WO2023200016A1 - 導電部材、電気化学セル装置、モジュールおよびモジュール収容装置 - Google Patents

導電部材、電気化学セル装置、モジュールおよびモジュール収容装置 Download PDF

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Publication number
WO2023200016A1
WO2023200016A1 PCT/JP2023/015252 JP2023015252W WO2023200016A1 WO 2023200016 A1 WO2023200016 A1 WO 2023200016A1 JP 2023015252 W JP2023015252 W JP 2023015252W WO 2023200016 A1 WO2023200016 A1 WO 2023200016A1
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WIPO (PCT)
Prior art keywords
conductive member
electrochemical cell
cell
resistivity
cell stack
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
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PCT/JP2023/015252
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English (en)
French (fr)
Japanese (ja)
Inventor
昌彦 東
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Kyocera Corp
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Kyocera Corp
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Filing date
Publication date
Application filed by Kyocera Corp filed Critical Kyocera Corp
Priority to JP2024515018A priority Critical patent/JP7843343B2/ja
Priority to US18/855,949 priority patent/US20250309481A1/en
Priority to EP23788433.3A priority patent/EP4492507A1/en
Priority to CN202380032853.0A priority patent/CN118985056A/zh
Publication of WO2023200016A1 publication Critical patent/WO2023200016A1/ja
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2465—Details of groupings of fuel cells
    • H01M8/247—Arrangements for tightening a stack, for accommodation of a stack in a tank or for assembling different tanks
    • H01M8/2475—Enclosures, casings or containers of fuel cell stacks
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/50—Current conducting connections for cells or batteries
    • H01M50/502—Interconnectors for connecting terminals of adjacent batteries; Interconnectors for connecting cells outside a battery casing
    • H01M50/503—Interconnectors for connecting terminals of adjacent batteries; Interconnectors for connecting cells outside a battery casing characterised by the shape of the interconnectors
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/20—Mountings; Secondary casings or frames; Racks, modules or packs; Suspension devices; Shock absorbers; Transport or carrying devices; Holders
    • H01M50/204—Racks, modules or packs for multiple batteries or multiple cells
    • H01M50/207—Racks, modules or packs for multiple batteries or multiple cells characterised by their shape
    • H01M50/209—Racks, modules or packs for multiple batteries or multiple cells characterised by their shape adapted for prismatic or rectangular cells
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/50—Current conducting connections for cells or batteries
    • H01M50/502—Interconnectors for connecting terminals of adjacent batteries; Interconnectors for connecting cells outside a battery casing
    • H01M50/507—Interconnectors for connecting terminals of adjacent batteries; Interconnectors for connecting cells outside a battery casing comprising an arrangement of two or more busbars within a container structure, e.g. busbar modules
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/02—Details
    • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0204—Non-porous and characterised by the material
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/02—Details
    • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0204—Non-porous and characterised by the material
    • H01M8/0206—Metals or alloys
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/02—Details
    • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0204—Non-porous and characterised by the material
    • H01M8/0215—Glass; Ceramic materials
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
    • H01M8/124—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte characterised by the process of manufacturing or by the material of the electrolyte
    • H01M8/1246—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte characterised by the process of manufacturing or by the material of the electrolyte the electrolyte consisting of oxides
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/241—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
    • H01M8/2425—High-temperature cells with solid electrolytes
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/50—Fuel cells

Definitions

  • the present disclosure relates to a conductive member, an electrochemical cell device, a module, and a module housing device.
  • a fuel cell is a type of electrochemical cell that can obtain electric power using a fuel gas such as a hydrogen-containing gas and an oxygen-containing gas such as air.
  • a conductive member includes a first portion and a second portion having a different resistivity from the first portion.
  • an electrochemical cell device of the present disclosure includes the electrically conductive member described above and an electrochemical cell connected to the electrically conductive member.
  • the electrochemical cell has a first portion connected to the first portion and a second portion connected to the second portion.
  • the temperature of the first portion is higher than the temperature of the second portion.
  • the resistivity of the first portion is greater than the resistivity of the second portion.
  • a module of the present disclosure includes the electrochemical cell device described above and a storage container that houses the electrochemical cell device.
  • a module housing device of the present disclosure includes the module described above, an auxiliary machine for operating the module, and an exterior case that houses the module and the auxiliary machine.
  • FIG. 1A is a cross-sectional view showing an example of an electrochemical cell according to the first embodiment.
  • FIG. 1B is a side view of an example of the electrochemical cell according to the first embodiment, viewed from the air electrode side.
  • FIG. 1C is a side view of an example of the electrochemical cell according to the first embodiment, viewed from the interconnector side.
  • FIG. 2A is a perspective view showing an example of the electrochemical cell device according to the first embodiment.
  • FIG. 2B is a cross-sectional view taken along line XX shown in FIG. 2A.
  • FIG. 2C is a top view showing an example of the electrochemical cell device according to the first embodiment.
  • FIG. 3 is an enlarged cross-sectional view of the electrochemical cell device according to the first embodiment.
  • FIG. 4 is a cross-sectional view showing an example of a conductive member included in the electrochemical cell device according to the first embodiment.
  • FIG. 5 is a cross-sectional view taken along line AA shown in FIG.
  • FIG. 6A is a cross-sectional view showing an example of a conductive member included in the electrochemical cell device according to the first embodiment.
  • FIG. 6B is a cross-sectional view showing another example of a conductive member included in the electrochemical cell device according to the first embodiment.
  • FIG. 6C is a cross-sectional view showing another example of a conductive member included in the electrochemical cell device according to the first embodiment.
  • FIG. 6D is a cross-sectional view showing another example of a conductive member included in the electrochemical cell device according to the first embodiment.
  • FIG. 5 is a cross-sectional view taken along line AA shown in FIG.
  • FIG. 6A is a cross-sectional view showing an example of a conductive member included in the electrochemical cell device according to the
  • FIG. 7 is an external perspective view showing an example of the module according to the first embodiment.
  • FIG. 8 is an exploded perspective view schematically showing an example of the module housing device according to the first embodiment.
