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JPS6318303B2 - - Google Patents
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JPS6318303B2 - - Google Patents

Info

Publication number
JPS6318303B2
JPS6318303B2 JP56071823A JP7182381A JPS6318303B2 JP S6318303 B2 JPS6318303 B2 JP S6318303B2 JP 56071823 A JP56071823 A JP 56071823A JP 7182381 A JP7182381 A JP 7182381A JP S6318303 B2 JPS6318303 B2 JP S6318303B2
Authority
JP
Japan
Prior art keywords
porous member
electrode
separation plate
gas separation
conductive porous
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
Application number
JP56071823A
Other languages
Japanese (ja)
Other versions
JPS57185676A (en
Inventor
Kai Nishama
Kazunao Sato
Hideaki Myoshi
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP56071823A priority Critical patent/JPS57185676A/en
Publication of JPS57185676A publication Critical patent/JPS57185676A/en
Publication of JPS6318303B2 publication Critical patent/JPS6318303B2/ja
Granted legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04276Arrangements for managing the electrolyte stream, e.g. heat exchange
    • H01M8/04283Supply means of electrolyte to or in matrix-fuel cells
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0271Sealing or supporting means around electrodes, matrices or membranes
    • H01M8/0273Sealing or supporting means around electrodes, matrices or membranes with sealing or supporting means in the form of a frame
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/24Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/241Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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】 本発明は新規な積層形燃料電池に関する。[Detailed description of the invention] The present invention relates to a novel stacked fuel cell.

従来より積層形燃料電池として第1図に示す装
置がある。
2. Description of the Related Art Conventionally, there is a device shown in FIG. 1 as a stacked fuel cell.

第1図は従来の積層形燃料電池の構成を示す一
部切欠見取図である。
FIG. 1 is a partially cutaway diagram showing the structure of a conventional stacked fuel cell.

第1図において1は導電性のガス分離板、2は
燃料通路、3は酸化剤通路であつて、それぞれガ
ス分離板1の上面および下面に設けられている。
4は多孔質の酸化剤電極、5は非導電性の多孔質
部材であつて電解質が含浸せしめられている。酸
化剤電極4がガス分離板1に接する側には撥水性
処理が施されている。6はガスケツトであり、分
離板1と多孔質部材5との間にはさまれ、酸化剤
電極4の周囲を囲つている。7は燃料電極であ
り、酸素電極と同様にもうひとつのガス分離板1
と多孔質部材5との間にはさまれて設置されたも
うひとつのガス分離板1に設けられた燃料通路2
に接する側に撥水性処理が施されている。なお多
孔質部材5の周囲には不透気処理が施されてい
る。
In FIG. 1, 1 is a conductive gas separation plate, 2 is a fuel passage, and 3 is an oxidizer passage, which are provided on the upper and lower surfaces of the gas separation plate 1, respectively.
4 is a porous oxidizer electrode, and 5 is a non-conductive porous member impregnated with an electrolyte. A water-repellent treatment is applied to the side where the oxidizer electrode 4 contacts the gas separation plate 1. A gasket 6 is sandwiched between the separation plate 1 and the porous member 5 and surrounds the oxidizer electrode 4. 7 is a fuel electrode, which, like the oxygen electrode, is connected to another gas separation plate 1.
A fuel passage 2 provided in another gas separation plate 1 installed between and a porous member 5
Water-repellent treatment is applied to the side that comes into contact with the Note that the area around the porous member 5 is treated to be air-impermeable.

前記不透気処理とは多孔質部材5を拡散するガ
スが端面からもれないようにする処理のことで、
通常テフロン(商標名)シートを圧着するなどの
処理がなされる。
The air impermeability treatment is a treatment that prevents the gas diffusing the porous member 5 from leaking from the end face.
Usually, a process such as crimping a Teflon (trade name) sheet is performed.

