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WO2021240723A1 - Fuel cell and fuel cell module - Google Patents

Fuel cell and fuel cell module Download PDF

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Publication number
WO2021240723A1
WO2021240723A1 PCT/JP2020/021116 JP2020021116W WO2021240723A1 WO 2021240723 A1 WO2021240723 A1 WO 2021240723A1 JP 2020021116 W JP2020021116 W JP 2020021116W WO 2021240723 A1 WO2021240723 A1 WO 2021240723A1
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WO
WIPO (PCT)
Prior art keywords
fuel cell
element portion
power generation
gas
film
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/JP2020/021116
Other languages
French (fr)
Japanese (ja)
Inventor
憲之 佐久間
佳孝 笹子
夏樹 横山
貴志 堤
有俊 杉本
徹 荒巻
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi High Tech Corp
Original Assignee
Hitachi High Tech Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi High Tech Corp filed Critical Hitachi High Tech Corp
Priority to PCT/JP2020/021116 priority Critical patent/WO2021240723A1/en
Priority to TW110111535A priority patent/TWI779539B/en
Publication of WO2021240723A1 publication Critical patent/WO2021240723A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0258Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04313Processes for controlling fuel cells or fuel cell systems characterised by the detection or assessment of variables; characterised by the detection or assessment of failure or abnormal function
    • H01M8/04664Failure or abnormal function
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/12Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/12Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
    • H01M8/1286Fuel cells applied on a support, e.g. miniature fuel cells deposited on silica supports
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/24Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/241Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
    • H01M8/2425High-temperature cells with solid electrolytes
    • H01M8/2428Grouping by arranging unit cells on a surface of any form, e.g. planar or tubular
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Definitions

