Fuel cell block and fuel cell system
The fuel cell block design addresses stress-induced short circuits and effective area reduction in thin-film SOFCs by using a plate and frame structure with optimized electrical connections, achieving high-density fuel cell unit arrangement and reduced parasitic resistance.
Patent Information
- Application Number
- JP2024060339
- Authority / Receiving Office
- JP · JP
- Patent Type
- Applications
- Current Assignee / Owner
- Filing Date
- 2024-04-03
- Publication Date
- 2025-10-16
AI Technical Summary
Thin-film SOFCs face issues with non-uniform pressure causing stress concentration and cracks in the solid electrolyte membrane, leading to short circuits between the anode and cathode electrodes, and reduced effective power generation area due to the use of intermediate substrates.
A fuel cell block design with a first and second plate member, a frame member, and fuel cell units arranged to minimize stress concentration, allowing high-density arrangement and efficient electrical connection through lead-out portions and current collecting wirings, reducing parasitic resistance.
The design suppresses a decrease in the effective power generation area and enables high-density arrangement of fuel cell units, enhancing power generation capacity and reducing parasitic resistance.
Smart Images

Figure 2025157956000001_ABST
Abstract
Description
[Technical Field]
[0001] The present invention relates to a fuel cell block having a plurality of fuel cell units, and a fuel cell system having a plurality of fuel cell blocks. [Background technology]
[0002] Patent Documents 1, 2 and 3 disclose techniques using solid oxide fuel cells (SOFCs).
[0003] Patent Document 1 discloses a stacked SOFC. In the stacked SOFC, a fuel gas flow path and an oxidant gas flow path are formed in each layer. In the stacking direction, fuel cells, fuel gas flow paths, separators which are conductors, and oxidant gas flow paths are repeatedly stacked in this order.
[0004] The generated electricity is extracted vertically via a current collector connected to the anode electrode and a current collector connected to the cathode electrode. The fuel cell units are connected in series via separators. Electrical power is output from the fuel cell unit located at the bottom and the fuel cell unit located at the top to the outside of the stack structure.
[0005] In response to this, Patent Document 2 discloses a stack structure equipped with a thin-film SOFC. Research and development of thin-film SOFCs has been actively carried out in recent years. A feature of thin-film SOFCs is that the thickness of the solid electrolyte membrane, yttria-stabilized zirconia (YSZ), is extremely thin, at 1 μm or less. The resistance of the electrolyte membrane is reduced by thinning the membrane, so the power generation capacity can be increased to several W / cm. 2 (∝A / cm 2 ) will improve.
[0006] Usually, a thin-film SOFC is formed on some kind of support. In Patent Document 2, an anode electrode film, a YSZ film, and a cathode electrode film are formed in this order on a porous insulating substrate (anodic alumina film). The planar size of the porous insulating substrate is several cm 2 Therefore, in Patent Document 2, multiple fuel cell units are connected in parallel and mounted on an intermediate substrate, and these intermediate substrates are stacked vertically, and multiple parallel-connected fuel cell units are connected in series to obtain high output.
[0007] In Patent Document 3, a stack structure is constructed by connecting multiple fuel cells in series or in parallel using intermediate substrates, stacking these intermediate substrates vertically, and connecting multiple fuel cells in series or in parallel, which further increases the output voltage and reduces ohmic loss caused by parasitic resistance within the stack structure. [Prior art documents] [Patent documents]
[0008] [Patent Document 1] Japanese Patent Publication No. 2022-66744 [Patent Document 2] Japanese Patent Application Publication No. 2023-167722 [Patent Document 3] Japanese Patent Publication No. 2023-155085 Summary of the Invention [Problem to be solved by the invention]
[0009] For example, in a thin-film SOFC, the 2 High power generation efficiency and low temperature operation, for example, at 500°C, are possible. However, there are problems inherent to thin-film SOFCs.
[0010] The first problem is the difficulty of extracting the cathode electrode using a current collector, as disclosed in Patent Document 1. An anode electrode is provided directly below the cathode electrode, with a solid electrolyte membrane interposed between them. When the current collector is pressed against the cathode electrode, the pressure is not uniform, and stress concentration causes cracks in the solid electrolyte membrane. As a result, a short circuit occurs between the anode electrode and the cathode electrode.
[0011] Even if there are no problems in the early stages immediately after manufacture, there is a problem that short-circuit defects can be induced over time due to residual stress and thermal stress caused by temperature cycles between room temperature and high temperatures during operation.
[0012] The second problem is that porous insulating substrates have structural defects at a certain density (several / cm 2 Therefore, from the viewpoint of yield, such as preventing short circuits between the anode and cathode electrodes, there is an upper limit to the size that can be used for the porous insulating substrate.
