstream side with respect to the flow of the oxygen-containing gas. Solid oxide electrolysis cell.

5. The solid oxide electrolysis cell according to claim 1 or 2, The fuel electrode is supplied with a fuel gas containing water vapor at a rate of 100 to 130 liters / min.cm. ２ ) is supplied and used at a flow rate of Solid oxide electrolysis cell.

6. The solid oxide electrolysis cell according to claim 1 or 2, The air electrode is supplied with a gas containing oxygen at a rate of 30 to 50 liters / min.cm. ２ ) is supplied and used at a flow rate of Solid oxide electrolysis cell.

7. The solid oxide electrolysis cell according to claim 1 or 2, The volume of the air chamber facing the air electrode is 9 cm ３ ~11cm ３ That is, Solid oxide electrolysis cell.

8. The solid oxide electrolysis cell according to claim 1 or 2; and a separator having an opening in the center and disposed on the solid electrolyte layer; Cell with separator.

9. An electrolysis stack comprising a plurality of solid oxide electrolysis cells according to claim 1 or 2 stacked one on top of the other.

10. 10. The electrolytic stack of claim 9; a vaporizer that generates water vapor that is supplied to the electrolysis stack; a heat exchanger that exchanges heat with the gas supplied to the electrolysis stack; a heater for heating the electrolysis stack; a thermal insulator in which the electrolysis stack, the vaporizer, the heat exchanger, and the heater are disposed, Hot module.

11. A hydrogen production device comprising the hot module according to claim 10.

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