  • FIG. 9 is an enlarged cross-sectional view of the electrochemical cell device according to the second embodiment.
  • FIG. 10 is a top view showing an example of an electrochemical cell device according to the third embodiment.
  • FIG. 11 is a perspective view showing an example of an electrochemical cell included in the electrochemical cell device according to the fourth embodiment.
  • FIG. 12 is a perspective view showing an example of temperature distribution in a flat plate electrochemical cell.
  • FIG. 13 is a longitudinal sectional view showing an example of a conductive member included in the electrochemical cell device according to the fourth embodiment.
  • FIG. 14 is a longitudinal cross-sectional view showing an example of a conductive member included in the electrochemical cell device according to the fifth embodiment.
  • FIG. 15A is a cross-sectional view showing an example of an electrochemical cell included in the electrochemical cell device according to the sixth embodiment.
  • FIG. 15B is a cross-sectional view showing another example of an electrochemical cell included in the electrochemical cell device according to the sixth embodiment.
  • FIG. 15C is a cross-sectional view showing another example of an electrochemical cell included in the electrochemical cell device according to the sixth embodiment.
  • FIG. 16 is a diagram comparing the durability of electrochemical cell devices.
  • drawings are schematic and the dimensional relationship of each element, the ratio of each element, etc. may differ from reality. Furthermore, drawings may include portions that differ in dimensional relationships, ratios, and the like.
  • the electrochemical cell device may include a cell stack having multiple electrochemical cells.
  • An electrochemical cell device having multiple electrochemical cells is simply referred to as a cell stack device.
  • FIG. 1A is a cross-sectional view showing an example of an electrochemical cell according to an embodiment
  • FIG. 1B is a side view of an example of an electrochemical cell according to an embodiment, viewed from the air electrode side
  • FIG. 1C is a cross-sectional view showing an example of an electrochemical cell according to an embodiment
  • FIG. 3 is a side view of an example of an electrochemical cell according to the embodiment, viewed from the interconnector side. Note that FIGS. 1A to 1C show enlarged portions of each structure of the electrochemical cell.
  • the electrochemical cell may be simply referred to as a cell.
  • the cell 1 is a hollow flat plate and has an elongated plate shape.
  • the shape of the entire cell 1 when viewed from the side has, for example, a side length in the length direction L of 5 cm to 50 cm, and a length in the width direction W perpendicular to the length direction L. is, for example, a rectangle with a size of 1 cm to 10 cm.
  • the overall thickness of this cell 1 in the thickness direction T is, for example, 1 mm to 5 mm.
  • the cell 1 includes a conductive support substrate 2, an element section 3, and an interconnector 4.
  • the support substrate 2 has a columnar shape having a pair of opposing flat surfaces n1 and n2 and a pair of arcuate side surfaces m connecting the flat surfaces n1 and n2.
  • the element section 3 is provided on the flat surface n1 of the support substrate 2.
  • the element section 3 includes a fuel electrode layer 5, a solid electrolyte layer 6, and an air electrode layer 8.
  • the interconnector 4 is located on the flat surface n2 of the cell 1.
  • the cell 1 may include an intermediate layer 7 between the solid electrolyte layer 6 and the air electrode layer 8.
  • the air electrode layer 8 does not extend to the lower end of the cell 1.
  • the solid electrolyte layer 6 is exposed on the surface of the flat surface n1.
  • the interconnector 4 may extend to the lower end of the cell 1.
  • the interconnector 4 and the solid electrolyte layer 6 are exposed to the surface.
  • the solid electrolyte layer 6 is exposed on the surface of the pair of arcuate side faces m of the cell 1.
  • the interconnector 4 does not have to extend to the lower end of the cell 1.
  • the support substrate 2 has a gas passage 2a inside thereof through which gas flows.
  • the example of the support substrate 2 shown in FIG. 1A has six gas flow paths 2a.
  • the support substrate 2 has gas permeability and allows the fuel gas flowing through the gas flow path 2 a to pass through to the fuel electrode layer 5 .
  • the support substrate 2 may be electrically conductive.
  • the conductive support substrate 2 collects electricity generated in the element section 3 to the interconnector 4 .
  • the material of the support substrate 2 includes, for example, an iron group metal component and an inorganic oxide.
  • the iron group metal component may be, for example, Ni (nickel) and/or NiO.
  • the inorganic oxide may be, for example, a specific rare earth element oxide.
  • the rare earth element oxide may contain one or more rare earth elements selected from, for example, Sc, Y, La, Nd, Sm, Gd, Dy, and Yb.
  • the fuel electrode layer 5 may be made of a porous conductive ceramic, such as a ceramic containing calcium oxide, magnesium oxide, or ZrO 2 in which a rare earth element oxide is dissolved as a solid solution, and Ni and/or NiO.
  • This rare earth element oxide may include a plurality of rare earth elements selected from, for example, Sc, Y, La, Nd, Sm, Gd, Dy, and Yb.
  • ZrO 2 containing calcium oxide, magnesium oxide, or rare earth element oxide as a solid solution is sometimes referred to as stabilized zirconia.
  • Stabilized zirconia may include partially stabilized zirconia.
  • the solid electrolyte layer 6 is an electrolyte and transfers ions between the fuel electrode layer 5 and the air electrode layer 8. At the same time, the solid electrolyte layer 6 has gas barrier properties, making it difficult for fuel gas and oxygen-containing gas to leak.
  • the material of the solid electrolyte layer 6 may be, for example, ZrO 2 in which 3 mol % to 15 mol % of rare earth element oxide, calcium oxide, and magnesium oxide are solidly dissolved.
  • the rare earth element oxide may contain one or more rare earth elements selected from, for example, Sc, Y, La, Nd, Sm, Gd, Dy, and Yb.
  • the solid electrolyte layer 6 may include, for example, CeO 2 in which La, Nd, Sm, Gd or Yb is dissolved in solid solution, BaZrO 3 in which Sc or Yb is dissolved in solid solution, BaCeO in which Sc or Yb is dissolved in solid solution. 3 may be included.
