WO2018167845A1 - Planar electrochemical cell stack - Google Patents
Planar electrochemical cell stack Download PDFInfo
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- WO2018167845A1 WO2018167845A1 PCT/JP2017/010210 JP2017010210W WO2018167845A1 WO 2018167845 A1 WO2018167845 A1 WO 2018167845A1 JP 2017010210 W JP2017010210 W JP 2017010210W WO 2018167845 A1 WO2018167845 A1 WO 2018167845A1
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- electrochemical cell
- separator
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- cell stack
- stack
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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
- H01M8/02—Details
- H01M8/0271—Sealing or supporting means around electrodes, matrices or membranes
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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
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
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- 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
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
-
- 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
- Embodiments of the present invention relate to a flat electrochemical cell stack.
- Fuel cells that convert chemical energy to electrical energy by electrochemically reacting hydrogen and oxygen are drawing attention. Fuel cells have high energy use efficiency and are being developed as large-scale distributed power sources, household power sources, and mobile power sources.
- Fuel cells are classified into solid polymer type, phosphoric acid type, molten carbonate type, solid oxide type, etc., depending on the temperature range and the type of material and fuel used.
- SOFC solid oxide fuel cell
- a high-temperature steam electrolysis method in which hydrogen is produced by a solid oxide electrolysis cell (SOEC) by utilizing the reverse reaction of SOFC has been developed.
- a cell which is the minimum constituent unit of SOFC and SOEC, is generally composed of an electrolyte and an electrode.
- the solid oxide electrolyte has oxygen ion conductivity.
- the electrolyte of the solid oxide for example, dense stabilized zirconia, perovskite oxide, a ceria-based solid solution molded body, or the like is used.
- the electrode taking SOFC as an example, it can be roughly divided into a fuel electrode and an air electrode.
- H 2 that is the fuel gas and oxygen ions that have moved through the electrolyte react electrochemically to generate H 2 O and electrons (e ⁇ ).
- oxygen in the air takes in electrons (e ⁇ ), generates oxygen ions by an electrochemical reaction, and these move to the electrolyte.
- a mixed sintered body (cermet) of metal and solid oxide is generally used for the fuel electrode.
- Ni—YSZ yttria stabilized zirconia
- Ni—ScSZ scandia stabilized zirconia
- a perovskite oxide or an oxide obtained by substituting a part of these sites is generally used for the air electrode.
- LaSrMn oxide, LaSrCo oxide, LaSrCoFe oxide, LaSrFe oxide, and the like can be given.
- a mixture with a solid oxide used for the electrolyte is also used, and examples thereof include LSM-YSZ, LSM-ScSZ, LSC-SDC, and LSC-GDC.
- the cell is at least a laminate of an air electrode, an electrolyte, and a fuel electrode.
- Different materials are used for the air electrode, the electrolyte, and the fuel electrode.
- the air electrode and the fuel electrode are porous, and different gases are supplied to the air electrode and the fuel electrode with a dense electrolyte as a boundary.
- the air electrode and the fuel electrode are electrical conductors, and the electrolyte is an ionic conductor that does not conduct electricity.
- the cell shape includes a flat plate type, a cylindrical type, and a cylindrical flat plate type.
- a flat cell has a shape in which an air electrode, an electrolyte, a fuel electrode, and the like are stacked in a flat plate shape.
- a collection of a plurality of these cells is generally called a stack.
- the stack is a stack of multiple flat cells, supplying different gases to the air electrode and fuel electrode of each cell, and the cells can be connected electrically in series. It has a simple structure.
- the cells are separated from each other by a separator, and the gas for each cell is separated by the separator. Since the separator is conductive, it also plays a role of electrical conduction between cells.
- a gas supply / discharge flow path to each cell is generally formed in the separator.
- the cell portion separates the fuel electrode and the air electrode by a dense electrolyte, while the other portions separate the atmosphere of adjacent cells by a dense separator. Further, the atmosphere of the fuel electrode and the air electrode of the same cell is isolated by closing a gap in a portion where the cell is not installed with a dense member.
- the gas flowing in the stack is prevented from flowing out of the stack, the supply gas to the fuel electrode and the air electrode is prevented from mixing inside the stack, that is, the gas sealing property is improved. It has become a big issue.
- methods using various sealing materials have been proposed.
- the cell Since the cell has a dense electrolyte, it is possible to prevent mixing of the atmospheric gas in each of the fuel electrode and the air electrode. However, it is necessary to take measures against gas leakage in the stack components other than the cells. For example, it is necessary to seal a gap between a cell and a stack constituent member other than the cell, or a portion that supplies gas to the cell.
- the problem to be solved by the present invention is to provide a flat plate electrochemical cell stack with improved gas sealability.