  • the present invention relates to a fuel cell and a fuel cell module.
  • Patent Document 1 describes that in a fuel cell system, the pressure difference between the fuel electrode and the air electrode is reduced to suppress deterioration of the electrolyte membrane.
  • Patent Document 2 anisotropic etching is performed on a single crystal silicon substrate having a (110) plane as a surface, so that the opening angle with the substrate surface in the cross section of the opening in which the battery elements are laminated is approximately 90 °. Is described.
  • Patent Document 1 The technology of Patent Document 1 is provided with a pressure adjusting device for dealing with the pressure difference between the fuel gas and the oxidant gas, but it is difficult to deal with the momentary pressure fluctuation. Further, this pressure adjusting device is based on the gas pressure difference between a plurality of fuel cell stacks, and it is difficult to cope with the pressure difference in a single fuel cell stack.
  • the present invention has been made in view of the above problems, and when the pressure difference between the fuel gas and the oxidant gas suddenly fluctuates or excessively increases by providing the protective element portion in the fuel cell.
  • An example of a fuel cell according to the present invention is A power generation element unit formed by laminating an electrolyte membrane and one or more conductive films and supplied with a fuel gas and an oxidant gas to generate power.
  • an example of the fuel cell module according to the present invention is with the above fuel cell It is characterized in that it is arranged in the fuel cell and includes a separator that separates the fuel gas and the oxidant gas.
  • the influence on the power generation element can be reduced and the fuel cell system can be prevented from being damaged.
  • FIG. It is a top view of the fuel cell which concerns on Embodiment 1.
  • FIG. It is sectional drawing which follows the AA line of FIG. It is sectional drawing which shows the manufacturing process of the fuel cell of FIG. It is sectional drawing which shows the manufacturing process of the fuel cell of FIG. It is sectional drawing which shows the manufacturing process of the fuel cell of FIG. It is sectional drawing which shows the manufacturing process of the fuel cell of FIG. It is a figure which shows the relationship between the opening area and the withstand voltage of a thin film membrane.
  • FIG. FIG. 5 is a cross-sectional view taken along the line BB of FIG. It is sectional drawing of the fuel cell module which concerns on Embodiment 1.
  • FIG. 9 is a cross-sectional view taken along the line CC of FIG.
  • FIG. 3 is a plan view of the fuel cell according to the third embodiment. It is sectional drawing along the DD line of FIG. It is a top view of the separator for a fuel cell which concerns on Embodiment 4.
  • FIG. FIG. 3 is a cross-sectional view taken along the line EE of FIG. It is sectional drawing of the fuel cell module which concerns on Embodiment 4.
  • FIG. 9 is a cross-sectional view taken along the line CC of FIG.
  • FIG. 3 is a plan view of the fuel cell according to the third embodiment. It is sectional drawing along the DD line of FIG. It is a top view of the separator for a fuel cell which concerns on Embodiment 4.
  • FIG. FIG. 3 is a cross-sectional view taken along the line EE of FIG. It is sectional drawing of the fuel cell module which concerns on Embodiment 4.
  • the present invention relates to a fuel cell and a fuel cell module.
  • fuel cells have been attracting attention as a clean energy source capable of high energy conversion and not emitting pollutants such as carbon dioxide gas and nitrogen oxides.
  • solid oxide fuel cells Solid Oxide Fuel Cell, hereinafter abbreviated as SOFC
  • SOFC Solid Oxide Fuel Cell
  • gases such as hydrogen, methane, and carbon monoxide, which have high power generation efficiency and are easy to handle, as fuel. ..
  • SOFC has many advantages over other types of fuel cells, and is expected as a cogeneration system having excellent energy saving and environmental friendliness.
  • SOFC has a structure in which a solid electrolyte is sandwiched between a fuel electrode and an air electrode.
  • the electrolyte is a partition wall, and a fuel gas such as hydrogen is supplied to the fuel electrode, and an oxidant gas such as air is supplied to the air electrode.
  • air is used as a representative of the oxidant gas, but it is also possible to use a gas other than air as the oxidant gas.
  • FIG. 1 is a plan view of the fuel cell 1 according to the first embodiment of the present invention.
  • FIG. 2 is a cross-sectional view taken along the line AA of FIG.
  • the vertical direction of the paper surface in FIG. 2 is the vertical direction of the fuel cell 1, but this direction has nothing to do with the orientation when the fuel cell is actually installed or used.
  • hatching may be added to the part that is not a cross section to facilitate understanding.
  • the fuel cell 1 has the following configuration. -Semiconductor substrate 2 (substrate) made of single crystal silicon (Si) -The first insulating film 3 formed on the semiconductor substrate 2 -The power generation element portion and the protection element portion formed on the first insulating film 3
  • the configuration of the power generation element unit can be a known configuration, but an example will be described below.
  • the power generation element portion is formed by laminating an electrolyte film and one or more conductive films.
  • the electrolyte membrane is the electrolyte membrane 5a
  • the conductive film is the first electrode 4a and the second electrode 6a.
  • the power generation element portion is laminated on the first insulating film 3 in the order of the first electrode 4a, the electrolyte film 5a, and the second electrode 6a.
  • the two fuel cell 1s are provided with two protective element units.
  • a protective film is formed on the protective element portion.
  • the protective film is configured by laminating the first electrodes 4b and 4c, the electrolyte films 5b and 5c, and the second electrodes 6b and 6c.
  • the power generation element portion and the protection element portion are formed on the same semiconductor substrate 2. Such a configuration simplifies the manufacturing process.
  • the semiconductor substrate 2 has a plurality of openings, and the power generation element portion and the protection element portion are formed in the openings.
  • the plurality of openings include a first opening 7 and second openings 8a, 8b. These openings are not visible from above, but are shown by broken lines in the plan view of FIG.
  • the power generation element portion is formed over a plurality of first openings 7. At least one of the conductive films (first electrode 4a and second electrode 6a in this embodiment) (both in this embodiment) is continuous over the plurality of first openings 7. With such a configuration, the process of forming the conductive film is simplified.
  • one of the conductive films of the power generation element portion (first electrode 4a and second electrode 6a in this modified example) (first electrode 4a in this modified example) and protection. It may be configured so that the conductive film of the element portion (the first electrode 4c in this modification) is continuous. According to such a modification, the process of forming the conductive film is simplified.
  • the two protective element portions are formed in the second opening 8a and the second opening 8b, respectively.
  • Fuel gas and air are supplied to the power generation element to generate electricity.
  • one of the first electrode 4a and the second electrode 6a becomes an anode electrode, and the other becomes a cathode electrode, which are connected to the outside and supply electric power to the outside.
  • the first electrode 4b and the second electrode 6b of the protective element portion can also be connected to the outside, and the capacitance or the resistance value between the first electrode 4b and the second electrode 6b can be measured. ing. The same applies to the first electrode 4c and the second electrode 6c.
  • the shape and dimensions of the first opening 7 can be arbitrarily designed, but for example, it is rectangular in a plan view (direction in FIG. 1), and the length of one side is about 5 mm.
  • the shapes and dimensions of the second openings 8a and 8b can be arbitrarily designed, but are, for example, rectangular and have a side length of about 6 mm.
  • the area of one second opening 8a (or the second opening 8b) related to the protective element portion is larger than the area of one first opening 7 related to the power generation element portion. It's getting bigger.
  • the measurement position of the area can be arbitrarily defined. For example, the area may be measured at the lower end of each opening, or the area may be measured at the upper end of each opening.
  • the area of the second opening 8a (or the second opening 8b) is larger than the area of the first opening 7 regardless of which of these measuring methods is used.
  • the semiconductor substrate 2 has a plurality of first openings 7 from which the inside has been removed, one second opening 8a, and one second opening 8b.
  • a first insulating film 3 is formed on both surfaces of the semiconductor substrate 2 other than these openings.
  • the first electrodes 4a, 4b, and 4c are formed on the first insulating film 3 so as to cover the first opening 7 and the second openings 8a and 8b, and the electrolyte films 5a, 5b, and 5c are formed on the first electrodes 4a, 4b, and 4c.
  • the second electrodes 6a, 6b, and 6c are formed on the second electrodes 6a, 6b, and 6c.
  • film composition means, for example, the composition, thickness and stacking order of each layer, and does not necessarily include the area of the film.
  • FIGS. 3A to 3D are diagrams showing a manufacturing process of the fuel cell 1. These figures are cross-sectional views of a portion corresponding to FIG.
  • a semiconductor substrate 2 made of single crystal Si and having a crystal orientation of Si ⁇ 100> is prepared.
  • the semiconductor substrate 2 has a thickness of, for example, 400 ⁇ m or more.
  • the first insulating film 3 is formed on the surface of the semiconductor substrate 2.
  • a silicon nitride film having a tensile stress is formed at about 200 nm by a CVD method.
  • silicon nitride films having the same film thickness are formed on the upper side and the lower side of the semiconductor substrate 2.
  • a metal film for example, platinum (Pt) film
  • Pt platinum
  • the first electrodes 4a, 4b, and 4c are formed. This is performed by performing patterning using a photolithography method and using a dry etching method using an argon (Ar) gas or the like.
  • the surface of the first insulating film 3 in order to improve the adhesive force between the Pt film and the first insulating film 3.
  • the modification is performed, for example, by etching the surface of the first insulating film 3 (for example, etching by about 10 to 15 nm) by sputtering etching with Ar gas before forming the Pt film.
  • a titanium film (Ti) or an aluminum film (Al) may be formed at about 2 nm as a barrier metal film that assists the adhesion. ..
  • a negative resist pattern is formed by photolithography technology.
  • a sputtering method for example, a YSZ film (zirconium oxide film containing yttrium) as an electrolyte film is formed at about 500 nm.
  • the negative resist is removed.
  • the electrolyte membranes 5a, 5b, 5c are formed.
  • a Pt film of about 100 nm is formed by a sputtering method.
  • patterning is performed using a photolithography method, and the second electrodes 6a, 6b, and 6c are formed by dry etching with Ar gas, as shown in FIG. 3C.
  • a part of the first insulating film 3 on the lower side of the semiconductor substrate 2 is removed by using a photolithography technique and an insulating film etching technique to expose the back surface of the semiconductor substrate 2.
  • first openings 7 and second openings 8a and 8b are formed. This is done, for example, by wet-etching and removing the Si film of the semiconductor substrate 2 with a KOH (potassium hydroxide) solution or a TMAH (tetramethylamide) solution. Alternatively, it is performed by removing the Si film of the semiconductor substrate 2 by dry etching using a fluorine-based gas as a main component. In this way, the fuel cell 1 shown in FIGS. 1 and 2 is formed.
  • KOH potassium hydroxide
  • TMAH tetramethylamide
  • the fluorine-based chemical resistance is excellent, the resistivity is low, and the melting point is higher than the operating temperature (for example, 600).
  • a film (° C or higher) can be used.
  • a silver film (Ag), a nickel film (Ni), a chromium film (Cr), a palladium film (Pd), a ruthenium film (Ru), a rhodium film (Rh), etc. can be used.
  • the first insulating film 3 is not limited to the silicon nitride film, but it is preferable to use an insulating film (aluminum nitride film or the like) having a tensile stress with respect to the Si substrate. Further, the first insulating film 3 may be a silicon oxide film containing a silicon nitride film and boron or phosphorus, or may be a laminated film containing a P-TEOS film containing an organic component at a low temperature. ..
  • FIG. 4 is a diagram showing the relationship between the opening area and the thin film membrane pressure resistance of the fuel cell 1 of FIG. Four rectangular openings are formed, each having a side length of 3 mm (opening area 9 mm 2 ), 4 mm (opening area 16 mm 2 ), 5 mm (opening area 25 mm 2 ), 6 mm (opening area 36 mm). 2 ). After forming a thin film membrane having the film structure shown in FIG. 2 on each opening, air was blown and the pressure at which the thin film membrane was damaged (membrane pressure resistance) was measured.
  • the pressure resistance of the thin film membrane decreases as the area of the opening increases.
  • the withstand voltage of the protective element portion is about 25 KPa.
  • the withstand voltage of the power generation element portion is about 32 KPa.
  • the withstand voltage of the membrane is different, and the withstand voltage of the protective element is lower than the withstand strength of the power generation element. That is, the strength of the film or laminate constituting the protective element portion is lower than the strength of the film or laminate constituting the power generation element portion. Therefore, when a sudden pressure fluctuation occurs, the protective element portion is damaged before the power generation element portion.
  • the ratio of compressive strength is about 1.3.
  • FIG. 5 is a plan view of the separator 9 according to the first embodiment of the present invention.
  • FIG. 6 is a cross-sectional view taken along the line BB of FIG.
  • the separator 9 is arranged in contact with the fuel cell 1.
  • the separator 9 is formed with an upper groove 11 and a lower groove 13.
  • the upper groove 11 is formed on the upper surface side of the ceramic substrate 10.
  • the upper groove 11 includes a gas inflow port 11a, a gas discharge port 11b, and a through hole 12.
  • the through hole 12 penetrates the ceramic substrate 10 up and down.
  • the lower groove 13 is formed on the lower surface side of the ceramic substrate 10.
  • the lower gutter 13 includes an air inlet 13a, an air discharge port 13b, and a through hole 14.
  • the through hole 14 penetrates the ceramic substrate 10 up and down.
  • the external dimensions of the separator 9 are almost the same as the external dimensions of the fuel cell 1.
  • the upper groove 11 of the separator 9 extends to a range including the entire first opening 7 of the fuel cell 1 and the entire second opening 8a when viewed from above. Therefore, when the fuel cell 1 is arranged above and below the separator 9 (for example, as will be described later in relation to FIG. 7), the first fuel cell 1 of the upper fuel cell 1 is passed through the upper groove 11. Gas spreads to the electrode 4a, the first electrode 4b of the upper fuel cell 1, and the second electrode 6b of the lower fuel cell 1.
  • the lower groove 13 of the separator 9 extends to a range including the entire first opening 7 of the fuel cell 1 and the entire second opening 8b when viewed from above. There is. Therefore, when the fuel cell 1 is arranged above and below the separator 9, the second electrode 6a of the lower fuel cell 1 and the lower fuel cell 1 pass through the lower groove 13. Gas spreads to the second electrode 6c and the first electrode 4c of the upper fuel cell 1.
  • the upper groove 11 includes a through hole 12 and serves as a flow path for a certain gas
  • the lower groove 13 includes a through hole 14 and serves as a flow path for another gas.
  • these two gases are not mixed.
  • the through hole 12 does not communicate with the lower groove 13 and the through hole 14 does not communicate with the upper groove 11, the fuel gas and air are separated and sent to the fuel cell.
  • the separator 9 is arranged in the fuel cell 1 to separate the fuel gas and the air. With such a configuration, it is possible to prevent mixing of the fuel gas and air.
  • FIG. 7 is a cross-sectional view of the fuel cell module 15 according to the first embodiment.
  • the fuel cell module 15 includes two fuel cell cells 1 and one separator 9. Each fuel cell 1 is arranged above and below the separator 9.
  • the fuel cell module 15 two fuel cell cells 1 are stacked.
  • the separator 9 is laminated between the two fuel cell 1s.
  • An upper substrate 17 and a lower substrate 16 having a gas flow path are provided at the upper end and the lower end of the fuel cell module 15, respectively.
  • the flow path of the lower substrate 16 is a groove having the same shape as the portion of the upper groove 11 of the separator 9 excluding the through hole 12.
  • the flow path of the lower substrate 16 is provided with at least two openings on the side surfaces to allow gas inflow and outflow.
  • the flow path of the upper substrate 17 is a groove having the same shape as the portion of the lower groove 13 of the separator 9 excluding the through hole 14.
  • the flow path of the upper substrate 17 is also provided with at least two openings on the side surfaces to allow gas inflow and outflow.
  • the fuel cell module 15 has a mechanism (not shown) for applying pressure to the lower substrate 16 and the upper substrate 17. As a result, the airtightness of the region where the fuel gas and the air flow is maintained, and the mixing of the gas is prevented.
  • the fuel gas 18 is supplied from the right side of the paper in FIG. 7.
  • the fuel gas 18 reaches each of the following electrodes. -The first electrode 4b and the second electrode 6b of the protective element portion of the fuel cell 1 above. -First electrode 4a of the power generation element of the fuel cell 1 above -The first electrode 4b and the second electrode 6b of the protective element portion of the lower fuel cell 1 -First electrode 4a of the power generation element of the lower fuel cell 1 Further, the fuel gas 18 consumed in the power generation is discharged from a gas discharge port (not shown).
  • air 19 is supplied from the left side of the paper in FIG. 7.
  • the air 19 reaches each of the following electrodes. -The first electrode 4c and the second electrode 6c of the protective element portion of the fuel cell 1 above. -Second electrode 6a of the power generation element of the fuel cell 1 above -First electrode 4c and second electrode 6c of the protective element part of the lower fuel cell 1 -Second electrode 6a of the power generation element of the lower fuel cell 1 Further, the air 19 consumed by the power generation is discharged from a gas discharge port (not shown).
  • the fuel gas 18 and the air 19 are supplied, consumed, and discharged while being separated by the separator 9, the lower substrate 16, and the upper substrate 17.
  • pressure is applied to the fuel cell module 15 between the upper substrate 17 and the lower substrate 16 to prevent the fuel gas 18 and the air 19 from leaking.
  • the fuel gas 18 is supplied from the upper, middle, and lower three places on the right side of the paper, but for example, it is assumed that the pressure rises sharply only in the middle stage.
  • the power generation element portion and the right side protection element portion receive a pressure difference
  • the right side protection element portion receives a pressure difference.
  • either (or both) of the two protective element portions are damaged before the power generation element portion, which reduces the pressure difference between the stages, the damage of the power generation element portion is avoided.
  • both the fuel gas 18 and the air 19 are supplied to the power generation element portion, and only one of the fuel gas 18 or the air 19 is supplied to the protection element portion. Therefore, although the protective element unit has a configuration capable of generating power in the present embodiment, it does not actually generate power as shown in FIG. 7. As described above, by making the configuration in which the operation of the protective element portion does not affect the power generation, it is possible to avoid the influence on the power generation operation of the fuel cell 1 even if the protective element portion is damaged. Further, in the first embodiment, such a configuration is realized by the separator 9 having through holes 12 and 14 at positions corresponding to the protective element portion.
  • a heat-resistant sealing material is used between the fuel cell 1 and the separator 9, between the fuel cell 1 and the upper substrate 17, and / or between the fuel cell 1 and the lower substrate 16. May be good. If a material that deforms when pressure is applied is used as the sealing material, damage to the fuel cell 1 when pressure is applied can be reduced.
  • the fuel cell module 15 of the first embodiment has a structure in which two fuel cell cells 1 are laminated, but a structure in which more stages are laminated by alternately stacking the fuel cell 1 and the separator 9 is also possible. good. In this way, the desired output can be obtained.
  • FIG. 8 shows a schematic diagram of the fuel cell system according to the first embodiment.
  • the fuel cell system mainly includes a blower 21 for supplying fuel gas 18 and air 19, a reformer 22 having a fuel gas flow rate adjusting mechanism, and a pressure regulator 23 for adjusting the air pressure.
  • the fuel cell module 15 is provided with a housing 24 for keeping the fuel cell module 15 at a constant temperature (300 ° C. to 600 ° C.), and a combustor 25 for burning the discharged fuel gas.
  • methane can be used as the fuel gas 18.
  • Methane is supplied by the blower 21 and the flow rate and pressure are adjusted in the reformer 22. As a result, a fuel gas having a temperature of about 600 ° C. containing hydrogen is generated. The fuel gas is sent to the fuel cell module 15.
  • the air 19 is also sent by the blower 21, the pressure and the flow rate are adjusted by the pressure regulator 23, and the air 19 is sent to the fuel cell module 15.
  • the temperature of the air is also set to about 600 ° C. by utilizing the heat of the reformer 22.
  • the flow rate of fuel gas and air needs to be increased to several liters / minute at the maximum output.
  • the reformed fuel gas 18 and the heated air 19 pass through the housing 24 kept at about 500 ° C. through piping, are sent to the fuel cell module 15, and are consumed for power generation. After that, each of the consumed gases passes through a pipe, merges with the combustor 25, burns at a high temperature, and is discharged.
  • a pressure gauge and a flow meter are provided in the fuel gas and air pipes discharged from the fuel cell module 15. As a result, feedback control is performed on the reformer 22 and the pressure regulator 23, and the average pressure and flow rate in the pipe are adjusted.
  • the pressure fluctuations of the fuel gas 18 and the air 19 are deflected by the thin film membranes (first electrodes 4a, 4b, 4c, electrolyte membranes 5a, 5b, 5c, second electrodes 6a, 6b, 6c) of the power generation element portion and the protection element portion.
  • first electrodes 4a, 4b, 4c electrolyte membranes 5a, 5b, 5c, second electrodes 6a, 6b, 6c
  • a protective element portion having a large area is provided near the gas inlet. Further, the withstand voltage strength of the protective element portion is set lower than the withstand voltage strength of the power generation element portion. Therefore, when a sudden pressure fluctuation occurs, the protective element portion is damaged before the power generation element portion is damaged.
  • the structure of the separator 9 prevents the fuel gas 18 and the air 19 from mixing even if the protective element portion is damaged, so that the adverse effects of gas mixing can be prevented.
  • the protective element portion even when the pressure difference between the fuel gas and the oxidant gas suddenly fluctuates or increases excessively, the power generation element portion is damaged. Can be prevented. This makes it possible to provide a highly reliable and highly efficient fuel cell system.
  • the limit value of pressure fluctuation can be controlled by designing the opening area of the protective element portion based on the relationship between the opening area shown in FIG. 4 and the pressure resistance of the thin film membrane. When the opening area of the power generation element portion is changed, the opening area of the protective element portion can be changed accordingly.
  • the protection element portion is damaged by monitoring the capacitance value between the first electrode and the second electrode of the protection element portion, or by monitoring the resistance value of the first electrode or the second electrode. Can be detected.
  • the fuel cell module can be safely stopped. After the stop, only the damaged fuel cell can be replaced and power can be generated again. In this way, maintenance can be easily performed.
  • methane is mentioned as the fuel gas, but the gas is not particularly limited as long as it can be reformed.
  • the hydrocarbon fuel natural gas, LP gas, coal reforming gas, lower hydrocarbon gas (ethane, ethylene, propane, butane), bioethanol and the like can be used.
  • a vaporizer may be provided in front of the reformer 22, and the vaporizer may vaporize water from the raw material gas (or liquid) of the hydrocarbon fuel.
  • the fuel cell module may be arranged horizontally. Even in that case, the gas can flow from the bottom to the top.
  • FIG. 9 is a plan view of the fuel cell 26 according to the second embodiment of the present invention.
  • FIG. 10 is a cross-sectional view taken along the line CC of FIG.
  • the second electrode of the protective element portion is configured as a temperature sensor 27.
  • the temperature sensor 27 can be wiring arranged on the second openings 8a and 8b. Unlike the first embodiment, the wiring of the temperature sensor 27 is formed only in a part of the second openings 8a and 8b.
  • Both ends of the wiring of the temperature sensor 27 can be arranged so that they can be connected to the outside.
  • the configuration other than the protective element portion (including the configuration of the power generation element portion) can be the same as that of the first embodiment.
  • the temperature of the protective element portion can be measured by the temperature sensor 27 formed in the protective element portion.
  • the temperature can be measured, for example, by detecting the resistance value of the wiring of the temperature sensor 27 and converting this resistance value into the temperature of the gas. Abnormalities can be detected by monitoring the temperature of the gas. Also, by monitoring the temperature of the gas, feedback can be given to the adjustment of the pressure, flow rate, and / or temperature of the gas. As a result, stable power generation can be performed.
  • the material of the film of the protective element portion is the same as that of the first embodiment and the film structure is almost the same, the effect as a safety valve against sudden pressure fluctuations of fuel gas and the like is exhibited as in the first embodiment.
  • a flow rate adjusting valve may be provided at the gas inlet into each fuel cell 26 to control the temperature value measured by the temperature sensor 27 so as to be within a certain range.
  • the gas temperature can be measured in a steady state, and when the protective element portion is damaged due to a sudden pressure fluctuation, the wiring of the temperature sensor 27 is broken, so that the damage can be detected. That is, the temperature sensor 27 functions as a detection unit for detecting damage to the protective element unit.
  • a fuel cell system capable of detecting damage to the protective element portion and performing stable power generation output is provided.
  • the temperature sensor 27 is provided in the protective element portion, but other sensors (for example, a pressure sensor using a piezo element, a vibration sensor, etc.) may be provided, and a plurality of sensors may be provided. May be good.
  • the wiring serving as the temperature sensor is formed as the second electrode on the upper side of the electrolyte membrane 5b and 5c, but as a modification, the first electrode 4b and 4c on the lower side of the electrolyte membrane 5b and 5c are formed. It may be formed.
  • FIG. 11 is a plan view of the fuel cell 28 according to the third embodiment of the present invention.
  • FIG. 12 is a cross-sectional view taken along the line DD of FIG.
  • the area of one of the second openings 8a and 8b related to the protective element portion is formed to be substantially the same as the area of one first opening 7 related to the power generation element portion. ing.
  • the area occupied by the protective element portion becomes smaller as compared with the first embodiment, and more power generation element portions can be arranged.
  • the film structure of the protective element portion is different from the film structure of the power generation element portion.
  • the first electrode and the electrolyte membrane are not formed on the protective element portion.
  • a second insulating film 29 is formed in place of the second electrode, and the same temperature sensor 27 as in the second embodiment is arranged on the second insulating film 29.
  • the structure of the second insulating film 29 can be appropriately designed based on the relationship between the area of the opening related to the protective element portion and the membrane withstand voltage. For example, for the second insulating film 29 having various structures, the membrane withstand voltage is measured by changing the area of the opening in various ways so that the withstand voltage strength of the protective element portion is lower than the withstand voltage strength of the power generation element portion. 2 The structure of the insulating film 29 and the area of the opening can be determined.
  • the second insulating film 29 is preferably an insulating film having a tensile stress with respect to the Si substrate, and for example, a silicon nitride film or an aluminum nitride film can be used.
  • the second insulating film 29 may be a laminated film of a film having a tensile stress with respect to the Si substrate and a film having a compressive stress with respect to the Si substrate, for example, a silicon nitride film and boron or phosphorus. It can be a laminated film with a silicon oxide film containing, or it can be a laminated film of a silicon nitride film and a P-TEOS film containing an organic component at a low temperature.
  • the thin film membrane pressure resistance of the second insulating film 29 can be controlled by changing the film thickness, and it is preferable that the membrane pressure resistance is lower than that of the power generation element portion. Therefore, if the membrane withstand voltage is lower than that of the power generation element portion, the area of the second openings 8a and 8b may be smaller than the area of the first opening 7 related to the power generation element portion.
  • the second insulating film may be formed of a thinned electrolyte film, or may be formed by leaving the first insulating film 3.
  • the third embodiment by reducing the area of the opening related to the protective element portion as compared with the first embodiment, more power generation element portions in the fuel cell 28 can be arranged, and the area of the power generation region can be increased. Can be wider. This results in higher power output.
  • FIG. 13 is a plan view of the separator 30 according to the fourth embodiment of the present invention.
  • FIG. 14 is a cross-sectional view taken along the line EE of FIG.
  • the separator 30 according to the fourth embodiment is composed of, for example, a ceramic substrate 31.
  • An upper groove 32 having a gas inlet 32a and a gas discharge port 32b for fuel gas and an upper groove 33 for air gas are formed on the upper surface side of the ceramic substrate 31.
  • a lower groove 34 having an air inlet 34a and an air discharge port 34b and a lower groove 35 for fuel gas are formed on the lower surface side of the ceramic substrate 31.
  • the external dimensions of the separator 30 are almost the same as those of the fuel cell 1.
  • the upper groove 32 of the separator 30 extends to a range including the entire first opening 7 of the fuel cell 1 and the entire second opening 8a when viewed from above. Therefore, when the fuel cell 1 is arranged above and below the separator 30 (for example, as will be described later in relation to FIG. 15), the first fuel cell 1 of the upper fuel cell 1 is passed through the upper groove 32. Gas spreads to the electrode 4a and the first electrode 4b of the upper fuel cell 1.
  • the lower groove 34 of the separator 30 extends to a range including the entire first opening 7 of the fuel cell 1 and the entire second opening 8b when viewed from above. There is. Therefore, when the fuel cell 1 is arranged above and below the separator 30, the second electrode 6a of the lower fuel cell 1 and the lower fuel cell 1 pass through the lower groove 34. Gas spreads to the second electrode 6c.
  • the separator 30 does not have a through hole that penetrates the ceramic substrate 31 up and down, unlike the separator 9 according to the first embodiment. Grooves for supplying fuel gas and air are formed on the upper surface side and the lower surface side of the ceramic substrate 31, respectively. Therefore, each gas is separated and sent to the fuel cell 1.
  • FIG. 15 is a cross-sectional view of the fuel cell module 40 according to the fourth embodiment.
  • the fuel cell module 40 two fuel cell cells 1 are stacked.
  • the separator 30 is laminated between the two fuel cell 1s.
  • An upper substrate 17 and a lower substrate 16 having a gas flow path are provided at the upper end and the lower end of the fuel cell module 40, respectively.
  • the lower substrate 16 and the upper substrate 17 have the same configuration as that of the first embodiment.
  • the fuel gas is divided into a fuel gas 36 and a fuel gas 37.
  • the fuel gas 36 is supplied to the first electrodes 4a and 4b via the plurality of first openings 7 and the second openings 8a.
  • the fuel gas 37 is supplied to the second electrode 6b of the protective element portion.
  • Air is divided into air 38 and air 39.
  • the air 38 is sent to the second electrode 6a of the power generation element portion and the second electrode 6c of the protection element portion.
  • the air 39 is sent to the first electrode 4c of the protective element portion through the second opening 8b.
  • the fuel gas 36 and the air 38 are sent to the power generation element unit to generate electricity.
  • the fuel gas 36 and the fuel gas 37 are sent to the protective element portion, or the air 38 and the air 39 are sent to the protective element portion.
  • the separator 30 since the separator 30 does not have a through hole, even if the protection element portion is damaged due to a sudden pressure fluctuation of fuel gas or air, the broken pieces of the protection element portion are further protected in the vertical direction. It does not scatter to the element part. Therefore, damage to one fuel cell does not affect the other fuel cells. Therefore, a highly reliable fuel cell system can be provided.
  • the pressure of the fuel gas 37 is slightly lower than the pressure of the fuel gas 36 so that the debris does not scatter to the power generation element portion.
  • the pressure of the air 39 is slightly lower than the pressure of the air 38.
  • the present invention is not limited to the above-described embodiments and modifications thereof, and includes various other modifications.
  • the above-described embodiment has been described in detail in order to explain the present invention in an easy-to-understand manner, and the present invention is not necessarily limited to the one including all the described configurations.
  • it is possible to replace a part of the configuration of one embodiment with the configuration of another embodiment and it is also possible to add the configuration of another embodiment to the configuration of one embodiment.

