JPH0544780B2 - - Google Patents
Info
- Publication number
- JPH0544780B2 JPH0544780B2 JP60002002A JP200285A JPH0544780B2 JP H0544780 B2 JPH0544780 B2 JP H0544780B2 JP 60002002 A JP60002002 A JP 60002002A JP 200285 A JP200285 A JP 200285A JP H0544780 B2 JPH0544780 B2 JP H0544780B2
- Authority
- JP
- Japan
- Prior art keywords
- molten carbonate
- titanium
- aluminum
- separator
- less
- 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 - Fee Related
Links
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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0206—Metals or alloys
-
- 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
- H01M8/14—Fuel cells with fused electrolytes
- H01M2008/147—Fuel cells with molten carbonates
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2300/00—Electrolytes
- H01M2300/0017—Non-aqueous electrolytes
- H01M2300/0048—Molten electrolytes used at high temperature
- H01M2300/0051—Carbonates
-
- 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
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0206—Metals or alloys
- H01M8/0208—Alloys
- H01M8/021—Alloys based on iron
-
- 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
〔発明の利用分野〕
本発明は、溶融炭酸塩型燃料電池用セパレータ
に関するものである。
〔発明の背景〕
近年、石油資源の枯渇及び価格の高騰に対拠
し、省エネルギー機器の開発・研究が重要な問題
となつている。それに対して、LNG及び石炭ガ
スを利用する溶融炭酸塩型燃料電池は省エネルギ
ー、石油代替エネルギーをめざすものであり、新
エネルギー開発の一環をなす火力発電技術であ
る。
第4図は溶融炭酸塩型燃料電池の基本構造図を
示す。電池の構成は電解質1、電極のアノード2
及びカソード3、そして本発明が対象としている
セパレータ4からなつている。溶融燃料電池は炭
酸リチユーム(Li2,CO3)、炭酸カリウム
(K2CO3)等のアルカリ金属炭酸塩を電解質とし
て、その融点以上の600〜750℃の温度域で作動さ
せる燃料電池である。電池はアノードに燃料であ
る水素、あるいは水素含有ガスを供給し、カソー
ドには酸化剤である空気+炭酸ガスを供給するこ
とにより、次式に示す電気化学的反応が進行して
発電が行なわれるものである。
アノード(水素極):2H2+2CO3 2-→2CO2
+2H2O+4e- …(1)
カソード(空気極):O2+2CO2+4e-→2CO3 2-
…(2)
(1)式+(2)式 :2H2+O2+2H2O …(3)
セパレータ4は水素燃焼ガス及び酸化剤ガスの
分離及び集電の役割を兼れている。第4図は単セ
パレータの電池の構成を示したが、実機では電圧
を高め大容量化するために電池を多数積層するこ
とになる。第5図は大容量化に伴つて適用される
セパレータ4の基本構造を示す。そのセパレータ
4は1枚の板の表裏面において、ガス流通用の溝
5が施されている。その表裏面には前述の(1),
(2),(3)式で示したごとく、電気的反応及びガス雰
囲気がそれぞれ異なる。したがつて、セパレータ
材料としては600〜750℃でアノード側における雰
囲気(水素含有ガス)及びカソード側ひおける雰
囲気(酸素ガス)の両者に対して耐食性の優れた
ものが要求される。
セパレータ材料としては富士時報(55巻 1982
年)に記載されているごとく、オーステナイト系
ステンレス鋼SUS316鋼が適用されている。しか
し、溶融炭酸塩型燃料電池の腐食環境において
は、SUS316は腐食量が多く、長期間使用する上
で問題であつた。
〔発明の目的〕
本発明の目的は前記の腐食環境においても耐食
性の優れた溶融炭酸塩型燃料電池用セパレータを
提供する。
〔発明の概要〕
本発明は、溶融炭酸塩型燃料電池用のセパレー
タとして、水素含有雰囲気及び酸化雰囲気におい
て、優れた耐食性が得られるものであり、重量で
C0.03〜0.1%、Si0.5〜1.5%、Mn0.5〜2.0%、
Cr21.5〜30.5%、Mo0.08〜2.80%、Al0.7%未満、
Ti0.7%未満、Al+Ti0.4〜0.7%、又はこれに
Y0.1〜1.0%を含み、残部がFe及び不可避不純物
からなることを特徴とする。
Cは組織の安定性及び強度向上のために0.03%
以上必要な元素である。しかし、0.1%以上添加
すると、靭性を低下させ、耐食性を低下させる。
したがつて、Cは0.03〜0.1%とする。Crは耐食
性を向上させる元素である。しかし、21.5%以下
ではその効果は少なく、逆に30.5%を越えても大
きな効果がなく、組織を不安定にし、著しく靭性
を低める。したがつて、Cr添加量は21.5〜30.5%
とする。Siは脱酸剤として添加する他、耐食性向
上のために添加するものであり、0.5〜1.5%とす
る。Al及びTiは耐食性向上のために微量添加す
るものである。各々は0.7%未満含有されるが、
両者の総量が0.4%以下ではその効果はなく、逆
に0.7%以上では大きな効果はなく、加工性を損