- the flat plate electrochemical cell stack includes a flat solid oxide electrochemical cell and a conductive separator surrounding the electrochemical cell, and a plurality of stacked unit electrochemical cells; A frame-shaped seal portion disposed between the separator of the unit electrochemical cell and the separator of the adjacent unit electrochemical cell and surrounding the periphery of the electrochemical cell; and the separator of the unit electrochemical cell And an insulating part that is disposed between the separators of the adjacent unit electrochemical cells and that is at least partially positioned on the outer peripheral side of the seal part and is thinner than the seal part.
- FIG. 1 is a diagram schematically illustrating a partial cross-sectional configuration of a flat plate electrochemical cell stack (hereinafter simply referred to as a stack) 100 according to an embodiment.
- a stack a flat plate electrochemical cell stack
- each component is shown in a disassembled state (with a space between the components) (the same applies to FIGS. 3 to 6 described later), but these components are stacked. It is integrally held under pressure.
- the flat cell 101 constituting the stack 100 is an electrode-supported flat electrochemical cell.
- the cell 101 has a laminated structure in which an electrolyte 103 made of a thin film is formed on a porous electrode support 102 and a counter electrode 104 is further formed on the electrolyte 103.
- the electrode support 102 or the counter electrode 104 is a fuel electrode, and the other is an air electrode.
- Conductive separators 105 and 106 are provided so as to surround the periphery of the cell 101, and the cell 101 is accommodated and supported in these. Between the electrode support 102 and the separator 106, a current collector (not shown) that electrically connects them is disposed. Further, a current collector (not shown) that electrically connects them is disposed between the counter electrode 104 and the adjacent separator 106.
- the material of the separators 105 and 106 is a material that is dense and has conductivity even in the temperature range of 600 to 1000 ° C. that is the operating temperature, such as metal or ceramics. Moreover, as this material, a material having a thermal expansion coefficient close to that of the cell 101 is desirable.
- the separator is configured by two separators 105 and 106 which are separate members will be described. However, the separators 105 and 106 may be formed as a single member.
- the outer shape of the flat cell 101 is, for example, a quadrangular shape.
- the separator 105 is configured in a rectangular frame shape so as to surround the periphery of the cell 101.
- a square opening 105a is formed at the center of the separator 105, and the cell 101 is disposed in the opening 105a.
- the outer shape of the separator 106 is, for example, a rectangular plate shape. Further, the separator 105 and the separator 106 are formed with through holes at corresponding positions, and a gas flow path 109 for flowing gas in the stacking direction is formed by these through holes.
- the separator 105 and the separator 106 constitute a support body that accommodates and supports the cell 101 in the opening 105a.
- These separators 105 and 106 and cell 101 constitute one unit chemical cell 110.
- a plurality of these unit chemical cells 110 are stacked, and end plates 120 and the like are arranged at both end portions (upper end portion and lower end portion in FIG. 2) in the stacking direction. These are fastened and fixed by fastening means such as a plurality of bolts 111 and nuts 112.
- fastening means such as a plurality of bolts 111 and nuts 112.
- a sheet-like insulating member 107 formed in a frame shape is provided between the separator 105 and the separator 106 of the adjacent unit chemical cell 110.
- the insulating member 107 is provided to prevent an electrical short circuit between the separator 105 and the separator 106 of the adjacent cell 101.
- the insulating member 107 constitutes an insulating portion.
- a sheet-like seal member 108 formed in a frame shape is provided inside the insulating member 107 between the separator 105 and the separator 106 of the adjacent unit chemical cell 110.
- the seal member 108 is disposed along the peripheral edge of the cell 101.
- the seal member 108 is disposed between the outer peripheral edge portion of the cell 101 and the inner peripheral edge portion of the separator 105.
- the seal member 108 is disposed so as to surround the periphery of the gas flow path 109. That is, the seal member 108 is a sheet shape, and when viewed from the upper surface or the lower surface side, the outer shape is a substantially square shape, and a shape (frame shape) having a substantially square opening smaller than the outer shape of the cell 101 at the center. ).
- An opening corresponding to the shape of the gas flow path 109 is provided at a portion corresponding to the gas flow path 109.
- the seal member 108 constitutes a seal portion.
- the seal member 108 is provided to prevent gas leakage from the gap between the cell 101 and the separators 105 and 106.
- the seal member 108 is provided to insulate between the separator 105 and the separator 106 of the adjacent unit chemical cell 110.
- the material of the insulating member 107 is not particularly limited, but a material having high electrical insulation (high electrical resistance) is desirable. Examples of this material include alumina, zirconia, silica, and a material containing at least these. The density is preferably dense, but may be porous.
- the material of the seal member 108 is not particularly limited, but a material having high electrical insulation is desirable. Examples of this material include alumina, zirconia, silica, and a material containing at least these. As for the density, a dense one is desirable.
- the material of the seal member 108 may be the same as the material of the insulating member 107.