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Abstract

A fuel cell 1, 26, 28 comprises a power-generating element and a protective element. The power-generating element is formed by stacking an electrolyte film 5a and one or more electroconductive films 4a, 6a, and receives supplied fuel gas 18, 36, 37 and air 19, 38, 39 to generate power. A protective film is formed on the protective element, to which only one of the fuel gas 18, 36, 37 and the air 19, 38, 39 is supplied. The compressive strength of the protective element is less than that of the power-generating element.

Description

燃料電池セルおよび燃料電池モジュールFuel cell and fuel cell module

 本発明は、燃料電池セルおよび燃料電池モジュールに関する。 The present invention relates to a fuel cell and a fuel cell module.

 特許文献1には、燃料電池システムにおいて、燃料極と空気極の圧力差を小さくして電解質膜の劣化を抑制することが記載されている。 Patent Document 1 describes that in a fuel cell system, the pressure difference between the fuel electrode and the air electrode is reduced to suppress deterioration of the electrolyte membrane.

 特許文献2には、(110)面を表面とする単結晶シリコン基板に異方性エッチングを施し、電池要素が積層された開口部の断面における基板表面との開口角度をほぼ90°にすることが記載されている。 In Patent Document 2, anisotropic etching is performed on a single crystal silicon substrate having a (110) plane as a surface, so that the opening angle with the substrate surface in the cross section of the opening in which the battery elements are laminated is approximately 90 °. Is described.

特開2017-183033号公報JP-A-2017-183033 特開2004-288382号公報Japanese Unexamined Patent Publication No. 2004-288382

 しかしながら、従来技術では、燃料ガスと酸化剤ガスとの圧力差が急激に変動または過度に増大した場合に、発電素子が破損する可能性があるという課題があった。 However, in the prior art, there is a problem that the power generation element may be damaged when the pressure difference between the fuel gas and the oxidant gas suddenly fluctuates or increases excessively.

 特許文献1の技術は、燃料ガスと酸化剤ガスとの圧力差に対応するための圧力調整装置を設けているが、瞬間的に発生する圧力変動には対応するのが困難である。また、この圧力調整装置は、複数の燃料電池セルスタック間のガス圧差に基づくものであり、単一の燃料電池セルスタック内での圧力差には対応が困難である。 The technology of Patent Document 1 is provided with a pressure adjusting device for dealing with the pressure difference between the fuel gas and the oxidant gas, but it is difficult to deal with the momentary pressure fluctuation. Further, this pressure adjusting device is based on the gas pressure difference between a plurality of fuel cell stacks, and it is difficult to cope with the pressure difference in a single fuel cell stack.

 特許文献2の技術でも、各電解質膜の面積が同一であるため、基板内のいずれかの単セルが破損する可能性がある。また、単セルが破損した場合には、水素と酸素が混合するので好ましくない。 Even in the technique of Patent Document 2, since the area of each electrolyte membrane is the same, there is a possibility that any single cell in the substrate may be damaged. Further, when the single cell is damaged, hydrogen and oxygen are mixed, which is not preferable.

 本発明は、上記のような課題に鑑みてなされたものであり、燃料電池セルに保護素子部を設けることにより、燃料ガスと酸化剤ガスとの圧力差が急激に変動または過度に増大した場合であっても、発電素子部の破損を防止する燃料電池セルおよび燃料電池モジュールを提供することを目的とする。 The present invention has been made in view of the above problems, and when the pressure difference between the fuel gas and the oxidant gas suddenly fluctuates or excessively increases by providing the protective element portion in the fuel cell. However, it is an object of the present invention to provide a fuel cell and a fuel cell module that prevent damage to the power generation element portion.

 本発明に係る燃料電池セルの一例は、
 電解質膜と、1以上の導電膜とが積層して形成され、燃料ガスおよび酸化剤ガスが供給されて発電を行う発電素子部と、
 保護膜が形成され、前記燃料ガスまたは前記酸化剤ガスの一方のみが供給される保護素子部と、
を備え、
 前記発電素子部の耐圧強度より前記保護素子部の耐圧強度のほうが低い
ことを特徴とする。
An example of a fuel cell according to the present invention is
A power generation element unit formed by laminating an electrolyte membrane and one or more conductive films and supplied with a fuel gas and an oxidant gas to generate power.
A protective element portion on which a protective film is formed and only one of the fuel gas or the oxidant gas is supplied.
Equipped with
It is characterized in that the withstand voltage strength of the protection element portion is lower than the withstand voltage strength of the power generation element portion.

 また、本発明に係る燃料電池モジュールの一例は、
 上述の燃料電池セルと、
 前記燃料電池セルに配置され、前記燃料ガスと前記酸化剤ガスとを分離するセパレータと
を備えることを特徴とする。
Further, an example of the fuel cell module according to the present invention is
With the above fuel cell
It is characterized in that it is arranged in the fuel cell and includes a separator that separates the fuel gas and the oxidant gas.

 本発明に係る燃料電池によれば、燃料ガスまたは酸化剤ガスの送気において急激な圧力変動があった場合においても、発電素子への影響を低減でき、燃料電池システムの破損を防止できる。 According to the fuel cell according to the present invention, even when there is a sudden pressure fluctuation in the air supply of the fuel gas or the oxidant gas, the influence on the power generation element can be reduced and the fuel cell system can be prevented from being damaged.

 その他の課題、新規な特徴、構成および効果は、本明細書の記述および添付図面から明らかになるであろう。 Other issues, novel features, configurations and effects will become apparent from the description and accompanying drawings herein.

実施形態1に係る燃料電池セルの平面図である。It is a top view of the fuel cell which concerns on Embodiment 1. FIG. 図1のA-A線に沿った断面図である。It is sectional drawing which follows the AA line of FIG. 図1の燃料電池セルの製造工程を示す断面図である。It is sectional drawing which shows the manufacturing process of the fuel cell of FIG. 図1の燃料電池セルの製造工程を示す断面図である。It is sectional drawing which shows the manufacturing process of the fuel cell of FIG. 図1の燃料電池セルの製造工程を示す断面図である。It is sectional drawing which shows the manufacturing process of the fuel cell of FIG. 図1の燃料電池セルの製造工程を示す断面図である。It is sectional drawing which shows the manufacturing process of the fuel cell of FIG. 開口部面積と薄膜メンブレン耐圧との関係を示す図である。It is a figure which shows the relationship between the opening area and the withstand voltage of a thin film membrane. 実施形態1に係る燃料電池用セパレータの平面図である。It is a top view of the separator for a fuel cell which concerns on Embodiment 1. FIG. 図5のB-B線に沿った断面図である。FIG. 5 is a cross-sectional view taken along the line BB of FIG. 実施形態1に係る燃料電池モジュールの断面図である。It is sectional drawing of the fuel cell module which concerns on Embodiment 1. FIG. 実施の形態1に係る燃料電池システムの概略図である。It is the schematic of the fuel cell system which concerns on Embodiment 1. FIG. 実施形態2に係る燃料電池セルの平面図である。It is a top view of the fuel cell which concerns on Embodiment 2. FIG. 図9のC-C線に沿った断面図である。9 is a cross-sectional view taken along the line CC of FIG. 実施形態3に係る燃料電池セルの平面図である。FIG. 3 is a plan view of the fuel cell according to the third embodiment. 図11のD-D線に沿った断面図である。It is sectional drawing along the DD line of FIG. 実施形態4に係る燃料電池用セパレータの平面図である。It is a top view of the separator for a fuel cell which concerns on Embodiment 4. FIG. 図13のE-E線に沿った断面図である。FIG. 3 is a cross-sectional view taken along the line EE of FIG. 実施形態4に係る燃料電池モジュールの断面図である。It is sectional drawing of the fuel cell module which concerns on Embodiment 4. FIG.

 以下、図面を参照して本発明の実施形態を説明する。実施例は、本発明を説明するための例示であって、説明の明確化のため、適宜、省略および簡略化がなされている。本発明は、他の種々の形態でも実施することが可能である。特に限定しない限り、各構成要素は単数でも複数でも構わない。 Hereinafter, embodiments of the present invention will be described with reference to the drawings. The examples are examples for explaining the present invention, and are appropriately omitted and simplified for the sake of clarification of the description. The present invention can also be implemented in various other forms. Unless otherwise specified, each component may be singular or plural.

