JP2603917B2 - Method for manufacturing electrolyte plate of molten carbonate fuel cell - Google Patents
Method for manufacturing electrolyte plate of molten carbonate fuel cellInfo
- Publication number
- JP2603917B2 JP2603917B2 JP59197224A JP19722484A JP2603917B2 JP 2603917 B2 JP2603917 B2 JP 2603917B2 JP 59197224 A JP59197224 A JP 59197224A JP 19722484 A JP19722484 A JP 19722484A JP 2603917 B2 JP2603917 B2 JP 2603917B2
- Authority
- JP
- Japan
- Prior art keywords
- electrolyte
- plate
- fuel cell
- molten carbonate
- carbonate fuel
- 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
- H01M8/0289—Means for holding the electrolyte
- H01M8/0295—Matrices for immobilising electrolyte melts
-
- 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
-
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Description
【発明の詳細な説明】 〔発明の技術分野〕 本発明は溶融炭酸塩燃料電池の電解質板の製造方法の
改良に関する。Description: TECHNICAL FIELD The present invention relates to an improvement in a method for manufacturing an electrolyte plate of a molten carbonate fuel cell.
〔発明の技術的背景〕 溶融炭酸塩燃料電池は、対向して配置された一対のガ
ス拡散電極、すなわち燃料極と空気極との間に炭酸塩を
電解質として保持した電解質層を配して単位電池とし、
通常この単位電池をインターコネクタを介在させて複数
積層して構成されている。このような構成の溶融炭酸塩
燃料電池は、炭酸塩を溶融させた高温下において積層体
の燃料極に水素及び一酸化炭素を含む燃料ガスを、また
空気極に酸素及び二酸化炭素を含む混合ガスをそれぞれ
通流させることにより運転される。[Technical Background of the Invention] A molten carbonate fuel cell is formed by disposing a pair of gas diffusion electrodes opposed to each other, that is, an electrolyte layer holding carbonate as an electrolyte between a fuel electrode and an air electrode. Battery and
Usually, a plurality of the unit batteries are stacked with an interconnector interposed therebetween. In a molten carbonate fuel cell having such a configuration, a fuel gas containing hydrogen and carbon monoxide is supplied to the fuel electrode of the laminate at a high temperature in which carbonate is melted, and a mixed gas containing oxygen and carbon dioxide is supplied to the air electrode. Is operated by flowing each of them.
通常、溶融炭酸塩燃料電池には電解質層として電解質
タイルと呼ばれる電解質板が使用されている。従来、こ
の電解質タイルは、電解質を保持する骨材及び炭酸塩の
粉末を混合し、この混合物を成形用金型に注入して400
〜500℃で200〜500kg/cm2の圧力を加えて製造されてい
る。Usually, an electrolyte plate called an electrolyte tile is used as an electrolyte layer in a molten carbonate fuel cell. Conventionally, this electrolyte tile is prepared by mixing an electrolyte-holding aggregate and a carbonate powder, injecting the mixture into a molding die,
It is manufactured by applying a pressure of 200 to 500 kg / cm 2 at ~ 500 ° C.
しかし、上述したように成形用金型を用いて製造され
る電解質タイルは、成形用金型の内部で変形応力を受け
る。具体的には、プレス成形時に電解質タイルは応力を
受けて横方向へ広がろうとするが、電解質タイルは金型
により拘束されているので金型から反力を受ける。この
ように電解質タイルは端面から中心部へ向かう金型から
の反力を受けるため、製造中に割れを生じ易い。特に、
電解質タイルの大型化に伴い割れの発生は顕著となる。
また、製造時に割れの発生が認められなかった場合で
も、保管中あるいは発電試験中に製造時の残留応力の解
放による貫通割れが生じ易い。更に、成形用金型は重量
が大きいため操作性に乏しく、量産化、大型化が困難で
ある。However, as described above, the electrolyte tile manufactured using the molding die receives a deformation stress inside the molding die. Specifically, at the time of press molding, the electrolyte tile is subjected to stress and tends to spread in the lateral direction. However, since the electrolyte tile is restrained by the mold, it receives a reaction force from the mold. As described above, since the electrolyte tile receives a reaction force from the mold toward the center from the end face, the electrolyte tile is likely to be cracked during manufacturing. Especially,
As the size of the electrolyte tile increases, the occurrence of cracks becomes significant.
Further, even if no cracking is observed at the time of manufacturing, through cracking is likely to occur due to release of residual stress at the time of manufacturing during storage or power generation test. Furthermore, since the molding die is heavy, it is poor in operability, and it is difficult to mass-produce and enlarge it.