- the thicknesses of the insulating member 107 and the seal member 108 arranged in the same plane are different from each other. That is, the thickness of the insulating member 107 is smaller than the thickness of the seal member 108.
- the insulating portion and the sealing portion are separated, and the thick sealing member 108 and the thin insulating member 107 are used, thereby increasing the surface pressure of the sealing portion with a simple structure.
- the sealing performance can be improved.
- a pressure is applied in the stacking direction to increase the surface pressure of the seal portion to perform sealing, but it is necessary to apply a very large pressure to increase the surface pressure over a wide area.
- the insulating function and the sealing function are provided in one member, and the insulating sealing member 508 having a large surface area is connected to the separator 105 and the separator 106 of the adjacent unit chemical cell 110. When it is disposed between the two, it is necessary to apply a very large pressure to increase the surface pressure. For this reason, a surface pressure cannot fully be raised and a sealing performance may fall.
- the insulating portion and the sealing portion are separated, and the thick sealing member 108 and the thin insulating member 107 are used, compared with the insulating sealing member 508 shown in FIG.
- the surface area of the seal member 108 can be reduced, and the surface pressure can be easily increased. Thereby, a sealing performance can be improved.
- a material that is porous at room temperature and becomes dense when exposed to high temperature in a compressed state can be used as the material of the seal member 108.
- Pores that are porous at room temperature have high compressibility.For example, when there is a step at the end of the cell, if the pressure is applied in the stacking direction and the surface pressure is applied to the seal part, the step can be absorbed. It becomes possible. And when exposed to high temperature in the compressed state, it becomes dense and the sealing performance is improved.
- the thickness of the sealing member 108 before and after being stacked and compressed is changed. That is, the thickness of the sealing member 108 after being stacked and compressed becomes thinner than that before compression. Therefore, the difference between the thickness of the seal member 108 and the thickness of the insulating member 107 is also reduced. In this case, it is sufficient that the thickness of the sealing member 108 is slightly larger than the thickness of the insulating member 107 after compression.
- FIG. 3 is a diagram schematically showing a partial cross-sectional configuration of the stack 200 according to the second embodiment.
- parts corresponding to those in FIG. 3 are corresponding to those in FIG.
- a coating film 207 formed by previously coating an insulating material on one surface of the separator 106 (the lower surface in FIG. 3) is used as an insulating portion.
- the coating film 207 is formed in a frame shape so as to surround the periphery of the seal member 108.
- the material of the coating film 207 is not particularly limited, but a material having high electrical insulation is desirable. Examples of this material include alumina, zirconia, silica, and a material containing at least these.
- the density is preferably dense, but may be porous.
- the coating method is not particularly limited, and examples thereof include a wet method, a dry method, a physical method, and a chemical method.
- the shape of the coating film 207 is not particularly limited, but may be provided at least in a portion that needs to be insulated.
- the insulating portion is constituted by the coating film 207
- the number of parts is reduced, the number of steps for stacking and assembling the stack 200 is reduced, and the insulating member and the seal member are overlapped during construction. Can be prevented. Furthermore, the occurrence of local electrical leakage can be suppressed.
- FIG. 4 is a diagram schematically illustrating a partial cross-sectional configuration of the stack 300 according to the third embodiment.
- parts corresponding to those in FIG. 4 are corresponding to those in FIG.
- an end plate 120 or the like is installed to ensure the strength of the stack 300 and the like. In this case, it is necessary to perform insulation and gas sealing between the end plate 120 and the separator 106. For this reason, in the stack 300, the insulating member 107 and the sealing member 108 are disposed between the upper end plate 120 and the separator 106.
- the insulating member 107 and the sealing member 108 having the same shape as those disposed between the separators 105 and 106 are provided between the end plate 120 and the separator 106.
- a surface pressure is applied to the same portion of the stack 300, and a surface pressure is uniformly applied to each seal member 108 in the stacking direction, so that the sealing performance can be improved.
- FIG. 5 is a diagram schematically showing a partial cross-sectional configuration of the stack 400 according to the fourth embodiment.
- parts corresponding to those in FIG. 5 are corresponding to those in FIG.
- a convex portion 401 having an area smaller than that of the seal member 108 is provided at a portion where the seal member 108 of the separator 106 contacts.
- the convex portion 401 is formed in a frame shape along the shape of the seal member 108. As the shape of the convex portion 401, a shape having no sharp portion is desirable so that the sealing member 108 is not broken. In the stack 400 configured as described above, the surface pressure applied to the seal member 108 is further increased, and the sealing performance is improved.
- the gas sealing performance can be improved.
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Abstract
Description
本発明の実施形態は、平板型電気化学セルスタックに関する。 Embodiments of the present invention relate to a flat electrochemical cell stack.