  • the air electrode layer 8 has gas permeability.
  • the open porosity of the air electrode layer 8 may be in the range of, for example, 20% to 50%, particularly 30% to 50%.
  • the material for the air electrode layer 8 is not particularly limited as long as it is commonly used for air electrodes.
  • the material of the air electrode layer 8 may be, for example, a conductive ceramic such as a so-called ABO 3 perovskite oxide.
  • the material of the air electrode layer 8 may be, for example, a composite oxide in which Sr (strontium) and La (lanthanum) coexist at the A site.
  • composite oxides include La x Sr 1-x Co y Fe 1-y O 3 , La x Sr 1-x MnO 3 , La x Sr 1-x FeO 3 , La x Sr 1-x Examples include CoO3 . Note that x is 0 ⁇ x ⁇ 1, and y is 0 ⁇ y ⁇ 1.
  • the intermediate layer 7 has a function as a diffusion suppressing layer.
  • an element such as Sr (strontium) contained in the air electrode layer 8 diffuses into the solid electrolyte layer 6, an electrical resistance layer such as SrZrO 3 is formed in the solid electrolyte layer 6.
  • the intermediate layer 7 makes it difficult for Sr to diffuse, thereby making it difficult for SrZrO 3 and other electrically insulating oxides to be formed.
  • the material for the intermediate layer 7 is not particularly limited as long as it generally makes it difficult for elements to diffuse between the air electrode layer 8 and the solid electrolyte layer 6.
  • the material of the intermediate layer 7 may include, for example, cerium oxide (CeO 2 ) in which a rare earth element other than Ce (cerium) is dissolved.
  • CeO 2 cerium oxide
  • rare earth elements for example, Gd (gadolinium), Sm (samarium), etc. may be used.
  • the interconnector 4 is dense and prevents leakage of the fuel gas flowing through the gas flow path 2a located inside the support substrate 2 and the oxygen-containing gas flowing outside the support substrate 2.
  • the interconnector 4 may have a relative density of 93% or more, in particular 95% or more.
  • a lanthanum chromite-based perovskite oxide (LaCrO 3 -based oxide), a lanthanum strontium titanium-based perovskite oxide (LaSrTiO 3 -based oxide), or the like may be used. These materials have electrical conductivity and are not easily reduced or oxidized even when they come into contact with fuel gas such as hydrogen-containing gas and oxygen-containing gas such as air. Furthermore, the interconnector 4 may be made of metal or an alloy.
  • FIG. 2A is a perspective view showing an example of the electrochemical cell device according to the first embodiment
  • FIG. 2B is a cross-sectional view taken along line XX shown in FIG. 2A
  • FIG. 2C is a perspective view showing an example of the electrochemical cell device according to the first embodiment
  • FIG. 2 is a top view showing an example of an electrochemical cell device according to the embodiment.
  • the cell stack device 10 includes a cell stack 11 having a plurality of cells 1 arranged (stacked) in the thickness direction T of the cells 1 (see FIG. 1A), and a fixing member 12.
  • the fixing member 12 includes a fixing member 13 and a support member 14.
  • the support member 14 supports the cell 1.
  • the fixing member 13 fixes the cell 1 to the support member 14 .
  • the support member 14 includes a support body 15 and a gas tank 16.
  • the support body 15 and the gas tank 16, which are the support members 14, are made of metal and have electrical conductivity, for example.
  • the cell stack device 10 may include a fixing member 12a positioned opposite the fixing member 12 with the cell stack 11 in between.
  • the fixing member 12 fixes the lower end of the cell 1
  • the fixing member 12a fixes the upper end of the cell 1. Note that in FIGS. 2A to 2C, illustration of the fixing member 12a is omitted.
  • the support body 15 has an insertion hole 15a into which the lower end portions of the plurality of cells 1 are inserted.
  • the lower ends of the plurality of cells 1 and the inner wall of the insertion hole 15a are joined with a fixing material 13.
  • the gas tank 16 has an opening for supplying reaction gas to the plurality of cells 1 through the insertion hole 15a, and a groove 16a located around the opening. An end of the outer periphery of the support body 15 is joined to the gas tank 16 by a joining material 21 filled in the groove 16a of the gas tank 16.
  • fuel gas is stored in the internal space 22 formed by the support body 15, which is the support member 14, and the gas tank 16.
  • a gas flow pipe 20 is connected to the gas tank 16.
  • the fuel gas is supplied to the gas tank 16 through the gas distribution pipe 20, supplied from the gas tank 16 to the gas passage 2a (see FIG. 1A) inside the cell 1, and discharged from the upper end side of the cell 1.
  • the fuel gas supplied to the gas tank 16 is generated in a reformer 102 (see FIG. 7), which will be described later.
  • the cell stack device 10 includes the fixing member 12a
  • the fuel gas discharged from the upper end side of the cell 1 to the fixing member 12a may be further discharged and processed from a gas exhaust pipe (not shown), or may be sent to the reformer again. It may be supplied to the cell stack 11 or a cell stack different from the cell stack 11 through the cell stack 11 .
  • Hydrogen-rich fuel gas can be produced by steam reforming raw fuel.
  • fuel gas is generated by steam reforming, the fuel gas contains steam.
  • the example shown in FIG. 2A has two rows of cell stacks 11 and support members 14.
  • the support member 14 includes two supports 15 and a gas tank 16.
  • Each of the two rows of cell stacks 11 has a plurality of cells 1 .
  • Each cell stack 11 is fixed to each support 15.
  • the gas tank 16 has two through holes on its upper surface.
  • Each support body 15 is arranged in each through hole.
  • Internal space 22 is formed by one gas tank 16 and two supports 15.
  • the support member 14a may include two supports and a gas tank like the support member 14.
  • FIG. 2A shows the cell stack device 10 having two rows of cell stacks 11, the cell stack device may have one row of cell stacks 11, or may have three or more rows of cell stacks 11. Good too.
  • the shape of the insertion hole 15a is, for example, an oval shape when viewed from above.
