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JPS6314815B2 - - Google Patents
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JPS6314815B2 - - Google Patents

Info

Publication number
JPS6314815B2
JPS6314815B2 JP56124058A JP12405881A JPS6314815B2 JP S6314815 B2 JPS6314815 B2 JP S6314815B2 JP 56124058 A JP56124058 A JP 56124058A JP 12405881 A JP12405881 A JP 12405881A JP S6314815 B2 JPS6314815 B2 JP S6314815B2
Authority
JP
Japan
Prior art keywords
conductive member
bipolar plate
alkali metal
cathode
fuel cell
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
JP56124058A
Other languages
Japanese (ja)
Other versions
JPS5826463A (en
Inventor
Hiroshi Hida
Masahito Takeuchi
Hideo Okada
Shigeru Okabe
Munehiko Tonami
Shinpei Matsuda
Fumito Nakajima
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.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP56124058A priority Critical patent/JPS5826463A/en
Publication of JPS5826463A publication Critical patent/JPS5826463A/en
Publication of JPS6314815B2 publication Critical patent/JPS6314815B2/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
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0204Non-porous and characterised by the material
    • H01M8/0206Metals or alloys
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/14Fuel cells with fused electrolytes
    • H01M2008/147Fuel cells with molten carbonates
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • H01M2300/0048Molten electrolytes used at high temperature
    • H01M2300/0051Carbonates
    • 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
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0204Non-porous and characterised by the material
    • H01M8/0206Metals or alloys
    • H01M8/0208Alloys
    • H01M8/021Alloys based on iron
    • 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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

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】[Detailed description of the invention]