 図面において示す各構成要素の位置、大きさ、形状、範囲などは、発明の理解を容易にするため、実際の位置、大きさ、形状、範囲などを表していない場合がある。このため、本発明は、必ずしも、図面に開示された位置、大きさ、形状、範囲などに限定されない。 The position, size, shape, range, etc. of each component shown in the drawings may not represent the actual position, size, shape, range, etc. in order to facilitate understanding of the invention. Therefore, the present invention is not necessarily limited to the position, size, shape, range and the like disclosed in the drawings.

 同一あるいは同様の機能を有する構成要素が複数ある場合には、同一の符号に異なる添字を付して説明する場合がある。また、これらの複数の構成要素を区別する必要がない場合には、添字を省略して説明する場合がある。 If there are multiple components with the same or similar functions, the same code may be described with different subscripts. Further, when it is not necessary to distinguish between these a plurality of components, the subscripts may be omitted in the description.

 本発明は、燃料電池セルおよび燃料電池モジュールに係る。近年、高エネルギー変換が可能であり、かつ炭酸ガスや窒素酸化物などの汚染物質を排出しないクリーンエネルギー源として、燃料電池が注目されている。燃料電池のなかでも、一例として固体電解質型燃料電池(Solid Oxide Fuel Cell。以下、SOFCと略す)は、発電効率が高く、取り扱いが容易な水素、メタン、一酸化炭素などのガスを燃料にできる。このように、SOFCは他の方式の燃料電池と比較して優位な点が多く、省エネ性および環境性に優れたコージェネレーションシステムとして期待されている。 The present invention relates to a fuel cell and a fuel cell module. In recent years, fuel cells have been attracting attention as a clean energy source capable of high energy conversion and not emitting pollutants such as carbon dioxide gas and nitrogen oxides. Among fuel cells, as an example, solid oxide fuel cells (Solid Oxide Fuel Cell, hereinafter abbreviated as SOFC) can use gases such as hydrogen, methane, and carbon monoxide, which have high power generation efficiency and are easy to handle, as fuel. .. As described above, SOFC has many advantages over other types of fuel cells, and is expected as a cogeneration system having excellent energy saving and environmental friendliness.

 SOFCは、固体電解質を燃料極と空気極で挟む構造となっている。電解質が隔壁であり、燃料極に水素などの燃料ガスを供給し、空気極に空気などの酸化剤ガスを供給する。 SOFC has a structure in which a solid electrolyte is sandwiched between a fuel electrode and an air electrode. The electrolyte is a partition wall, and a fuel gas such as hydrogen is supplied to the fuel electrode, and an oxidant gas such as air is supplied to the air electrode.

 以下では、酸化剤ガスの代表として空気を用いているが、空気以外のガスを酸化剤ガスとして用いることも可能である。 In the following, air is used as a representative of the oxidant gas, but it is also possible to use a gas other than air as the oxidant gas.

<実施形態1>
 図1は、本発明の実施形態1に係る燃料電池セル1の平面図である。図2は、図1のA-A線に沿った断面図である。説明の便宜上、図2の紙面上下方向を燃料電池セル1の上下方向とするが、この方向は、燃料電池セルが実際に設置または使用される際の向きとは関係しない。
<Embodiment 1>
FIG. 1 is a plan view of the fuel cell 1 according to the first embodiment of the present invention. FIG. 2 is a cross-sectional view taken along the line AA of FIG. For convenience of explanation, the vertical direction of the paper surface in FIG. 2 is the vertical direction of the fuel cell 1, but this direction has nothing to do with the orientation when the fuel cell is actually installed or used.

 なお、添付図面では、理解を容易にするため、断面でない部分にハッチングを付して示す場合がある。 In the attached drawing, hatching may be added to the part that is not a cross section to facilitate understanding.

 燃料電池セル1は以下の構成を備える。
 ‐単結晶シリコン(Si)からなる半導体基板2(基板)
 ‐半導体基板2上に形成された第1絶縁膜3
 ‐第1絶縁膜3上に形成された発電素子部および保護素子部
The fuel cell 1 has the following configuration.
-Semiconductor substrate 2 (substrate) made of single crystal silicon (Si)
-The first insulating film 3 formed on the semiconductor substrate 2
-The power generation element portion and the protection element portion formed on the first insulating film 3

 発電素子部の構成は公知の構成とすることができるが、一例を以下に説明する。発電素子部は、電解質膜と、1以上の導電膜とが積層して形成されている。本実施形態では、電解質膜は電解質膜5aであり、導電膜は第1電極4aおよび第2電極6aである。発電素子部は、第1絶縁膜3の上に、第1電極4a、電解質膜5a、第2電極6aの順で積層されている。 The configuration of the power generation element unit can be a known configuration, but an example will be described below. The power generation element portion is formed by laminating an electrolyte film and one or more conductive films. In the present embodiment, the electrolyte membrane is the electrolyte membrane 5a, and the conductive film is the first electrode 4a and the second electrode 6a. The power generation element portion is laminated on the first insulating film 3 in the order of the first electrode 4a, the electrolyte film 5a, and the second electrode 6a.

 本実施形態では、2つの燃料電池セル1は2つの保護素子部を備える。保護素子部には保護膜が形成されている。本実施形態では、保護膜は、第1電極4b,4cと、電解質膜5b,5cと、第2電極6b,6cとが積層されて構成されている。 In the present embodiment, the two fuel cell 1s are provided with two protective element units. A protective film is formed on the protective element portion. In the present embodiment, the protective film is configured by laminating the first electrodes 4b and 4c, the electrolyte films 5b and 5c, and the second electrodes 6b and 6c.

 発電素子部および保護素子部は、同一の半導体基板2に形成されている。このような構成によれば製造工程が簡素になる。 The power generation element portion and the protection element portion are formed on the same semiconductor substrate 2. Such a configuration simplifies the manufacturing process.

 半導体基板2は、複数の開口部を備えており、発電素子部および保護素子部は開口部に形成される。複数の開口部は、第1開口部7と、第2開口部8a,8bとを含む。これらの開口部は、上方向からは見えないが、図1の平面図では破線で示す。 The semiconductor substrate 2 has a plurality of openings, and the power generation element portion and the protection element portion are formed in the openings. The plurality of openings include a first opening 7 and second openings 8a, 8b. These openings are not visible from above, but are shown by broken lines in the plan view of FIG.

 発電素子部は複数の第1開口部7にわたって形成される。導電膜(本実施形態では第1電極4aおよび第2電極6a)の少なくとも1つ(本実施形態では双方)は、複数の第1開口部7にわたって連続している。このような構成によれば、導電膜の形成工程が簡素になる。 The power generation element portion is formed over a plurality of first openings 7. At least one of the conductive films (first electrode 4a and second electrode 6a in this embodiment) (both in this embodiment) is continuous over the plurality of first openings 7. With such a configuration, the process of forming the conductive film is simplified.

 また、図2に変形例として示すように、発電素子部の導電膜(本変形例では第1電極4aおよび第2電極6a)のうち1つ(本変形例では第1電極4a)と、保護素子部の導電膜(本変形例では第1電極4c)とが連続しているように構成してもよい。このような変形例によれば、導電膜の形成工程が簡素になる。 Further, as shown in FIG. 2 as a modified example, one of the conductive films of the power generation element portion (first electrode 4a and second electrode 6a in this modified example) (first electrode 4a in this modified example) and protection. It may be configured so that the conductive film of the element portion (the first electrode 4c in this modification) is continuous. According to such a modification, the process of forming the conductive film is simplified.

 2つの保護素子部は、それぞれ第2開口部8aおよび第2開口部8bに形成される。 The two protective element portions are formed in the second opening 8a and the second opening 8b, respectively.

 発電素子部は、燃料ガスおよび空気が供給されて発電を行う。この際に、第1電極4aおよび第2電極6aの一方はアノード電極となり、他方はカソード電極となり、それぞれ外部と接続されて電力を外部に供給する。また、保護素子部の第1電極4bおよび第2電極6bも、外部と接続することができ、第1電極4bと第2電極6bとの間の静電容量または抵抗値を計測できるようになっている。第1電極4cおよび第2電極6cについても同様である。 Fuel gas and air are supplied to the power generation element to generate electricity. At this time, one of the first electrode 4a and the second electrode 6a becomes an anode electrode, and the other becomes a cathode electrode, which are connected to the outside and supply electric power to the outside. Further, the first electrode 4b and the second electrode 6b of the protective element portion can also be connected to the outside, and the capacitance or the resistance value between the first electrode 4b and the second electrode 6b can be measured. ing. The same applies to the first electrode 4c and the second electrode 6c.

 第1開口部7の形状および寸法は任意に設計可能であるが、例えば平面視(図1の向き)で矩形状であり、1辺の長さは約5mmである。第2開口部8a,8bの形状および寸法も任意に設計可能であるが、例えば矩形状であり、1辺の長さは約6mmである。 The shape and dimensions of the first opening 7 can be arbitrarily designed, but for example, it is rectangular in a plan view (direction in FIG. 1), and the length of one side is about 5 mm. The shapes and dimensions of the second openings 8a and 8b can be arbitrarily designed, but are, for example, rectangular and have a side length of about 6 mm.

 各開口部の面積の関係は、発電素子部に係る1つの第1開口部7の面積よりも、保護素子部に係る1つの第2開口部8a(または第2開口部8b)の面積のほうが大きくなっている。ここで、開口部の位置(たとえば深さ位置)によって面積が変化する場合には、面積の測定位置は任意に定義可能である。たとえば、各開口部の下端において面積を測定してもよいし、各開口部の上端において面積を測定してもよい。本実施形態では、これらの測定方法のいずれを用いても、第1開口部7の面積より第2開口部8a(または第2開口部8b)の面積のほうが大きくなっている。 Regarding the relationship of the area of each opening, the area of one second opening 8a (or the second opening 8b) related to the protective element portion is larger than the area of one first opening 7 related to the power generation element portion. It's getting bigger. Here, when the area changes depending on the position of the opening (for example, the depth position), the measurement position of the area can be arbitrarily defined. For example, the area may be measured at the lower end of each opening, or the area may be measured at the upper end of each opening. In the present embodiment, the area of the second opening 8a (or the second opening 8b) is larger than the area of the first opening 7 regardless of which of these measuring methods is used.

 図2に示すように、半導体基板2は、内側が除去された複数の第1開口部7と、1つの第2開口部8aと、1つの第2開口部8bとを有する。半導体基板2の両表面のうち、これらの開口部以外の部分には、第1絶縁膜3が形成されている。第1絶縁膜3上には、第1開口部7、および第2開口部8a、8bを覆うように第1電極4a、4b、4cが形成され、その上に電解質膜5a、5b、5cが形成され、その上に第2電極6a、6b、6cが形成されている。 As shown in FIG. 2, the semiconductor substrate 2 has a plurality of first openings 7 from which the inside has been removed, one second opening 8a, and one second opening 8b. A first insulating film 3 is formed on both surfaces of the semiconductor substrate 2 other than these openings. The first electrodes 4a, 4b, and 4c are formed on the first insulating film 3 so as to cover the first opening 7 and the second openings 8a and 8b, and the electrolyte films 5a, 5b, and 5c are formed on the first electrodes 4a, 4b, and 4c. The second electrodes 6a, 6b, and 6c are formed on the second electrodes 6a, 6b, and 6c.

 したがって、第1開口部7と、第2開口部8aと、第2開口部8bとにおいて、いずれも同一の膜構成による薄膜メンブレン構造が形成されている。すなわち、発電素子部と保護素子部とが同一の膜構成を有する。このような構成によれば、発電素子部および保護素子部の耐圧強度を設計する際の計算処理が簡素になる。なお、ここでいう「膜構成」とは、たとえば各層の組成、厚さおよび積層順を意味し、膜の面積については必ずしも含まない。 Therefore, a thin film membrane structure having the same film structure is formed in the first opening 7, the second opening 8a, and the second opening 8b. That is, the power generation element portion and the protection element portion have the same film configuration. With such a configuration, the calculation process when designing the withstand voltage of the power generation element portion and the protection element portion is simplified. The term "film composition" as used herein means, for example, the composition, thickness and stacking order of each layer, and does not necessarily include the area of the film.

 図3A~図3Dは、燃料電池セル1の製造工程を示す図である。これらの図は、図2に対応する部分の断面図である。まず図3Aに示すように、単結晶Siで、Si<100>の結晶方位からなる半導体基板2を用意する。半導体基板2は、例えば400μm以上の厚みを有している。 3A to 3D are diagrams showing a manufacturing process of the fuel cell 1. These figures are cross-sectional views of a portion corresponding to FIG. First, as shown in FIG. 3A, a semiconductor substrate 2 made of single crystal Si and having a crystal orientation of Si <100> is prepared. The semiconductor substrate 2 has a thickness of, for example, 400 μm or more.

 半導体基板2の表面に第1絶縁膜3を形成する。第1絶縁膜3としては、例えば、引張り応力を有する窒化シリコン膜を、CVD法によって約200nm形成する。CVD法の場合には、半導体基板2の上側および下側に、同じ膜厚の窒化シリコン膜が形成される。 The first insulating film 3 is formed on the surface of the semiconductor substrate 2. As the first insulating film 3, for example, a silicon nitride film having a tensile stress is formed at about 200 nm by a CVD method. In the case of the CVD method, silicon nitride films having the same film thickness are formed on the upper side and the lower side of the semiconductor substrate 2.