  • the length of the insertion hole 15a in the arrangement direction of the cells 1, that is, the thickness direction T is larger than the distance between the two end current collecting members 17 located at both ends of the cell stack 11.
  • the width of the insertion hole 15a is, for example, larger than the length of the cell 1 in the width direction W (see FIG. 1A).
  • the joint between the inner wall of the insertion hole 15a and the lower end of the cell 1 is filled with the fixing material 13 and solidified.
  • the inner wall of the insertion hole 15a and the lower end portions of the plurality of cells 1 are respectively joined and fixed, and the lower end portions of the cells 1 are joined and fixed to each other.
  • the gas flow path 2a of each cell 1 communicates with the internal space 22 of the support member 14 at its lower end.
  • materials with low conductivity such as glass can be used.
  • amorphous glass or the like may be used, and in particular, crystallized glass or the like may be used.
  • crystallized glass examples include SiO 2 -CaO system, MgO-B 2 O 3 system, La 2 O 3 -B 2 O 3 -MgO system, La 2 O 3 -B 2 O 3 -ZnO system, SiO 2 -CaO--ZnO-based materials may be used, and in particular, SiO 2 -MgO-based materials may be used.
  • a conductive member 18 is interposed between adjacent cells 1 among the plurality of cells 1.
  • the conductive member 18 electrically connects the fuel electrode layer 5 of one adjacent cell 1 and the air electrode layer 8 of the other cell 1 in series. More specifically, the conductive member 18 connects the interconnector 4, which is electrically connected to the fuel electrode layer 5 of one adjacent cell 1, and the air electrode layer 8 of the other cell 1.
  • the interconnector 4 is made of metal or an alloy, the interconnector 4 and the conductive member 18 may be integrated, or the conductive member 18 may also serve as the interconnector 4. Note that details of the conductive member 18 will be described later.
  • the end current collecting member 17 is electrically connected to the outermost cell 1 in the arrangement direction of the plurality of cells 1.
  • the end current collecting member 17 is connected to a conductive portion 19 protruding to the outside of the cell stack 11 .
  • the conductive part 19 collects electricity generated by the power generation of the cell 1 and draws it to the outside. Note that in FIG. 2A, illustration of the end current collecting member 17 is omitted.
  • the conductive portion 19 of the cell stack device 10 is divided into a positive terminal 19A, a negative terminal 19B, and a connection terminal 19C.
  • the positive electrode terminal 19A is a positive electrode for outputting the electric power generated by the cell stack 11 to the outside, and is electrically connected to the end current collecting member 17 on the positive electrode side of the cell stack 11A.
  • the negative electrode terminal 19B is a negative electrode for outputting the electric power generated by the cell stack 11 to the outside, and is electrically connected to the end current collecting member 17 on the negative electrode side of the cell stack 11B.
  • connection terminal 19C electrically connects the negative end current collecting member 17 of the cell stack 11A and the positive end current collecting member 17 of the cell stack 11B.
  • FIG. 3 is an enlarged cross-sectional view of the electrochemical cell device according to the first embodiment.
  • the cell stack device 10 shown in FIG. 3 corresponds to an enlarged view of the cell stack 11 included in the cell stack device 10 shown in FIG. 2B.
  • the cell 1, the conductive member 18, etc. are shown in a simplified manner. Further, in other drawings to be described later, constituent elements may be illustrated in a simplified manner.
  • a conductive member 18 extending in the length direction is located between adjacent cells 1 in the thickness direction T.
  • the cell 1 has a gas flow path 2a through which gas flows.
  • the gas flow path 2a has a supply port two a1 and a discharge port two a2.
  • the fuel gas stored in the internal space 22 is supplied to the supply port two a1.
  • the exhaust port 2a2 exhausts fuel gas from inside the cell 1.
  • variations in temperature may occur during power generation. Specifically, the temperature of the portion 1a of the cell 1 closer to the discharge port 2a2 side increases than that of the portion 1b of the cell 1 closer to the supply port 2a1 side. Therefore, in the portion 1a of the cell 1, for example, the temperature becomes higher than the temperature suitable for power generation, and the durability tends to decrease.
  • temperature variations are reduced by applying a conductive member 18 having a first portion 181 and a second portion 182 having different electrical resistivities between cells 1 adjacent in the thickness direction T.
  • the conductive member 18 is positioned such that the first portion 181 is connected to the portion 1a and the second portion 182 is connected to the portion 1b.
  • the electrical resistivity of the first portion 181 is greater than the electrical resistivity of the second portion 182.
  • electrical resistivity may be simply referred to as resistivity, and electrical resistance may simply be referred to as resistance.
  • the amount of current applied to the first portion 181 is lower than that of the second portion 182, and resistance heating in the first portion 181 is suppressed.
  • the temperature rise in the first portion 181 and the portion 1a of the cell 1 connected thereto is lower than that in the second portion 181 and the portion 1b of the cell 1 connected thereto. Therefore, according to this embodiment, the durability of the conductive member 18 and the cell stack device 10 is increased.
  • the first portion 181 may be the end of the conductive member 18 on the discharge port side
  • the second portion 182 may be the end of the conductive member 18 on the supply port side.
  • the first portion 181 is located 1/3 away from the end of the conductive member 18 on the discharge port side.
  • the second portion 182 may be a portion 1/3 away from the end of the conductive member 18 on the supply port side.
  • the electrical resistance of the first portion 181 located between the cells 1A and 1B may be greater than the electrical resistance of the second portion 182 located between the cells 1A and 1B by, for example, 0.05 ⁇ or more. Since the difference between the electrical resistance of the first portion 181 and the electrical resistance of the second portion 182 is 0.05 ⁇ or more, the amount of current applied to the first portion 181 is reduced, resistance heating in the first portion 181 is reduced, and the conductive member 18 and the durability of the cell stack device 10 are increased.
  • the half of the conductive member 18 located on the discharge port side may be the first portion 181, and the half located on the supply port side may be the second portion 182.
  • a portion from the end of the conductive member 18 on the discharge port side to 1/3 is defined as the first portion 181.
  • the second portion 182 may be a portion up to 1 ⁇ 3 from the end of the conductive member 18 on the supply port side.
