TWI779539B - Fuel cell and fuel cell module - Google Patents
Fuel cell and fuel cell module Download PDFInfo
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Classifications
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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
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0258—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
-
- 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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/04313—Processes for controlling fuel cells or fuel cell systems characterised by the detection or assessment of variables; characterised by the detection or assessment of failure or abnormal function
- H01M8/04664—Failure or abnormal function
-
- 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
-
- 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
- H01M8/1286—Fuel cells applied on a support, e.g. miniature fuel cells deposited on silica supports
-
- 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
- H01M8/2428—Grouping by arranging unit cells on a surface of any form, e.g. planar or tubular
-
- 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
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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
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Abstract
燃料電池胞(1,26,28),具備發電元件部及保護元件部。發電元件部,係層積電解質膜(5a),與1層以上之導電膜(4a,6a)而形成,被供給燃料氣體(18,36,37)及空氣(19,38,39)而進行發電。保護元件部,被形成保護膜,僅被供給燃料氣體(18,36,37)或空氣(19,38,39)之中的一方。保護元件部的耐壓強度比發電元件部的耐壓強度還低。The fuel cell (1, 26, 28) has a power generation element part and a protection element part. The power generation element part is formed by laminating an electrolyte film (5a) and one or more layers of conductive films (4a, 6a), and is carried out by supplying fuel gas (18, 36, 37) and air (19, 38, 39). generate electricity. The protective element part is formed with a protective film, and only one of fuel gas (18, 36, 37) or air (19, 38, 39) is supplied. The compressive strength of the protective element portion is lower than that of the power generating element portion.
Description
本發明係有關燃料電池胞及燃料電池模組。The invention relates to a fuel cell cell and a fuel cell module.
於專利文獻1,記載著於燃料電池系統,縮小燃料極與空氣極之壓力差以抑制電解質膜之劣化。In
於專利文獻2,記載著對以(110)面為表面的單晶矽基板施以向異性蝕刻,使被層積電池要素的開口部的剖面之與基板表面的開口夾角幾乎為90°。
[先前技術文獻]
[專利文獻]In
[專利文獻1]日本特開2017-183033號公報 [專利文獻2]日本特開2004-288382號公報[Patent Document 1] Japanese Patent Laid-Open No. 2017-183033 [Patent Document 2] Japanese Patent Laid-Open No. 2004-288382
[發明所欲解決之課題][Problem to be Solved by the Invention]
然而,在先前技術,存在的技術課題是在燃料氣體與氧化劑氣體之壓力差急劇變動或者過度增大的場合,發電元件有破損的可能性。However, in the prior art, there is a technical problem that the power generating element may be damaged when the pressure difference between the fuel gas and the oxidant gas fluctuates rapidly or increases excessively.
專利文獻1之技術,是設置對應於燃料氣體與氧化劑氣體的壓力差之壓力調整裝置,但要對應於瞬間發生的壓力變動還是困難的。此外,此壓力調整裝置,是根據複數燃料電池的電池堆間的氣體壓差者,對於單一燃料電池的電池堆內的壓力差,對應是困難的。The technique of
即使專利文獻2的技術,也因為各電解質膜的面積為相同,所以有基板內之某一單電池破損的可能性。此外,在單電池破損的場合,氫與氧會混合所以不佳。Even in the technology of
本發明係有鑑於前述的課題而完成之發明,目的在於提供藉由在燃料電池胞設保護元件部,即使在燃料氣體與氧化劑氣體之壓力差急劇變動或者過度增大的場合,也可以防止發電元件部的破損之燃料電池胞及燃料電池模組。 [供解決課題之手段]The present invention has been made in view of the foregoing problems, and aims to provide protection against power generation even when the pressure difference between the fuel gas and the oxidant gas fluctuates sharply or increases excessively by providing a protective element in the fuel cell cell. Damaged fuel cell cells and fuel cell modules in the component part. [Means for solving problems]
相關於本發明之燃料電池胞之一例, 具備:電解質膜,1層以上的導電膜層積形成,被供給燃料氣體及氧化劑氣體進行發電之發電元件部, 被形成保護膜,僅被供給前述燃料氣體或前述氧化劑氣體之一方的保護元件部; 前述保護元件部之耐壓強度比前述發電元件部之耐壓強度還低。Regarding an example of the fuel cell of the present invention, Equipped with: Electrolyte membrane, one or more layers of conductive film are laminated and formed, and the power generation element part is supplied with fuel gas and oxidant gas to generate power, A protective film is formed and only one of the aforementioned fuel gas or the aforementioned oxidant gas is supplied to the protective element portion; The compressive strength of the protective element portion is lower than that of the power generating element portion.
此外,相關於本發明之燃料電池模組之一例, 具備前述燃料電池胞,及 被配置於前述燃料電池胞,分離前述燃料氣體與前述氧化劑氣體之隔板。 [發明之效果]In addition, regarding an example of the fuel cell module of the present invention, having the aforementioned fuel cell, and A separator arranged in the fuel cell to separate the fuel gas and the oxidant gas. [Effect of Invention]
根據相關於本發明之燃料電池,即使在燃料氣體與氧化劑氣體之送氣有急劇的壓力變動的場合,也可以減低對發電元件的影響,可防止燃料電池系統的破損。According to the fuel cell according to the present invention, even when there is a sudden pressure change in the supply of fuel gas and oxidant gas, the influence on the power generation element can be reduced, and damage to the fuel cell system can be prevented.
其他課題,新穎的特徵、構成以及效果可以由本說明書的記載以及附圖而詳細得知。Other subjects, novel features, configurations, and effects can be found in detail from the description of this specification and the accompanying drawings.