つぎに動作について説明する。酸化剤通路3に
供給された酸化剤は多孔質の酸化剤電極4を拡散
し、電解質液との界面でイオン化し、非導電性の
多孔質部材5に至る。電解質の種類によりいずれ
かのイオンが電解質液中を移動し、もうひとつの
イオンと反応して化合物を形成する。燃料が水素
のばあいには水が生成し、外部回路に電流が流れ
る。その際生成した水は余剰の燃料や酸化剤と共
に系外に排出されるが、一部は電解質液を希釈し
膨張させる。この膨張を一旦吸収し、またもとに
もどすために電解質液のリザーバ(図示されてい
ない)を設けることが提案されている。電解質液
の膨張〜収縮は燃料電池が熱サイクルをうけるば
あいにも生じる。これらの要因により、多孔質部
材5に含浸せしめられた電解質液は、燃料電極7
および酸化剤電極4を通り、ガス分離板方向や外
側方向へ浸み出ようとする。そのため電極のガス
分離板側に撥水性処理を施すとともに電極の周囲
にガスケツト6を設け、電解質液の浸み出しを防
いでいる。このガスケツト6はまた燃料および酸
化剤が外部へ洩れるのを防止している。なお多孔
質部材5から外側方向への洩れは、周囲に施した
不透気処理で防止している。
Next, the operation will be explained. The oxidizing agent supplied to the oxidizing agent passage 3 diffuses through the porous oxidizing agent electrode 4, is ionized at the interface with the electrolyte, and reaches the non-conductive porous member 5. Depending on the type of electrolyte, one of the ions moves through the electrolyte solution and reacts with another ion to form a compound. If the fuel is hydrogen, water is produced and current flows in the external circuit. The water generated at this time is discharged from the system together with excess fuel and oxidizer, but some of it dilutes and expands the electrolyte. It has been proposed to provide an electrolyte reservoir (not shown) to temporarily absorb this expansion and restore it to its original state. Expansion and contraction of the electrolyte also occur when the fuel cell is subjected to thermal cycles. Due to these factors, the electrolyte solution impregnated into the porous member 5 is
The gas then passes through the oxidizer electrode 4 and tends to seep out toward the gas separation plate and outward. Therefore, the gas separation plate side of the electrode is treated to be water repellent, and a gasket 6 is provided around the electrode to prevent the electrolyte from seeping out. This gasket 6 also prevents fuel and oxidant from leaking to the outside. Note that leakage outward from the porous member 5 is prevented by air-impermeable treatment applied to the periphery.

従来の積層形燃料電池は前記のように構成され
ているので、電解質液が外部へ洩れるのを防止す
るために電解質液のリザーバを設けることが必要
であり、通常、リザーバはガス分離板の外周部に
設けられ、非導電性多孔質部材5とガスケツト6
にあけた孔を液通路として接続している。このた
めリザーバのスペースを確保するために電池とし
て働く有効面積が小さくなる他、ガスケツトの構
造が複雑になるという問題がある。
Since conventional stacked fuel cells are configured as described above, it is necessary to provide an electrolyte reservoir to prevent the electrolyte from leaking to the outside, and the reservoir is usually located around the outer periphery of the gas separation plate. A non-conductive porous member 5 and a gasket 6 are provided in the
The hole drilled in is connected as a liquid passage. For this reason, there are problems in that the effective area that functions as a battery is reduced in order to secure space for the reservoir, and the structure of the gasket is complicated.

本発明者らは叙上の欠点を克服すべく鋭意研究
を重ねた結果、電解質液を含浸させた非導電性の
多孔質部材と、これをはさむ通気性および撥水性
を有する2枚の電極と、これに燃料および酸化剤
を供給するガス分離板とからなる積層形燃料電池
において、多孔質部材および2枚の電極の周囲に
不透気処理が施され、2枚の電極の最外周の不透
気処理部に内装する部分の少なくとも一部には親
水性処理部が設けられ、かつ電極とガス分離板と
の間に周囲がガスケツトで囲われ、部分的に親水
性処理が施された導電性多孔質部材が挿入されて
いることにより、リザーバ構造が簡単になり、か
つ電極および多孔質部材の製造上の制約を除去し
た積層形燃料電池がえられることを見出し、本発
明を完成するにいたつた。
As a result of intensive research to overcome the above-mentioned drawbacks, the inventors of the present invention have developed a non-conductive porous member impregnated with an electrolyte solution, and two electrodes with air permeability and water repellency sandwiching the member. In a stacked fuel cell consisting of a porous member and a gas separation plate that supplies fuel and an oxidizer, an air-impermeable treatment is applied around the porous member and two electrodes, and an impermeable layer on the outermost periphery of the two electrodes is used. A hydrophilic treated part is provided in at least a part of the internal part of the air permeable treated part, and the periphery is surrounded by a gasket between the electrode and the gas separation plate, and a part of the conductive part is partially treated to make it hydrophilic. The present inventors have discovered that by inserting a porous member, a stacked fuel cell can be obtained which simplifies the reservoir structure and eliminates restrictions on manufacturing electrodes and porous members, and has completed the present invention. It was it.

つぎに実施例をあげて本発明の積層形燃料電池
を説明するが、本発明はこれのみに限定されるも
のではない。
Next, the stacked fuel cell of the present invention will be explained with reference to Examples, but the present invention is not limited thereto.