[0013] Therefore, as disclosed in Patent Documents 2 and 3, it is necessary to use an intermediate substrate to increase the number of small-area fuel cells, but arranging the fuel cells requires clearance between the bonding area and its surroundings, and also requires wiring areas for electrically connecting to the anode and cathode electrodes. Therefore, Patent Documents 2 and 3 have the problem of reducing the effective area available for power generation, which reduces power generation capacity.
[0014] The main objective of the present application is to provide a fuel cell block that can suppress a decrease in the effective area available for power generation and that allows multiple fuel cell units to be arranged at high density, and a fuel cell system that includes multiple fuel cell blocks, as well as fuel cell units for realizing such a fuel cell block and fuel cell system.
[0015] Other objects and novel features will become apparent from the description of this specification and the accompanying drawings. [Means for solving the problem]
[0016] A fuel cell block in one embodiment includes a first plate member, a second plate member arranged to face the first plate member, a frame member sandwiched between the first plate member and the second plate member, and a plurality of fuel cell units arranged in a gas container surrounded by the first plate member, the second plate member, and the frame member. The fuel cell units have a laminated structure consisting of a first electrode film, a second electrode film, and a solid electrolyte film formed between the first electrode film and the second electrode film on a porous insulating substrate, the fuel cell units have a rectangular shape when viewed from a plane in a direction in which the first electrode film, the electrolyte film, and the second electrode film are laminated, a portion of the first electrode film located on one long side of the fuel cell units forms a first lead-out portion for electrical conduction with the outside of the fuel cell, and a portion of the second electrode film located on the other long side of the fuel cell units forms a second lead-out portion for electrical conduction with the outside of the fuel cell, and the plurality of fuel cell units are arranged in a gas container surrounded by the first plate member, the second plate member, and the frame member. The number of fuel cells includes a plurality of first fuel cells in which the first drawer portion is located on the first plate member side and the second drawer portion is located on the second plate member side, and a plurality of second fuel cells in which the second drawer portion is located on the first plate member side and the first drawer portion is located on the second plate member side, and the first fuel cells and the second fuel cells are repeatedly arranged side by side so that the first electrode film of the first fuel cells faces the first electrode film of the second fuel cells and the porous insulating substrate of the first fuel cells faces the porous insulating substrate of the second fuel cells. [Effects of the Invention]
[0017] According to one embodiment, it is possible to provide a fuel cell block that can suppress a decrease in the effective area available for power generation and that can densely arrange multiple fuel cell units, and a fuel cell system that includes multiple fuel cell blocks. It is also possible to provide fuel cell units for realizing such a fuel cell block and fuel cell system. [Brief explanation of the drawings]
[0018] [Figure 1] 1 is a plan view showing a fuel cell according to a first embodiment. [Figure 2] 1 is a cross-sectional view showing a fuel cell according to a first embodiment. [Figure 3] 1 is a cross-sectional view showing a fuel cell according to a first embodiment. [Figure 4] 1 is a plan view showing a fuel cell block according to a first embodiment. FIG. [Figure 5] 1 is a cross-sectional view showing a fuel cell block according to a first embodiment. [Figure 6] 1 is a cross-sectional view showing a fuel cell block according to a first embodiment. [Figure 7] 1 is a cross-sectional view showing a fuel cell block according to a first embodiment. [Figure 8] 1 is a cross-sectional view showing a fuel cell block according to a first embodiment. [Figure 9] 1 is a plan view showing a fuel cell block according to a first embodiment. FIG. [Figure 10] 1 is a front view showing a fuel cell block according to a first embodiment. [Figure 11] 2 is a right side view showing the fuel cell block according to the first embodiment. FIG. [Figure 12] 1 is a right side view showing a fuel cell system according to a first embodiment. [Figure 13] 1 is a right side view showing a fuel cell system according to a first embodiment. [Figure 14] 1 is a plan view showing a fuel cell system according to a first embodiment. [Figure 15] 1 is a plan view showing a fuel cell system according to a first embodiment. DETAILED DESCRIPTION OF THE INVENTION
[0019] Hereinafter, embodiments will be described in detail with reference to the drawings. In all drawings for explaining the embodiments, components having the same functions are designated by the same reference numerals, and repeated explanations thereof will be omitted. In the following embodiments, explanations of the same or similar parts will not be repeated unless particularly necessary.
[0020] Furthermore, the X direction, Y direction, and Z direction described in this application intersect with each other and are perpendicular to each other.