以下,參照圖式說明本發明之實施型態。實施例,僅是供說明本發明之例示,為了說明的明確化,適當地進行了省略及簡化。本發明亦能以其他種種型態來實施。只要沒有特別限定,各構成要素可為單數亦可為複數。Hereinafter, embodiments of the present invention will be described with reference to the drawings. The examples are merely examples for explaining the present invention, and omissions and simplifications are appropriately made for clarity of description. The present invention can also be implemented in other various forms. Unless otherwise specified, each component may be singular or plural.
於圖式所示的各構成要素的位置、大小、形狀、範圍等,為了更容易理解發明,亦有不表示實際的位置、大小、形狀、範圍等的場合。因此,本發明,不一定限定於圖式所揭示的位置、大小、形狀、範圍等。The position, size, shape, range, etc. of each component shown in the drawings may not show the actual position, size, shape, range, etc. in order to facilitate understanding of the invention. Therefore, the present invention is not necessarily limited to the positions, sizes, shapes, ranges, etc. disclosed in the drawings.
具有同一或同等機能的構成要素有複數個的場合,亦有對同一符號賦予不同的下標而說明的情形。此外,沒有必要區別這些複數個構成要素的場合,亦有省略下標而說明的情形。When there are a plurality of components having the same or equivalent function, the same symbol may be described with different subscripts. In addition, when it is not necessary to distinguish these plural constituent elements, the subscript may be omitted for description.
本發明係有關燃料電池胞及燃料電池模組。近年來,作為可以進行高能量變換,而且不會排出二氧化碳或氮氧化物等汙染物質的清潔能源,燃料電池受到矚目。燃料電池之中,作為一例之固體電解質型燃料電池(Solid Oxide Fuel Cell,以下簡稱為SOFC),發電效率高,能夠以處理容易的氫、甲烷、一氧化碳等氣體為燃料。如此,SOFC與其他方式的燃料電池比較優點很多,作為節能性及環境性優良的熱電共生系統受到期待。The invention relates to a fuel cell cell and a fuel cell module. In recent years, fuel cells have attracted attention as a clean energy source that can perform high-energy conversion without emitting pollutants such as carbon dioxide or nitrogen oxides. Among the fuel cells, a solid oxide fuel cell (Solid Oxide Fuel Cell, hereinafter abbreviated as SOFC) as an example has high power generation efficiency and can use easily handled gases such as hydrogen, methane, and carbon monoxide as fuel. Thus, SOFC has many advantages compared with other types of fuel cells, and is expected as a thermoelectric cogeneration system excellent in energy saving and environmental performance.
SOFC為以燃料極與空氣極夾住固體電解質的構造。電解質為隔壁,對燃料極供給氫等燃料氣體,對空氣極供給空氣等氧化劑氣體。SOFC has a structure in which a solid electrolyte is sandwiched between a fuel electrode and an air electrode. The electrolyte serves as a partition, and a fuel gas such as hydrogen is supplied to the fuel electrode, and an oxidizing gas such as air is supplied to the air electrode.
以下,作為氧化劑氣體之代表使用空氣,但亦可把空氣以外的氣體作為氧化劑氣體使用。Hereinafter, air is used as a representative oxidizing gas, but a gas other than air may also be used as the oxidizing gas.
<實施型態1>
圖1係相關於本發明的實施型態1的燃料電池胞1之平面圖。圖2係沿著圖1的A-A線之剖面圖。為了說明的方便,把圖2的紙面上下方向作為燃料電池胞1的上下方向,但此方向,與燃料電池胞實際設置或者使用時的方向無關。<
又,在附圖,為了容易理解,亦有對非剖面的部分附加陰影表示的場合。In addition, in the drawings, in order to make it easier to understand, the parts that are not cross-sectional are sometimes shown with hatching.
燃料電池胞1,具備以下的構成。
‐ 單晶矽(Si)所構成的半導體基板2(基板)
- 被形成於半導體基板2上的第1絕緣膜3
- 被形成於第1絕緣膜3上的發電元件部及保護元件部The
發電元件部的構成可以為公知的構成,以下說明一例。發電元件部,係層積電解質膜,與1層以上之導電膜而形成。在本實施型態,電解質膜為電解質膜5a,導電膜為第1電極4a及第2電極6a。發電元件部,於第1絕緣膜3之上,依序被層積第1電極4a、電解質膜5a、第2電極6a。The configuration of the power generating element unit may be a known configuration, and an example will be described below. The power generation element part is formed by laminating an electrolyte membrane and one or more conductive membranes. In this embodiment, the electrolyte membrane is the
