JPS6322025B2 - - Google Patents
Info
- Publication number
- JPS6322025B2 JPS6322025B2 JP55161053A JP16105380A JPS6322025B2 JP S6322025 B2 JPS6322025 B2 JP S6322025B2 JP 55161053 A JP55161053 A JP 55161053A JP 16105380 A JP16105380 A JP 16105380A JP S6322025 B2 JPS6322025 B2 JP S6322025B2
- Authority
- JP
- Japan
- Prior art keywords
- cooling
- gas
- air
- expanded graphite
- joint surface
- 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.)
- Expired
Links
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 18
- 238000001816 cooling Methods 0.000 claims description 18
- 229910002804 graphite Inorganic materials 0.000 claims description 15
- 239000010439 graphite Substances 0.000 claims description 15
- 239000000446 fuel Substances 0.000 claims description 5
- 238000012856 packing Methods 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 4
- 239000007789 gas Substances 0.000 description 13
- 238000000926 separation method Methods 0.000 description 9
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 7
- 239000010410 layer Substances 0.000 description 7
- 239000003792 electrolyte Substances 0.000 description 4
- 239000011159 matrix material Substances 0.000 description 4
- 239000000112 cooling gas Substances 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 239000002737 fuel gas Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000012495 reaction gas Substances 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 2
- KMUONIBRACKNSN-UHFFFAOYSA-N potassium dichromate Chemical compound [K+].[K+].[O-][Cr](=O)(=O)O[Cr]([O-])(=O)=O KMUONIBRACKNSN-UHFFFAOYSA-N 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000001050 lubricating effect Effects 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- VKJKEPKFPUWCAS-UHFFFAOYSA-M potassium chlorate Chemical compound [K+].[O-]Cl(=O)=O VKJKEPKFPUWCAS-UHFFFAOYSA-M 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- 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
- H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
- H01M8/04067—Heat exchange or temperature measuring elements, thermal insulation, e.g. heat pipes, heat pumps, fins
- H01M8/04074—Heat exchange unit structures specially adapted for fuel cell
-
- 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
- H01M8/0267—Collectors; Separators, e.g. bipolar separators; Interconnectors having heating or cooling means, e.g. heaters or coolant flow channels
-
- 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
- H01M8/02—Details
- H01M8/0297—Arrangements for joining electrodes, reservoir layers, heat exchange units or bipolar separators to each other
-
- 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
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fuel Cell (AREA)
Description
【発明の詳細な説明】
本発明は空冷式燃料電池の改良に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to improvements in air-cooled fuel cells.
酸性電解液を用いるマトリツクス型燃料電池
は、170〜180度程度の高温で作動させるため、冷
却が必要となる。一般に冷却媒体として空気を用
い、陽極へ供給される反応ガスとしての空気を冷
却ガスに兼用する方式がとられているが、この方
式では電池堆が大型化すると、陽極への供給空気
流量が過大となつてマトリツクス中の電解液が蒸
発し、電池性能を損う欠点がある。そこで電極と
は隔離された冷却専用の通路を形成する方法も提
案されている。これは二分割されたカーボン製ガ
ス分離板の接合面に、空気通路を形成するもので
あるが、この接合面特に燃料ガス供給マニホルド
に面する部分の接合面を通してガスの混合が起
る。従来これを防止するため導電性を付与したゴ
ムパツキングや接着剤を用いているが、電池の高
温長期間の作動により劣下して気密性を損うと共
に、これらの低抗により電圧降下が生ずるなどの
欠点があつた。 Matrix fuel cells that use acidic electrolytes operate at high temperatures of around 170 to 180 degrees, so they require cooling. Generally, a method is used in which air is used as a cooling medium and the air as a reaction gas supplied to the anode is also used as a cooling gas, but with this method, as the battery stack becomes larger, the flow rate of air supplied to the anode becomes excessive. This has the disadvantage that the electrolyte in the matrix evaporates, impairing battery performance. Therefore, a method has also been proposed in which a dedicated cooling path is formed that is isolated from the electrodes. This is to form an air passage at the joint surface of the two-part carbon gas separation plate, and gas mixing occurs through this joint surface, particularly the joint surface of the portion facing the fuel gas supply manifold. Conventionally, conductive rubber packing and adhesives have been used to prevent this, but they deteriorate due to long-term operation of batteries at high temperatures, impairing airtightness, and their low resistance causes voltage drops. There were some shortcomings.
本発明は接合時に冷却通路を構成する凹所を有
した二枚の板の接合面にパツキング材として膨脹
黒鉛層を用いることを特徴とするもので、気密且
導電的接合性の改善により、ガス間の混合を防止
すると共に、内部抵抗の低減を図るものである。 The present invention is characterized in that an expanded graphite layer is used as a packing material on the joining surface of two plates having recesses that constitute cooling passages during joining. This is to prevent mixing between the two and to reduce internal resistance.