水素と酸素を電気化学的に反応させることにより、化学エネルギーを電気エネルギーに変換する燃料電池が注目されている。燃料電池は高いエネルギー利用効率を有し、大規模分散電源、家庭用電源、移動用電源として開発が進められている。 Fuel cells that convert chemical energy to electrical energy by electrochemically reacting hydrogen and oxygen are drawing attention. Fuel cells have high energy use efficiency and are being developed as large-scale distributed power sources, household power sources, and mobile power sources.
燃料電池は、温度域や使用する材料・燃料の種類に応じて、固体高分子型、リン酸型、溶融炭酸塩型、固体酸化物型、などに分けられる。これらの中で効率などの観点から、固体酸化物から成る電解質を使用して電気化学反応により電気エネルギーを得る固体酸化物型燃料電池(SOFC)が注目されている。また、SOFCの逆反応を利用して、固体酸化物型電解セル(SOEC)により水素の製造を行う、高温水蒸気電解法も近年、開発がすすめられている。 Fuel cells are classified into solid polymer type, phosphoric acid type, molten carbonate type, solid oxide type, etc., depending on the temperature range and the type of material and fuel used. Among these, from the viewpoint of efficiency and the like, a solid oxide fuel cell (SOFC) that obtains electric energy by an electrochemical reaction using an electrolyte made of a solid oxide has attracted attention. In recent years, a high-temperature steam electrolysis method in which hydrogen is produced by a solid oxide electrolysis cell (SOEC) by utilizing the reverse reaction of SOFC has been developed.
SOFCおよびSOECの最小構成単位であるセルは、一般的に、電解質と電極とから構成される。固体酸化物の電解質は、酸素イオン導電性を有する。固体酸化物の電解質としては、例えば、緻密な安定化ジルコニアやペロブスカイト型酸化物、セリア系固溶体の成形体などが用いられる。 A cell, which is the minimum constituent unit of SOFC and SOEC, is generally composed of an electrolyte and an electrode. The solid oxide electrolyte has oxygen ion conductivity. As the electrolyte of the solid oxide, for example, dense stabilized zirconia, perovskite oxide, a ceria-based solid solution molded body, or the like is used.
電極に関しては、SOFCを例にとると、大きく燃料極と空気極に分けられる。燃料極では、燃料ガスであるH2と、電解質を移動してきた酸素イオンとが電気化学的に反応し、H2Oと電子(e-)が生成する。空気極では、(空気中の)酸素が、電子(e-)を取り込み、電気化学反応により、酸素イオンが生成し、これらが電解質へと移動する。 Regarding the electrode, taking SOFC as an example, it can be roughly divided into a fuel electrode and an air electrode. At the fuel electrode, H 2 that is the fuel gas and oxygen ions that have moved through the electrolyte react electrochemically to generate H 2 O and electrons (e−). At the air electrode, oxygen (in the air) takes in electrons (e−), generates oxygen ions by an electrochemical reaction, and these move to the electrolyte.
燃料極には、一般的に金属と固体酸化物の混合焼結体(サーメット)が用いられる。たとえば、Ni-YSZ(イットリア安定化ジルコニア)、Ni-ScSZ(スカンジア安定化ジルコニア)などが用いられる。 A mixed sintered body (cermet) of metal and solid oxide is generally used for the fuel electrode. For example, Ni—YSZ (yttria stabilized zirconia), Ni—ScSZ (scandia stabilized zirconia) and the like are used.
一方、空気極には、一般的にペロブスカイト型酸化物やこれらの一部サイトを置換した酸化物が用いられる。例えば、LaSrMn酸化物、LaSrCo酸化物、LaSrCoFe酸化物、LaSrFe酸化物などが挙げられる。また、電解質に用いている固体酸化物との混合体なども用いられ、例えば、LSM-YSZ、LSM-ScSZ、LSC-SDC、LSC-GDCなどが挙げられる。 On the other hand, a perovskite oxide or an oxide obtained by substituting a part of these sites is generally used for the air electrode. For example, LaSrMn oxide, LaSrCo oxide, LaSrCoFe oxide, LaSrFe oxide, and the like can be given. Further, a mixture with a solid oxide used for the electrolyte is also used, and examples thereof include LSM-YSZ, LSM-ScSZ, LSC-SDC, and LSC-GDC.
上記のようにセルは、少なくとも、空気極と電解質と燃料極の積層体である。空気極と電解質と燃料極には、各々異なる特性の材料を用いている。空気極と燃料極は多孔質であり、空気極と燃料極には緻密な電解質を境にそれぞれ異なるガスが供給される。空気極と燃料極は電気伝導体であり、電解質は電気を通さないイオン伝導体である。 As described above, the cell is at least a laminate of an air electrode, an electrolyte, and a fuel electrode. Different materials are used for the air electrode, the electrolyte, and the fuel electrode. The air electrode and the fuel electrode are porous, and different gases are supplied to the air electrode and the fuel electrode with a dense electrolyte as a boundary. The air electrode and the fuel electrode are electrical conductors, and the electrolyte is an ionic conductor that does not conduct electricity.