在本實施型態,2個燃料電池胞1具備2個保護元件部。於保護元件部被形成保護膜。在本實施型態,保護膜係第1電極4b,4c、電解質膜5b,5c、第2電極6b,6c被層積而構成的。In this embodiment, two
發電元件部及保護元件部,被形成於同一半導體基板2。根據這樣的構成,製造步驟變得簡化。The power generating element portion and the protection element portion are formed on the
半導體基板2,具備複數開口部,發電元件部及保護元件部被形成於開口部。複數開口部,包含第1開口部7、第2開口部8a,8b。這些開口部,由上方無法看見,在圖1的平面圖是以虛線表示。The
發電元件部被形成為跨複數之第1開口部7。導電膜(在本實施型態為第1電極4a及第2電極6a)之至少1個(在本實施型態為雙方),跨複數個第1開口部7而連續著。根據這樣的構成,導電膜的形成步驟變得簡化。The power generating element portion is formed across a plurality of
此外,如圖2作為變形例所顯示的,亦可以發電元件部的導電膜(在本變形例為第1電極4a及第2電極6a)之中的1個(在本變形例為第1電極4a),與保護元件部的導電膜(在本變形例為第1電極4c)為連續的方式構成。根據這樣變形例,導電膜的形成步驟變得簡化。In addition, as shown in FIG. 2 as a modified example, one of the conductive films (the
2個保護元件部,分別被形成於第2開口部8a及第2開口部8b。Two protective element parts are respectively formed in the 2nd opening
發電元件部,被供給燃料氣體及空氣而進行發電。此時,第1電極4a與第2電極6a之一方,成為陽極電極,另一方成為陰極電極,分別與外部連接而把電力供給至外部。此外,保護元件部的第1電極4b及第2電極6b,也可以與外部連接,可以量測第1電極4b及第2電極6b之間的靜電電容或電阻值。針對第1電極4c及第2電極6c也同樣。The power generating element unit is supplied with fuel gas and air to generate power. At this time, one of the
第1開口部7的形狀及尺寸可以任意設計,例如平面俯視(圖1的方向)為矩形狀,1邊的長度約5mm。第2開口部8a,8b的形狀及尺寸也可以任意設計,例如為矩形狀,1邊長度約為6mm。The shape and size of the
各開口部的面積的關係,是相關於保護元件部的1個第2開口部8a(或者第2開口部8b)的面積,比相關於發電元件部的1個第1開口部7的面積還要大。在此,面積隨著開口部的位置(例如深度位置)而改變的場合,面積的測定位置可以任意定義。例如,於各開口部的下端測定面積亦可,於各開口部的上端測定面積亦可。在本實施型態,使用這些測定方法之任一,都是第2開口部8a(或第2開口部8b)的面積比第1開口部7的面積還要大。The relationship between the areas of the openings is that the area of one
如圖2所示,半導體基板2,具有內側被除去的複數第1開口部7、1個第2開口部8a、與1個第2開口部8b。半導體基板2的兩表面之中,這些開口部以外的部分,被形成第1絕緣膜3。第1絕緣膜3上,被形成第1開口部7,及以覆蓋第2開口部8a、8b的方式被形成第1電極4a、4b、4c,於其上被形成電解質膜5a、5b、5c,於其上被形成第2電極6a、6b、6c。As shown in FIG. 2 , the
亦即,於第1開口部7,第2開口部8a,及第2開口部8b,均被形成根據同一膜構成的薄膜膜構造。亦即,發電元件部與保護元件部具有同一膜構成。根據這樣的構成,在設計發電元件部及保護元件部的耐壓強度時的計算處理變得簡化。又,此處所謂「膜構成」,例如意味著各層的組成、厚度及層積順序,不一定包含膜的面積。That is, the
圖3A~圖3D係顯示燃料電池胞1的製造步驟之圖。這些圖係對應於圖2的部分剖面圖。首先,如圖3A所示,準備單晶矽,且矽<100>的結晶方位所構成的半導體基板2。半導體基板2,例如具有400μm以上的厚度。3A to 3D are diagrams showing the manufacturing steps of the
在半導體基板2之表面形成第1絕緣膜3。作為第1絕緣膜3,例如藉由CVD法形成約200nm具有拉伸應力的氮化矽膜。CVD法的場合,於半導體基板2的上側及下側,形成相同膜厚的氮化矽膜。The first
接著,藉由濺鍍法,形成約100nm厚的金屬膜(例如鉑(Pt)膜)。接著,如圖3A所示,形成第1電極4a、4b、4c。這是使用微影法實施圖案化,使用根據氬(Ar)氣之乾蝕刻法等來進行的。Next, a metal film (for example, a platinum (Pt) film) is formed to a thickness of about 100 nm by a sputtering method. Next, as shown in FIG. 3A ,
此時,為了提高鉑膜與第1絕緣膜3之間的接著力,以先改質第1絕緣膜3的表面為佳。改質,例如在形成鉑膜之前,藉著根據氬氣的濺鍍蝕刻把第1絕緣膜3的表面蝕刻(例如約僅蝕刻10~15nm)而進行。At this time, in order to increase the adhesive force between the platinum film and the first insulating
或者是為了提高鉑膜與第1絕緣膜3之間的接著力,亦可作為幫助接著的障壁(barrier)金屬膜,將鈦(Ti)膜或鋁(Al)膜形成約2nm。Alternatively, in order to improve the adhesion between the platinum film and the first insulating
接著,藉由光蝕刻技術形成負型光阻的圖案。接著,使用濺鍍法作為電解質膜形成約500nm之例如YSZ膜(含釔的氧化鋯膜)。其後,除去負型光阻。藉此,如圖3B所示,形成電解質膜5a,5b,5c。Next, a negative photoresist pattern is formed by photolithography. Next, a YSZ film (yttrium-containing zirconia film) of, for example, about 500 nm is formed as an electrolyte film by sputtering. Thereafter, the negative photoresist is removed. Thereby, as shown in FIG. 3B,