[0021] (Embodiment 1) <Fuel cell structure> A fuel cell 100 according to a first embodiment will be described below with reference to Figs. 1 to 3. The fuel cell 100 is a thin-film SOFC. Fig. 1 shows a plan view of the fuel cell 100. Fig. 2 is a cross-sectional view taken along line AA shown in Fig. 1. Fig. 3 is a cross-sectional view taken along line BB shown in Fig. 1.
[0022] As shown in Figures 1 to 3, the fuel cell 100 comprises a porous insulating substrate 11, a second electrode film (anode electrode) 12, a first electrode film (cathode electrode) 14, and a solid electrolyte membrane 13 formed between the second electrode film 12 and the first electrode film 14.
[0023] The porous insulating substrate 11 is an insulating substrate. The porous insulating substrate 11 includes, for example, anodized aluminum, and is formed by anodizing aluminum to form a porous coating. The porous insulating substrate 11 may also be a porous glass substrate or may be made of a track-etched polymer.
[0024] The second electrode film 12 is formed on the porous insulating substrate 11. The second electrode film 12 is, for example, a metal film such as a platinum (Pt) film or a nickel (Ni) film, a composite film of platinum or nickel and yttria-stabilized zirconia (YSZ), or a laminate film in which these are appropriately laminated. The thickness of the second electrode film 12 is, for example, 50 nm or more and 50 μm or less.
[0025] The electrolyte membrane 13 is formed on the second electrode film 12. The electrolyte membrane 13 is a stabilized zirconia film to which a rare earth element is added. When the rare earth element is Y, the electrolyte membrane 13 is made of yttria-stabilized zirconia (YSZ). The thickness of the electrolyte membrane 13 is, for example, 10 nm or more and 1 μm or less.
[0026] The first electrode film 14 is formed on the electrolyte membrane 13. The first electrode film 14 is, for example, a metal film such as a nickel film or a La film. 0.5 Sr 0.5 CoO 3-δ The first electrode film 14 is an oxide electrode material such as a (LSC) film, or a laminated film in which these are appropriately laminated. The thickness of the first electrode film 14 is, for example, 50 nm or more and 50 μm or less.
[0027] The porous insulating substrate 11, the second electrode film 12, and the first electrode film 14 are gas permeable. The electrolyte film 13 is not gas permeable, but is permeable to hydrogen ions (H + ) or oxygen ions (O - ) permeates. An oxidant gas and a fuel gas are used in the fuel cell 100. The oxidant gas is, for example, air, and the fuel gas is, for example, hydrogen (H2).
[0028] Oxygen (O2) contained in the oxidant gas enters the fuel cell 100, receives electrons at the first electrode film 14, and becomes oxygen ions. The oxygen ions move through the electrolyte membrane 13, release electrons at the second electrode film 12, and react with hydrogen (H2) to become water (H2O). As the oxygen ions pass through the fuel cell 100, a current is generated in the fuel cell 100.
[0029] As shown in FIG. 1, the fuel cell 100 has a rectangular shape when viewed from the stacking direction (Y direction) of the porous insulating substrate 11, second electrode film 12, solid electrolyte film 13 and first electrode film 14 in a plan view.
[0030] As shown in FIGS. 1 and 3, the second electrode film 12 and the first electrode film 14 are not provided on either short side of the fuel cell 100, and only the electrolyte membrane 13 is provided.
[0031] 1 and 2, a portion of the first electrode film 14 located on one long side of the fuel cell 100 constitutes a first lead portion 14a for electrical conduction with the outside of the fuel cell 100. A portion of the second electrode film 12 located on the other long side of the fuel cell 100 constitutes a second lead portion 12a for electrical conduction with the outside of the fuel cell 100.
[0032] The second electrode film 12 is not provided on one long side of the fuel cell 100, and the first electrode film 14 is not provided on the other long side of the fuel cell 100. In other words, in a plan view perpendicular to the stacking direction (Y direction), the first lead portion 14a does not overlap the second electrode film 12, and the second lead portion 12a does not overlap the first electrode film 14.
[0033] In the case of a fuel cell 100 having such a structure, the generated current flows from the second lead-out portion 12a through the electrolyte membrane 13 toward the first lead-out portion 14a. The voltage drop ΔV that occurs in this case is proportional to the density α [A / cm 2 ] of the generated current per unit area. 2 ] and the volume resistivity ρ [Ω / cm ] of the second electrode film 12 and the first electrode film 14. 3 ] and the film thickness d [cm] of the second electrode film 12 and the first electrode film 14, it is expressed by the following "Formula 1".