こゝに云う膨脹黒鉛は黒鉛結晶構造の層間を拡
張処理したもので、その作成例を示す。即ち黒鉛
は第1図に示すように六方晶系の六角板状扁平な
結晶で、六炭素環が連なつてつくる層状構造をも
つ。この黒鉛を例えば濃硫酸と濃硝酸の混酸及び
塩素酸カリウム、重クロム酸カリウム等の強力な
酸化剤を併用して湿式酸化し、これを900℃以上
の高温で急速加熱すると、黒鉛の結晶構造におけ
る前記層間がC軸方向に50〜1000倍にも膨脹す
る。 The expanded graphite referred to here is obtained by expanding the interlayers of graphite crystal structure, and an example of its preparation is shown below. That is, graphite is a hexagonal hexagonal plate-like flat crystal, as shown in FIG. 1, and has a layered structure formed by a series of six carbon rings. This graphite is wet-oxidized using a mixed acid of concentrated sulfuric acid and concentrated nitric acid, and a strong oxidizing agent such as potassium chlorate or potassium dichromate, and then rapidly heated at a high temperature of 900°C or more. The space between the layers expands 50 to 1000 times in the C-axis direction.
このようにして得た膨脹黒鉛は、熱化学的に安
定で導電性、潤滑性に富んだ多孔質粒子を構成
し、特性上成型性が極めて良好で、結着剤などを
全く必要とせず加圧成型後の導電性は黒鉛固有の
値に近い値を示す。 The expanded graphite obtained in this way constitutes porous particles that are thermochemically stable, highly conductive, and highly lubricating, and has extremely good moldability and can be processed without the need for any binders. The conductivity after pressure molding shows a value close to the value inherent to graphite.
以下本発明の実施例を図について説明する。燃
料電池は、陰・陽のガス電極1,2と電解質マト
リクス3とよりなる単位セルが、その間にカーボ
ン製ガス分離板4を介して積重されている。各ガ
ス分離板4は、その上下両面に夫々水素ガスの如
き燃料ガス供給溝5と空気供給溝6とを互に交錯
する方向に配列形成し、陰・陽各電極1,2の背
面に夫々水素ガス及び空気が供給される。 Embodiments of the present invention will be described below with reference to the drawings. In a fuel cell, unit cells each consisting of negative and positive gas electrodes 1 and 2 and an electrolyte matrix 3 are stacked with a carbon gas separation plate 4 interposed therebetween. Each gas separation plate 4 has fuel gas supply grooves 5 such as hydrogen gas and air supply grooves 6 arranged in intersecting directions on its upper and lower surfaces, respectively, and on the back surfaces of the negative and positive electrodes 1 and 2, respectively. Hydrogen gas and air are supplied.
このような電池堆のうち数セルおきに前記分離
板4に代え冷却板7が設けられる。この冷却板は
二枚の板8,8を接合してその接合面に冷却通路
9を形成しているが、冷却板の上下両面には前記
ガス分離板の場合と同様に水素ガス及び空気の各
供給溝5′,6′を配列し、ガス分離板としての機
能も兼ねている。二枚の板8,8の接合面には、
第3図及び第4図に示すように、前記膨脹黒鉛を
シート状にして介挿し、電池堆の締付力によりこ
の膨脹黒鉛層10が圧縮されて接合面間の気密性
と導電性を保つ。 In such a battery stack, a cooling plate 7 is provided in place of the separation plate 4 every few cells. This cooling plate has two plates 8, 8 joined together to form a cooling passage 9 on the joint surface, but the upper and lower surfaces of the cooling plate contain hydrogen gas and air as in the case of the gas separation plate. Each supply groove 5', 6' is arranged and also functions as a gas separation plate. On the joint surface of the two plates 8, 8,
As shown in FIGS. 3 and 4, the expanded graphite is inserted in the form of a sheet, and the expanded graphite layer 10 is compressed by the tightening force of the battery stack to maintain airtightness and conductivity between the joint surfaces. .
層10は第3図のように接合面全面にはさみ込
んでもよいが、第4図に示すように電池堆の水素
ガス供給面に対応する接合部のみに入れるだけで
もよい。 The layer 10 may be sandwiched over the entire joint surface as shown in FIG. 3, but it may also be inserted only in the joint portion corresponding to the hydrogen gas supply surface of the battery stack, as shown in FIG.