接著,藉由濺鍍法,形成約100nm鉑膜。其次,藉由光蝕刻法實施圖案化,藉由使用根據氬氣之乾蝕刻,如圖3C所示,形成第2電極6a、6b、6c。Next, a platinum film of about 100 nm was formed by a sputtering method. Next, patterning is performed by a photolithography method, and by dry etching using argon gas, as shown in FIG. 3C , the
接著,如圖3D所示,使用光蝕刻技術與絕緣膜蝕刻技術,除去半導體基板2的下側之第1絕緣膜3的一部分,使半導體基板2的背面露出。Next, as shown in FIG. 3D , a part of the first insulating
接著,把被圖案化的半導體基板2下側表面的第1絕緣膜3作為遮罩,形成複數之第1開口部7及第2開口部8a、8b。這是例如將半導體基板2的矽膜,藉由氫氧化鉀(KOH)溶液或者四甲基醯胺(TMAH)溶液進行濕蝕刻,藉由除去而進行的。此外,藉由將半導體基板2的矽膜,藉由把氟系氣體為主成分使用的乾蝕刻進行除去而進行的。如此進行,形成圖1及圖2所示的燃料電池胞1。Next, using the patterned first insulating
又,作為第1電極4a、4b、4c及第2電極6a、6b、6c之適宜的材料,可以使用對氟系的耐藥品性優異,電阻率低,而且融點比使用溫度更高(例如600℃以上)的膜。例如為鉑膜,鉑膜以外,還可以使用銀(Ag)膜、鎳(Ni)膜、鉻(Cr)膜、鈀(Pd)膜、釕(Ru)膜、銠(Rh)膜等。In addition, as suitable materials for the
此外,第1絕緣膜3不限於氮化矽膜,以對矽基板具有拉伸應力的絕緣膜(氮化鋁膜等)為適宜。此外,第1絕緣膜3,亦可為氮化矽膜、或含有硼或磷之矽氧化膜,亦可為是包含在低溫含有有機成分的P-TEOS膜之層積膜。In addition, the first insulating
圖4係針對圖1之燃料電池胞1,顯示開口部面積與薄膜膜耐壓之關係之圖。形成4個矩形的開口部,分別成為1邊長度3mm(開口面積9mm2
)、4mm(開口面積16mm2
)、5mm(開口面積25mm2
)、6mm(開口面積36mm2
)。於各開口部上,形成圖2的膜構成之薄膜之後,送出空氣,量測薄膜破損的壓力(膜耐壓)。FIG. 4 is a graph showing the relationship between the area of the opening and the pressure resistance of the thin film for the
由圖4的結果,可知隨著開口部的面積變大,薄膜膜耐壓降低。在實施型態1,第2開口部8a,8b的1邊長度為6mm,所以保護元件部的耐壓約25KPa。另一方面,第1開口部7的1邊長度為5mm,發電元件部的耐壓約為32KPa。From the results in FIG. 4 , it can be seen that the withstand voltage of the thin film decreases as the area of the opening increases. In
如此,膜耐壓不同,保護元件部的耐壓強度比發電元件部的耐壓強度還低。亦即,比起構成發電元件部的膜或層積體的強度,構成保護元件部的膜或層積體的強度比較低。亦即,在發生急劇壓力變動的場合,保護元件部會先於發電元件部而發生破損。又,在實施型態1,耐壓強度之比為約1.3。In this way, the withstand voltage of the membrane is different, and the withstand voltage strength of the protective element portion is lower than that of the power generating element portion. That is, the strength of the film or laminate constituting the protective element portion is relatively lower than the strength of the film or laminate constituting the power generating element portion. That is, when a sudden pressure fluctuation occurs, the protection element portion is damaged before the power generation element portion. Also, in
圖5係相關於本發明的實施型態1的隔板9之平面圖。圖6係沿著圖5的B-B線之剖面圖。隔板9,接於燃料電池胞1而配置。Fig. 5 is a plan view of the
於隔板9,被形成上側溝11及下側溝13。上側溝11,被形成於陶瓷基板10的上面側。上側溝11,具備氣體流入口11a、氣體排出口11b、貫通孔12。貫通孔12,上下貫通陶瓷基板10。The
下側溝13,被形成於陶瓷基板10的下面側。下側溝13,具備空氣流入口13a、空氣排出口13b、貫通孔14。貫通孔14,上下貫通陶瓷基板10。The
隔板9的外形尺寸,與燃料電池胞1的外形尺寸幾乎同等。在本實施型態,隔板9的上側溝11,由上方來看,延伸於包含燃料電池胞1的第1開口部7全部全體,與第2開口部8a全體的範圍。因此,於隔板9的上下分別配置燃料電池胞1的場合(例如關連於圖7如稍後所述),氣體透過上側溝11,擴散到上側的燃料電池胞1的第1電極4a,上側的燃料電池胞1的第1電極4b、下側的燃料電池胞1的第2電極6b。The external dimensions of the
同樣地,在本實施型態,隔板9的下側溝13,由上方來看,延伸於包含燃料電池胞1的第1開口部7全部全體,與第2開口部8b全體的範圍。因此,於隔板9的上下分別配置燃料電池胞1的場合,氣體透過下側溝13,擴散到下側的燃料電池胞1的第2電極6a,下側的燃料電池胞1的第2電極6c、上側的燃料電池胞1的第1電極4c。Similarly, in this embodiment, the
如圖6所示,上側溝11包含貫通孔12,成為某氣體的流道,下側溝13包含貫通孔14,成為其他氣體的流道。但是,上側溝11與下側溝13,以隔板9的基板遮蔽,所以這2種氣體不混合。特別是貫通孔12與下側溝13不連通,貫通孔14與上側溝11不連通,所以燃料氣體與空氣分離被送至燃料電池胞。As shown in FIG. 6 , the
如此,隔板9被配置於燃料電池胞1,分離燃料氣體與空氣。根據這樣的構成,可以防止燃料氣體與空氣之混合。In this way, the
圖7係相關於實施型態1的燃料電池模組15的剖面圖。燃料電池模組15,具備2個燃料電池胞1,與1個隔板9。隔板9的上下,被配置各燃料電池胞1。FIG. 7 is a cross-sectional view of the
如圖7所示,於燃料電池模組15,燃料電池胞1被堆疊2個。2個燃料電池胞1之間被層積隔板9。於燃料電池模組15的上端及下端,設有分別具有氣體的流道的上側基板17及下側基板16。As shown in FIG. 7 , in the