[0034] Equation 1: ΔV=α×(ρ / d)×L 2
[0035] Here, the voltage drop ΔV depends on the length L of the fuel cell 100 in the short side direction, not on the length W of the fuel cell 100 in the long side direction. In other words, once the allowable voltage drop ΔV and the density α of the generated current are determined, the volume resistivity ρ, film thickness d, and length L can be set so as to satisfy "Equation 1."
[0036] <Fuel cell block> The fuel cell block 200 according to the first embodiment will be described below with reference to FIGS. 4 to 11. FIG. 4 shows a plan view of the fuel cell block 200. FIG. 5 is a cross-sectional view taken along line CC shown in FIG. 4. FIG. 6 is a cross-sectional view taken along line DD shown in FIG. 4. FIG. 7 is a cross-sectional view taken along line EE shown in FIG. 4. FIG. 8 is a cross-sectional view taken along line FF shown in FIG. 4.
[0037] 4 to 8, the fuel cell block 200 includes a plurality of fuel cell units 100, a first plate member 21, a second plate member 22, and a frame member 23. The second plate member 22 is disposed opposite the first plate member 21. The frame member 23 connects the first plate member 21 and the second plate member 22. The first plate member 21, the second plate member 22, and the frame member 23 form a panel-shaped gas container.
[0038] Note that Figure 4 is a plan view seen from the first plate member 21 side, but in order to make the structure easier to understand, Figure 4 omits the illustration of part of the first plate member 21 and illustrates only the second plate member 22, and also illustrates not only the second plate member 22 but also the collector wiring 25 provided inside the second plate member 22.
[0039] A plurality of current collecting wires 24 are provided inside the first plate member 21. A plurality of current collecting wires 25 are provided inside the second plate member 22. A plurality of fuel cell units 100 are arranged in a gas container surrounded by the first plate member 21, the second plate member 22, and the frame member 23.
[0040] The first plate member 21 and the second plate member 22 are substrates having metal wiring therein, and are made of, for example, ceramic, glass, or polymer. In particular, ceramic substrates having copper wiring with very low electrical resistance, known as green sheets, are most suitable for the first plate member 21 and the second plate member 22. Such metal wiring (copper wiring) constitutes the current collecting wiring 24 and the current collecting wiring 25. Furthermore, the frame member 23 is made of the same material as the first plate member 21 and the second plate member 22 in order to match the thermal expansion coefficient.
[0041] Countersunk holes are formed by machining or the like at predetermined positions of the first plate member 21, the second plate member 22, and the frame member 23 in order to fit and fix the multiple fuel cell units 100. At the locations where the countersunk holes are formed, the current collecting wiring 24 is exposed from the first plate member 21, and the current collecting wiring 25 is exposed from the second plate member 22.
[0042] Frit glass or a highly heat-resistant adhesive is used to join the first plate member 21, the second plate member 22, and the frame member 23. A conductive paste such as silver paste or gold paste is used for the electrical connections. These connection materials are applied to the connection points by screen printing or a dispenser before assembling the components, and then the connection materials are pre-baked. After assembling the components, the panel-shaped gas container is formed by final baking.
[0043] 5 to 8, the plurality of fuel cell units 100 function as a partition wall that divides the gas container into an oxidant gas flow path 27 (Air) and a fuel gas flow path 28 (H2). Piping for supplying and discharging gas to and from the oxidant gas flow path 27 and the fuel gas flow path 28 will be described later with reference to FIG. 9 and other figures.
[0044] 4 and 5, the plurality of fuel cells 100 includes a plurality of first fuel cells 100a and a plurality of second fuel cells 100b. The orientation in which the plurality of fuel cells 100 are arranged will be described below.
[0045] In a plan view perpendicular to the direction along the long side of the fuel cell 100 (X direction), the first fuel cell 100a and the second fuel cell 100b are arranged at 180 degrees inversion from each other. That is, in the first fuel cell 100a, the first drawn-out portion 14a is located on the first plate member 21 side, and the second drawn-out portion 12a is located on the second plate member 22 side. In the second fuel cell 100b, the second drawn-out portion 12a is located on the first plate member 21 side, and the first drawn-out portion 14a is located on the second plate member 22 side.
[0046] In addition, the first fuel cell 100a and the second fuel cell 100b are repeatedly arranged side by side so that the first electrode film 14 of the first fuel cell 100a faces the first electrode film 14 of the second fuel cell 100b, and the porous insulating substrate 11 of the first fuel cell 100a faces the porous insulating substrate 11 of the second fuel cell 100b.
[0047] By arranging the first fuel cell 100a and the second fuel cell 100b in this manner, an oxidant gas (Air) is supplied to the opposing first electrode film 14 in the oxidant gas flow path 27, and a fuel gas (H2) is supplied to the opposing second electrode film 12 in the fuel gas flow path 28.