本発明は、燃料電池及びその製造法に係り、特
に溶融炭酸塩型燃料電池とその製造法に係る。 燃料電池のバイポーラプレートは、別名、セパ
レータ、ガス分離板或は集電体とも呼ばれる。こ
のバイポーラプレートは、一般にさびにくい材料
たとえばオーステナイト系ステンレス鋼或はニツ
ケルで作られている。 バイポーラプレートは、このようにさびにくい
材料で作られているにも拘らず、溶融炭酸塩型燃
料電池においては使用中にカソード側バイポーラ
プレートの酸化剤通路側全面に電気絶縁性の酸化
皮膜が形成されることがわかつた。これは、電池
の運転中にバイポーラプレート酸化剤によつて酸
化を受けて表面に酸化皮膜ができ、この皮膜がカ
ソードとの接触面まで進行していくことによる。 かかる酸化皮膜が形成されると接触抵抗が増し
て電池の出力が低下することがわかつた。 本発明の目的は、カソード側バイポーラプレー
トのカソードとの接触面が良導電性を有する燃料
電池及びその製造法を提供するにある。 本発明は、カソード側バイポーラプレートのカ
ソードとの接触面を、アルカリ金属元素を含有す
る導電性部材で構成するものである。 本発明は、アルカリ金属元素を含有する導電性
部材は酸化雰囲気下で高温(500〜800℃)に加熱
しても導電性を有するという発見に基づくもので
ある。 カソード側バイポーラプレートは前記導電性部
材と他の部材との張り合せ構造にしてもよいが、
望ましくは全体を前記導電性部材で作るべきであ
る。その方が製作がし易いし又機械的強さの面か
らみても強くなる。 カソード側バイポーラプレートにおいて、電気
絶縁性の皮膜が問題となるのはカソードとの接触
面であるから、この表面のアルカリ金属元素濃度
を最も高くし、導電性が損なわれるのを防止する
ことが望ましい。 本発明では、動電性部材をオーステナイト系ス
テンレス鋼或はニツケルだけでなく、純鉄、炭素
鋼、けい素鋼板、金属粉末の成型品たとえば焼結
品、導電性金属酸化物粉末の成型品などで作るこ
とができる。このように多種類の導電性部材を使
えることは、本発明によつてもたらされたもう1
つの大きな効果である。 溶融塩電解質に対する耐食性或は耐酸化性を考
慮すると、導電性部材はやはりオーステナイト系
ステンレス鋼或は純ニツケルが望ましい。 本発明におけるカソード側バイポーラプレート
は、一例として導電性部材をアルカリ金属塩中に
置き加熱処理してアルカリ金属元素を含有させる
ことによつて作ることができる。この方法は、ア
ルカリ金属元素の濃度を表面部で最も高くできる
のできわめて好ましい。かかる方法の具体的な実
施手段としては400〜1200℃に加熱され溶融状態
になつたアルカリ金属塩中に導電性部材を浸漬す
る方法がある。固体状態のアルカリ金属塩粉末中
に導電性部材を置き加熱してもよい。前記2つの
方法の中では前者のアルカリ金属塩を用いる方が
アルカリ金属元素が導電性部材中に入りやすい。 前記加熱処理を酸化雰囲気中で行つたときに
は、使用中における接触抵抗の増加はきわめて少
なくなる。従つて、本発明においては、酸化雰囲
気下でアルカリ金属塩の溶融物中に導電性部材を
浸漬する方法が最も望ましい。 アルカリ金属塩は少なくともリチウム塩を含む
ことが望ましい。リチウム塩を含むものを使用す
ると、導電性部材の表面にリチウムを含む固溶体
の層ができる。この層は溶融炭酸塩型燃料電池の
運転温度ですぐれた導電性を有する。 実施例 1 SUS316製のオーステナイト系ステンレス鋼か
らなる導電性部材を、炭酸リチウムと炭酸カリウ
ムを1対1の重量比で混合した炭酸塩の溶融物中
に浸漬し、空気中で700℃で3時間加熱してバイ
ポーラプレートを作つた。 実施例 2 純ニツケル製の導電性部材を、炭酸リチウムと
炭酸カリウムを1対1の重量比で混合した溶融炭
酸塩中に浸漬し、空気中で750℃で5時間加熱し
て、バイポーラプレートを作つた。 比較例 1 SUS316でバイポーラプレートを作つた。 比較例 2 純ニツケルでバイポーラプレートを作つた。 実験例 前記実施例1,2及び比較例1,2で得たバイ
ポーラプレートを用い、図に示す方法で接触抵抗
を測定した。 バイポーラプレート2は2つ用意し、その間に
直径30mmφ、厚さ1.5mmの円板状をした電極板1
を設置した。ガス室3,4に酸素と炭酸ガスを1
対1の比率で混合したガスを1l/分の流量で送り
込んだ。バイポーラプレート2は両側から矢印で
示す方向にプレス圧力をかけた。以上の状態でバ
イポーラプレート2間に直流電源5から数〜
10mAの直流電流を可変抵抗器6で調整しつつ流
した。電流値は電流計7で読み取り、その時の電
圧降下を電圧計8で計測して接触抵抗を求めた。
電極板とバイポーラプレート2の接触面積は両面
合せて8cm2である。
TECHNICAL FIELD The present invention relates to a fuel cell and a method for manufacturing the same, and particularly to a molten carbonate fuel cell and a method for manufacturing the same. The bipolar plate of a fuel cell is also called a separator, a gas separation plate, or a current collector. The bipolar plate is generally made of a rust-resistant material such as austenitic stainless steel or nickel. Although the bipolar plate is made of a rust-resistant material, an electrically insulating oxide film forms on the entire surface of the cathode bipolar plate on the oxidant passage side during use in molten carbonate fuel cells. I found out that it would happen. This is because during operation of the battery, the battery is oxidized by the bipolar plate oxidizer, forming an oxide film on the surface, and this film progresses to the contact surface with the cathode. It has been found that when such an oxide film is formed, the contact resistance increases and the output of the battery decreases. An object of the present invention is to provide a fuel cell in which the contact surface of the cathode-side bipolar plate with the cathode has good conductivity, and a method for manufacturing the same. In the present invention, the contact surface of the cathode-side bipolar plate with the cathode is made of a conductive member containing an alkali metal element. The present invention is based on the discovery that a conductive member containing an alkali metal element has conductivity even when heated to a high temperature (500 to 800°C) in an oxidizing atmosphere. The cathode side bipolar plate may have a structure in which the conductive member and another member are laminated together,