う。したがつて、0.4〜0.7%とする。Mnは脱酸
剤と添加するものである。その効果は0.5〜2.0%
で十分である。Moは耐食性及び強度を向上させ
るのに効果がある。その効果は0.08%以下では効
果がなく、2.80%を越えても大きな効果がない。
したがつて0.08〜2.80%とする。更にYは微量で
耐食性を向上させるのに効果がある。その量は
0.1%以下では効果がなく、1.0%を越えても大き
な効果がない。したがつて、0.1〜1.0%とする。
〔発明の実施例〕
第1表はセパレータ材として用いた試料の化学
組成(重量%)である。残部はFeである。第2
表は耐食性腐食実験で行なつた腐食試験条件を示
す。腐食試験条件は実機の環境を模擬し、2種類
の腐食条件を用いた。試験温度及び時間はいずれ
も650℃、100時間で実施した。また、試験片には
あらかじめLiCO3:K2CO3=62:38(モル比)の
炭酸塩を塗布した。
比較のために市販のSUS304及び316について
試験した。
腐食試験片の形状は幅15mm、長さ25mm、厚さ4
mmである。
[Field of Application of the Invention] The present invention relates to a separator for a molten carbonate fuel cell. [Background of the Invention] In recent years, in response to the depletion of oil resources and soaring prices, the development and research of energy-saving equipment has become an important issue. In contrast, molten carbonate fuel cells that use LNG and coal gas aim to save energy and replace oil, and are a thermal power generation technology that is part of new energy development. FIG. 4 shows a basic structural diagram of a molten carbonate fuel cell. The battery consists of 1 electrolyte and 2 anode electrodes.
and a cathode 3, and a separator 4, which is the object of the present invention. A molten fuel cell is a fuel cell that uses an alkali metal carbonate such as lithium carbonate (Li 2 , CO 3 ) or potassium carbonate (K 2 CO 3 ) as an electrolyte and operates at a temperature range of 600 to 750°C, above its melting point. . In a battery, hydrogen or hydrogen-containing gas is supplied as a fuel to the anode, and air + carbon dioxide as an oxidizing agent is supplied to the cathode, whereby the electrochemical reaction shown in the following formula progresses and power is generated. It is something. Anode (hydrogen electrode): 2H 2 +2CO 3 2- →2CO 2 +2H 2 O+4e - …(1) Cathode (air electrode): O 2 +2CO 2 +4e - →2CO 3 2-
...(2) Equation (1) + Equation (2): 2H 2 +O 2 +2H 2 O ...(3) The separator 4 has the role of separating hydrogen combustion gas and oxidant gas and collecting current. Although FIG. 4 shows the configuration of a single separator battery, in an actual machine, a large number of batteries will be stacked to increase the voltage and increase the capacity. FIG. 5 shows the basic structure of a separator 4 that is applied as capacity increases. The separator 4 is a single plate with grooves 5 for gas circulation on the front and back surfaces. On the front and back sides are the above-mentioned (1),
As shown in equations (2) and (3), the electrical reactions and gas atmospheres are different. Therefore, the separator material is required to have excellent corrosion resistance in both the atmosphere (hydrogen-containing gas) on the anode side and the atmosphere (oxygen gas) on the cathode side at 600 to 750°C. Fuji Jiho (volume 55, 1982) is used as a separator material.