 次にスパッタ法により、金属膜(例えば白金(Pt)膜)を約100nmの厚さで形成する。次に、図3Aに示すように、第1電極4a、4b、4cを形成する。これは、ホトリソグラフィ法を用いてパターニングを実施し、アルゴン(Ar)ガスによるドライエッチング法などを用いて行われる。 Next, a metal film (for example, platinum (Pt) film) is formed to a thickness of about 100 nm by a sputtering method. Next, as shown in FIG. 3A, the first electrodes 4a, 4b, and 4c are formed. This is performed by performing patterning using a photolithography method and using a dry etching method using an argon (Ar) gas or the like.

 このとき、Pt膜と第1絶縁膜3との間の接着力を向上させるために、第1絶縁膜3の表面を改質しておくことが望ましい。改質は、たとえば、Pt膜を形成する前に、Arガスによるスパッタエッチングで、第1絶縁膜3の表面をエッチングする(例えば約10~15nmだけエッチングする)ことにより行われる。 At this time, it is desirable to modify the surface of the first insulating film 3 in order to improve the adhesive force between the Pt film and the first insulating film 3. The modification is performed, for example, by etching the surface of the first insulating film 3 (for example, etching by about 10 to 15 nm) by sputtering etching with Ar gas before forming the Pt film.

 あるいは、Pt膜と第1絶縁膜3との間の接着力を向上させるために、接着を手助けするバリア金属膜として、チタン膜(Ti)またはアルミニウム膜(Al)を約2nm形成してもよい。 Alternatively, in order to improve the adhesive force between the Pt film and the first insulating film 3, a titanium film (Ti) or an aluminum film (Al) may be formed at about 2 nm as a barrier metal film that assists the adhesion. ..

 次に、ホトリソグラフィ技術によりネガレジストのパターンを形成する。次に、スパッタ法を用いて、電解質膜として例えばYSZ膜(イットリウムを含んだ酸化ジルコニウム膜)を約500nm形成する。その後、ネガレジストを除去する。これによって、図3Bに示すように、電解質膜5a,5b,5cが形成される。 Next, a negative resist pattern is formed by photolithography technology. Next, using a sputtering method, for example, a YSZ film (zirconium oxide film containing yttrium) as an electrolyte film is formed at about 500 nm. After that, the negative resist is removed. As a result, as shown in FIG. 3B, the electrolyte membranes 5a, 5b, 5c are formed.

 次に、スパッタ法により、Pt膜を約100nm形成する。次に、ホトリソグラフィ法を用いてパターニングを実施し、Arガスによるドライエッチングにより、図3Cに示すように、第2電極6a、6b、6cを形成する。 Next, a Pt film of about 100 nm is formed by a sputtering method. Next, patterning is performed using a photolithography method, and the second electrodes 6a, 6b, and 6c are formed by dry etching with Ar gas, as shown in FIG. 3C.

 次に、図3Dに示すように、ホトリソグラフィ技術と絶縁膜エッチング技術を用いて、半導体基板2の下側の第1絶縁膜3の一部を除去し、半導体基板2の裏面を露出させる。 Next, as shown in FIG. 3D, a part of the first insulating film 3 on the lower side of the semiconductor substrate 2 is removed by using a photolithography technique and an insulating film etching technique to expose the back surface of the semiconductor substrate 2.

 次に、パターニングされた半導体基板2下側表面の第1絶縁膜3をマスクとして、複数の第1開口部7、および第2開口部8a、8bを形成する。これは、たとえば、半導体基板2のSi膜を、KOH(水酸化カリウム)溶液またはTMAH(テトラメチルアミド)溶液によってウェットエッチングし、除去することによって行われる。または、半導体基板2のSi膜を、フッ素系ガスを主成分として用いるドライエッチングにより除去することによって行われる。このようにして、図1および図2に示す燃料電池セル1が形成される。 Next, using the first insulating film 3 on the lower surface of the patterned semiconductor substrate 2 as a mask, a plurality of first openings 7 and second openings 8a and 8b are formed. This is done, for example, by wet-etching and removing the Si film of the semiconductor substrate 2 with a KOH (potassium hydroxide) solution or a TMAH (tetramethylamide) solution. Alternatively, it is performed by removing the Si film of the semiconductor substrate 2 by dry etching using a fluorine-based gas as a main component. In this way, the fuel cell 1 shown in FIGS. 1 and 2 is formed.

 なお、第1電極4a、4b、4cおよび第2電極6a、6b、6cの好適な材料としては、フッ素系の耐薬品性に優れ、抵抗率が低く、且つ融点が使用温度より高い(例えば600℃以上)膜を用いることができる。例えばPt膜であるが、Pt膜以外にも、銀膜(Ag)、ニッケル膜(Ni)、クロム膜(Cr)、パラジウム膜(Pd)、ルテニウム膜(Ru)、ロジウム膜(Rh)などを用いることができる。 As suitable materials for the first electrodes 4a, 4b, 4c and the second electrodes 6a, 6b, 6c, the fluorine-based chemical resistance is excellent, the resistivity is low, and the melting point is higher than the operating temperature (for example, 600). A film (° C or higher) can be used. For example, although it is a Pt film, in addition to the Pt film, a silver film (Ag), a nickel film (Ni), a chromium film (Cr), a palladium film (Pd), a ruthenium film (Ru), a rhodium film (Rh), etc. Can be used.

 また、第1絶縁膜3は、窒化シリコン膜に限られないが、Si基板に対して引張り応力を有する絶縁膜(窒化アルミニウム膜など)とすると好適である。また、第1絶縁膜3は、窒化シリコン膜と、ボロンまたはリンとを含んだシリコン酸化膜であってもよく、低温で有機成分を含んだP-TEOS膜を含む積層膜であってもよい。 Further, the first insulating film 3 is not limited to the silicon nitride film, but it is preferable to use an insulating film (aluminum nitride film or the like) having a tensile stress with respect to the Si substrate. Further, the first insulating film 3 may be a silicon oxide film containing a silicon nitride film and boron or phosphorus, or may be a laminated film containing a P-TEOS film containing an organic component at a low temperature. ..

 図4は、図1の燃料電池セル1について、開口部面積と薄膜メンブレン耐圧との関係を示す図である。矩形の開口部を4つ形成し、それぞれ1辺の長さが3mm(開口面積が9mm)、4mm(開口面積が16mm)、5mm(開口面積が25mm)、6mm(開口面積が36mm)となるようにした。各開口部上に、図2の膜構成の薄膜メンブレンを形成したのち、空気を送気し、薄膜メンブレンが破損する圧力(メンブレン耐圧)を計測した。 FIG. 4 is a diagram showing the relationship between the opening area and the thin film membrane pressure resistance of the fuel cell 1 of FIG. Four rectangular openings are formed, each having a side length of 3 mm (opening area 9 mm 2 ), 4 mm (opening area 16 mm 2 ), 5 mm (opening area 25 mm 2 ), 6 mm (opening area 36 mm). 2 ). After forming a thin film membrane having the film structure shown in FIG. 2 on each opening, air was blown and the pressure at which the thin film membrane was damaged (membrane pressure resistance) was measured.

 図4の結果から、開口部の面積が大きくなるにつれて薄膜メンブレンの耐圧が低下することがわかる。実施形態1では、第2開口部8a,8bの1辺の長さが6mmであるため、保護素子部の耐圧は約25KPaである。一方で、第1開口部7の1辺の長さが5mmであるため、発電素子部の耐圧は約32KPaである。 From the results shown in FIG. 4, it can be seen that the pressure resistance of the thin film membrane decreases as the area of the opening increases. In the first embodiment, since the length of one side of the second openings 8a and 8b is 6 mm, the withstand voltage of the protective element portion is about 25 KPa. On the other hand, since the length of one side of the first opening 7 is 5 mm, the withstand voltage of the power generation element portion is about 32 KPa.

 このように、メンブレン耐圧が異なり、発電素子部の耐圧強度より保護素子部の耐圧強度のほうが低い。すなわち、発電素子部を構成する膜または積層体の強度よりも、保護素子部を構成する膜または積層体の強度のほうが低い。したがって、急激な圧力変動が発生した場合には、発電素子部より先に保護素子部が破損する。なお実施形態1では耐圧強度の比は約1.3となる。 In this way, the withstand voltage of the membrane is different, and the withstand voltage of the protective element is lower than the withstand strength of the power generation element. That is, the strength of the film or laminate constituting the protective element portion is lower than the strength of the film or laminate constituting the power generation element portion. Therefore, when a sudden pressure fluctuation occurs, the protective element portion is damaged before the power generation element portion. In the first embodiment, the ratio of compressive strength is about 1.3.

 図5は、本発明の実施形態1に係るセパレータ9の平面図である。図6は、図5のB-B線に沿った断面図である。セパレータ9は、燃料電池セル1に接して配置される。 FIG. 5 is a plan view of the separator 9 according to the first embodiment of the present invention. FIG. 6 is a cross-sectional view taken along the line BB of FIG. The separator 9 is arranged in contact with the fuel cell 1.

 セパレータ9には、上側溝11および下側溝13が形成されている。上側溝11はセラミック基板10の上面側に形成される。上側溝11は、ガス流入口11aと、ガス排出口11bと、貫通孔12とを備える。貫通孔12は、セラミック基板10を上下に貫通する。 The separator 9 is formed with an upper groove 11 and a lower groove 13. The upper groove 11 is formed on the upper surface side of the ceramic substrate 10. The upper groove 11 includes a gas inflow port 11a, a gas discharge port 11b, and a through hole 12. The through hole 12 penetrates the ceramic substrate 10 up and down.

 下側溝13はセラミック基板10の下面側に形成される。下側溝13は、空気流入口13aと、空気排出口13bと、貫通孔14とを備える。貫通孔14は、セラミック基板10を上下に貫通する。 The lower groove 13 is formed on the lower surface side of the ceramic substrate 10. The lower gutter 13 includes an air inlet 13a, an air discharge port 13b, and a through hole 14. The through hole 14 penetrates the ceramic substrate 10 up and down.

 セパレータ9の外形寸法は、燃料電池セル1の外形寸法とほぼ同等である。本実施形態では、セパレータ9の上側溝11は、上方向から見て、燃料電池セル1の第1開口部7すべての全体と、第2開口部8aの全体とを含む範囲に延在する。このため、セパレータ9の上下にそれぞれ燃料電池セル1が配置された場合(たとえば図7に関連して後述するように)には、上側溝11を介して、上側の燃料電池セル1の第1電極4aと、上側の燃料電池セル1の第1電極4bと、下側の燃料電池セル1の第2電極6bとにガスがいきわたる。 The external dimensions of the separator 9 are almost the same as the external dimensions of the fuel cell 1. In the present embodiment, the upper groove 11 of the separator 9 extends to a range including the entire first opening 7 of the fuel cell 1 and the entire second opening 8a when viewed from above. Therefore, when the fuel cell 1 is arranged above and below the separator 9 (for example, as will be described later in relation to FIG. 7), the first fuel cell 1 of the upper fuel cell 1 is passed through the upper groove 11. Gas spreads to the electrode 4a, the first electrode 4b of the upper fuel cell 1, and the second electrode 6b of the lower fuel cell 1.

 同様に、本実施形態では、セパレータ9の下側溝13は、上方向から見て、燃料電池セル1の第1開口部7すべての全体と、第2開口部8bの全体とを含む範囲に延在する。このため、セパレータ9の上下にそれぞれ燃料電池セル1が配置された場合には、下側溝13を介して、下側の燃料電池セル1の第2電極6aと、下側の燃料電池セル1の第2電極6cと、上側の燃料電池セル1の第1電極4cとにガスがいきわたる。 Similarly, in the present embodiment, the lower groove 13 of the separator 9 extends to a range including the entire first opening 7 of the fuel cell 1 and the entire second opening 8b when viewed from above. There is. Therefore, when the fuel cell 1 is arranged above and below the separator 9, the second electrode 6a of the lower fuel cell 1 and the lower fuel cell 1 pass through the lower groove 13. Gas spreads to the second electrode 6c and the first electrode 4c of the upper fuel cell 1.

 図6に示すように、上側溝11は貫通孔12を含み、あるガスの流路となり、下側溝13は貫通孔14を含み、別のガスの流路となる。ただし、上側溝11と下側溝13とは、セパレータ9の基板で遮蔽されているため、これら2つのガスは混合しない。とくに、貫通孔12は下側溝13とは連通せず、貫通孔14は上側溝11とは連通しないので、燃料ガスと空気は分離されて燃料電池セルに送られる。 As shown in FIG. 6, the upper groove 11 includes a through hole 12 and serves as a flow path for a certain gas, and the lower groove 13 includes a through hole 14 and serves as a flow path for another gas. However, since the upper groove 11 and the lower groove 13 are shielded by the substrate of the separator 9, these two gases are not mixed. In particular, since the through hole 12 does not communicate with the lower groove 13 and the through hole 14 does not communicate with the upper groove 11, the fuel gas and air are separated and sent to the fuel cell.

 このように、セパレータ9は燃料電池セル1に配置され、燃料ガスと空気とを分離する。このような構成によれば、燃料ガスと空気との混合を防止することができる。 In this way, the separator 9 is arranged in the fuel cell 1 to separate the fuel gas and the air. With such a configuration, it is possible to prevent mixing of the fuel gas and air.

 図7は、実施形態1に係る燃料電池モジュール15の断面図である。燃料電池モジュール15は、2つの燃料電池セル1と、1つのセパレータ9とを備える。セパレータ9の上下に、各燃料電池セル1が配置される。 FIG. 7 is a cross-sectional view of the fuel cell module 15 according to the first embodiment. The fuel cell module 15 includes two fuel cell cells 1 and one separator 9. Each fuel cell 1 is arranged above and below the separator 9.