[0048] As described above, the current collecting wiring 24 is exposed in the recess formed in the first plate member 21, and the current collecting wiring 25 is exposed in the recess formed in the second plate member 22. Therefore, the multiple current collecting wirings 24 are each electrically connected to the first lead-out portion 14a of the first fuel cell 100a and the second lead-out portion 12a of the second fuel cell 100b. The multiple current collecting wirings 25 are each electrically connected to the first lead-out portion 14a of the second fuel cell 100b and the second lead-out portion 12a of the first fuel cell 100a. In this way, the multiple fuel cell units 100 are connected in series with each other.
[0049] Some of the multiple current collecting wirings 25 drawn out to the outside of the second plate member 22 can be electrically connected to the outside of the fuel cell block 200 via the negative output terminal 25a and the positive output terminal 25b, which constitute the negative output terminal 25a and the positive output terminal 25b.
[0050] The positive and negative output terminals may be formed by the current collecting wires 24. That is, some of the multiple current collecting wires 24 drawn out to the outside of the first plate member 21 may form the positive and negative output terminals.
[0051] Furthermore, the number of fuel cells 100 provided in the fuel cell block 200 is not limited to six and can be changed as appropriate.
[0052] The piping for supplying and discharging gas will be described below with reference to Figures 9 to 11. Like Figure 4, Figure 9 is a plan view of the fuel cell block 200 as seen from the Z direction, but the first plate member 21 and the second plate member 22 are not shown to make it easier to see the oxidant gas flow path 27 and the fuel gas flow path 28. Figure 10 is a front view of the fuel cell block 200 as seen from the Y direction. Figure 11 is a right side view of the fuel cell block 200 as seen from the X direction.
[0053] As shown in FIGS. 9 to 11, the fuel cell block 200 includes an oxidizing gas supply pipe 27a, an oxidizing gas exhaust pipe 27b, a fuel gas supply pipe 28a, and a fuel gas exhaust pipe 28b.
[0054] The oxidizing gas supply pipe 27a is provided to supply the oxidizing gas to the oxidizing gas flow path 27, and the oxidizing gas exhaust pipe 27b is provided to exhaust gas remaining in the oxidizing gas flow path 27. The fuel gas supply pipe 28a is provided to supply fuel gas to the fuel gas flow path 28, and the fuel gas exhaust pipe 28b is provided to exhaust gas remaining in the fuel gas flow path 28.
[0055] 10 , the negative electrode output terminal 25a is extended to the front side of the fuel cell block 200, and the positive electrode output terminal 25b is extended to the back side of the fuel cell block 200. Therefore, so as not to interfere with the negative electrode output terminal 25a and the positive electrode output terminal 25b, the oxidant gas supply pipe 27a and the fuel gas exhaust pipe 28b are provided on the right side of the fuel cell block 200, and the fuel gas supply pipe 28a and the oxidant gas exhaust pipe 27b are provided on the left side of the fuel cell block 200. Alternatively, the oxidant gas supply pipe 27a and the fuel gas exhaust pipe 28b may be provided on the left side of the fuel cell block 200, and the fuel gas supply pipe 28a and the oxidant gas exhaust pipe 27b may be provided on the right side of the fuel cell block 200.
[0056] 9, a plurality of through holes 26 are formed in the frame member 23, which connect the oxidant gas flow path 27 or the fuel gas flow path 28 to the respective pipes 27a, 27b, 28a, and 28b. Specifically, the frame member 23 is provided with a through hole 26 that connects the oxidant gas flow path 27 to the oxidant gas supply pipe 27a, a through hole 26 that connects the oxidant gas flow path 27 to the oxidant gas exhaust pipe 27b, a through hole 26 that connects the fuel gas flow path 28 to the fuel gas supply pipe 28a, and a through hole 26 that connects the fuel gas flow path 28 to the fuel gas exhaust pipe 28b.
[0057] With this configuration, the oxidant gas enters the oxidant gas flow path 27 from the oxidant gas supply pipe 27a and is discharged to the outside of the fuel cell block 200 via the oxidant gas exhaust pipe 27b extending in the Z direction from the oxidant gas flow path 27. Similarly, the fuel gas enters the fuel gas flow path 28 from the fuel gas supply pipe 28a and is discharged to the outside of the fuel cell block 200 via the fuel gas exhaust pipe 28b extending in the Z direction from the fuel gas flow path 28.