Preferably, it should be made entirely of the electrically conductive material. This is easier to manufacture and is also stronger in terms of mechanical strength. In the cathode side bipolar plate, the electrically insulating film is a problem at the contact surface with the cathode, so it is desirable to have the highest concentration of alkali metal elements on this surface to prevent loss of conductivity. . In the present invention, the electrodynamic member is not only made of austenitic stainless steel or nickel, but also pure iron, carbon steel, silicon steel sheets, molded products of metal powder, such as sintered products, molded products of conductive metal oxide powder, etc. It can be made with. The ability to use a wide variety of conductive members in this way is another advantage brought about by the present invention.
This has two major effects. Considering the corrosion resistance or oxidation resistance of the molten salt electrolyte, the conductive member is preferably made of austenitic stainless steel or pure nickel. The cathode-side bipolar plate in the present invention can be made, for example, by placing a conductive member in an alkali metal salt and heat-treating it to contain an alkali metal element. This method is extremely preferable because it allows the concentration of the alkali metal element to be highest at the surface. A specific method for carrying out such a method is to immerse the conductive member in an alkali metal salt that has been heated to 400 to 1200° C. and is in a molten state. A conductive member may be placed in solid alkali metal salt powder and heated. Of the above two methods, the former method using an alkali metal salt allows the alkali metal element to enter the conductive member more easily. When the heat treatment is performed in an oxidizing atmosphere, the increase in contact resistance during use is extremely small. Therefore, in the present invention, the most desirable method is to immerse the conductive member in a melt of an alkali metal salt in an oxidizing atmosphere. It is desirable that the alkali metal salt contains at least a lithium salt. When a material containing lithium salt is used, a layer of a solid solution containing lithium is formed on the surface of the conductive member. This layer has excellent electrical conductivity at the operating temperatures of the molten carbonate fuel cell. Example 1 A conductive member made of SUS316 austenitic stainless steel was immersed in a carbonate melt made by mixing lithium carbonate and potassium carbonate at a weight ratio of 1:1, and was heated at 700°C in air for 3 hours. I heated it up and made a bipolar plate. Example 2 A conductive member made of pure nickel was immersed in a molten carbonate mixture of lithium carbonate and potassium carbonate at a weight ratio of 1:1, and heated in air at 750°C for 5 hours to form a bipolar plate. I made it. Comparative Example 1 A bipolar plate was made from SUS316. Comparative Example 2 A bipolar plate was made from pure nickel. Experimental Example Using the bipolar plates obtained in Examples 1 and 2 and Comparative Examples 1 and 2, contact resistance was measured by the method shown in the figure. Two bipolar plates 2 are prepared, and a disc-shaped electrode plate 1 with a diameter of 30 mmφ and a thickness of 1.5 mm is placed between them.
was installed. Oxygen and carbon dioxide gas are added to gas chambers 3 and 4.
Gases mixed at a ratio of 1:1 were fed at a flow rate of 1 l/min. Press pressure was applied to the bipolar plate 2 from both sides in the direction indicated by the arrow. In the above condition, several ~
A direct current of 10 mA was applied while being adjusted with a variable resistor 6. The current value was read with an ammeter 7, and the voltage drop at that time was measured with a voltmeter 8 to determine the contact resistance.
The total contact area between the electrode plate and the bipolar plate 2 is 8 cm 2 on both sides.