  • the resistivity of the first portion 181 may be greater than the resistivity of the second portion 182 by 0.8 ⁇ m or more.
  • the resistivity of the first portion 181 is greater than the resistivity of the second portion 182 by 0.8 ⁇ m or more, the amount of current flowing through the first portion 181 is significantly reduced.
  • the resistivity may be an average value obtained by measuring, for example, three or more points at each location.
  • FIG. 4 is a cross-sectional view showing an example of a conductive member included in the electrochemical cell device according to the first embodiment.
  • the conductive member 18 has a connecting portion 18a connected to one cell 1, ie, cell 1A, among adjacent cells 1, and a connecting portion 18a, connected to the other cell 1, ie, cell 1B. 18b. Further, the conductive member 18 has connecting portions 18c at both ends in the width direction W, and connects the connecting portions 18a and 18b. Thereby, the conductive member 18 can electrically connect cells 1 adjacent to each other in the thickness direction T.
  • connecting portions 18a, 18b have contact portions 18a1, 18b1 that contact the cells 1A, 1B, and non-contact portions 18a2, 18b2 that do not contact the cells 1A, 1B.
  • FIG. 5 is a cross-sectional view taken along line AA shown in FIG. 4.
  • the conductive member 18 extends in the length direction L of the cell 1.
  • the conductive member 18 has a comb-like shape when viewed in cross section, and the connecting portions 18a and 18b extend alternately from the connecting portion 18c toward the cells 1A and 1B.
  • FIG. 6A is a cross-sectional view showing an example of a conductive member included in the electrochemical cell device according to the first embodiment.
  • the conductive member 18 may include a base material 180 and a coating 30 that covers the base material 180.
  • the base material 180 has electrical conductivity and heat resistance.
  • Base material 180 contains chromium.
  • Base material 180 is, for example, stainless steel.
  • the base material 180 may contain, for example, a metal oxide.
  • the coating 30 has electrical insulation or low conductivity.
  • the coating 30 contains, for example, chromium oxide (Cr 2 O 3 ), aluminum oxide (Al 2 O 3 ), a composite oxide containing Al and/or Si, and the like.
  • the conductive member 18 shown in FIG. 6A has a first portion 181 and a second portion 182 having different resistivities by making the thickness of the coating 30 different. That is, the resistivity of the first portion 181, where the coating 30 is thicker than the second portion 182, is greater than the resistivity of the second portion 182.
  • 6B to 6D are cross-sectional views showing another example of a conductive member included in the electrochemical cell device according to the first embodiment.
  • the conductive member 18 may have a base material 180 and a coating 31 that covers the base material 180.
  • the coating 31 has electrical conductivity.
  • the coating 31 contains, for example, a conductive metal material and/or a metal oxide.
  • the conductive member 18 may have a first portion 181 and a second portion 182 having different resistivities by making the thickness of the coating 31 different. That is, the resistivity of the second portion 182, where the coating 31 is thicker than the first portion 181, is smaller than the resistivity of the first portion 181.
  • the conductive metal oxide contained in the film 31 is , for example, a complex oxide having a spinel structure, such as Zn( CoxMn1 -x ) 2O4 (0 ⁇ x ⁇ 1) such as ZnMnCoO4 , Mn 1.5 Co 1.5 O 4 , MnCo 2 O 4 , CoMn 2 O 4 , etc. may be used.
  • the electrically conductive metal oxide may be a so-called ABO 3 perovskite oxide.
  • the conductive member 18 may include both the coating 30 and the coating 31 having higher conductivity than the coating 30.
  • the conductive member 18 may have, for example, a coating 30 that covers the base material 180 and a coating 31 that further covers the coating 30.
  • the thickness of the coating 30 in the second portion 182 may be smaller than that in the first portion 181.
  • the thickness of the coating 31 in the second portion 182 may be greater than that in the first portion 181.
  • the conductive member 18 may have a base material 180 and coatings 32 and 33 that cover the base material 180.
  • the coatings 32 and 33 have conductivity or insulation. Coating 32 may have higher insulating properties than coating 33. Further, the coating 33 may have higher conductivity than the coating 32.
  • the conductive member 18 may have a first portion 181 and a second portion 182 having different resistivities by using different materials for the coatings 32 and 33. That is, the resistivity of the second portion 182 having the coating 33 having lower insulation or higher conductivity than the coating 32 is smaller than the resistivity of the first portion 181.
  • the coatings 32 and 33 may be made of the same material with different porosity. If the porosity of the coating 32 is greater than the porosity of the coating 33, the coating 32 will have higher insulating properties than the coating 33. If the porosity of coating 32 is greater than the porosity of coating 33, coating 32 will have lower conductivity than coating 33.
  • the material of the coatings 32 and 33 may be the same material as that contained in the coatings 30 and 31.
  • the conductive member 18 may have portions 180a and 180b where the base material 180 is made of different materials. Portion 180b has higher conductivity than portion 180a. As a result, the resistivity of the second portion 182 becomes smaller than the resistivity of the first portion 181.
  • the conductive member 18 included in the electrochemical cell device may be manufactured by any method.
  • the films 30 and 31 shown in FIGS. 6A and 6B may be formed, for example, by changing the number of coatings and/or the concentration of the dip liquid in a dip method, or by changing the film forming electrode in an electrodeposition or plating method. It may also be formed by Further, the coatings 32 and 33 shown in FIG. 6C may be formed, for example, by changing the type of dipping liquid in a dipping method. Further, the conductive member 18 shown in FIG. 6D may be formed by, for example, welding or joining.
  • FIG. 7 is an external perspective view showing the module according to the first embodiment.
  • FIG. 7 shows a state in which the front and rear surfaces, which are part of the storage container 101, are removed and the fuel cell cell stack device 10 housed inside is taken out rearward.
  • the module 100 includes a storage container 101 and a cell stack device 10 housed within the storage container 101. Further, above the cell stack device 10, a reformer 102 is arranged.
  • the reformer 102 generates fuel gas by reforming raw fuel such as natural gas or kerosene, and supplies the fuel gas to the cell 1.