 図7に示すように、燃料電池モジュール15において、燃料電池セル1が2個スタックされる。2つの燃料電池セル1の間にセパレータ9が積層される。燃料電池モジュール15の上端および下端には、それぞれガスの流路を持つ上側基板17および下側基板16が設けられる。 As shown in FIG. 7, in the fuel cell module 15, two fuel cell cells 1 are stacked. The separator 9 is laminated between the two fuel cell 1s. An upper substrate 17 and a lower substrate 16 having a gas flow path are provided at the upper end and the lower end of the fuel cell module 15, respectively.

 なお、下側基板16の流路は、セパレータ9の上側溝11のうち貫通孔12を除く部分と同形状の溝となっている。下側基板16の流路には、ガスの流入および流出を可能にするために、側面に少なくとも2つの開口部が設けられている。同様に、上側基板17の流路は、セパレータ9の下側溝13のうち貫通孔14を除く部分と同形状の溝となっている。上側基板17の流路にも、ガスの流入および流出を可能にするために、側面に少なくとも2つの開口部が設けられている。 The flow path of the lower substrate 16 is a groove having the same shape as the portion of the upper groove 11 of the separator 9 excluding the through hole 12. The flow path of the lower substrate 16 is provided with at least two openings on the side surfaces to allow gas inflow and outflow. Similarly, the flow path of the upper substrate 17 is a groove having the same shape as the portion of the lower groove 13 of the separator 9 excluding the through hole 14. The flow path of the upper substrate 17 is also provided with at least two openings on the side surfaces to allow gas inflow and outflow.

 燃料電池モジュール15は、下側基板16と上側基板17に圧力を加える機構(図示せず)を有している。これによって、燃料ガスと空気とが流れる領域の気密性が保たれ、ガスの混合が防止される。 The fuel cell module 15 has a mechanism (not shown) for applying pressure to the lower substrate 16 and the upper substrate 17. As a result, the airtightness of the region where the fuel gas and the air flow is maintained, and the mixing of the gas is prevented.

 この構造において、図7の紙面右側から燃料ガス18が供給される。燃料ガス18は、次の各電極に達する。
 ‐上の燃料電池セル1の保護素子部の第1電極4bおよび第2電極6b
 ‐上の燃料電池セル1の発電素子部の第1電極4a
 ‐下の燃料電池セル1の保護素子部の第1電極4bおよび第2電極6b
 ‐下の燃料電池セル1の発電素子部の第1電極4a
また、発電で消費された燃料ガス18は、図示しないガス排出口から排出される。
In this structure, the fuel gas 18 is supplied from the right side of the paper in FIG. 7. The fuel gas 18 reaches each of the following electrodes.
-The first electrode 4b and the second electrode 6b of the protective element portion of the fuel cell 1 above.
-First electrode 4a of the power generation element of the fuel cell 1 above
-The first electrode 4b and the second electrode 6b of the protective element portion of the lower fuel cell 1
-First electrode 4a of the power generation element of the lower fuel cell 1
Further, the fuel gas 18 consumed in the power generation is discharged from a gas discharge port (not shown).

 同様に、図7の紙面左側から空気19が供給される。空気19は、次の各電極に達する。
 ‐上の燃料電池セル1の保護素子部の第1電極4cおよび第2電極6c
 ‐上の燃料電池セル1の発電素子部の第2電極6a
 ‐下の燃料電池セル1の保護素子部の第1電極4cおよび第2電極6c
 ‐下の燃料電池セル1の発電素子部の第2電極6a
また、発電で消費された空気19は、図示しないガス排出口から排出される。
Similarly, air 19 is supplied from the left side of the paper in FIG. 7. The air 19 reaches each of the following electrodes.
-The first electrode 4c and the second electrode 6c of the protective element portion of the fuel cell 1 above.
-Second electrode 6a of the power generation element of the fuel cell 1 above
-First electrode 4c and second electrode 6c of the protective element part of the lower fuel cell 1
-Second electrode 6a of the power generation element of the lower fuel cell 1
Further, the air 19 consumed by the power generation is discharged from a gas discharge port (not shown).

 したがって、セパレータ9、下側基板16、上側基板17によって、燃料ガス18および空気19は、分離されたまま供給され、消費され、かつ排出される。なお、図示されていないが、燃料電池モジュール15には、上側基板17と下側基板16との間に圧力が加えられ、燃料ガス18および空気19が漏れないようにされている。 Therefore, the fuel gas 18 and the air 19 are supplied, consumed, and discharged while being separated by the separator 9, the lower substrate 16, and the upper substrate 17. Although not shown, pressure is applied to the fuel cell module 15 between the upper substrate 17 and the lower substrate 16 to prevent the fuel gas 18 and the air 19 from leaking.

 図7では燃料ガス18が紙面右側において上・中・下の3ヶ所から供給されるが、たとえばこのうち中段のみ圧力が急激に上昇したとする。上の燃料電池セル1のうち、発電素子部と右側の保護素子部とが圧力差を受け、下の燃料電池セル1のうち、右側の保護素子部が圧力差を受ける。しかしながら、2つの保護素子部のいずれか(または双方)が、発電素子部よりも先に破損し、これによって段間の圧力差が減少するので、発電素子部の破損は回避される。 In FIG. 7, the fuel gas 18 is supplied from the upper, middle, and lower three places on the right side of the paper, but for example, it is assumed that the pressure rises sharply only in the middle stage. In the upper fuel cell 1, the power generation element portion and the right side protection element portion receive a pressure difference, and in the lower fuel cell 1, the right side protection element portion receives a pressure difference. However, since either (or both) of the two protective element portions are damaged before the power generation element portion, which reduces the pressure difference between the stages, the damage of the power generation element portion is avoided.

 また、上記から明らかなように、発電素子部には燃料ガス18および空気19の双方が供給され、保護素子部には燃料ガス18または空気19の一方のみが供給される。このため、保護素子部は、本実施形態では発電可能な構成を備えているが、図7に示すように、実際には発電しない。このように、保護素子部の動作が発電に影響を与えない構成とすることにより、保護素子部が破損した場合でも、燃料電池セル1の発電動作への影響を回避することができる。また、このような構成は、実施形態1では、セパレータ9が、保護素子部に対応する位置に貫通孔12および14を有することによって実現される。 Further, as is clear from the above, both the fuel gas 18 and the air 19 are supplied to the power generation element portion, and only one of the fuel gas 18 or the air 19 is supplied to the protection element portion. Therefore, although the protective element unit has a configuration capable of generating power in the present embodiment, it does not actually generate power as shown in FIG. 7. As described above, by making the configuration in which the operation of the protective element portion does not affect the power generation, it is possible to avoid the influence on the power generation operation of the fuel cell 1 even if the protective element portion is damaged. Further, in the first embodiment, such a configuration is realized by the separator 9 having through holes 12 and 14 at positions corresponding to the protective element portion.

 燃料電池セル1とセパレータ9との間、燃料電池セル1と上側基板17との間、および/または、燃料電池セル1と下側基板16との間に、耐熱性の良いシール材を用いてもよい。シール材には、圧力を加えられた際に変形する材料を用いると、圧力が加わった際の燃料電池セル1へのダメージを低減することができる。 A heat-resistant sealing material is used between the fuel cell 1 and the separator 9, between the fuel cell 1 and the upper substrate 17, and / or between the fuel cell 1 and the lower substrate 16. May be good. If a material that deforms when pressure is applied is used as the sealing material, damage to the fuel cell 1 when pressure is applied can be reduced.

 なお、実施形態1の燃料電池モジュール15は、燃料電池セル1を2個積層した構造であるが、燃料電池セル1とセパレータ9を交互に重ねることで、より多くの段を積層した構造としてもよい。このようにすると、所望の出力を得ることができる。 The fuel cell module 15 of the first embodiment has a structure in which two fuel cell cells 1 are laminated, but a structure in which more stages are laminated by alternately stacking the fuel cell 1 and the separator 9 is also possible. good. In this way, the desired output can be obtained.

 図8は、実施の形態1に係る燃料電池システムの概略図を示す。燃料電池システムは、主要な構成として、燃料ガス18および空気19を送気するブロア21と、燃料ガスの流量調整機構を有した改質器22と、空気の圧力を調整する圧力調整器23と、燃料電池モジュール15と、燃料電池モジュール15を一定温度(300℃~600℃)に保つための筐体24と、排出した燃料ガスを燃焼させる燃焼器25とを備えている。 FIG. 8 shows a schematic diagram of the fuel cell system according to the first embodiment. The fuel cell system mainly includes a blower 21 for supplying fuel gas 18 and air 19, a reformer 22 having a fuel gas flow rate adjusting mechanism, and a pressure regulator 23 for adjusting the air pressure. The fuel cell module 15 is provided with a housing 24 for keeping the fuel cell module 15 at a constant temperature (300 ° C. to 600 ° C.), and a combustor 25 for burning the discharged fuel gas.

 例えば、燃料ガス18としてメタンを用いることができる。メタンは、ブロア21により送気され、改質器22内にて流量と圧力が調整される。これによって、水素を含む600℃程度の燃料ガスが生成される。燃料ガスは燃料電池モジュール15に送られる。 For example, methane can be used as the fuel gas 18. Methane is supplied by the blower 21 and the flow rate and pressure are adjusted in the reformer 22. As a result, a fuel gas having a temperature of about 600 ° C. containing hydrogen is generated. The fuel gas is sent to the fuel cell module 15.

 また、空気19もブロア21により送気され、圧力調整器23により圧力と流量が調整され、燃料電池モジュール15に送られる。なお、改質器22の熱を利用して、空気の温度も600℃程度にする。 Further, the air 19 is also sent by the blower 21, the pressure and the flow rate are adjusted by the pressure regulator 23, and the air 19 is sent to the fuel cell module 15. The temperature of the air is also set to about 600 ° C. by utilizing the heat of the reformer 22.

 燃料ガスおよび空気の流量は、最大出力時には、例えば数リットル/分と大きくする必要がある。 The flow rate of fuel gas and air needs to be increased to several liters / minute at the maximum output.

 その後、改質後の燃料ガス18と熱せられた空気19とは、配管を通じて約500℃に保たれた筐体24内を通り、燃料電池モジュール15に送られ、発電に消費される。その後、消費された各ガスは、配管を通り燃焼器25で合流し、高温で燃焼し、排出される。 After that, the reformed fuel gas 18 and the heated air 19 pass through the housing 24 kept at about 500 ° C. through piping, are sent to the fuel cell module 15, and are consumed for power generation. After that, each of the consumed gases passes through a pipe, merges with the combustor 25, burns at a high temperature, and is discharged.

 なお、図示していないが、燃料電池モジュール15から排出した燃料ガスおよび空気の配管には、圧力計および流量計が設けられる。これによって、改質器22および圧力調整器23に対してフィードバック制御が行われ、配管内の平均的な圧力および流量が調整される。 Although not shown, a pressure gauge and a flow meter are provided in the fuel gas and air pipes discharged from the fuel cell module 15. As a result, feedback control is performed on the reformer 22 and the pressure regulator 23, and the average pressure and flow rate in the pipe are adjusted.

 筐体24より前の配管において、温度維持は難しいため、燃料電池モジュール15に到達するまでに、熱によるガスの膨張および収縮が発生する場合がある。また、燃料電池セル1に入る部分では配管径が小さく絞られているので、急激且つ瞬間的な圧力変動が発生する場合がある。この傾向は、燃料電池セル1での発電が高効率に行われるほど強く現れ、温度変化による圧力変動がより大きくなる。 Since it is difficult to maintain the temperature in the piping before the housing 24, expansion and contraction of the gas due to heat may occur before reaching the fuel cell module 15. Further, since the pipe diameter is narrowed down in the portion entering the fuel cell 1, sudden and instantaneous pressure fluctuations may occur. This tendency appears more strongly as the power generation in the fuel cell 1 is performed with higher efficiency, and the pressure fluctuation due to the temperature change becomes larger.

 燃料ガス18および空気19の圧力変動は、発電素子部および保護素子部の薄膜メンブレン(第1電極4a,4b,4c、電解質膜5a,5b,5c、第2電極6a,6b,6c)にたわみを生じさせる。なお、この圧力変動は、急激に起こる場合が多く、改質器22および圧力調整器23にフィードバック制御をかけても対応が困難な場合が多い。 The pressure fluctuations of the fuel gas 18 and the air 19 are deflected by the thin film membranes (first electrodes 4a, 4b, 4c, electrolyte membranes 5a, 5b, 5c, second electrodes 6a, 6b, 6c) of the power generation element portion and the protection element portion. Causes. It should be noted that this pressure fluctuation often occurs suddenly, and it is often difficult to deal with it even if feedback control is applied to the reformer 22 and the pressure regulator 23.

 実施形態1の燃料電池セル1では、ガス流入口付近に面積の大きい保護素子部が設けられている。また、保護素子部の耐圧強度は、発電素子部の耐圧強度より低く設定されている。このため、急激な圧力変動が発生した場合には、発電素子部が破損するより先に、保護素子部が破損する。 In the fuel cell 1 of the first embodiment, a protective element portion having a large area is provided near the gas inlet. Further, the withstand voltage strength of the protective element portion is set lower than the withstand voltage strength of the power generation element portion. Therefore, when a sudden pressure fluctuation occurs, the protective element portion is damaged before the power generation element portion is damaged.

 保護素子部が破損することにより、破損した保護素子部を通じたガス流路ができ、これによってガスの流れが分岐するので、圧力差が小さくなり、圧力変動を緩和することができる。したがって、発電素子部への影響が低減され、発電素子部の破損を防止できる。 When the protective element portion is damaged, a gas flow path is created through the damaged protective element portion, which branches the gas flow, so that the pressure difference becomes small and the pressure fluctuation can be mitigated. Therefore, the influence on the power generation element portion is reduced, and damage to the power generation element portion can be prevented.