セルの形状は、平板型、円筒型、円筒平板型などがある。例えば、平板型のセルは、空気極、電解質、燃料極などを平板状に積層した形状のものである。このセルを複数、集積したものは一般的にスタックと呼ばれる。 The cell shape includes a flat plate type, a cylindrical type, and a cylindrical flat plate type. For example, a flat cell has a shape in which an air electrode, an electrolyte, a fuel electrode, and the like are stacked in a flat plate shape. A collection of a plurality of these cells is generally called a stack.
例えば、平板型のセルの場合、スタックは複数の平板型のセルを積層したものであり、各セルの空気極と燃料極に異なるガスを供給し、かつセル同士は電気的に直列に接続可能な構造を持つ。セルとセルの間はセパレータによって隔てられ、このセパレータによってセルごとのガスが区切られる。セパレータは導電性なのでセル同士の電気的導通の役割も担う。また、各セルへのガスの供給・排出流路も一般的にセパレータ中に形成される。 For example, in the case of flat cells, the stack is a stack of multiple flat cells, supplying different gases to the air electrode and fuel electrode of each cell, and the cells can be connected electrically in series. It has a simple structure. The cells are separated from each other by a separator, and the gas for each cell is separated by the separator. Since the separator is conductive, it also plays a role of electrical conduction between cells. In addition, a gas supply / discharge flow path to each cell is generally formed in the separator.
スタックでは、セル部分は緻密な電解質により、燃料極と空気極が隔離されるが、それ以外の部分は緻密なセパレータにより隣接するセル同士の雰囲気を隔離する。また、同一セルの燃料極と空気極の雰囲気については、セルが設置されていない部分の隙間などを緻密な部材で塞ぎ、隔離している。 In the stack, the cell portion separates the fuel electrode and the air electrode by a dense electrolyte, while the other portions separate the atmosphere of adjacent cells by a dense separator. Further, the atmosphere of the fuel electrode and the air electrode of the same cell is isolated by closing a gap in a portion where the cell is not installed with a dense member.
平板型のセルのスタックでは、スタック内を流れるガスのスタック外部への流出を防ぐこと、スタック内部において燃料極と空気極への供給ガスが混合することを防ぐこと、すなわち、ガスのシール性が大きな課題となっている。このようなガスのシール性を高めるためには、例えば、各種のシール材を用いる方法等が提案されている。 In the flat cell stack, the gas flowing in the stack is prevented from flowing out of the stack, the supply gas to the fuel electrode and the air electrode is prevented from mixing inside the stack, that is, the gas sealing property is improved. It has become a big issue. In order to improve such gas sealing performance, for example, methods using various sealing materials have been proposed.
セルは緻密な電解質を有するため、燃料極と空気極の各々の雰囲気ガスの混合を防ぐことが可能である。しかし、セル以外のスタック構成部において、ガスリークへの対策が必要である。例えば、セルとセル以外のスタック構成部材との隙間部分や、ガスをセルに供給する部分をシールする必要がある。 Since the cell has a dense electrolyte, it is possible to prevent mixing of the atmospheric gas in each of the fuel electrode and the air electrode. However, it is necessary to take measures against gas leakage in the stack components other than the cells. For example, it is necessary to seal a gap between a cell and a stack constituent member other than the cell, or a portion that supplies gas to the cell.
また、セルは導電性のセパレータを介して積層されるため、セパレータ間をなんらかの形で絶縁することが必要である。そのため、シール性と絶縁性を両立させた構造が必要となる。 Also, since the cells are stacked via conductive separators, it is necessary to insulate the separators in some form. Therefore, a structure that achieves both sealing properties and insulating properties is required.
本発明が解決しようとする課題は、ガスシール性を高めた平板型電気化学セルスタックを提供することにある。 The problem to be solved by the present invention is to provide a flat plate electrochemical cell stack with improved gas sealability.
実施形態の平板型電気化学セルスタックは、平板状の固体酸化物型の電気化学セルと、前記電気化学セルの周囲を囲む導電性のセパレータとを含み、複数積層された単位電気化学セルと、前記単位電気化学セルの前記セパレータと、隣接する前記単位電気化学セルの前記セパレータとの間に配置され、前記電気化学セルの周囲を囲む枠状のシール部と、 前記単位電気化学セルの前記セパレータと、隣接する前記単位電気化学セルの前記セパレータとの間に配置され、少なくとも一部が前記シール部の外周側に位置し、前記シール部より厚さの薄い絶縁部とを具備している。 The flat plate electrochemical cell stack according to the embodiment includes a flat solid oxide electrochemical cell and a conductive separator surrounding the electrochemical cell, and a plurality of stacked unit electrochemical cells; A frame-shaped seal portion disposed between the separator of the unit electrochemical cell and the separator of the adjacent unit electrochemical cell and surrounding the periphery of the electrochemical cell; and the separator of the unit electrochemical cell And an insulating part that is disposed between the separators of the adjacent unit electrochemical cells and that is at least partially positioned on the outer peripheral side of the seal part and is thinner than the seal part.