  • Raw fuel is supplied to the reformer 102 through a raw fuel supply pipe 103.
  • the reformer 102 may include a vaporizing section 102a that vaporizes water, and a reforming section 102b.
  • the reforming section 102b includes a reforming catalyst (not shown), and reformes the raw fuel into fuel gas.
  • Such a reformer 102 can perform steam reforming, which is a highly efficient reforming reaction.
  • the fuel gas generated in the reformer 102 is supplied to the gas flow path 2a of the cell 1 (see FIG. 1A) through the gas distribution pipe 20 and the fixing member 12.
  • the temperature inside the module 100 during normal power generation is about 500° C. to 1000° C. due to combustion of gas, power generation of the cell 1, etc.
  • the module 100 can have high durability.
  • FIG. 8 is an exploded perspective view showing an example of the module housing device according to the first embodiment.
  • the module housing device 110 includes an exterior case 111, the module 100 shown in FIG. 7, and auxiliary equipment not shown.
  • the auxiliary equipment operates the module 100.
  • the module 100 and auxiliary equipment are housed in an exterior case 111. Note that in FIG. 8, some configurations are omitted.
  • the exterior case 111 of the module housing device 110 shown in FIG. 8 includes a support 112 and an exterior plate 113.
  • the partition plate 114 divides the interior of the exterior case 111 into upper and lower sections.
  • the space above the partition plate 114 in the exterior case 111 is a module storage chamber 115 that accommodates the module 100, and the space below the partition plate 114 in the exterior case 111 accommodates auxiliary equipment that operates the module 100.
  • This is the auxiliary equipment storage chamber 116. Note that, in FIG. 8, the auxiliary equipment accommodated in the auxiliary equipment storage chamber 116 is omitted.
  • the partition plate 114 has an air flow port 117 for flowing air from the auxiliary equipment storage chamber 116 to the module storage chamber 115 side.
  • the exterior plate 113 configuring the module storage chamber 115 has an exhaust port 118 for exhausting the air inside the module storage chamber 115 .
  • the module accommodating device 110 by providing the highly durable modules 100 in the module accommodating chamber 115 as described above, the module accommodating device 110 can have high durability.
  • FIG. 9 is an enlarged cross-sectional view of the electrochemical cell device according to the second embodiment.
  • the cell stack device 10 shown in FIG. 9 has a first conductive member 18A and a second conductive member 18B having different resistivities as the conductive members 18, which is different from the cell stack device 10 according to the first embodiment described above. This is different from the conductive member 18.
  • the resistivity of the second conductive member 18B is smaller than the resistivity of the first conductive member 18A, and the first conductive member 18A and the second conductive member 18B are respectively arranged between adjacent cells 1.
  • the temperature rise in the first conductive member 18A and the portion 1a of the cell 1 is reduced. Ru. Therefore, according to the electrochemical cell device according to this embodiment, the durability of the conductive member 18 and the cell stack device 10 is increased.
  • the first conductive member 18A and the second conductive member 18B can be manufactured, for example, in accordance with the first portion 181 and the second portion 182 shown in FIGS. 6A to 6D, respectively. Further, the first conductive member 18A and the second conductive member 18B may be in contact with each other or may be separated from each other. When the first conductive member 18A and the second conductive member 18B are spaced apart, the current flowing through the first conductive member 18A can be further reduced, which increases the durability of the conductive member 18 and the cell stack device 10.
  • FIG. 10 is a top view showing an example of an electrochemical cell device according to the third embodiment.
  • the cell stack device 10 shown in FIG. 10 has a cell stack 11 including a plurality of cells 1 arranged in the thickness direction T (first direction).
  • the cell stack 11 includes a cell stack 11A (first cell stack) and a cell stack 11B (second cell stack) that are adjacent to each other in the width direction W (second direction) of the cell 1.
  • heat generated during power generation may be trapped between the cell stacks 11A and 11B, causing variations in temperature within the cell stack device 10.
  • the temperature of the portion 11Aa of the cell stack 11A that is closer to the cell stack 11B is higher than that of the portion 11Ab that is farther from the cell stack 11B. Therefore, in the portion 11Aa, for example, the temperature becomes higher than the temperature suitable for power generation, and the durability tends to decrease.
  • a conductive member 18 having a first portion 181 and a second portion 182 having different resistivities depending on the distance from the cell stack 11B is applied between the cells 1 included in the cell stack 11A. This may reduce temperature variations.
  • the conductive member 18 is positioned such that the first portion 181 is connected to the cell 1 located in the portion 11Aa, and the second portion 182 is connected to the cell 1 located in the portion 11Ab.
  • the resistivity of the first portion 181 is greater than the resistivity of the second portion 182.
  • the electrochemical cell device As a result, the amount of current is reduced in the portion 11Aa having the cell 1 connected to the first portion 181 than in the portion 11Ab having the cell 1 connected to the second portion 182, and in the first conductive member 18A and the portion 11Aa. temperature rise is reduced. Therefore, according to the electrochemical cell device according to this embodiment, the durability of the conductive member 18 and the cell stack device 10 is increased.
  • FIG. 11 is a perspective view showing an example of an electrochemical cell included in the electrochemical cell device according to the fourth embodiment.
  • the cell 1 shown in FIG. 11 is a flat electrochemical cell having an element part 3B and conductive members 91 and 92 sandwiching the element part 3B.
  • the element section 3B includes a solid electrolyte layer (for example, solid electrolyte layer 6), a first electrode layer (for example, fuel electrode layer 5) and a second electrode layer (for example, air electrode layer 8) that sandwich the solid electrolyte layer.
  • the conductive members 91 and 92 have channels 97 and 98, respectively, through which the reaction gas flows, and are sealed with a seal member (not shown) or the like.
  • FIG. 12 is a plan view showing an example of temperature distribution in a flat plate electrochemical cell.
  • a separator 40 in contact with conductive members 91 and 92 is located around the element portion 3B.