本発明は上記欠点を解消するためになされたものであ
り、製造時や保管中に割れが生じず、しかも量産化、大
型化が容易な溶融炭酸塩燃料電池の電解質板の製造方法
を提供しようとするものである。The present invention has been made in order to solve the above-mentioned drawbacks, and it is an object of the present invention to provide a method for producing an electrolyte plate of a molten carbonate fuel cell, which does not crack during production or storage, and can be easily mass-produced and enlarged. It is assumed that.
本発明の溶融炭酸塩燃料電池の電解質板の製造方法
は、上下一対のカーボン製プレス板のうち下方のプレス
板上に粘土製の枠を形成し、この枠の内側に電解質粉末
を充填し、前記一対のプレス板により直接ホットプレス
成形することを特徴とするものである。The method for producing an electrolyte plate of a molten carbonate fuel cell according to the present invention comprises forming a clay frame on a lower press plate of a pair of upper and lower carbon press plates, and filling electrolyte powder inside the frame. The hot pressing is directly performed by the pair of press plates.
このような方法によれば、ホットプレス成形時に下方
のプレス板上に形成された粘土製の枠は塑性変形するの
で、電解質板が応力を受けて横方向へ広がろうとする力
は粘土製の枠の塑性変形により吸収することができ、電
解質板の割れを減少させることができる。According to such a method, the clay frame formed on the lower press plate at the time of hot press molding is plastically deformed, so that the force for the electrolyte plate to expand in the lateral direction under stress is made of clay. It can be absorbed by plastic deformation of the frame, and cracks in the electrolyte plate can be reduced.
上述したような作用を有する枠を構成する粘土として
は、例えば焼結温度が600℃以上で有機成分を含有しな
いものが望ましい。As the clay constituting the frame having the above-described action, for example, a clay having a sintering temperature of 600 ° C. or more and containing no organic component is desirable.
また、プレス板としては、金属に比べて熱伝導性の良
好なカーボン板を用いることが望ましい。このようにカ
ーボン板を用いると、高温での加圧成形時の温度分布及
び付加圧力が均一となり、金型を用いる場合と比べて密
度変動の少ない均質な電解質板を製造することができ
る。また、カーボン板は金型に比べて軽量であるので、
操作し易く大型化も容易である。Further, as the press plate, it is desirable to use a carbon plate having better thermal conductivity than metal. When the carbon plate is used in this manner, the temperature distribution and the applied pressure at the time of high-pressure molding at a high temperature become uniform, and a homogeneous electrolyte plate having less density fluctuation than when a mold is used can be manufactured. Also, since the carbon plate is lighter than the mold,
It is easy to operate and large.
更に、カーボン板を用いれば、金型と比べてヒーター
容量を低減し、加熱・冷却時間ともに短縮することがで
きる。しかも、粘土製の枠を形成したプレス板を多層重
ねることにより複数枚の電解質板を同時にホットプレス
成形することができ、量産性を向上することができる。Further, if a carbon plate is used, the heater capacity can be reduced as compared with the mold, and both the heating and cooling times can be shortened. In addition, a plurality of electrolyte plates can be simultaneously hot-pressed by stacking a plurality of press plates each having a clay frame, thereby improving mass productivity.
以下、本発明の実施例を図面を参照して説明する。 Hereinafter, embodiments of the present invention will be described with reference to the drawings.
実施例1 まず、図に示すように厚さ10mm、36cm角のカーボン板
1上の20cm角の正方形の領域を囲むように幅10mm、厚さ
9mmの粘土製の枠2を形成した下部プレス板3を用意
し、粘土製の枠2に囲まれたカーボン板1上に200gの電
解質粉末(LiAlO2:80g、Li2CO3:56g、K2CO3:64g)を均
一に充填した。次に、前記下部プレス板3を構成するカ
ーボン板1と同一形状のカーボン板からなる上部プレス
板4を粉末充填面上に乗せ、上下のプレス板3、4で粉
末を挟んだ状態で高温加圧装置の下部ヒーター板上に設
置し、温度465℃、圧力300kg/cm2の条件で30分間プレス
成形を行なった。Example 1 First, as shown in the figure, a width of 10 mm and a thickness of 10 mm were applied so as to surround a square area of 20 cm square on a 36 cm square carbon plate 1.