第2図は本発明の積層形燃料電池の構成を示す
一部切欠見取図である。第2図において1はガス
分離板、2は燃料通路、3は酸化剤通路、4は酸
化剤電極、5は非導電性の多孔質部材、7は燃料
電極である。8は酸化剤電極4とガス分離板1と
の間に挿入された導電性多孔質部材Aであつて、
電解質液を局所的に保持しうるように部分的に親
水性処理部12が設けられており、9はその多孔
質部材A8の周囲を囲つたガスケツトである。1
0は燃料電極7ともうひとつのガス分離板1との
間に挿入された導電性多孔質部材Bであつて、や
はり部分的に親水性処理部12が設けられてお
り、その周囲がガスケツト9で囲われている。ま
た酸化剤電極4、非導電性多孔質部材5および燃
料電極7の最外周部分には不透気処理部11が設
けられており、酸化剤電極4および燃料電極7の
最外周の不透気処理部11に内接する部分の少な
くとも一部には親水性処理部13が設けられてい
る。
FIG. 2 is a partially cutaway sketch showing the structure of the stacked fuel cell of the present invention. In FIG. 2, 1 is a gas separation plate, 2 is a fuel passage, 3 is an oxidizer passage, 4 is an oxidizer electrode, 5 is a non-conductive porous member, and 7 is a fuel electrode. 8 is a conductive porous member A inserted between the oxidizer electrode 4 and the gas separation plate 1,
Hydrophilic treatment portions 12 are partially provided so as to locally retain the electrolyte solution, and 9 is a gasket surrounding the porous member A8. 1
Reference numeral 0 denotes a conductive porous member B inserted between the fuel electrode 7 and another gas separation plate 1, which is also partially provided with a hydrophilic treatment section 12, and surrounded by a gasket 9. surrounded by Further, an air-impermeable treatment portion 11 is provided at the outermost periphery of the oxidizer electrode 4 , the non-conductive porous member 5 , and the fuel electrode 7 . A hydrophilic treatment portion 13 is provided in at least a portion of the portion inscribed in the treatment portion 11 .

つぎに動作について説明する。酸化剤通路3に
供給された酸化剤は導電性の多孔質部材A8およ
び酸化剤電極4を順次拡散して、電解質液との界
面でイオン化し、非導電性多孔質部材5に至る。
一方、もうひとつのガス分離板に設けられた燃料
通路2に供給された燃料は、導電性多孔質部材B
10および燃料電極7を順次拡散して、電解質液
との界面でイオン化し、非導電性多孔質部材5に
至る。電解質の種類によりいずれかのイオンが電
解質中を移動し、もうひとつのイオンと反応して
化合物を形成する。燃料が水素のばあいには水が
生成され、外部回路に電流が取り出される。その
際生成された水によつて電解質液が膨張すること
は従来の燃料電池と同様であるが、そのとき膨張
した電解質液は酸化剤電極の周囲に設けられた親
水性部分を通り、本発明による導電性多孔質部材
A8およびB10中に吸収される。しかしその際
膨張した電解質液が酸化剤電極4、非導電性多孔
質部材5、燃料電極7から外側方向へ洩れること
は、これらの最外周に施した不透気処理部11に
よつて防止されている。酸化剤および燃料が多孔
質部材および電極を拡散する以外にこれら構成要
素間から外部へ洩れることはガスケツト9によつ
て防止されている。導電性多孔質部材A8、B1
0には部分的に親水性処理が施されているので、
これら多孔質部材に吸収された電解質液は親水性
部分に吸収され、ガス分離板から供給される燃料
および酸化剤の拡散通過を妨げない。
Next, the operation will be explained. The oxidizing agent supplied to the oxidizing agent passage 3 sequentially diffuses through the conductive porous member A8 and the oxidizing agent electrode 4, is ionized at the interface with the electrolyte, and reaches the non-conductive porous member 5.
On the other hand, the fuel supplied to the fuel passage 2 provided in the other gas separation plate is transferred to the conductive porous member B.
10 and the fuel electrode 7 are sequentially diffused and ionized at the interface with the electrolyte solution, reaching the non-conductive porous member 5. Depending on the type of electrolyte, one type of ion moves through the electrolyte and reacts with another ion to form a compound. If the fuel is hydrogen, water is produced and current is extracted to the external circuit. The electrolyte liquid expands due to the water generated at that time, as in conventional fuel cells, but the expanded electrolyte liquid passes through the hydrophilic part provided around the oxidizer electrode, and in the present invention is absorbed into the conductive porous members A8 and B10. However, the expanded electrolyte solution is prevented from leaking outward from the oxidizer electrode 4, the non-conductive porous member 5, and the fuel electrode 7 by the air-impermeable treatment portion 11 applied to the outermost periphery of these electrodes. ing. The gasket 9 prevents the oxidant and fuel from leaking between these components to the outside, other than by diffusing through the porous member and the electrodes. Conductive porous member A8, B1
0 has been partially hydrophilic treated, so
The electrolyte liquid absorbed by these porous members is absorbed by the hydrophilic portion, and does not impede the diffusion and passage of the fuel and oxidizer supplied from the gas separation plate.