又,下側基板16的流道,成為隔板9的上側溝11之中除了貫通孔12的部分外為相同形狀之溝。於下側基板16的流道,為了使氣體可以流入及流出,側面設有至少2個開口部。同樣地,上側基板17的流道,成為隔板9的下側溝13之中除了貫通孔14的部分外為相同形狀之溝。於上側基板17的流道,也是為了使氣體可以流入及流出,側面設有至少2個開口部。Furthermore, the flow path of the
燃料電池模組15,具有對下側基板16與上側基板17施加壓力的機構(未圖示)。藉此,保持燃料氣體與空氣流通的區域之氣密性,防止氣體的混合。The
於此構造,由圖7的紙面右側供給燃料氣體18。燃料氣體18,到達下列各電極。
- 上側的燃料電池胞1的保護元件部的第1電極4b及第2電極6b
- 上側的燃料電池胞1之發電元件部的第1電極4a
- 下側的燃料電池胞1的保護元件部的第1電極4b及第2電極6b
- 下側的燃料電池胞1的發電元件部的第1電極4a
此外,在發電消耗的燃料氣體18,由未圖示的氣體排出口排出。In this configuration, the
同樣地,由圖7的紙面左側供給空氣19。空氣19,到達下列各電極。
- 上側的燃料電池胞1的保護元件部的第1電極4c及第2電極6c
- 上側的燃料電池胞1的發電元件部的第2電極6a
- 下側的燃料電池胞1的保護元件部的第1電極4c及第2電極6c
- 下側的燃料電池胞1的發電元件部的第2電極6a
此外,在發電消耗的空氣19,由未圖示的氣體排出口排出。Similarly, the
亦即,藉由隔板9、下側基板16、上側基板17,使燃料氣體18及空氣19以被分離的狀態供給、消費,而且排出。又,雖未圖示,但在燃料電池模組15,在上側基板17與下側基板16之間被施加壓力,使燃料氣體18及空氣19不洩漏。That is, the
在圖7,燃料氣體18於紙面右側由上/中/下之3處供給,但例如假設由這些之中僅中段壓力急劇上升。上側燃料電池胞1之中,發電元件部與右側的保護元件部受到壓力差,下側的燃料電池胞1之中,右側的保護元件部受到壓力差。然而,2個保護元件部之任一(或雙方),比發電元件部還先破損,因此減少段間的壓力差,所以避免發電元件部的破損。In FIG. 7 , the
此外,由前述可知,於發電元件部被供給燃料氣體18及空氣19雙方,於保護元件部僅被供給燃料氣體18或空氣19之中的一方。因此,保護元件部,在本實施型態具備可發電的構成,但如圖7所示那樣,實際上並不發電。如此,藉由成為使保護元件部的動作對發電不造成影響的構成,即使保護元件部破損的場合,也可以避免對燃料電池胞1的發電動作的影響。此外,這樣的構成,在實施型態1,藉由隔板9在對應於保護元件部的位置具有貫通孔12及14而實現。In addition, it can be seen from the foregoing that both the
燃料電池胞1與隔板9之間,燃料電池胞1與上側基板17之間,及/或燃料電池胞1與下側基板16之間,使用耐熱性良好的密封材亦可。密封材,使用在施加壓力時會變形的材料的話,可以減低在施加壓力時之對燃料電池胞1的損傷。Between the
又,實施型態1的燃料電池模組15,為層積2個燃料電池胞1的構造,亦可為藉著交互重疊燃料電池胞1與隔板9,層積更多段之構成。如此構成的話,可以得到所要的輸出。In addition, the
圖8顯示相關於實施型態1的燃料電池系統的概略圖。燃料電池系統,主要的構成具備送出燃料氣體18與空氣19的送風機21、具有燃料氣體的流量調整機構的改質器22、調整空氣的壓力之壓力調整器23、燃料電池模組15、使燃料電池模組15保持於一定溫度(300℃~600℃)之用的筐體24、使排出的燃料氣體燃燒的燃燒器25。FIG. 8 shows a schematic diagram of a fuel cell system related to
例如,作為燃料氣體18可以使用甲烷。甲烷藉由送風機21送氣,在改質器22內調整流量與壓力。藉此,產生含氫的600℃程度的燃料氣體。燃料氣體被送至燃料電池模組15。For example, methane can be used as
此外,空氣19也藉由送風機21送氣,藉由壓力調整器23調整壓力與流量,被送至燃料電池模組15。又,利用改質器22的熱,空氣的溫度也為600℃程度。In addition, the
燃料氣體及空氣的流量,在最大輸出時,例如有必要增大到數公升/分鐘。The flow rates of fuel gas and air need to be increased to, for example, several liters/minute at the time of maximum output.
其後,改質後的燃料氣體18與被加熱的空氣19,通過配管通過被保持在約500℃的筐體24內,送至燃料電池模組15,為發電所消耗。其後,消耗的各氣體,通過配管在燃燒器25合流,在高溫下燃燒,排出。Thereafter, the reformed
又,雖未圖示,但在由燃料電池模組15排出的燃料氣體及空氣的配管,設有壓力計與流量計。藉此,對改質器22及壓力調整器23進行反饋控制,調整配管內的平均壓力及流量。Also, although not shown, pressure gauges and flowmeters are provided in piping for fuel gas and air discharged from the
於筐體24之前的配管,溫度維持很難,所以直到到達燃料電池模組15為止,有發生熱導致氣體的膨脹或者收縮的場合。此外,在進入燃料電池胞1的部分配管直徑縮小,所以會有發生急劇且瞬間的壓力變動的場合。此傾向,越是在燃料電池胞1的發電以高效率進行時越容易出現,溫度變化導致的壓力變動變得更大。Since it is difficult to maintain the temperature of the piping before the
燃料氣體18及空氣19的壓力變動,是跨發電元件部及保護元件部的薄膜(第1電極4a,4b,4c、電解質膜5a,5b,5c、第2電極6a,6b,6c)產生的。又,此壓力變動,多有急劇發生的場合,即使對改質器22及壓力調整器23施加反饋控制也多有難以對應的場合。Pressure fluctuations of
在實施型態1的燃料電池胞1,於氣體流入口附近設有面積大的保護元件部。此外,保護元件部的耐壓強度,設定為比發電元件部的耐壓強度更低。因此,在發生急劇壓力變動的場合,在發電元件部發生破損之前,保護元件部會破損。In the
藉由保護元件部破損,形成通過破損的保護元件部之氣體流道,藉此可以使氣體流動產生分歧,壓力差變小,可以緩和壓力變動。亦即,可以減低對發電元件部的影響,防止發電元件部的破損。When the protective element part is damaged, a gas channel passing through the damaged protective element part is formed, so that the gas flow can be diverged, the pressure difference can be reduced, and the pressure fluctuation can be eased. That is, it is possible to reduce the influence on the power generating element portion and prevent damage to the power generating element portion.