A lower press plate 3 having a 9 mm clay frame 2 is prepared, and 200 g of electrolyte powder (LiAlO 2 : 80 g, Li 2 CO 3 : 56 g, K) is placed on a carbon plate 1 surrounded by the clay frame 2. 2 CO 3 : 64 g). Next, an upper press plate 4 made of a carbon plate having the same shape as the carbon plate 1 constituting the lower press plate 3 is placed on the powder filling surface, and the powder is sandwiched between the upper and lower press plates 3 and 4 at a high temperature. It was set on the lower heater plate of the pressure device and press-formed at a temperature of 465 ° C. and a pressure of 300 kg / cm 2 for 30 minutes.
この工程で電解質粉末および粘土製の枠2は上下のプ
レス板3、4からの成形応力を受ける。この際、電解質
粉末はプレス板から圧縮応力を受けて圧縮されるととも
に横方向へ広がろうとする。また、粘土製の枠2もその
上部が押し潰されるとともに横方向へ広がろうとする
が、内側からも電解質粉末が横方向へ広がろうとする力
を受ける。したがって、電解質粉末が横方向へ広がろう
とする力は粘土製の枠2の塑性変形により吸収すること
ができ、電解質板の割れを減少させることができる。な
お、上記のような機構により、粘土製の枠2自体が横方
向へ広がろうとする力と、その内側の電解質粉末が横方
向へ広がろうとする力とはほぼ拮抗するので、粘土製の
枠2の内側の寸法は成形前の寸法からそれほど変化しな
い。ただし、最終的には電解質板の端面を加工した後、
実用に供する。In this step, the frame 2 made of the electrolyte powder and the clay receives molding stress from the upper and lower press plates 3 and 4. At this time, the electrolyte powder is compressed by receiving compressive stress from the press plate and tends to spread in the lateral direction. The clay frame 2 is also crushed at its upper part and tends to spread in the lateral direction, but also receives a force from the inside to spread the electrolyte powder in the lateral direction. Therefore, the force by which the electrolyte powder tries to spread in the lateral direction can be absorbed by the plastic deformation of the clay frame 2, and cracks in the electrolyte plate can be reduced. In addition, by the mechanism as described above, the force of the clay frame 2 itself trying to spread in the horizontal direction and the force of the electrolyte powder inside it trying to spread in the horizontal direction substantially oppose each other. The dimensions inside the frame 2 do not change much from the dimensions before molding. However, after processing the end face of the electrolyte plate,
Put it to practical use.
この方法により10枚中8枚の割れ、反りのない20cm角
の電解質板を得ることができた。また、得られた電解質
板の密度分布を超音波パルスエコー法により測定したと
ころ、同一電解質板内における密度変動は4%以内であ
った。更に、製造後の電解質板を真空デシケータ中に2
週間保管したものについて、遅れ割れを発生したものは
なかった。By this method, eight out of ten sheets of 20 cm square electrolyte plates without cracks and warpage could be obtained. When the density distribution of the obtained electrolyte plate was measured by an ultrasonic pulse echo method, the density variation within the same electrolyte plate was within 4%. Further, the manufactured electrolyte plate is placed in a vacuum desiccator for 2 minutes.
None of the items stored for weeks exhibited delayed cracking.
実施例2 上記実施例1と同様に200gの電解質粉末を充填した下
部プレス板3を2層重ね、更に上部プレス板4を載せた
状態で高温加圧装置の下部ヒーター上に設置し、実施例
1と同様な条件でプレス成形を行なった。Example 2 In the same manner as in Example 1 above, two layers of the lower press plate 3 filled with 200 g of electrolyte powder were stacked, and further placed on the lower heater of the high-temperature pressurizing device with the upper press plate 4 placed thereon. Press molding was performed under the same conditions as in Example 1.
この方法により2枚の電解質板を一度に製造すること
ができ、16枚中13枚の割れ、反りのない20cm角の電解質
板を得ることができた。また、得られた電解質板の密度
分布を超音波パルスエコー法により測定したところ、同
一電解質板内における密度変動は4.5%以内であった。
更に、製造後の電解質板を真空デシケータ中に2週間保
管したものについて、遅れ割れを発生したものはなかっ
た。By this method, two electrolyte plates could be manufactured at a time, and 13 out of 16 electrolyte plates of 20 cm square without cracks and warpage could be obtained. When the density distribution of the obtained electrolyte plate was measured by the ultrasonic pulse echo method, the density variation within the same electrolyte plate was within 4.5%.
Furthermore, none of the manufactured electrolyte plates was stored in a vacuum desiccator for 2 weeks, and no delayed cracking occurred.
比較例 内寸法20cmの金型に電解質粉末を200g充填し、十分均
一にならした後、上パンチを載せ、上記実施例1と同一
の装置内に設置した後、実施例1と同様に温度465℃、
圧力300kg/cm2の条件で30分間プレス成形を行なった。Comparative Example 200 g of an electrolyte powder was filled into a mold having an inner size of 20 cm, and after uniforming sufficiently, an upper punch was placed, and the mold was placed in the same apparatus as in the first embodiment. ℃,
Press molding was performed under a pressure of 300 kg / cm 2 for 30 minutes.