【表】【table】

【表】 比較例1は、バイポーラプレート表面の酸化皮
膜をグラインダーで研磨して除去してから測定に
用いた。 表から明らかな通り、実施例1及び2は溶融炭
酸塩型燃料電池の運転温度である500〜700℃にお
ける接触抵抗が比較例1,2にくらべて小さい。
又、実施例2から明らかなように、本発明による
ものは時間経過に伴う接触抵抗の増加が少ない。 従つて、かかるバイポーラプレートをカソード
側バイポーラプレートに用いれば、これに起因す
る電池出力の低下を抑えられることは明らかであ
る。
[Table] Comparative Example 1 was used for measurement after the oxide film on the surface of the bipolar plate was removed by polishing with a grinder. As is clear from the table, the contact resistance of Examples 1 and 2 at 500 to 700° C., which is the operating temperature of a molten carbonate fuel cell, is smaller than that of Comparative Examples 1 and 2.
Further, as is clear from Example 2, the contact resistance increases little with the passage of time in the case of the present invention. Therefore, it is clear that if such a bipolar plate is used as the cathode side bipolar plate, the decrease in battery output caused by this can be suppressed.

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

図は、接触抵抗の測定方法を示す説明図であ
る。 2…バイポーラプレート。
The figure is an explanatory diagram showing a method for measuring contact resistance. 2...Bipolar plate.

Claims (1)

【特許請求の範囲】 1 カソード側バイポーラプレートのカソードと
の接触面がアルカリ金属元素を含有する導電性部
材からなり、該導電性部材がオーステナイト系ス
テンレス鋼およびニツケルの少なくともいずれか
一方からなることを特徴とする溶融炭酸塩型燃料
電池。 2 特許請求の範囲第1項において、前記バイポ
ーラプレート全体が前記導電性部材からなること
を特徴とする溶融炭酸塩型燃料電池。 3 特許請求の範囲第1項又は第2項において、
前記バイポーラプレートの前記カソードとの接触
部表面のアルカリ金属元素濃度が最も高いことを
特徴とする溶融炭酸塩型燃料電池。 4 カソード側バイポーラプレートのカソードと
の接触面がアルカリ金属元素を含有する導電性部
材からなり、該導電性部材がオーステナイト系ス
テンレス鋼およびニツケルの少なくともいずれか
一方からなる溶融炭酸塩型燃料電池において、該
導電性部材をアルカリ金属塩の溶融物中に浸漬
し、加熱処理して該導電性部材にアルカリ金属元
素を含有させることを特徴とする溶融炭酸塩型燃
料電池の製造法。
[Claims] 1. The contact surface of the cathode-side bipolar plate with the cathode is made of a conductive member containing an alkali metal element, and the conductive member is made of at least one of austenitic stainless steel and nickel. Characteristics of molten carbonate fuel cells. 2. The molten carbonate fuel cell according to claim 1, wherein the entire bipolar plate is made of the conductive member. 3 In claim 1 or 2,
A molten carbonate fuel cell characterized in that a surface of the bipolar plate in contact with the cathode has the highest alkali metal element concentration. 4. In a molten carbonate fuel cell in which the contact surface of the cathode-side bipolar plate with the cathode is made of a conductive member containing an alkali metal element, and the conductive member is made of at least one of austenitic stainless steel and nickel, A method for producing a molten carbonate fuel cell, which comprises immersing the conductive member in a melt of an alkali metal salt and subjecting the conductive member to a heat treatment to cause the conductive member to contain an alkali metal element.
JP56124058A 1981-08-10 1981-08-10 Fuel cell and its manufacturing method Granted JPS5826463A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56124058A JPS5826463A (en) 1981-08-10 1981-08-10 Fuel cell and its manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56124058A JPS5826463A (en) 1981-08-10 1981-08-10 Fuel cell and its manufacturing method

Publications (2)

Publication Number Publication Date
JPS5826463A JPS5826463A (en) 1983-02-16
JPS6314815B2 true JPS6314815B2 (en) 1988-04-01

Family

ID=14875920

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56124058A Granted JPS5826463A (en) 1981-08-10 1981-08-10 Fuel cell and its manufacturing method

Country Status (1)

Country Link
JP (1) JPS5826463A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0637801B2 (en) * 1985-07-30 1994-05-18 清水建設株式会社 Architectural concrete member and manufacturing method thereof
US6432567B1 (en) * 1999-03-17 2002-08-13 Sulzer Hexis Ag Fuel cell battery with afterburning at the periphery of a cell stack

Also Published As

Publication number Publication date
JPS5826463A (en) 1983-02-16

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