  • the surface 3a of the element part 3B facing the conductive member 91 or 92 has a high temperature at the part near the center P1 of the element part 3B when the cell 1 is generating electricity, and the surface 3a is concentrically shaped toward the outer edge away from the center P1. Temperature decreases.
  • FIG. 13 is a longitudinal cross-sectional view showing an example of a conductive member included in the electrochemical cell device according to the fourth embodiment.
  • a conductive member 91 of one cell 1 adjacent to each other and a conductive member 92 of another cell 1 are electrically connected via an interconnector 93 which is a conductive member. It is connected.
  • the conductive members 91 and 92 and the interconnector 93 located between the element portions 3B may be collectively referred to as the conductive member 18.
  • the temperature in the vicinity of the center P1 of the element portion 3B which is at a high temperature during power generation, is difficult to decrease, so that the temperature within the cell stack device 10 may vary.
  • the temperature of the portion of the cell 1 that is closer to the center P1 of the element portion 3B increases than the outer edge side that is farther from the center P1 of the element portion 3B, and for example, becomes higher than the temperature suitable for power generation. , durability tends to decrease.
  • a conductive member 18 having a first portion 181 and a second portion 182 having different resistivities depending on the distance from the center P1 is applied between the element portions 3B of the cell stack device 10B. By doing so, variations in temperature may be reduced.
  • the first portion 181 is connected to the first electrode layer of the element portion 3B near the center P1
  • the second portion 182 is connected to the first electrode layer of the element portion 3B distant from the center P1.
  • the conductive member 18 is positioned.
  • the resistivity of the first portion 181 is greater than the resistivity of the second portion 182.
  • the electrochemical cell device As a result, the amount of current is reduced in the part having the element part 3B connected to the first part 181 than in the part having the element part 3B connected to the second part 182, and The temperature rise in the area is reduced. Therefore, according to the electrochemical cell device according to this embodiment, the durability of the conductive member 18 and the cell stack device 10B is increased.
  • the conductive members 91, 92 and the interconnector 93 were collectively described as the conductive member 18 in the above, the interconnector 93, which is different from the conductive members 91, 92, is applied as a third conductive member, and the conductive members 91, 92 may be connected in parallel.
  • FIG. 14 is a longitudinal cross-sectional view showing an example of a conductive member included in the electrochemical cell device according to the fifth embodiment.
  • the cell stack device 10C may include a first conductive member 18A and a second conductive member 18B having different resistivities as the conductive members 18.
  • the resistivity of the second conductive member 18B is smaller than the resistivity of the first conductive member 18A, and the first conductive member 18A and the second conductive member 18B are respectively arranged between adjacent cells 1.
  • the first conductive member 18A and the second conductive member 18B having different resistivities are used as the conductive member 18, the temperature will rise in the first conductive member 18A and the portion of the cell 1 connected thereto. is reduced. Therefore, according to the electrochemical cell device according to this embodiment, the durability of the conductive member 18 and the cell stack device 10C is increased.
  • FIG. 15A is a cross-sectional view showing an example of an electrochemical cell included in the electrochemical cell device according to the sixth embodiment.
  • 15B and 15C are cross-sectional views showing other examples of electrochemical cells included in the electrochemical cell device according to the sixth embodiment.
  • the cell 1 includes an element section 3C in which a fuel electrode layer 5, a solid electrolyte layer 6, an intermediate layer 7, and an air electrode layer 8 are laminated, and a support substrate 2.
  • the support substrate 2 has a through hole or pore at a portion of the element portion 3C that contacts the fuel electrode layer 5, and also has a member 120 located outside the gas flow path 2a.
  • the support substrate 2 can allow gas to flow between the gas flow path 2a and the element section 3C.
  • Support substrate 2 may include, for example, one or more metal plates.
  • the material of the metal plate may contain chromium.
  • the metal plate may have a conductive coating layer.
  • the support substrate 2 is a conductive member that electrically connects adjacent cells 1 to each other.
  • the element portion 3C may be directly formed on the support substrate 2, or may be bonded to the support substrate 2 with a bonding material.
  • the side surface of the fuel electrode layer 5 is covered with a solid electrolyte layer 6, and the gas flow path 2a through which the fuel gas flows is hermetically sealed.
  • the side surface of the fuel electrode layer 5 may be covered and sealed with a dense sealing material 9 containing glass or ceramic.
  • the sealing material 9 covering the side surface of the fuel electrode layer 5 may have electrical insulation properties.
  • gas flow path 2a of the support substrate 2 may be formed of a member 120 having unevenness as shown in FIG. 15C.
  • the member 120 is joined to the air electrode layer 8 of another adjacent cell 1 via another conductive member such as an inter-cell connecting member and a bonding material. Note that the member 120 may be in direct contact with the air electrode layer 8 of another cell 1 without using another conductive member or the like.
  • the support substrate 2 has a first portion 181 and a second portion 182 having different resistivities.
  • the support substrate 2 has a first portion 181 located in the high temperature portion 1a of the cell 1, and a second portion 182 located in the high temperature portion 1a of the cell 1. It may be located in the portion 1b of the cell 1 where the temperature is relatively low. Since the resistivity of the first portion 181 is greater than the resistivity of the second portion 182, the portion 1a of the cell 1 connected to the first portion 181 is more energized than the portion 1b connected to the second portion 182. The temperature increase in the first portion 181 and the portion 1a is reduced.
  • the durability of the support substrate 2 (conductive member 18) and the cell stack device 10 is increased.
  • the portion 1a of the cell 1 that becomes high temperature is shown as a portion near the center of the element portion 3C as in the second embodiment, but for example, as in the first embodiment, A portion close to the fuel gas outlet side may be the portion 1a of the cell 1 that becomes high temperature.
  • a cell stack device 10 (cell stack 11) shown in FIG. 5 was manufactured.
  • the size of the cell 1 was a hollow flat plate of 170 mm (length direction L) x 27 mm (width direction W) x 2.3 mm (thickness direction T).
  • the shape of the conductive member 18 was a comb shape shown in FIGS. 4 and 5, and the first portion 181 and the second portion 182 had the same shape.