又,藉由隔板9的構造,即使保護元件部破損也不會使燃料氣體18與空氣19混合,所以可防止氣體混合導致的不良影響。In addition, due to the structure of the
如此,根據實施型態1的話,藉由設保護元件部,即使在燃料氣體與氧化劑氣體之壓力差急劇變動或者過度增大的場合,也可以防止發電元件部的破損。藉此,可以提供高可信賴性且高效率的燃料電池系統。Thus, according to
又,根據圖4所示的開口部面積與薄膜膜耐壓的關係,藉由設計保護元件部的開口面積,可以控制壓力變動的界限值。改變發電元件部的開口面積的場合,可以因應於此而改變保護元件部的開口面積。In addition, according to the relationship between the opening area and the pressure resistance of the thin film shown in Fig. 4, by designing the opening area of the protection element, the limit value of pressure fluctuation can be controlled. When the opening area of the power generating element portion is changed, the opening area of the protection element portion can be changed accordingly.
此外,藉由監視保護元件部的第1電極與第2電極之間的靜電電容值,或者藉由監視第1電極或第2電極的電阻值,可以檢測到保護元件部的破損。檢測到保護元件部的破損的場合,可以安全地停止燃料電池模組。停止後,僅交換破損的燃料電池胞,可以再度進行發電。如此,維修可簡單地進行。In addition, damage to the protective element can be detected by monitoring the capacitance value between the first electrode and the second electrode of the protective element, or by monitoring the resistance value of the first electrode or the second electrode. When damage to the protective element portion is detected, the fuel cell module can be stopped safely. After stopping, only the damaged fuel cells can be replaced to generate electricity again. In this way, maintenance can be easily performed.
燃料電池胞1被堆疊複數個的場合,即使保護元件部之1個發生破損,也不會對發電元件部的構造造成影響。此外,在實施型態1,燃料氣體與空氣被分離而流動,所以可以繼續發電動作。When a plurality of
在實施型態1,作為燃料氣體舉出甲烷,但只要是可以改質的氣體即可,沒有特別限定。例如,作為碳化氫燃料,可以使用天然氣、LP氣(液化石油氣)、煤改質氣體、低級烴氣體(乙烷、乙烯、丙烷、丁烷),生質乙醇等。又,於改質器22的前段設氣化器,藉由氣化器由碳化氫燃料之原料氣體(或者液體)使水分氣化亦可。In
燃料電池模組,舉出使燃料電池胞1上下重疊之例,但在水平方向上排列亦可。在該場合,可以使氣體由下往上流通。For the fuel cell module, an example is given in which the
<實施型態2>
圖9係相關於本發明的實施型態2的燃料電池胞26之平面圖。圖10係沿著圖9的C-C線之剖面圖。保護元件部的第2電極,被構成為溫度感測器27。溫度感測器27,可以為被配置在第2開口部8a、8b上的配線。與實施型態1不同,僅第2開口部8a、8b上的一部分被形成溫度感測器27的配線。<
又,溫度感測器27的配線的兩端,能夠以可與外部連接的方式配置。於燃料電池胞26,保護元件部以外的構成(包含發電元件部的構成),可以與實施型態1相同。In addition, both ends of the wiring of the
於相關於本實施型態2的燃料電池胞26,藉由形成於保護元件部的溫度感測器27,可以測定保護元件部的溫度。溫度的測定,例如可以檢測出溫度感測器27的配線的電阻值,藉由將此電阻值換算為氣體的溫度而進行。藉由監視氣體的溫度可以檢測出異常。此外,藉由監視氣體的溫度,可以對氣體的壓力、流量、及/或溫度的調整進行反饋。藉此,可以進行安定的發電。In the
又,保護元件部的膜的材質與實施型態1相同,膜構造也幾乎等同,所以與實施型態1同樣發揮對燃料氣體等急劇的壓力變動作為安全閥的效果。Moreover, the material of the membrane of the protective element portion is the same as that of
亦可在往各燃料電池胞26內的氣體流入口設流量調整閥,以藉由溫度感測器27測定的溫度的值進入一定範圍內的方式進行控制。例如,可以在穩定狀態下測量氣體溫度,在保護元件部因為急劇的壓力變動而破損的場合,溫度感測器27的配線會斷開,所以可檢測到破損。亦即,溫度感測器27,作為檢測保護元件部的破損之檢測部而發揮機能。藉此,提供可以檢測出保護元件部的破損,進行安定的發電輸出之燃料電池系統。A flow rate adjustment valve may be provided at the gas inflow port into each
又,在實施型態2,於保護元件部設溫度感測器27,但亦可設其他感測器(例如使用壓電元件之壓力感測器,振動感測器等),亦可設複數感測器。此外,在實施型態2,把成為溫度感測器的配線形成為電解質膜5b、5c上側的第2電極,但作為變形例,亦可形成為電解質膜5b、5c的下側的第1電極4b、4c。Also, in
<實施型態3>
圖11係相關於本發明的實施型態3的燃料電池胞28之平面圖。圖12係沿著圖11的D-D線之剖面圖。於相關於實施型態3的燃料電池胞28,被形成為相關於保護元件部的第2開口部8a、8b單個的面積,與相關於發電元件部的第1開口部7單個的面積為大致同等。藉此,與實施型態1相比保護元件部所佔的區域變小,可以配置更多的發電元件部。<
在實施型態3,保護元件部的膜構造與發電元件部的膜構造不同。於保護元件部,未被形成第1電極及電解質膜。此外,替代第2電極而形成第2絕緣膜29,於其上配置與實施型態2同樣的溫度感測器27。In
第2絕緣膜29的構造,根據相關於保護元件部的開口部面積,與膜耐壓的關係,可以適當地設計。例如,可以針對種種構造的第2絕緣膜29,使開口部的面積進行種種改變而測定膜耐壓,以使保護元件部的耐壓強度比發電元件部的耐壓強度更低的方式,決定第2絕緣膜29的構造及開口部的面積。The structure of the second insulating