なお前記実施例では、導電性多孔質部材A8お
よびB10は部分的に親水性処理を施したものを
示したが、導電性多孔質部材に局所的に孔径の分
布を変化させて親水性にした部分を設けてもよ
い。
In the above example, the conductive porous members A8 and B10 were partially subjected to hydrophilic treatment, but the conductive porous members were made hydrophilic by locally changing the pore size distribution. You may provide a portion.

以上のように本発明の積層形燃料電池によれ
ば、導電性多孔質部材をガス分離板と電極の間に
挿入したことにより、燃料電池の動作に伴なう電
解質液の膨張分を導電性多孔質部材中に吸収する
ことができ、積層形燃料電池の信頼性の一層の向
上がはかられる。
As described above, according to the stacked fuel cell of the present invention, by inserting the conductive porous member between the gas separation plate and the electrode, the expansion of the electrolyte caused by the operation of the fuel cell is made conductive. It can be absorbed into the porous member, further improving the reliability of the stacked fuel cell.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来の積層形燃料電池の構成を示す一
部切欠見取図、第2図は本発明の積層形燃料電池
の構成を示す一部切欠見取図である。 (図面の符号)、1:ガス分離板、2:燃料通
路、3:酸化剤通路、4:酸化剤電極、5:非導
電性多孔質部材、6,9:ガスケツト、7:燃料
電極、8:導電性多孔質部材A、10:導電性多
孔質部材B、11:不透気処理部、12,13:
親水性処理部。
FIG. 1 is a partially cutaway sketch showing the structure of a conventional stacked fuel cell, and FIG. 2 is a partially cutaway sketch showing the structure of the stacked fuel cell of the present invention. (Numbers in the drawing), 1: Gas separation plate, 2: Fuel passage, 3: Oxidizer passage, 4: Oxidizer electrode, 5: Non-conductive porous member, 6, 9: Gasket, 7: Fuel electrode, 8 : Conductive porous member A, 10: Conductive porous member B, 11: Air-impermeable treated portion, 12, 13:
Hydrophilic treatment section.

Claims (1)

【特許請求の範囲】[Claims] 1 電解質液を含浸させた非導電性の多孔質部材
と、これをはさむ通気性および撥水性を有する2
枚の電極と、これに燃料および酸化剤を供給する
ガス分離板とからなる積層形燃料電池において、
多孔質部材および2枚の電極の周囲に不透気処理
が施され、2枚の電極の最外周の不透気処理部に
内接する部分の少なくとも一部に親水性処理部が
設けられ、かつ電極とガス分離板との間に周囲が
ガスケツトで囲われ、部分的に親水性処理が施さ
れた導電性多孔質部材が挿入されていることを特
徴とする積層形燃料電池。
1. A non-conductive porous member impregnated with an electrolyte solution, and 2.
In a stacked fuel cell consisting of two electrodes and a gas separation plate that supplies fuel and oxidizer to the electrodes,
Air-impermeable treatment is applied to the periphery of the porous member and the two electrodes, and a hydrophilic-treated portion is provided on at least a portion of the portion inscribed in the air-impermeable treatment portion on the outermost periphery of the two electrodes, and A stacked fuel cell characterized in that a conductive porous member surrounded by a gasket and partially subjected to hydrophilic treatment is inserted between an electrode and a gas separation plate.
JP56071823A 1981-05-09 1981-05-09 Layer-built fuel cell Granted JPS57185676A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56071823A JPS57185676A (en) 1981-05-09 1981-05-09 Layer-built fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56071823A JPS57185676A (en) 1981-05-09 1981-05-09 Layer-built fuel cell

Publications (2)

Publication Number Publication Date
JPS57185676A JPS57185676A (en) 1982-11-15
JPS6318303B2 true JPS6318303B2 (en) 1988-04-18

Family

ID=13471653

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56071823A Granted JPS57185676A (en) 1981-05-09 1981-05-09 Layer-built fuel cell

Country Status (1)

Country Link
JP (1) JPS57185676A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59186271A (en) * 1983-04-05 1984-10-23 Sanyo Electric Co Ltd Stack for fuel battery
JPS60101874A (en) * 1983-11-07 1985-06-05 Fuji Electric Corp Res & Dev Ltd Sealing structure of fuel cell

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4129685A (en) * 1977-08-15 1978-12-12 United Technologies Corp. Fuel cell structure

Also Published As

Publication number Publication date
JPS57185676A (en) 1982-11-15

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