以下、実施形態について図面を参照して説明する。図1は、実施形態の平板型電気化学セルスタック(以下、単にスタックという。)100の一部の断面構成を模式的に示す図である。なお、図1では、各構成部品を分解した状態(部品間に間隔を開けた状態)で図示しているが(後述する図3~6も同じ)、これらの各構成部品は、積層されて加圧状態で一体的に保持される。 Hereinafter, embodiments will be described with reference to the drawings. FIG. 1 is a diagram schematically illustrating a partial cross-sectional configuration of a flat plate electrochemical cell stack (hereinafter simply referred to as a stack) 100 according to an embodiment. In FIG. 1, each component is shown in a disassembled state (with a space between the components) (the same applies to FIGS. 3 to 6 described later), but these components are stacked. It is integrally held under pressure.
本実施形態において、スタック100を構成する平板型のセル101は、電極支持型平板型電気化学セルである。セル101は、多孔質の電極支持体102の上に、薄膜からなる電解質103を形成し、さらに電解質103の上に対極104を形成した積層構造である。SOFCの場合、電極支持体102又は対極104のいずれか一方が燃料極であり、他方が空気極である。
In this embodiment, the
セル101の周囲を囲むように、導電性のセパレータ105,106が設けられており、これらの中にセル101が収容され、支持される。電極支持体102とセパレータ106との間には、これらを電気的に接続する図示しない集電体などが配設される。また、対極104と隣接するセパレータ106との間にも、これらを電気的に接続する図示しない集電体などが配設される。
セパレータ105,106の材料は、緻密で、かつ、動作温度である600~1000℃の温度域でも導電性がある材料、例えば金属やセラミックスを用いる。また、この材料としては、セル101と熱膨張係数が近いものが望ましい。なお、本実施形態では、セパレータを、別部材である2つのセパレータ105,106によって構成した例について説明する。しかし、セパレータ105,106が一体となった1つの部材から構成してもよい。
The material of the
平板型のセル101の外形は、例えば、四角形状とされている。また、セパレータ105は、セル101の周囲を囲むように、矩形の枠状に構成されている。セパレータ105の中央部には、四角形の開口105aが形成され、セル101は、開口105aの中に配置される。
The outer shape of the
セパレータ106の外形は、例えば、四角形の板状とされている。また、セパレータ105と、セパレータ106には、夫々対応する位置に貫通孔が形成され、これらの貫通孔によって、ガスを積層方向に流通させるためのガス流路109が形成されている。
The outer shape of the
セパレータ105とセパレータ106とによって、開口105a内にセル101を収容して支持する支持体が構成される。そして、これらのセパレータ105,106、セル101によって1つの単位化学セル110が構成される。図2に示すように、これらの単位化学セル110が複数積層され、積層方向の両側端部(図2における上側端部と下側端部)には、エンドプレート120などが配置される。そして、これらが、締結手段、例えば、複数のボルト111とナット112等によって締め付けられて固定される。なお、図2中、同一構造の単位化学セル110が配置される部分の一部の図示を省略している。
The
図1に示すように、セパレータ105と、隣接する単位化学セル110のセパレータ106との間には、枠状に形成されたシート状の絶縁部材107が設けられている。絶縁部材107は、セパレータ105と隣接するセル101のセパレータ106との間での電気的な短絡を防止するために設けられている。この絶縁部材107によって、絶縁部が構成されている。
As shown in FIG. 1, a sheet-like insulating
さらに、セパレータ105と、隣接する単位化学セル110のセパレータ106との間で、絶縁部材107の内側には、枠状に形成されたシート状のシール部材108が設けられている。シール部材108は、セル101の周縁部に沿って配設されている。シール部材108は、セル101の外周縁部とセパレータ105の内周縁部との間に跨って配設されている。また、シール部材108は、ガス流路109の周囲を囲むように配設されている。すなわち、シール部材108は、シート状であり、上面又は下面側から見たときに、外形が略四角形状とされ、中央部にセル101の外形より小さな略四角形状の開口を有する形状(枠状)となっている。そして、ガス流路109に対応する部位に、ガス流路109の形状に応じた開口が設けられている。このシール部材108によって、シール部が構成されている。
Furthermore, a sheet-
シール部材108は、セル101、セパレータ105,106の間の隙間などからのガスのリークを防止するために設けられている。また、シール部材108は、セパレータ105と隣接する単位化学セル110のセパレータ106との間を絶縁するために設けられている。
The
絶縁部材107の材料は、特に限定されないが、電気的な絶縁性が高い(電気抵抗が高い)ものが望ましい。この材料としては、例えば、アルミナ、ジルコニア、シリカ、少なくともこれらが含まれる材料、などが挙げられる。密度については、緻密なものが望ましいが、多孔質のものでもよい。
The material of the insulating
シール部材108の材料は、特に限定されないが、電気的な絶縁性が高いものが望ましい。この材料としては、例えば、アルミナ、ジルコニア、シリカ、少なくともこれらが含まれる材料、などが挙げられる。密度については、緻密なものが望ましい。シール部材108の材料は、絶縁部材107の材料と同じものを用いてもよい。
The material of the
本実施形態では、同一面内に配置される、絶縁部材107とシール部材108の厚みを異なる厚みとしている。すなわち、絶縁部材107の厚みが、シール部材108の厚みよりも薄くなっている。
In the present embodiment, the thicknesses of the insulating