[0058] 6 and 8, the first plate member 21 has portions where the multiple current collecting wires 24 are not provided, and the second plate member 22 has portions where the multiple current collecting wires 25 are not provided. A plurality of through holes 26 may be formed in those portions to connect the oxidant gas flow path 27 or the fuel gas flow path 28 to the respective pipes 27a, 27b, 28a, 28b.
[0059] Furthermore, each of the pipes 27a, 27b, 28a, and 28b is made of, for example, a metal, ceramic, or polymer material. From the viewpoint of matching the thermal expansion coefficient, each of the pipes 27a, 27b, 28a, and 28b is preferably made of the same material as the frame member 23. Each of the pipes 27a, 27b, 28a, and 28b is joined to the frame member 23 using a frit material or a highly heat-resistant adhesive, or is mechanically fixed with a jig via a sealing material made of a ceramic or vermiculite-based material.
[0060] As described above, in the fuel cell block 200 of the first embodiment, the oxidant gas flow path 27 and the fuel gas flow path 28, which serve as gas flow paths, can be configured using a plurality of fuel cell units 100 as partition walls. Furthermore, by arranging two first electrode films 14 opposite each other in the oxidant gas flow path 27 and two second electrode films 12 opposite each other in the fuel gas flow path 28, it is possible to extract current efficiently. This makes it possible to prevent a decrease in the effective area available for power generation, and to arrange a plurality of fuel cell units 100 at high density.
[0061] Furthermore, by providing the fuel cell unit 100 with the first lead-out portion 14a and the second lead-out portion 12a, adjusting the orientation of the fuel cell unit 100, and using the current collecting wiring 24 and the current collecting wiring 25, the fuel cell unit 100 can be connected in series. Therefore, the voltage output from the negative output terminal 25a and the positive output terminal 25b can be amplified according to the number of fuel cell units 100. Amplifying the output voltage in this manner is a very effective means for reducing power loss due to parasitic resistance (internal resistance) present in the fuel cell block 200.
[0062] <Fuel cell system> A fuel cell system 300 according to the first embodiment will be described below with reference to Figures 12 to 15. The fuel cell system 300 includes a plurality of fuel cell blocks 200. Figures 12 to 15 show two of the plurality of fuel cell blocks 200 arranged adjacent to each other. The plurality of fuel cell blocks 200 are connected in series or in parallel.
[0063] 12 and 13 show an example in which two fuel cell blocks 200 are stacked in the Z direction. As shown in FIG. 12, the two fuel cell blocks 200 are adjacently arranged such that the first plate member 21 of one block faces the second plate member 22 of the other block. A connecting conductor is used to electrically connect the negative electrode output terminal 25a and the positive electrode output terminal 25b. The connecting conductor may be a cable or the like, but here a bus bar 31 with sufficiently low electrical resistance is used as the connecting conductor.
[0064] In the two fuel cell blocks 200 shown in Fig. 12, the pipes 27a, 27b, 28a, and 28b are aligned, so that the negative output terminals 25a are drawn in the same direction, and the positive output terminals 25b are drawn in the same direction. Therefore, to reduce parasitic resistance, the negative output terminals 25a are electrically connected to each other, and the positive output terminals 25b are electrically connected to each other. Thus, the example shown in Fig. 12 can be suitably used when two fuel cell blocks 200 are connected in parallel to amplify current.
[0065] When two fuel cell blocks 200 are stacked, the two fuel cell blocks 200 are mechanically fixed using a jig or the like, or are bonded using frit or a heat-resistant adhesive, etc. The pipes 27a, 27b, 28a, and 28b are also bonded to each other.
[0066] In addition, from the viewpoint of suppressing temperature rise due to heat dissipation, it is preferable that the periphery of the bus bar 31, the periphery of each pipe 27a, 27b, 28a, 28b, and the surfaces of each of the first plate member 21, the second plate member 22 and the frame member 23 are covered with a heat insulating material.
[0067] In the example of FIG. 13, two fuel cell blocks 200 are arranged adjacent to each other so that one first plate member 21 faces the other first plate member 21. The positions of the respective pipes 27a, 27b, 28a, and 28b are aligned, so that the respective negative output terminals 25a are drawn in opposite directions, and the respective positive output terminals 25b are drawn in opposite directions. Therefore, to reduce power loss due to parasitic resistance, the negative output terminal 25a of one fuel cell block is electrically connected to the positive output terminal 25b of the other fuel cell block. Thus, the example of FIG. 13 can be suitably used when two fuel cell blocks 200 are connected in series to amplify voltage.
[0068] Note that even when one second plate member 22 and the other second plate member 22 are disposed adjacent to each other so as to face each other, the directions in which the negative output terminals 25a and the positive output terminals 25b are drawn out are opposite to each other. Therefore, this configuration is suitable for use when two fuel cell blocks 200 are connected in series.