  • the conductive member 18 has a contact area between the cell 1 and the connecting parts 18a and 18b of 21 mm x 0.8 mm x 60 pieces, of which the first portion 181 has 30 pieces and the second portion 182 has 30 pieces. It was made in pieces.
  • the conductive member 18 shown in FIG. 6A was used.
  • the number of cells 1 included in the cell stack 11 was set to 32, and the temperature difference in the cell 1 located at the center of the cell stack 11 was evaluated.
  • the temperature of the cell 1 is determined based on the length l in the length direction L of the conductive member 18, with the first portion 181 being a position approximately 1/3 away from the end on the discharge port side, and the end on the supply port side being the first portion 181.
  • a position approximately 1/3 away from the second part 182 was defined as the second part 182, and thermocouples were placed in each part of the cell 1 corresponding to the first part 181 and the second part 182, respectively.
  • Example 2 The temperature difference in the cell 1 located at the center of the cell stack 11 was fabricated in the same manner as in Experimental Example 1 except that the cell stack device 10 shown in FIG. 9 was used instead of the cell stack device 10 shown in FIG. evaluated.
  • Example 4 A cell stack device 10B shown in FIG. 13 was manufactured.
  • the size of cell 1 was 200 mm x 200 mm x 3.2 mm.
  • the shape of the conductive member 18 was such that the first portion 181 (140 mm x 140 mm) and the second portion 182 (the remaining portion excluding the first portion 181) had the same contact area.
  • the number of cells 1 included in the cell stack device 10B was set to 20, and the temperature difference was evaluated in the cell 1 located at the center of the cell stack device 10B. Note that the temperature of the cell 1 was measured by placing thermocouples at a portion 30 mm away from the center P1 and a portion 80 mm away from the center P, respectively.
  • ⁇ Experiment example 5> In place of the cell stack device 10B shown in FIG. 13, a cell stack device 10C shown in FIG. 14 was manufactured in the same manner as in Experimental Example 4, and the temperature difference was evaluated in the cell 1 located in the center of the cell stack device 10C.
  • FIG. 16 is a diagram comparing the durability of electrochemical cell devices.
  • An accelerated test was performed when the temperature of the fuel gas supplied into the cell was set to 950°C, 900°C, and 850°C, and the time required for the voltage drop to reach 10% from the initial value was determined for each test temperature. I measured it. Specifically, the current density of each cell stack device set at each test temperature was adjusted to 0.4 A/cm 2 , and the temperature of each cell stack device was lowered from the test temperature to 750°C every 100 hr to adjust the voltage. Measurements were taken. After measuring the voltage, each cell stack device was set to the test temperature again and the accelerated test was continued.
  • the acceleration coefficient is calculated from the time it takes for the measured voltage to drop to a value 10% lower than the initial value, and when the voltage is continuously operated at 750°C, the voltage drops to a value 10% lower than the initial value.
  • durability time we estimated the time it would take to do so (durability time).
  • relative values of durability time based on Experimental Example 3 and Experimental Example 6 were calculated to evaluate durability.
  • both Experimental Examples 1 and 2 had improved durability compared to Experimental Example 3.
  • the durability was improved compared to Experimental Example 6.
  • the conductive member 18 according to each embodiment has improved durability, and the cell stack using the conductive member 18 also has improved durability.
  • a fuel cell, a fuel cell stack device, a fuel cell module, and a fuel cell device are used as examples of a “battery chemical cell,” a “battery chemical cell device,” a “module,” and a “module housing device.”
  • a battery chemical cell a “battery chemical cell”
  • a “battery chemical cell device” a “module”
  • a “module housing device” a “module housing device.”
  • other examples may be an electrolytic cell, an electrolytic cell stack device, an electrolytic module, and an electrolytic device, respectively.
  • the electrolytic cell has a first electrode layer and a second electrode layer, and decomposes water vapor into hydrogen and oxygen or decomposes carbon dioxide into carbon monoxide and oxygen by supplying electric power. According to such an electrolytic cell, an electrolytic cell stack device, an electrolytic module, and an electrolytic device, durability becomes high.
  • the conductive member 18 includes the first portion 181 and the second portion 182 having a different resistivity from the first portion 181. This makes it possible to provide the conductive member 18 with high durability.
  • the electrochemical cell device (eg, cell stack device 10) of the present disclosure includes the electrically conductive member 18 described above and an electrochemical cell (eg, cell 1) connected to the electrically conductive member 18.
  • the electrochemical cell has a first portion (eg, portion 1a) connected to a first portion 181 and a second portion (eg, portion 1b) connected to a second portion 182.
  • the temperature of the first portion is higher than the temperature of the second portion, and the resistivity of the first portion 181 is greater than the resistivity of the second portion 182. This makes it possible to provide an electrochemical cell device with high durability.
  • the electrochemical cell device for example, cell stack device 10C
  • the electrochemical cell device includes a solid electrolyte layer, an electrochemical cell (for example, cell 1), a first conductive member 18A, and a second conductive member 18B.
  • the second conductive member 18B is spaced apart from the first conductive member 18A.
  • the resistivity of the first conductive member 18A is different from the resistivity of the second conductive member 18B. This makes it possible to provide an electrochemical cell device with high durability.
  • the module 100 of the present disclosure includes the electrochemical cell device described above and a storage container 101 that houses the electrochemical cell device. This allows the module 100 to have high durability.
  • the module housing device 110 of the present disclosure includes the module 100 described above, an auxiliary machine for operating the module 100, and an exterior case 111 that houses the module 100 and the auxiliary machine. This allows the module housing device 110 to have high durability.

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PCT/JP2023/015252 2022-04-15 2023-04-14 導電部材、電気化学セル装置、モジュールおよびモジュール収容装置 Ceased WO2023200016A1 (ja)

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US18/855,949 US20250309481A1 (en) 2022-04-15 2023-04-14 Electrically conductive member, electrochemical cell device, module, and module housing device
EP23788433.3A EP4492507A1 (en) 2022-04-15 2023-04-14 Electroconductive member, electrochemical cell device, module, and module accommodation device
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