このように、本実施形態では、絶縁部分とシール部分を分離し、厚さの厚いシール部材108と厚さの薄い絶縁部材107としたことにより、単純な構造でシール部分の面圧を高めることができ、シール性を向上させることができる。
As described above, in this embodiment, the insulating portion and the sealing portion are separated, and the
平板型のスタックの場合、積層方向に圧力をかけて、シール部の面圧を上げてシールをするが、広い面積への面圧を高めるには非常に大きな圧力をかける必要がある。例えば図6に示す比較例のスタック500のように、絶縁機能とシール機能を一つの部材に持たせ、表面積の大きな絶縁シール部材508を、セパレータ105と、隣接する単位化学セル110のセパレータ106との間に配置した場合、面圧を高めるには非常に大きな圧力をかける必要がある。このため、面圧を十分に高めることができず、シール性が低下する場合がある。
In the case of a flat type stack, a pressure is applied in the stacking direction to increase the surface pressure of the seal portion to perform sealing, but it is necessary to apply a very large pressure to increase the surface pressure over a wide area. For example, like the
これに対して、絶縁部分とシール部分を分離し、厚さの厚いシール部材108と厚さの薄い絶縁部材107とした本実施形態では、図6に示した絶縁シール部材508の場合に比べて、シール部材108の表面積を小さくすることができ、容易に面圧を高めることができる。これにより、シール性を向上させることができる。
On the other hand, in this embodiment, the insulating portion and the sealing portion are separated, and the
なお、シール部材108の材料として、室温で多孔質であり、圧縮された状態で高温暴露することにより、緻密になる材料を用いることができる。室温で多孔質なものは圧縮性が高く、例えば、セル端部で段差などがある場合に、スタック積層方向に圧力をかけてシール部分に面圧をかけた場合、その段差を吸収することが可能となる。そして、圧縮された状態で高温暴露することにより、緻密になり、シール性が向上する。
Note that a material that is porous at room temperature and becomes dense when exposed to high temperature in a compressed state can be used as the material of the
上記のような材料を使用して、シール部材108を構成した場合、積層して圧縮する前と、積層して圧縮した後のシール部材108の厚さが変化する。すなわち、積層して圧縮した後のシール部材108の厚さは、圧縮前より薄くなる。したがって、シール部材108の厚さと絶縁部材107の厚さの差も減少する。この場合、圧縮後において僅かにシール部材108の厚さが絶縁部材107の厚さよりも厚ければよい。
When the sealing
図3は、第2実施形態に係るスタック200の一部の断面構成を模式的に示す図である。なお、図3において、図1と対応する部分には同一の符号が付してある。
FIG. 3 is a diagram schematically showing a partial cross-sectional configuration of the
図3に示すように、スタック200では、絶縁部として、セパレータ106の一方の面(図3において下側の面)に予め絶縁材料をコーティングして形成したコーティング膜207を用いている。コーティング膜207は、シール部材108の周囲を囲むように枠状に形成されている。
As shown in FIG. 3, in the
コーティング膜207の材料は、特に限定されないが、電気的な絶縁性が高いものが望ましい。この材料としては例えば、アルミナ、ジルコニア、シリカ、少なくともこれらが含まれる材料、などが挙げられる。密度については、緻密なものが望ましいが、多孔質なものでもよい。また、コーティング方法は、特に限定されないが、例えば、湿式法、乾式法、物理的手法、化学的手法、などが挙げられる。コーティング膜207の形状については、特に限定されないが、絶縁する必要のある部分に最低限設けられていればよい。
The material of the
上記のように、絶縁部をコーティング膜207によって構成した場合、部品点数が減り、スタック200を積層して組み立てる際の工程が減り、また、施工時に絶縁部材とシール部材の重なりが生じるなどの不具合が生じることを防止できる。さらに、局所的な電気のリークの発生を抑制することができる。
As described above, when the insulating portion is constituted by the
図4は、第3実施形態に係るスタック300の一部の断面構成を模式的に示す図である。なお、図4において、図1と対応する部分には同一の符号が付してある。
FIG. 4 is a diagram schematically illustrating a partial cross-sectional configuration of the
スタック300の積層方向端部には、スタック300の強度などを確保するため、エンドプレート120などが設置される。この場合、エンドプレート120とセパレータ106との間の絶縁やガスシールを行う必要がある。このため、スタック300では、絶縁部材107とシール部材108が、上側のエンドプレート120とセパレータ106との間に配置されている。
At the end of the
上記のスタック300では、エンドプレート120とセパレータ106との間に、セパレータ105,106の間に配置するものと同様な形状の絶縁部材107とシール部材108を設けている。これにより、スタック300の同じ個所に面圧がかかるようになり、積層方向において各シール部材108に均一に面圧がかかり、シール性を向上させることができる。
In the
図5は、第4実施形態に係るスタック400の一部の断面構成を模式的に示す図である。なお、図5において、図1と対応する部分には同一の符号が付してある。
FIG. 5 is a diagram schematically showing a partial cross-sectional configuration of the
スタック400では、セパレータ106のシール部材108が接する部分に、シール部材108より面積が小さい凸部401が設けられている。この凸部401は、シール部材108の形状に沿って枠状に形成されている。凸部401の形状としては、シール部材108の破断などが発生しないように鋭利な部分がない形状のものが望ましい。上記構成のスタック400では、シール部材108への面圧がさらに高まり、シール性が向上する。
In the
以上説明した少なくともひとつの実施形態によれば、ガスシール性を高めることができる。 According to at least one embodiment described above, the gas sealing performance can be improved.
以上、本発明の実施形態を説明したが、この実施形態は、例として提示したものであり、発明の範囲を限定することは意図していない。この新規な実施形態は、その他の様々な形態で実施されることが可能であり、発明の要旨を逸脱しない範囲で、種々の省略、置き換え、変更を行うことができる。これら実施形態やその変形は、発明の範囲や要旨に含まれるとともに、請求の範囲に記載された発明とその均等の範囲に含まれる。 As mentioned above, although embodiment of this invention was described, this embodiment is shown as an example and is not intending limiting the range of invention. The novel embodiment can be implemented in various other forms, and various omissions, replacements, and changes can be made without departing from the scope of the invention. These embodiments and modifications thereof are included in the scope and gist of the invention, and are included in the invention described in the claims and the equivalents thereof.
100,200,300,400,500…スタック、101…セル、102…電極支持体、103…電解質、104…対極、105…セパレータ、105a…開口、106…セパレータ、107…絶縁部材、108…シール部材、109…ガス流路、110…単位化学セル、111…ボルト、112…ナット、120…エンドプレート、207…コーティング膜、401…凸部。
100, 200, 300, 400, 500 ... Stack, 101 ... Cell, 102 ... Electrode support, 103 ... Electrolyte, 104 ... Counter electrode, 105 ... Separator, 105a ... Opening, 106 ... Separator, 107 ... Insulating member, 108 ...
Claims (7)
前記単位電気化学セルの前記セパレータと、隣接する前記単位電気化学セルの前記セパレータとの間に配置され、前記電気化学セルの周囲を囲む枠状のシール部と、
前記単位電気化学セルの前記セパレータと、隣接する前記単位電気化学セルの前記セパレータとの間に配置され、少なくとも一部が前記シール部の外周側に位置し、前記シール部より厚さの薄い絶縁部と、
を具備した平板型電気化学セルスタック。 A plurality of stacked unit electrochemical cells including a flat solid oxide electrochemical cell and a conductive separator surrounding the electrochemical cell;
A frame-shaped seal portion disposed between the separator of the unit electrochemical cell and the separator of the adjacent unit electrochemical cell, and surrounding the periphery of the electrochemical cell;
An insulating member disposed between the separator of the unit electrochemical cell and the separator of the adjacent unit electrochemical cell, wherein at least a part is located on the outer peripheral side of the seal portion and is thinner than the seal portion. And
A flat plate electrochemical cell stack comprising:
前記エンドプレートと前記セパレータとの間に、前記シール部と前記絶縁部が配設されている、請求項1~4いずれか1項記載の平板型電気化学セルスタック。 Comprising an end plate disposed at an end portion in the stacking direction of the unit electrochemical cells stacked in a plurality;
The flat plate electrochemical cell stack according to any one of claims 1 to 4, wherein the seal portion and the insulating portion are disposed between the end plate and the separator.
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| WO2025105416A1 (en) * | 2023-11-16 | 2025-05-22 | 日本特殊陶業株式会社 | Solid oxide electrolyzer cell and use of same |
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