As stated in 2012), austenitic stainless steel SUS316 steel is used. However, in the corrosive environment of molten carbonate fuel cells, SUS316 suffers from a large amount of corrosion, which poses a problem for long-term use. [Object of the Invention] An object of the present invention is to provide a separator for a molten carbonate fuel cell that has excellent corrosion resistance even in the above-mentioned corrosive environment. [Summary of the Invention] The present invention provides a separator for molten carbonate fuel cells that provides excellent corrosion resistance in a hydrogen-containing atmosphere and an oxidizing atmosphere, and is
C0.03~0.1%, Si0.5~1.5%, Mn0.5~2.0%,
Cr21.5~30.5%, Mo0.08~2.80%, Al less than 0.7%,
Ti less than 0.7%, Al + Ti 0.4~0.7%, or above
It is characterized by containing 0.1 to 1.0% Y, with the remainder consisting of Fe and inevitable impurities. C is 0.03% to improve the stability and strength of the structure.
These are the necessary elements. However, adding 0.1% or more lowers toughness and corrosion resistance.
Therefore, C should be 0.03 to 0.1%. Cr is an element that improves corrosion resistance. However, if the content is less than 21.5%, the effect is small, and if it exceeds 30.5%, there is no significant effect, making the structure unstable and significantly reducing the toughness. Therefore, the amount of Cr added is 21.5 to 30.5%.
shall be. In addition to being added as a deoxidizing agent, Si is added to improve corrosion resistance, and is set at 0.5 to 1.5%. Al and Ti are added in small amounts to improve corrosion resistance. Each contains less than 0.7%,
If the total amount of both is less than 0.4%, there is no effect, and on the other hand, if it is more than 0.7%, there is no significant effect and workability is impaired. Therefore, it is set at 0.4 to 0.7%. Mn is added as a deoxidizing agent. The effect is 0.5-2.0%
is sufficient. Mo is effective in improving corrosion resistance and strength. There is no effect below 0.08%, and there is no significant effect even above 2.80%.
Therefore, it is set at 0.08 to 2.80%. Furthermore, even a small amount of Y is effective in improving corrosion resistance. The amount is
There is no effect when it is less than 0.1%, and there is no significant effect even when it exceeds 1.0%. Therefore, it is set at 0.1 to 1.0%. [Examples of the Invention] Table 1 shows the chemical compositions (% by weight) of samples used as separator materials. The remainder is Fe. Second
The table shows the corrosion test conditions conducted in the corrosion resistance corrosion experiment. The corrosion test conditions simulated the environment of the actual machine, and two types of corrosion conditions were used. The test temperature and time were both 650°C and 100 hours. Further, a carbonate of LiCO 3 :K 2 CO 3 =62:38 (mole ratio) was coated on the test piece in advance. For comparison, commercially available SUS304 and 316 were tested. The shape of the corrosion test piece is 15 mm wide, 25 mm long, and 4 mm thick.
mm.
【表】【table】
【表】【table】
以上のごとく、本発明は腐食性に優れており、
溶融炭酸塩型燃料電池用セパレータとして長寿命
となることが明らかである。
As described above, the present invention has excellent corrosion resistance,
It is clear that the separator has a long life as a separator for molten carbonate fuel cells.
第1図、第2図、第3図はそれぞれ本発明の溶
融炭酸塩型燃料電池用セパレータ材としての腐食
量を示す図、第4図は本発明のセパレータを適用
する溶融炭酸塩型燃料電池の斜視図、第5図は第
4図の電池を大容量化した場合の積層構造図であ
る。
1…電解質、2…アノード、3…カソード、4
…セパレータ。
Figures 1, 2, and 3 are diagrams showing the amount of corrosion of the separator material for a molten carbonate fuel cell according to the present invention, and Figure 4 is a diagram showing the amount of corrosion in a molten carbonate fuel cell to which the separator of the present invention is applied. FIG. 5 is a perspective view of the battery shown in FIG. 4, and a diagram of the laminated structure when the capacity is increased. 1... Electrolyte, 2... Anode, 3... Cathode, 4
...Separator.