 なお、セパレータ9の構造によって、保護素子部が破損しても燃料ガス18と空気19が混合することがないので、ガス混合による悪影響を防止することができる。 Note that the structure of the separator 9 prevents the fuel gas 18 and the air 19 from mixing even if the protective element portion is damaged, so that the adverse effects of gas mixing can be prevented.

 このように、実施形態1によれば、保護素子部を設けることにより、燃料ガスと酸化剤ガスとの圧力差が急激に変動または過度に増大した場合であっても、発電素子部の破損を防止することができる。これによって、高信頼かつ高効率の燃料電池システムを提供することができる。 As described above, according to the first embodiment, by providing the protective element portion, even when the pressure difference between the fuel gas and the oxidant gas suddenly fluctuates or increases excessively, the power generation element portion is damaged. Can be prevented. This makes it possible to provide a highly reliable and highly efficient fuel cell system.

 なお、図4に示す開口部面積と薄膜メンブレン耐圧の関係に基づいて、保護素子部の開口面積を設計することにより、圧力変動の限界値を制御することができる。発電素子部の開口面積を変更する場合には、これに応じて保護素子部の開口面積を変更することができる。 The limit value of pressure fluctuation can be controlled by designing the opening area of the protective element portion based on the relationship between the opening area shown in FIG. 4 and the pressure resistance of the thin film membrane. When the opening area of the power generation element portion is changed, the opening area of the protective element portion can be changed accordingly.

 また、保護素子部の第1電極と第2電極との間の静電容量値をモニターすることにより、あるいは、第1電極または第2電極の抵抗値をモニターすることにより、保護素子部の破損を検知することができる。保護素子部の破損が検知された場合には、燃料電池モジュールを安全に停止することができる。停止後は、破損した燃料電池セルのみを交換して、再度発電を行うことができる。このように、メンテナンスが簡単に行える。 Further, the protection element portion is damaged by monitoring the capacitance value between the first electrode and the second electrode of the protection element portion, or by monitoring the resistance value of the first electrode or the second electrode. Can be detected. When damage to the protective element is detected, the fuel cell module can be safely stopped. After the stop, only the damaged fuel cell can be replaced and power can be generated again. In this way, maintenance can be easily performed.

 燃料電池セル1が複数スタックされている場合には、仮に保護素子部の1つが破損しても、発電素子部の構造には影響を与えない。また、実施形態1では、燃料ガスと空気が分離されて流れるので、発電動作を継続することも可能である。 When a plurality of fuel cell 1s are stacked, even if one of the protective element portions is damaged, the structure of the power generation element portion is not affected. Further, in the first embodiment, since the fuel gas and the air flow separately, it is possible to continue the power generation operation.

 実施形態1では、燃料ガスとしてメタンを挙げたが、改質が可能なガスであれば特に限定されない。たとえば、炭化水素燃料として、天然ガス、LPガス、石炭改質ガス、低級炭化水素ガス(エタン、エチレン、プロパン、ブタン)、バイオエタノール、等を用いることができる。なお、改質器22の前段に気化器を設け、気化器によって炭化水素燃料の原料ガス(または液体)から水分を気化させてもよい。 In the first embodiment, methane is mentioned as the fuel gas, but the gas is not particularly limited as long as it can be reformed. For example, as the hydrocarbon fuel, natural gas, LP gas, coal reforming gas, lower hydrocarbon gas (ethane, ethylene, propane, butane), bioethanol and the like can be used. A vaporizer may be provided in front of the reformer 22, and the vaporizer may vaporize water from the raw material gas (or liquid) of the hydrocarbon fuel.

 燃料電池モジュールは、燃料電池セル1を上下に重ねた例を挙げたが、水平方向に並べてもよい。その場合でも、ガスを下から上方向に流すことができる。 Although the example of the fuel cell module in which the fuel cell 1 is stacked one above the other is given, the fuel cell module may be arranged horizontally. Even in that case, the gas can flow from the bottom to the top.

<実施形態2>
 図9は、本発明の実施形態2に係る燃料電池セル26の平面図である。図10は、図9のC-C線に沿った断面図である。保護素子部の第2電極は、温度センサ27として構成される。温度センサ27は、第2開口部8a、8b上に配置される配線とすることができる。実施形態1とは異なり、第2開口部8a、8b上の一部にのみ温度センサ27の配線が形成されている。
<Embodiment 2>
FIG. 9 is a plan view of the fuel cell 26 according to the second embodiment of the present invention. FIG. 10 is a cross-sectional view taken along the line CC of FIG. The second electrode of the protective element portion is configured as a temperature sensor 27. The temperature sensor 27 can be wiring arranged on the second openings 8a and 8b. Unlike the first embodiment, the wiring of the temperature sensor 27 is formed only in a part of the second openings 8a and 8b.

 なお、温度センサ27の配線の両端は、外部と接続できるように配置することができる。燃料電池セル26において、保護素子部以外の構成(発電素子部の構成を含む)は、実施形態1と同一とすることができる。 Both ends of the wiring of the temperature sensor 27 can be arranged so that they can be connected to the outside. In the fuel cell 26, the configuration other than the protective element portion (including the configuration of the power generation element portion) can be the same as that of the first embodiment.

 本実施形態2に係る燃料電池セル26において、保護素子部に形成した温度センサ27により、保護素子部の温度を測定することができる。温度の測定は、たとえば温度センサ27の配線の抵抗値を検出し、この抵抗値をガスの温度に換算することにより行うことができる。ガスの温度を監視することにより異常を検知することができる。また、ガスの温度を監視することにより、ガスの圧力、流量、および/または温度の調整にフィードバックを行うことができる。これによって安定した発電を行うことができる。 In the fuel cell 26 according to the second embodiment, the temperature of the protective element portion can be measured by the temperature sensor 27 formed in the protective element portion. The temperature can be measured, for example, by detecting the resistance value of the wiring of the temperature sensor 27 and converting this resistance value into the temperature of the gas. Abnormalities can be detected by monitoring the temperature of the gas. Also, by monitoring the temperature of the gas, feedback can be given to the adjustment of the pressure, flow rate, and / or temperature of the gas. As a result, stable power generation can be performed.

 なお、保護素子部の膜の材質は実施形態1と同一であり、膜構造もほぼ等しいため、燃料ガス等の急激な圧力変動に対する安全弁としての効果は、実施形態1と同様に発揮される。 Since the material of the film of the protective element portion is the same as that of the first embodiment and the film structure is almost the same, the effect as a safety valve against sudden pressure fluctuations of fuel gas and the like is exhibited as in the first embodiment.

 各燃料電池セル26内へのガス流入口に流量調整弁を設け、温度センサ27によって測定される温度の値が一定範囲内に入るように制御してもよい。たとえば、定常時には、ガス温度の測定を行うことができ、急激な圧力変動によって保護素子部が破損した場合には、温度センサ27の配線が断線するので、破損を検知することができる。すなわち、温度センサ27は、保護素子部の破損を検知する検知部として機能する。これによって、保護素子部の破損を検知することができ、安定した発電出力を行う燃料電池システムが提供される。 A flow rate adjusting valve may be provided at the gas inlet into each fuel cell 26 to control the temperature value measured by the temperature sensor 27 so as to be within a certain range. For example, the gas temperature can be measured in a steady state, and when the protective element portion is damaged due to a sudden pressure fluctuation, the wiring of the temperature sensor 27 is broken, so that the damage can be detected. That is, the temperature sensor 27 functions as a detection unit for detecting damage to the protective element unit. As a result, a fuel cell system capable of detecting damage to the protective element portion and performing stable power generation output is provided.

 なお、実施形態2では、保護素子部に温度センサ27を設けているが、その他のセンサ(例えばピエゾ素子を用いた圧力センサ、振動センサ、など)を設けてもよく、複数のセンサを設けてもよい。また、実施形態2では、温度センサとなる配線を電解質膜5b、5c上側の第2電極として形成しているが、変形例として、電解質膜5b、5cの下側の第1電極4b、4cとして形成してもよい。 In the second embodiment, the temperature sensor 27 is provided in the protective element portion, but other sensors (for example, a pressure sensor using a piezo element, a vibration sensor, etc.) may be provided, and a plurality of sensors may be provided. May be good. Further, in the second embodiment, the wiring serving as the temperature sensor is formed as the second electrode on the upper side of the electrolyte membrane 5b and 5c, but as a modification, the first electrode 4b and 4c on the lower side of the electrolyte membrane 5b and 5c are formed. It may be formed.

<実施形態3>
 図11は、本発明の実施形態3に係る燃料電池セル28の平面図である。図12は、図11のD-D線に沿った断面図である。実施形態3に係る燃料電池セル28において、保護素子部に係る第2開口部8a、8bひとつの面積が、発電素子部に係る第1開口部7ひとつの面積とほぼ同等となるように形成されている。これによって、実施形態1に比較して保護素子部が占める領域が小さくなり、より多くの発電素子部を配置することができる。
<Embodiment 3>
FIG. 11 is a plan view of the fuel cell 28 according to the third embodiment of the present invention. FIG. 12 is a cross-sectional view taken along the line DD of FIG. In the fuel cell 28 according to the third embodiment, the area of one of the second openings 8a and 8b related to the protective element portion is formed to be substantially the same as the area of one first opening 7 related to the power generation element portion. ing. As a result, the area occupied by the protective element portion becomes smaller as compared with the first embodiment, and more power generation element portions can be arranged.

 実施形態3では、保護素子部の膜構造が発電素子部の膜構造とは異なっている。保護素子部には、第1電極および電解質膜が形成されない。また、第2電極に代えて第2絶縁膜29が形成され、その上に実施形態2と同様の温度センサ27が配置されている。 In the third embodiment, the film structure of the protective element portion is different from the film structure of the power generation element portion. The first electrode and the electrolyte membrane are not formed on the protective element portion. Further, a second insulating film 29 is formed in place of the second electrode, and the same temperature sensor 27 as in the second embodiment is arranged on the second insulating film 29.

 第2絶縁膜29の構造は、保護素子部に係る開口部の面積と、メンブレン耐圧との関係に基づいて、適宜設計することができる。たとえば、様々な構造の第2絶縁膜29について、開口部の面積を様々に変化させてメンブレン耐圧を測定し、発電素子部の耐圧強度より保護素子部の耐圧強度のほうが低くなるように、第2絶縁膜29の構造および開口部の面積を決定することができる。 The structure of the second insulating film 29 can be appropriately designed based on the relationship between the area of the opening related to the protective element portion and the membrane withstand voltage. For example, for the second insulating film 29 having various structures, the membrane withstand voltage is measured by changing the area of the opening in various ways so that the withstand voltage strength of the protective element portion is lower than the withstand voltage strength of the power generation element portion. 2 The structure of the insulating film 29 and the area of the opening can be determined.

 第2絶縁膜29は、Si基板に対して引張り応力を有する絶縁膜とすると好適であり、例えば、窒化シリコン膜、または窒化アルミニウム膜などが可能である。または、第2絶縁膜29は、Si基板に対して引っ張り応力を有する膜と、Si基板に対して圧縮応力を有する膜との積層膜としてもよく、例えば、窒化シリコン膜と、ボロンまたはリンとを含んだシリコン酸化膜との積層膜とすることができ、または、窒化シリコン膜と、低温で有機成分を含んだP-TEOS膜との積層膜とすることができる。 The second insulating film 29 is preferably an insulating film having a tensile stress with respect to the Si substrate, and for example, a silicon nitride film or an aluminum nitride film can be used. Alternatively, the second insulating film 29 may be a laminated film of a film having a tensile stress with respect to the Si substrate and a film having a compressive stress with respect to the Si substrate, for example, a silicon nitride film and boron or phosphorus. It can be a laminated film with a silicon oxide film containing, or it can be a laminated film of a silicon nitride film and a P-TEOS film containing an organic component at a low temperature.

 第2絶縁膜29の薄膜メンブレン耐圧は、膜厚を変化させることにより制御することが可能であり、発電素子部よりメンブレン耐圧を低くすると好適である。したがって、メンブレン耐圧が発電素子部より低ければ、第2開口部8a,8bの面積は、発電素子部に係る第1開口部7の面積より小さくてもよい。 The thin film membrane pressure resistance of the second insulating film 29 can be controlled by changing the film thickness, and it is preferable that the membrane pressure resistance is lower than that of the power generation element portion. Therefore, if the membrane withstand voltage is lower than that of the power generation element portion, the area of the second openings 8a and 8b may be smaller than the area of the first opening 7 related to the power generation element portion.

 実施形態3の変形例として、第2絶縁膜は、薄膜化した電解質膜により構成してもよいし、第1絶縁膜3を残すことにより構成してもよい。 As a modification of the third embodiment, the second insulating film may be formed of a thinned electrolyte film, or may be formed by leaving the first insulating film 3.

 実施形態3において、保護素子部に係る開口部の面積を、実施形態1に比べて縮小することにより、燃料電池セル28内の発電素子部をより多く配置することができ、発電領域の面積をより広くすることができる。これによって発電出力がより高くなる。 In the third embodiment, by reducing the area of the opening related to the protective element portion as compared with the first embodiment, more power generation element portions in the fuel cell 28 can be arranged, and the area of the power generation region can be increased. Can be wider. This results in higher power output.