第2絕緣膜29,以對矽基板具有拉伸應力的絕緣膜為適宜,例如可以使用氮化矽膜,或者氮化鋁膜等。此外,第2絕緣膜29,亦可為對矽基板具有拉伸應力的膜、與對矽基板具有壓縮應力的膜之層積膜,例如,可以為氮化矽膜,與含硼或磷的矽氧化膜之層積膜,此外,可以為氮化矽膜,與在低溫含有有機成分的P-TEOS膜之層積膜。The second insulating
第2絕緣膜29的薄膜膜耐壓,可以藉由改變膜厚而控制,以使膜耐壓比發電元件部更低為適宜。亦即,膜耐壓比發電元件部更低的話,第2開口部8a,8b的面積,亦可比相關於發電元件部的第1開口部7的面積更小。The film withstand voltage of the second insulating
作為實施型態3的變形例,第2絕緣膜,亦可藉由薄膜化的電解質膜構成,亦可藉由殘留第1絕緣膜3而構成。As a modified example of
於實施型態3,藉由使相關於保護元件部的開口部的面積,比實施型態1還縮小,可以配置更多燃料電池胞28內的發電元件部,可以更為擴展發電區域的面積。藉此,發電輸出變得更高。In
<實施型態4>
圖13係相關於本發明的實施型態4的隔板30之平面圖。圖14係沿著圖13的E-E線之剖面圖。相關於實施型態4的隔板30,例如由陶瓷基板31構成。於陶瓷基板31的上面側,被形成具有燃料氣體用的氣體流入口32a及氣體排出口32b之上側溝32,與空氣氣體用的上側溝33。於陶瓷基板31的下面側,被形成具有空氣流入口34a及空氣排出口34b之下側溝34,與燃料氣體用的下側溝35。<Implementation Type 4>
Fig. 13 is a plan view of a
與實施型態1的隔板9同樣,隔板30的外形尺寸,與燃料電池胞1幾乎同等。在本實施型態,隔板30的上側溝32,由上方來看,延伸於包含燃料電池胞1的第1開口部7全部全體,與第2開口部8a全體的範圍。因此,於隔板30的上下分別配置燃料電池胞1的場合(例如關連於圖15如稍後所述),氣體透過上側溝32,擴散到上側的燃料電池胞1的第1電極4a,上側的燃料電池胞1的第1電極4b。Like the
同樣地,在本實施型態,隔板30的下側溝34,由上方來看,延伸於包含燃料電池胞1的第1開口部7全部全體,與第2開口部8b全體的範圍。因此,於隔板30的上下分別配置燃料電池胞1的場合,氣體透過下側溝34,擴散到下側的燃料電池胞1的第2電極6a,下側的燃料電池胞1的第2電極6c。Similarly, in this embodiment, the
如圖14所示,作為與相關於實施型態1的隔板9不同之處,隔板30不具有上下貫通陶瓷基板31的貫通孔。於陶瓷基板31的上面側及下面側,分別被形成隔開燃料氣體與空氣而供給之溝。因此,各氣體被分離而送氣至燃料電池胞1。As shown in FIG. 14 , as a difference from the
圖15係相關於實施型態4的燃料電池模組40的剖面圖。於燃料電池模組40,燃料電池胞1被堆疊2個。2個燃料電池胞1之間被層積隔板30。於燃料電池模組40的上端及下端,設有分別具有氣體的流道的上側基板17及下側基板16。又,下側基板16、上側基板17具有與實施型態1同樣的構成。FIG. 15 is a sectional view of the
於此構造,燃料氣體,被分為燃料氣體36與燃料氣體37。燃料氣體36,透過複數之第1開口部7與第2開口部8a,被送氣至第1電極4a、4b。燃料氣體37,被送氣至保護元件部的第2電極6b。In this configuration, the fuel gas is divided into
空氣,被分為空氣38與空氣39。空氣38,被送氣至發電元件部的第2電極6a,與保護元件部的第2電極6c。空氣39,透過第2開口部8b被送氣至保護元件部的第1電極4c。Air is divided into
亦即,於發電元件部被送氣以燃料氣體36及空氣38而進行發電。另一方面,於保護元件部,燃料氣體36與燃料氣體37被送氣,或者是空氣38與空氣39被送氣。That is, the
在實施型態4,隔板30不具有貫通孔,所以即使因燃料氣體或空氣的急劇壓力變動而使保護元件部破損,破損的保護元件部的破片,也不會飛散到上下方向或者飛往其他的保護元件部。因此,1個燃料電池胞的破損不會對其他燃料電池胞造成影響。亦即,可以提供可信賴性高的燃料電池系統。In Embodiment 4, the
又,在保護元件部破損的場合,以破片不往發電元件部飛散的方式,控制使燃料氣體37的壓力比燃料氣體36的壓力變得稍微低些為適宜。針對空氣也相同,以控制使空氣39的壓力比空氣38的壓力還稍微低些為適宜。Also, when the protective element part is damaged, it is appropriate to control the pressure of the
<其他變形例> 本發明不限定於前述之實施型態及其變形例,也包含其他種種變形例。例如,前述實施型態係為了使本發明易於了解而進行了詳細的說明,但本發明並不限定於具備先前說明的全部構成。此外,把某個實施型態的構成的一部分置換至其他實施型態的構成亦為可能,此外,在某個實施型態的構成加上其他實施型態的構成亦為可能。此外,針對各實施型態的構成的一部分,進行其他構成的追加、削除、置換是可能的。<Other modifications> The present invention is not limited to the aforementioned embodiments and modifications thereof, but also includes other various modifications. For example, the foregoing embodiments have been described in detail to facilitate understanding of the present invention, but the present invention is not limited to having all the configurations described above. In addition, it is also possible to replace a part of the configuration of a certain embodiment type with the configuration of another embodiment type, and it is also possible to add the configuration of another embodiment type to the configuration of a certain embodiment type. In addition, it is possible to add, delete, or substitute other configurations for a part of the configurations of each embodiment.