[0069] Figures 14 and 15 show an example of a planar arrangement of two fuel cell blocks 200. In the example of Figures 14 and 15, the two fuel cell blocks 200 are arranged adjacent to each other so that their frame members 23 face each other.
[0070] In the two fuel cell blocks 200 shown in FIG. 14, the frame members 23 face each other in the direction in which the negative output terminal 25a or the positive output terminal 25b is pulled out (Y direction). The negative output terminal 25a of one block and the positive output terminal 25b of the other block are integrated. Therefore, the two fuel cell blocks 200 are connected in series. There is no need to use a connecting conductor such as a bus bar 31 for electrically connecting the negative output terminal 25a and the positive output terminal 25b. Therefore, in the example shown in FIG. 14, the parasitic resistance between the two fuel cell blocks 200 can be reduced by the amount of the connecting conductor.
[0071] In the two fuel cell blocks 200 shown in Fig. 15, the frame members 23 face each other in the direction (X direction) in which the negative output terminal 25a or the positive output terminal 25b is not drawn out. In the example shown in Fig. 15, at least one of the pipes 27a, 27b, 28a, 28b is shared, which is an advantage in that it promotes downsizing of the fuel cell system 300.
[0072] 15 are arranged at 180-degree angles relative to each other in a plan view perpendicular to the Z direction. Since one of the oxidizing gas supply pipes 27a can be shared, the space required for arranging the other oxidizing gas supply pipe 27a can be reduced, thereby facilitating the miniaturization of the fuel cell system 300 in the X direction.
[0073] 15, a fuel cell block 200 that is inverted 180 degrees can also be provided to the left of the left fuel cell block 200. In this case, one of the fuel gas supply pipes 28a can be shared, and the space required for arranging the other fuel gas supply pipe 28a can be reduced, thereby further promoting the miniaturization of the fuel cell system 300 in the X direction.
[0074] 15, the negative output terminals 25a are drawn in opposite directions, and the positive output terminals 25b are drawn in opposite directions. Therefore, in order to reduce power loss due to parasitic resistance, one negative output terminal 25a and the other positive output terminal 25b are electrically connected. In this way, the example of FIG. 15 can be suitably used when two fuel cell blocks 200 are connected in series.
[0075] In the example of FIG. 15, two fuel cell blocks 200 may also be connected in parallel.
[0076] The fuel cell system 300 has been described above using Figures 12 to 15, but the arrangement of the fuel cell blocks 200 is not limited to the examples in Figures 12 to 15, and the examples in Figures 12 to 15 can be combined as appropriate. For example, the first layer of fuel cell blocks 200 can be arranged in a plane, and then the second and subsequent layers of fuel cell blocks 200 can be stacked on top of the first layer of fuel cell blocks 200.
[0077] The present invention has been specifically described above based on the above embodiment, but the present invention is not limited to the above embodiment and can be modified in various ways without departing from the spirit of the present invention. [Explanation of symbols]
[0078] 100 fuel cell 100a First fuel cell 100b Second fuel cell 11 Porous insulating substrate 12 Second electrode film 12a Second drawer 13 Electrolyte membrane 14 First electrode film 14a First drawer 200 fuel cell block 21 1st plate member 22 Second plate member 23 Frame members 24 Current collector wiring 25 Collector wiring 25a Negative output terminal 25b Positive output terminal 26 Through hole 27 Oxidant gas flow path 27a Oxidant gas supply pipe 27b Oxidant gas exhaust piping 28 Fuel gas flow path 28a Fuel gas supply pipe 28b Fuel gas exhaust piping 300 Fuel Cell System 31 Busbar
Claims
1. A first plate member; a second plate member disposed opposite the first plate member; a frame member sandwiched between the first plate member and the second plate member; a plurality of fuel cell units arranged in a gas container surrounded by the first plate member, the second plate member, and the frame member; Equipped with the fuel cell has a laminated structure including a first electrode film, a second electrode film, and a solid electrolyte film formed between the first electrode film and the second electrode film, on a porous insulating substrate; the fuel cell has a rectangular shape when viewed from a plane in a stacking direction of the first electrode film, the electrolyte membrane, and the second electrode film, a part of the first electrode film located on one long side of the fuel cell constitutes a first lead portion for electrical conduction with the outside of the fuel cell, a part of the second electrode film located on the other long side of the fuel cell constitutes a second lead portion for electrical conduction with the outside of the fuel cell, the plurality of fuel cell units include a plurality of first fuel cell units in which the first drawer portion is located on the first plate member side and the second drawer portion is located on the second plate member side, and a plurality of second fuel cell units in which the second drawer portion is located on the first plate member side and the first drawer portion is located on the second plate member side, A fuel cell block in which the first fuel cell cell and the second fuel cell cell are repeatedly arranged side by side so that the first electrode film of the first fuel cell cell faces the first electrode film of the second fuel cell cell, and the porous insulating substrate of the first fuel cell cell faces the porous insulating substrate of the second fuel cell cell.