<実施の形態4>
 図13は、本発明の実施形態4に係るセパレータ30の平面図である。図14は、図13のE-E線に沿った断面図である。実施形態4に係るセパレータ30は、例えばセラミック基板31から構成される。セラミック基板31の上面側に、燃料ガス用のガス流入口32aおよびガス排出口32bを有する上側溝32と、空気ガス用の上側溝33とが形成されている。セラミック基板31の下面側に、空気流入口34aおよび空気排出口34bを有する下側溝34と、燃料ガス用の下側溝35とが形成されている。
<Embodiment 4>
FIG. 13 is a plan view of the separator 30 according to the fourth embodiment of the present invention. FIG. 14 is a cross-sectional view taken along the line EE of FIG. The separator 30 according to the fourth embodiment is composed of, for example, a ceramic substrate 31. An upper groove 32 having a gas inlet 32a and a gas discharge port 32b for fuel gas and an upper groove 33 for air gas are formed on the upper surface side of the ceramic substrate 31. A lower groove 34 having an air inlet 34a and an air discharge port 34b and a lower groove 35 for fuel gas are formed on the lower surface side of the ceramic substrate 31.

 実施形態1のセパレータ9と同様に、セパレータ30の外形寸法は、燃料電池セル1とほぼ同等である。本実施形態では、セパレータ30の上側溝32は、上方向から見て、燃料電池セル1の第1開口部7すべての全体と、第2開口部8aの全体とを含む範囲に延在する。このため、セパレータ30の上下にそれぞれ燃料電池セル1が配置された場合(たとえば図15に関連して後述するように)には、上側溝32を介して、上側の燃料電池セル1の第1電極4aと、上側の燃料電池セル1の第1電極4bとにガスがいきわたる。 Similar to the separator 9 of the first embodiment, the external dimensions of the separator 30 are almost the same as those of the fuel cell 1. In the present embodiment, the upper groove 32 of the separator 30 extends to a range including the entire first opening 7 of the fuel cell 1 and the entire second opening 8a when viewed from above. Therefore, when the fuel cell 1 is arranged above and below the separator 30 (for example, as will be described later in relation to FIG. 15), the first fuel cell 1 of the upper fuel cell 1 is passed through the upper groove 32. Gas spreads to the electrode 4a and the first electrode 4b of the upper fuel cell 1.

 同様に、本実施形態では、セパレータ30の下側溝34は、上方向から見て、燃料電池セル1の第1開口部7すべての全体と、第2開口部8bの全体とを含む範囲に延在する。このため、セパレータ30の上下にそれぞれ燃料電池セル1が配置された場合には、下側溝34を介して、下側の燃料電池セル1の第2電極6aと、下側の燃料電池セル1の第2電極6cとにガスがいきわたる。 Similarly, in the present embodiment, the lower groove 34 of the separator 30 extends to a range including the entire first opening 7 of the fuel cell 1 and the entire second opening 8b when viewed from above. There is. Therefore, when the fuel cell 1 is arranged above and below the separator 30, the second electrode 6a of the lower fuel cell 1 and the lower fuel cell 1 pass through the lower groove 34. Gas spreads to the second electrode 6c.

 図14に示すように、実施形態1に係るセパレータ9と異なる点として、セパレータ30は、セラミック基板31を上下に貫通する貫通孔を有しない。セラミック基板31の上面側および下面側に、それぞれ燃料ガスと空気とを隔てて供給する溝が形成される。このため、各ガスが分離されて燃料電池セル1に送気される。 As shown in FIG. 14, the separator 30 does not have a through hole that penetrates the ceramic substrate 31 up and down, unlike the separator 9 according to the first embodiment. Grooves for supplying fuel gas and air are formed on the upper surface side and the lower surface side of the ceramic substrate 31, respectively. Therefore, each gas is separated and sent to the fuel cell 1.

 図15は、実施形態4に係る燃料電池モジュール40の断面図である。燃料電池モジュール40において、燃料電池セル1が2個スタックされる。2つの燃料電池セル1の間にセパレータ30が積層される。燃料電池モジュール40の上端および下端には、それぞれガスの流路を持つ上側基板17および下側基板16が設けられる。なお、下側基板16、上側基板17は、実施形態1と同様の構成を有する。 FIG. 15 is a cross-sectional view of the fuel cell module 40 according to the fourth embodiment. In the fuel cell module 40, two fuel cell cells 1 are stacked. The separator 30 is laminated between the two fuel cell 1s. An upper substrate 17 and a lower substrate 16 having a gas flow path are provided at the upper end and the lower end of the fuel cell module 40, respectively. The lower substrate 16 and the upper substrate 17 have the same configuration as that of the first embodiment.

 この構造において、燃料ガスは、燃料ガス36と燃料ガス37とに分かれる。燃料ガス36は、複数の第1開口部7と、第2開口部8aとを介して、第1電極4a、4bに送気される。燃料ガス37は、保護素子部の第2電極6bに送気される。 In this structure, the fuel gas is divided into a fuel gas 36 and a fuel gas 37. The fuel gas 36 is supplied to the first electrodes 4a and 4b via the plurality of first openings 7 and the second openings 8a. The fuel gas 37 is supplied to the second electrode 6b of the protective element portion.

 空気は、空気38と空気39とに分かれる。空気38は、発電素子部の第2電極6aと、保護素子部の第2電極6cとに送気される。空気39は、第2開口部8bを介して保護素子部の第1電極4cに送気される。 Air is divided into air 38 and air 39. The air 38 is sent to the second electrode 6a of the power generation element portion and the second electrode 6c of the protection element portion. The air 39 is sent to the first electrode 4c of the protective element portion through the second opening 8b.

 したがって、発電素子部には燃料ガス36と空気38が送気され発電がなされる。一方、保護素子部には、燃料ガス36と燃料ガス37が送気されるか、または、空気38と空気39が送気される。 Therefore, the fuel gas 36 and the air 38 are sent to the power generation element unit to generate electricity. On the other hand, the fuel gas 36 and the fuel gas 37 are sent to the protective element portion, or the air 38 and the air 39 are sent to the protective element portion.

 実施形態4では、セパレータ30が貫通孔を有しないので、燃料ガスまたは空気の急激な圧力変動によって保護素子部が破損しても、破損した保護素子部の破片が、上下方向にある別の保護素子部へと飛散することがない。このため、1つの燃料電池セルの破損が他の燃料電池セルに影響を及ぼさない。したがって、信頼性の高い燃料電池システムを提供できる。 In the fourth embodiment, since the separator 30 does not have a through hole, even if the protection element portion is damaged due to a sudden pressure fluctuation of fuel gas or air, the broken pieces of the protection element portion are further protected in the vertical direction. It does not scatter to the element part. Therefore, damage to one fuel cell does not affect the other fuel cells. Therefore, a highly reliable fuel cell system can be provided.

 なお、保護素子部が破損した場合には、破片が発電素子部に飛散しないように、燃料ガス36の圧力より燃料ガス37の圧力が若干低くなるように制御すると好適である。空気についても同様に、空気38の圧力より空気39の圧力を若干低く制御するようにすると好適である。 If the protective element portion is damaged, it is preferable to control the pressure of the fuel gas 37 to be slightly lower than the pressure of the fuel gas 36 so that the debris does not scatter to the power generation element portion. Similarly, for air, it is preferable to control the pressure of the air 39 to be slightly lower than the pressure of the air 38.

<その他の変形例について>
 本発明は、前述した実施形態およびその変形例に限定されるものではなく、他の様々な変形例が含まれる。例えば、上記した実施形態は本発明を分かりやすく説明するために詳細に説明したものであり、本発明は必ずしも説明した全ての構成を備えるものに限定されるものではない。また、ある実施形態の構成の一部を他の実施形態の構成に置き換えることが可能であり、また、ある実施形態の構成に他の実施形態の構成を加えることも可能である。また、各実施形態の構成の一部について、他の構成の追加・削除・置換をすることが可能である。
<About other modifications>
The present invention is not limited to the above-described embodiments and modifications thereof, and includes various other modifications. For example, the above-described embodiment has been described in detail in order to explain the present invention in an easy-to-understand manner, and the present invention is not necessarily limited to the one including all the described configurations. Further, it is possible to replace a part of the configuration of one embodiment with the configuration of another embodiment, and it is also possible to add the configuration of another embodiment to the configuration of one embodiment. Further, it is possible to add / delete / replace a part of the configuration of each embodiment with another configuration.

 1,26,28…燃料電池セル
 2…半導体基板
 3…第1絶縁膜
 4a,4b,4c…第1電極(導電膜)
 5a,5b,5c…電解質膜
 6a,6b,6c…第2電極(導電膜)
 7…第1開口部
 8a,8b…第2開口部
 9,30…セパレータ
 10,31…セラミック基板
 11,32,33…上側溝
 11a,32a…ガス流入口
 11b,32b…ガス排出口
 12,14…貫通孔
 13a,34a…空気流入口
 13b,34b…空気排出口
 13,34,35…下側溝
 15,40…燃料電池モジュール
 16…下側基板
 17…上側基板
 18,36,37…燃料ガス
 19,38,39…空気(酸化剤ガス)
 21…ブロア
 22…改質器
 23…圧力調整器
 24…筐体
 25…燃焼器
 27…温度センサ(検知部)
 29…第2絶縁膜
1, 26, 28 ... Fuel cell 2 ... Semiconductor substrate 3 ... First insulating film 4a, 4b, 4c ... First electrode (conductive film)
5a, 5b, 5c ... Electrolyte film 6a, 6b, 6c ... Second electrode (conductive film)
7 ... 1st opening 8a, 8b ... 2nd opening 9,30 ... Separator 10, 31 ... Ceramic substrate 11, 32, 33 ... Upper groove 11a, 32a ... Gas inlet 11b, 32b ... Gas outlet 12, 14 ... Through holes 13a, 34a ... Air inlet 13b, 34b ... Air outlets 13, 34, 35 ... Lower grooves 15, 40 ... Fuel cell module 16 ... Lower substrate 17 ... Upper substrate 18, 36, 37 ... Fuel gas 19 , 38, 39 ... Air (oxidizing agent gas)
21 ... Blower 22 ... Reformer 23 ... Pressure regulator 24 ... Housing 25 ... Combustor 27 ... Temperature sensor (detector)
29 ... Second insulating film

Claims (10)

 電解質膜と、1以上の導電膜とが積層して形成され、燃料ガスおよび酸化剤ガスが供給されて発電を行う発電素子部と、
 保護膜が形成され、前記燃料ガスまたは前記酸化剤ガスの一方のみが供給される保護素子部と、
を備え、
 前記発電素子部の耐圧強度より前記保護素子部の耐圧強度のほうが低い
ことを特徴とする燃料電池セル。
A power generation element unit formed by laminating an electrolyte membrane and one or more conductive films and supplied with a fuel gas and an oxidant gas to generate power.
A protective element portion on which a protective film is formed and only one of the fuel gas or the oxidant gas is supplied.
Equipped with
A fuel cell cell characterized in that the withstand voltage of the protection element is lower than the withstand strength of the power generation element.
 前記保護素子部は、前記保護素子部の破損を検知する検知部をさらに備える
 ことを特徴とする請求項1記載の燃料電池セル。
The fuel cell according to claim 1, wherein the protective element unit further includes a detection unit that detects damage to the protective element unit.
 前記発電素子部および前記保護素子部は、同一の基板に形成される
 ことを特徴とする請求項1記載の燃料電池セル。
The fuel cell according to claim 1, wherein the power generation element portion and the protection element portion are formed on the same substrate.
 前記発電素子部および前記保護素子部は、基板における複数の開口部に形成され、
 前記発電素子部に係る1つの開口部の面積より、前記保護素子部に係る1つの開口部の面積のほうが大きい、
 ことを特徴とする請求項1記載の燃料電池セル。
The power generation element portion and the protection element portion are formed in a plurality of openings in the substrate, and the power generation element portion and the protection element portion are formed in a plurality of openings in the substrate.
The area of one opening related to the protective element portion is larger than the area of one opening related to the power generation element portion.
The fuel cell according to claim 1.
 前記発電素子部は、基板における複数の開口部に形成され、
 前記発電素子部は、前記導電膜を複数備え、
 前記導電膜の少なくとも1つは、複数の前記開口部にわたって連続している、
ことを特徴とする請求項1記載の燃料電池セル。
The power generation element portion is formed in a plurality of openings in the substrate and is formed.
The power generation element portion includes a plurality of the conductive films, and has a plurality of the conductive films.
At least one of the conductive films is continuous across the plurality of openings.
The fuel cell according to claim 1.
 前記保護素子部は導電膜を備え、
 前記発電素子部の前記導電膜のうち1つと、前記保護素子部の前記導電膜とは連続している、
 ことを特徴とする請求項1記載の燃料電池セル。
The protective element portion is provided with a conductive film and has a conductive film.
One of the conductive films of the power generation element portion and the conductive film of the protective element portion are continuous.
The fuel cell according to claim 1.
 前記発電素子部および前記保護素子部は、同一の膜構成を有する
 ことを特徴とする請求項1記載の燃料電池セル。
The fuel cell according to claim 1, wherein the power generation element portion and the protection element portion have the same film configuration.
 前記保護素子部は発電しないことを特徴とする請求項1記載の燃料電池セル。 The fuel cell according to claim 1, wherein the protective element unit does not generate electricity.  請求項1記載の前記燃料電池セルと、
 前記燃料電池セルに配置され、前記燃料ガスと前記酸化剤ガスとを分離するセパレータと
を備えることを特徴とする燃料電池モジュール。
The fuel cell according to claim 1 and the fuel cell.
A fuel cell module arranged in the fuel cell and comprising a separator for separating the fuel gas and the oxidant gas.
 前記セパレータは、前記保護素子部に対応する位置に貫通孔を有する、
 ことを特徴とする請求項9記載の燃料電池モジュール。
The separator has a through hole at a position corresponding to the protective element portion.
9. The fuel cell module according to claim 9.
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