水素ガスは導入マニホルド(図示せず)より各
分離板4及び冷却板7の供給溝5及び5′を経て
陰極背面に送られ、反応済のガスは導出マニホル
ド(図示せず)から排出される。一方空気は導入
マニホルド(図示せず)より、各供給溝6を経て
陽極背面に流れる反応ガスと、冷却板7の冷却通
路9に流れる冷却ガスとに分れて電池堆を通り、
これら反応ガスと冷却ガス(いずれ約180℃に昇
温)とは導出マニホルド(図示せず)で一緒にな
つて排出される。 Hydrogen gas is sent to the back of the cathode from an introduction manifold (not shown) through the supply grooves 5 and 5' of each separation plate 4 and cooling plate 7, and the reacted gas is discharged from an output manifold (not shown). . On the other hand, the air is separated from the introduction manifold (not shown) into a reaction gas flowing to the back side of the anode through each supply groove 6 and a cooling gas flowing into the cooling passage 9 of the cooling plate 7, and passes through the battery stack.
These reaction gas and cooling gas (temperature increased to approximately 180° C.) are discharged together through a discharge manifold (not shown).
このような両ガスの供給時、電池堆の水素ガス
流通方向にある両側面において、冷却板7の接合
部分から空気通路9への水素ガスの浸入、又は、
その逆のケースにより、両ガスが混合するような
ことはなくなる。 When both gases are supplied in this manner, hydrogen gas may enter the air passage 9 from the joint portion of the cooling plate 7 on both sides of the battery stack in the hydrogen gas flow direction, or
Due to the opposite case, there will be no mixing of both gases.
上述の如く本発明は、ガス分離板を兼ねる冷却
板が二枚の板を接合してその接合面に冷却通路を
形成する場合、接合面のパツキング材として膨脹
黒鉛層を用いたもので、この層は膨脹黒鉛の導電
性・高気密性及び弾力性により極めて良好なパツ
キング材となり、両ガスの混合を防止すると共に
接触抵抗を減少し、空冷式燃料電池としてすぐれ
た特性を発揮する。 As described above, the present invention uses an expanded graphite layer as a packing material for the joint surface when two cooling plates that also serve as gas separation plates are joined to form a cooling passage on the joint surface. The layer is an extremely good packing material due to the conductivity, high airtightness, and elasticity of expanded graphite, which prevents mixing of both gases and reduces contact resistance, demonstrating excellent characteristics as an air-cooled fuel cell.
第1図は本発明に云う膨脹黒鉛を説明するため
の黒鉛結晶構造図、第2図は電池堆を部分的に破
断して内部を示す斜面図、第3図及び第4図はい
ずれも本発明による冷却板の斜面図、第5図は本
発明による電池堆の斜面図である。
1……陰極、2……陽極、3……電解質マトリ
クス、4……ガス分離板、5,5′……燃料ガス
供給溝、6,6′……空気供給溝、7……冷却板
(二枚の板)、9……冷却通路、10……膨脹黒鉛
層。
Fig. 1 is a graphite crystal structure diagram for explaining the expanded graphite referred to in the present invention, Fig. 2 is a partially cutaway perspective view of a battery stack showing the inside, and Figs. 3 and 4 are both from this book. FIG. 5 is a perspective view of a cooling plate according to the invention, and FIG. 5 is a perspective view of a battery stack according to the invention. 1... Cathode, 2... Anode, 3... Electrolyte matrix, 4... Gas separation plate, 5, 5'... Fuel gas supply groove, 6, 6'... Air supply groove, 7... Cooling plate ( two plates), 9...cooling passage, 10...expanded graphite layer.
Claims (1)
した二枚の板の接合面にパツキング材として膨張
黒鉛を用いたことを特徴とする燃料電池の冷却
板。1. A cooling plate for a fuel cell, characterized in that expanded graphite is used as a packing material on the joint surface of two plates each having a recess that forms a cooling air passage when joined.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55161053A JPS5784575A (en) | 1980-11-14 | 1980-11-14 | Air-cooled fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55161053A JPS5784575A (en) | 1980-11-14 | 1980-11-14 | Air-cooled fuel cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5784575A JPS5784575A (en) | 1982-05-26 |
| JPS6322025B2 true JPS6322025B2 (en) | 1988-05-10 |
Family
ID=15727707
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55161053A Granted JPS5784575A (en) | 1980-11-14 | 1980-11-14 | Air-cooled fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5784575A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA1259101A (en) * | 1984-04-09 | 1989-09-05 | Hiroyuki Fukuda | Carbonaceous fuel cell electrode substrate incorporating three-layer separator, and process for preparation thereof |
| US4794043A (en) * | 1985-04-30 | 1988-12-27 | Kureha Kagaku Kogyo Kabushiki Kaisha | Carbon product comprising carbonaceous materials joined together, said carbon product for electrode substrate of fuel cells and process for production thereof |
| KR100536218B1 (en) * | 2004-01-28 | 2005-12-12 | 삼성에스디아이 주식회사 | Fuel cell system |
| JP2007018924A (en) * | 2005-07-08 | 2007-01-25 | Fuji Electric Holdings Co Ltd | Fuel cell |
-
1980
- 1980-11-14 JP JP55161053A patent/JPS5784575A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5784575A (en) | 1982-05-26 |
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