2. 2. The fuel cell block according to claim 1, In a plan view seen from the stacking direction, the first lead portion does not overlap the second electrode film, and the second lead portion does not overlap the first electrode film.
3. 2. The fuel cell block according to claim 1, The plurality of fuel cell cells function as a partition wall that divides the gas container into a first gas flow path for supplying oxidant gas to the opposing first electrode film and a second gas flow path for supplying fuel gas to the opposing second electrode film.
4. 4. The fuel cell block according to claim 3, a plurality of first current collecting wires provided inside the first plate member; a plurality of second current collecting wires provided inside the second plate member; Further provided with the plurality of first current collecting wirings are each electrically connected to the first drawn-out portion of the first fuel cell and the second drawn-out portion of the second fuel cell, the plurality of second current collecting wirings are each electrically connected to the first drawn-out portion of the second fuel cell and the second drawn-out portion of the first fuel cell, a fuel cell block in which the plurality of fuel cells are connected in series with each other;
5. 5. The fuel cell block according to claim 4, A fuel cell block, wherein a portion of the plurality of first collector wirings drawn out to the outside of the first plate member, or a portion of the plurality of second collector wirings drawn out to the outside of the second plate member, constitutes a positive output terminal and a negative output terminal for electrical conduction with the outside of the fuel cell block.
6. 6. The fuel cell block according to claim 5, a first gas supply pipe for supplying the oxidant gas to the first gas flow path; a first gas exhaust pipe for exhausting gas remaining in the first gas flow path; a second gas supply pipe for supplying the fuel gas to the second gas flow path; a second gas exhaust pipe for exhausting gas remaining in the second gas flow path; The fuel cell block further comprises:
7. 7. The fuel cell block according to claim 6, a fuel cell block, wherein the frame member is formed with a first through-hole connecting the first gas flow path to the first gas supply pipe, a second through-hole connecting the first gas flow path to the first gas exhaust pipe, a third through-hole connecting the second gas flow path to the second gas supply pipe, and a fourth through-hole connecting the second gas flow path to the second gas exhaust pipe.
8. 7. The fuel cell block according to claim 6, a fuel cell block, wherein a first through hole connecting the first gas flow path to the first gas supply pipe, a second through hole connecting the first gas flow path to the first gas exhaust pipe, a third through hole connecting the second gas flow path to the second gas supply pipe, and a fourth through hole connecting the second gas flow path to the second gas exhaust pipe are formed in a portion of the first plate member where the plurality of first current collecting wirings are not provided, or in a portion of the second plate member where the plurality of second current collecting wirings are not provided.
9. A fuel cell system including a plurality of fuel cell blocks according to claim 6, the plurality of fuel cell blocks include two fuel cell blocks arranged adjacent to each other, The plurality of fuel cell blocks are connected in series or in parallel, A fuel cell system in which the two fuel cell blocks are arranged adjacent to each other so that one first plate member and the other second plate member, one first plate member and the other first plate member, or one second plate member and the other second plate member face each other, or are arranged adjacent to each other so that their frame members face each other.
10. 10. The fuel cell system according to claim 9, the two fuel cell blocks are disposed adjacent to each other such that the first plate member of one of the fuel cell blocks and the second plate member of the other of the fuel cell blocks face each other; The two fuel cell blocks are connected in parallel.
11. 10. The fuel cell system according to claim 9, the two fuel cell blocks are disposed adjacent to each other such that the one first plate member and the other first plate member, or the one second plate member and the other second plate member, face each other; The two fuel cell blocks are connected in series.
12. 10. The fuel cell system according to claim 9, the two fuel cell blocks are disposed adjacent to each other so that the frame members face each other; The positive output terminal on one side and the negative output terminal on the other side are integrated, The two fuel cell blocks are connected in series.
13. 10. The fuel cell system according to claim 9, the two fuel cell blocks are disposed adjacent to each other so that the frame members face each other; A fuel cell system in which at least one of the first gas supply pipe, the first gas exhaust pipe, the second gas supply pipe, and the second gas exhaust pipe provided in the two fuel cell blocks is shared.
Citation Information
Patent Citations
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