こうした従来の方法では10枚中6枚しか割れ、反りの
ない20cm角の電解質板が得られなかった。また、得られ
た電解質板の密度分布を超音波パルスエコー法により測
定したところ、同一電解質板内の密度変動は6%と本発
明方法による場合よりも大きかった。更に、製造後の電
解質板を真空デシケータ中に2週間保管したところ6枚
中2枚に割れが発生した。According to such a conventional method, only six sheets out of ten sheets were broken, and a 20 cm square electrolyte plate without warpage could not be obtained. When the density distribution of the obtained electrolyte plate was measured by the ultrasonic pulse echo method, the density fluctuation in the same electrolyte plate was 6%, which was larger than that in the case of the method of the present invention. Further, when the manufactured electrolyte plate was stored in a vacuum desiccator for two weeks, cracks occurred in two of the six plates.
以上詳述した如く本発明の溶融炭酸塩燃料電池の電解
質板の製造方法によれば、製造中あるいは保管中の電解
質板の割れの発生が少なく、かつ均質性を向上すること
ができ、しかも量産性を発揮できる等顕著な効果を奏す
るものである。As described above in detail, according to the method for producing an electrolyte plate of a molten carbonate fuel cell of the present invention, the occurrence of cracks in the electrolyte plate during production or storage can be reduced, the homogeneity can be improved, and mass production can be achieved. It has a remarkable effect, such as being able to exert its properties.
第1図は本発明の実施例において用いられるプレス板の
斜視図である。 1……カーボン板、2……粘土製の枠、3……下部プレ
ス板、4……上部プレス板。FIG. 1 is a perspective view of a press plate used in an embodiment of the present invention. 1 ... carbon plate, 2 ... clay frame, 3 ... lower press plate, 4 ... upper press plate.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 柘植 章彦 川崎市幸区小向東芝町1番地 株式会社 東芝総合研究所内 (56)参考文献 特開 昭57−29407(JP,A) 特開 昭50−9173(JP,A) 実公 昭29−16172(JP,Y1) ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Akihiko Tsuge 1 Toshiba-cho, Komukai, Sachi-ku, Kawasaki-shi Inside Toshiba Research Institute, Inc. (56) References JP-A-57-29407 (JP, A) JP-A-50 −9173 (JP, A) Jiko 29-16172 (JP, Y1)
Claims (2)
のプレス板上に粘土製の枠を形成し、この枠の内側に電
解質粉末を充填し、前記一対のプレス板により直接ホッ
トプレス成形することを特徴とする溶融炭酸塩燃料電池
の電解質板の製造方法。1. A clay frame is formed on a lower press plate of a pair of upper and lower carbon press plates, and the inside of the frame is filled with an electrolyte powder, and directly hot-pressed by the pair of press plates. A method for producing an electrolyte plate of a molten carbonate fuel cell, characterized by comprising:
ることにより複数枚の電解質板を同時にホットプレス成
形することを特徴とする特許請求の範囲第1項記載の溶
融炭酸塩燃料電池の電解質板の製造方法。2. The molten carbonate fuel cell according to claim 1, wherein a plurality of electrolyte plates are simultaneously hot-pressed by stacking a plurality of press plates each having a clay frame formed thereon. A method for manufacturing an electrolyte plate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59197224A JP2603917B2 (en) | 1984-09-20 | 1984-09-20 | Method for manufacturing electrolyte plate of molten carbonate fuel cell |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59197224A JP2603917B2 (en) | 1984-09-20 | 1984-09-20 | Method for manufacturing electrolyte plate of molten carbonate fuel cell |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6177272A JPS6177272A (en) | 1986-04-19 |
JP2603917B2 true JP2603917B2 (en) | 1997-04-23 |
Family
ID=16370900
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59197224A Expired - Fee Related JP2603917B2 (en) | 1984-09-20 | 1984-09-20 | Method for manufacturing electrolyte plate of molten carbonate fuel cell |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2603917B2 (en) |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5427806B2 (en) * | 1973-05-30 | 1979-09-12 | ||
JPS5729407A (en) * | 1980-07-29 | 1982-02-17 | Ibigawa Electric Ind Co Ltd | Graphitic hot press mold |
-
1984
- 1984-09-20 JP JP59197224A patent/JP2603917B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPS6177272A (en) | 1986-04-19 |
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