1,26,28:燃料電池胞
2:半導體基板
3:第1絕緣膜
4a,4b,4c:第1電極(導電膜)
5a,5b,5c:電解質膜
6a,6b,6c:第2電極(導電膜)
7:第1開口部
8a,8b:第2開口部
9,30:隔板
10,31:陶瓷基板
11,32,33:上側溝
11a,32a:氣體流入口
11b,32b:氣體排出口
12,14:貫通孔
13a,34a:空氣流入口
13b,34b:空氣排出口
13,34,35:下側溝
15,40:燃料電池模組
16:下側基板
17:上側基板
18,36,37:燃料氣體
19,38,39:空氣(氧化劑氣體)
21:送風機
22:改質器
23:壓力調整器
24:筐體
25:燃燒器
27:溫度感測器(檢測部)
29:第2絕緣膜1,26,28: fuel cell
2: Semiconductor substrate
3: The first
[圖1]係相關於實施型態1的燃料電池胞的平面圖。
[圖2]係沿著圖1的A-A線之剖面圖。
[圖3A]係顯示圖1的燃料電池胞的製造步驟之剖面圖。
[圖3B]係顯示圖1的燃料電池胞的製造步驟之剖面圖。
[圖3C]係顯示圖1的燃料電池胞的製造步驟之剖面圖。
[圖3D]係顯示圖1的燃料電池胞的製造步驟之剖面圖。
[圖4]係顯示開口部面積與薄膜膜耐壓之關係之圖。
[圖5]係相關於實施型態1的燃料電池用隔板的平面圖。
[圖6]係沿著圖5的B-B線之剖面圖。
[圖7]係相關於實施型態1的燃料電池模組的剖面圖。
[圖8]係相關於實施型態1的燃料電池系統的概略圖。
[圖9]係相關於實施型態2的燃料電池胞的平面圖。
[圖10]係沿著圖9的C-C線之剖面圖。
[圖11]係相關於實施型態3的燃料電池胞的平面圖。
[圖12]係沿著圖11的D-D線之剖面圖。
[圖13]係相關於實施型態4的燃料電池用隔板的平面圖。
[圖14]係沿著圖13的E-E線之剖面圖。
[圖15]係相關於實施型態4的燃料電池模組的剖面圖。[FIG. 1] A plan view of a fuel cell related to
1:燃料電池胞1: Fuel cell
2:半導體基板2: Semiconductor substrate
3:第1絕緣膜3: The first insulating film
4a,4b,4c:第1電極(導電膜)4a, 4b, 4c: 1st electrode (conductive film)
5a,5b,5c:電解質膜5a, 5b, 5c: electrolyte membrane
6a,6b,6c:第2電極(導電膜)6a, 6b, 6c: 2nd electrode (conductive film)
7:第1開口部7: The first opening
8a,8b:第2開口部8a, 8b: the second opening
Claims (10)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/JP2020/021116 WO2021240723A1 (en) | 2020-05-28 | 2020-05-28 | Fuel cell and fuel cell module |
| WOPCT/JP2020/021116 | 2020-05-28 |
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| Publication Number | Publication Date |
|---|---|
| TW202145630A TW202145630A (en) | 2021-12-01 |
| TWI779539B true TWI779539B (en) | 2022-10-01 |
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| Application Number | Title | Priority Date | Filing Date |
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| TW110111535A TWI779539B (en) | 2020-05-28 | 2021-03-30 | Fuel cell and fuel cell module |
Country Status (2)
| Country | Link |
|---|---|
| TW (1) | TWI779539B (en) |
| WO (1) | WO2021240723A1 (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1459134A (en) * | 2001-01-31 | 2003-11-26 | 松下电器产业株式会社 | Polymer electrolyte fuel cell and its electrolyte membrane-gasket assembly |
| CN1489799A (en) * | 2000-11-27 | 2004-04-14 | �ղ��Զ�����ʽ���� | Single cells for fuel cells and solid oxide fuel cells |
| CN102856569A (en) * | 2012-10-09 | 2013-01-02 | 复旦大学 | Porous cathode coating matrix type miniature solid oxide fuel cell device |
| JP2018163811A (en) * | 2017-03-27 | 2018-10-18 | 株式会社豊田中央研究所 | Fuel battery |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI558568B (en) * | 2015-11-03 | 2016-11-21 | 行政院原子能委員會核能研究所 | Permeable metal substrate, metal-supported solid oxide fuel cell and their manufacturing methods thereof |
-
2020
- 2020-05-28 WO PCT/JP2020/021116 patent/WO2021240723A1/en not_active Ceased
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Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1489799A (en) * | 2000-11-27 | 2004-04-14 | �ղ��Զ�����ʽ���� | Single cells for fuel cells and solid oxide fuel cells |
| CN1459134A (en) * | 2001-01-31 | 2003-11-26 | 松下电器产业株式会社 | Polymer electrolyte fuel cell and its electrolyte membrane-gasket assembly |
| CN102856569A (en) * | 2012-10-09 | 2013-01-02 | 复旦大学 | Porous cathode coating matrix type miniature solid oxide fuel cell device |
| JP2018163811A (en) * | 2017-03-27 | 2018-10-18 | 株式会社豊田中央研究所 | Fuel battery |
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| Publication number | Publication date |
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| TW202145630A (en) | 2021-12-01 |
| WO2021240723A1 (en) | 2021-12-02 |
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