Claims (1)
空気と二酸化炭素からなる混合ガスにさらされる
と共に、表面に溶融炭酸塩が付着し、温度が600
〜750℃になる溶融炭酸塩型燃料電池用セパレー
タにおいて、重量で炭素0.03〜0.1%、ケイ素0.5
〜1.5%、マンガン0.5〜2%、クローム21.5〜
30.5%、モリブデン0.08〜2.80%、アルミニウム
0.7%未満、チタン0.7%未満、アルミニウムとチ
タンの総量が0.4〜0.7%、残部が鉄及び不可避不
純物からなることを特徴とする溶融炭酸塩型燃料
電池用セパレータ。 2 水素、二酸化炭素、水からなる混合ガス及び
空気と二酸化炭素からなる混合ガスにさらされる
と共に、表面に溶融炭酸塩が付着し、温度が600
〜750℃になる溶融炭酸塩型燃料電池用セパレー
タにおいて、重量で炭素0.03〜0.1%、ケイ素0.5
〜1.5%、マンガン0.5〜2%、クローム21.5〜
30.5%、モリブデン0.08〜2.80%、アルミニウム
0.7%未満、チタン0.7%未満、アルミニウムとチ
タンの総量が0.4〜0.7%、イツトリウム0.1〜1.0
%、残部が鉄及び不可避不純物からなることを特
徴とする溶融炭酸塩型燃料電池用セパレータ。[Claims] 1. It is exposed to a mixed gas consisting of hydrogen, carbon dioxide, and water, and a mixed gas consisting of air and carbon dioxide, and molten carbonate adheres to the surface, and the temperature is 600℃.
In separators for molten carbonate fuel cells that reach ~750°C, 0.03-0.1% carbon and 0.5% silicon by weight.
~1.5%, manganese 0.5~2%, chromium 21.5~
30.5%, molybdenum 0.08-2.80%, aluminum
A separator for a molten carbonate fuel cell, characterized in that the total amount of aluminum and titanium is less than 0.7%, less than 0.7% titanium, the total amount of aluminum and titanium is 0.4 to 0.7%, and the balance is iron and inevitable impurities. 2. It is exposed to a mixed gas consisting of hydrogen, carbon dioxide, and water, and a mixed gas consisting of air and carbon dioxide, and molten carbonate adheres to the surface, and the temperature reaches 600℃.
In separators for molten carbonate fuel cells that reach ~750°C, 0.03-0.1% carbon and 0.5% silicon by weight.
~1.5%, manganese 0.5~2%, chromium 21.5~
30.5%, molybdenum 0.08-2.80%, aluminum
less than 0.7%, titanium less than 0.7%, total amount of aluminum and titanium 0.4-0.7%, yttrium 0.1-1.0
%, the balance being iron and unavoidable impurities.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60002002A JPS61161665A (en) | 1985-01-11 | 1985-01-11 | Separator for molten carbonate fuel cells |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60002002A JPS61161665A (en) | 1985-01-11 | 1985-01-11 | Separator for molten carbonate fuel cells |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61161665A JPS61161665A (en) | 1986-07-22 |
| JPH0544780B2 true JPH0544780B2 (en) | 1993-07-07 |
Family
ID=11517208
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60002002A Granted JPS61161665A (en) | 1985-01-11 | 1985-01-11 | Separator for molten carbonate fuel cells |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61161665A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0644488B2 (en) * | 1987-10-28 | 1994-06-08 | 株式会社日立製作所 | Molten carbonate fuel cell |
| EP1942539B1 (en) * | 2006-12-07 | 2010-03-17 | Ansaldo Fuel Cells S.p.A. | Flanges for the separator plate of molten carbonate fuel cells |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS505973A (en) * | 1973-05-20 | 1975-01-22 | ||
| JPS5188413A (en) * | 1975-02-01 | 1976-08-03 | Kotaishokuseifueraitosutenresuko | |
| JPS5919984B2 (en) * | 1980-09-19 | 1984-05-10 | 大同特殊鋼株式会社 | Corrosion-resistant material for molten sodium polysulfide |
| JPS59201371A (en) * | 1983-04-30 | 1984-11-14 | Agency Of Ind Science & Technol | Molten carbonate fuel cell |
-
1985
- 1985-01-11 JP JP60002002A patent/JPS61161665A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61161665A (en) | 1986-07-22 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |