JPH0320970A - Removing method of binder in electrolyte plate in fuel cell - Google Patents
Removing method of binder in electrolyte plate in fuel cellInfo
- Publication number
- JPH0320970A JPH0320970A JP1154461A JP15446189A JPH0320970A JP H0320970 A JPH0320970 A JP H0320970A JP 1154461 A JP1154461 A JP 1154461A JP 15446189 A JP15446189 A JP 15446189A JP H0320970 A JPH0320970 A JP H0320970A
- Authority
- JP
- Japan
- Prior art keywords
- binder
- organic solvent
- electrolyte plate
- fuel cell
- cathode
- 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.)
- Granted
Links
- 239000011230 binding agent Substances 0.000 title claims abstract description 60
- 239000003792 electrolyte Substances 0.000 title claims abstract description 44
- 239000000446 fuel Substances 0.000 title claims abstract description 34
- 238000000034 method Methods 0.000 title claims description 21
- 239000003960 organic solvent Substances 0.000 claims abstract description 37
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 239000002904 solvent Substances 0.000 abstract description 5
- 230000001172 regenerating effect Effects 0.000 abstract 2
- 239000007789 gas Substances 0.000 description 16
- 238000005238 degreasing Methods 0.000 description 7
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 6
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 5
- YQNQTEBHHUSESQ-UHFFFAOYSA-N lithium aluminate Chemical compound [Li+].[O-][Al]=O YQNQTEBHHUSESQ-UHFFFAOYSA-N 0.000 description 5
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 description 4
- 230000001590 oxidative effect Effects 0.000 description 3
- 230000008929 regeneration Effects 0.000 description 3
- 238000011069 regeneration method Methods 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000011164 primary particle Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004811 liquid chromatography Methods 0.000 description 1
- 239000011812 mixed powder Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920002037 poly(vinyl butyral) polymer Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
Classifications
-
- 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
- Fuel Cell (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は燃利の有する化学エネルギーを直接電気エネル
ギーに変換させるエネルギ一部門で用いる燃料電池にお
ける電解質板中の結合剤除去方法に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for removing a binder from an electrolyte plate in a fuel cell used in the energy sector for directly converting the chemical energy of fuel into electrical energy. .
[従来の技術]
現在までに提案されている燃料電池のうち、溶融炭酸塩
型の燃料電池としては、たとえば、第3図に一例を示づ
如く、電解質として溶融炭酸塩を多孔貿物質にしみ込ま
せた電解貿仮(タイノレ)1を、カソード〈酸素4垂〉
2とアノード(燃料極)3の両電極で両面から挟み、カ
ソード2側に酸化ガスOGを供給すると共にアノート3
側に燃料ガスFGを供給づることによりカソード2とア
ノード3との間で発生する電位差により発電が行われる
ようにしたものを1セルCとし、各セルCをセパレータ
4を介し多層に積層して燃料電池スタックSとするよう
にしてある。[Prior Art] Among the fuel cells that have been proposed to date, the molten carbonate type fuel cell is one in which molten carbonate is impregnated into a porous material as an electrolyte, as shown in an example in Fig. 3. Electrolytic trade temporary (TAINORE) 1 with a cathode (oxygen 4 drops)
It is sandwiched between both electrodes 2 and anode (fuel electrode) 3, and oxidizing gas OG is supplied to the cathode 2 side, and the anode 3
One cell C is one in which electricity is generated by the potential difference generated between the cathode 2 and anode 3 by supplying fuel gas FG to the side, and each cell C is stacked in multiple layers with a separator 4 in between. It is designed to be a fuel cell stack S.
上記燃料電池において、内部マニホールド型のものでは
、上記電解質板1及びヒパレータ4の各周辺部間をウエ
ットシールできるようにしてあると共に、上記各周辺部
に、酸化ガスOGの供給側及び排出側の流路孔5及び6
と、燃料ガスFGの供給側−及び排出側の流路孔7及び
8をそれぞれ設け、各セパレータ4の表裏両面に設けた
凹凸により形成されるカソード2側のガス通路9とアノ
ード3側のガス通路10を各々のガスが流れるようにし
てある。In the fuel cell described above, in the case of the internal manifold type, it is possible to wet-seal between the peripheral parts of the electrolyte plate 1 and the hipparator 4, and a supply side and a discharge side of the oxidizing gas OG are attached to each peripheral part. Channel holes 5 and 6
A gas passage 9 on the cathode 2 side and a gas passage on the anode 3 side are provided with passage holes 7 and 8 on the supply side and discharge side of the fuel gas FG, respectively, and are formed by unevenness provided on both the front and back sides of each separator 4. Each gas is made to flow through the passage 10.
上記燃料電池で用いられる電解質板1は、当初、リチウ
ムアルミネート(LiANO2)と炭酸塩の混合粉を金
型に充填し、真空中で加熱した後高圧でプレス或形を行
うというポットプレス法により¥1していたが、大型化
、量産化が困難であるため、近年はテープ或形法により
製造されるようになってきている。The electrolyte plate 1 used in the above fuel cell was initially manufactured using a pot press method in which a mixed powder of lithium aluminate (LiANO2) and carbonate was filled into a mold, heated in a vacuum, and then pressed or shaped under high pressure. It used to cost 1 yen, but because it is difficult to make it large and mass-produce it, in recent years it has been manufactured using a tape molding method.
上記テープ或形法による電解質板の製造方法は、第4図
に示す如く、先ず、リチウムアルミネート粉末の原料粉
11にアセトン、アルコール類、MEK (メチルエチ
ルケトン)等の有機溶剤12と、界面活性剤からなる分
敗剤13とを添加し、ボールミル等の粉砕装置14でこ
れらを粉砕し混合して上記リチウムアルミネートを一次
粒子まで分改させ、次に、この一次粒子まで分散させた
りチウムアルミネートにフタル酸等の可塑剤15と、ポ
リビニルブヂラール等の結合剤(バインダー〉16とを
添加し混合してスラリ17化し、続いて、このスラリ1
7をドクターブレード装置や押し出し成形装置、カレン
ダロール装置等のテープ或形装置18によりテープ成形
し、更に乾燥室19にて焼成することにより、電解質板
1を製造するものである。As shown in FIG. 4, the method for producing an electrolyte plate using the above-mentioned tape or shaping method is as follows: First, a raw material powder 11 of lithium aluminate powder is mixed with an organic solvent 12 such as acetone, alcohol, MEK (methyl ethyl ketone), and a surfactant. The lithium aluminate is divided into primary particles by adding a separating agent 13 consisting of a lithium aluminate, pulverizing and mixing them with a pulverizer 14 such as a ball mill, and then dispersing the lithium aluminate to primary particles. A plasticizer 15 such as phthalic acid and a binder 16 such as polyvinyl butyral are added and mixed to form a slurry 17, and then this slurry 1
The electrolyte plate 1 is manufactured by forming the electrolyte plate 7 into a tape using a tape forming device 18 such as a doctor blade device, an extrusion molding device, or a calender roll device, and then baking it in a drying chamber 19.
上述したテープ成形法により製造された電解質板1は、
結合剤16という有機物を含んでいるため、電池運転前
に電解質板1から結合剤16を除去する脱脂処理が必要
である。すなわら、電解質板1に結合剤16及びこれに
起因する炭素分が除去されないで残っている状態のまま
で電池の運転が行われると、電解質としての溶融炭酸塩
が電解質板1にしみ込むことができなくて電池として使
用できないばかりでなく、特に、ウエットシール部に結
合剤16が残っていると、このウェットシール部に炭酸
塩がしみ込まなくなってシール性が阻害されることにな
るため、製造された電解質板1から結合剤16を除去ず
ることが必要である。従来、電解質板1から結合剤16
を除去する方法として、電池を組み立てた後、徐々に昇
温ざせて焼くことにより上記結合剤16の除去を行うよ
うにしていた。The electrolyte plate 1 manufactured by the tape molding method described above is
Since it contains an organic substance called binder 16, it is necessary to perform a degreasing process to remove binder 16 from electrolyte plate 1 before battery operation. In other words, if the battery is operated with the binder 16 and the resulting carbon remaining on the electrolyte plate 1 without being removed, molten carbonate as the electrolyte may seep into the electrolyte plate 1. Not only is it impossible to use the battery as a result of the failure, but in particular, if the binder 16 remains in the wet seal area, the carbonate will no longer penetrate into the wet seal area and the sealing performance will be impaired. It is necessary to remove the binder 16 from the electrolyte plate 1. Conventionally, from the electrolyte plate 1 to the binder 16
As a method for removing the binder 16, after the battery is assembled, the binder 16 is removed by gradually raising the temperature and baking it.
[発明が解決しようとする課題]
ところが、上記従来の結合剤の除去方法では、数10〜
100時間という長時間をかけて焼かねばならないため
除去に多くの時間がかかること、除去の際、かなりの悪
臭が発生すること、更に除去が終了したかどうかの判定
(脱脂判定)が難しいこと、等の問題があった。[Problems to be Solved by the Invention] However, in the conventional binder removal method described above, the number of
It takes a long time to remove because it has to be baked for a long time of 100 hours, a considerable odor is generated during removal, and it is difficult to judge whether the removal has been completed (degreasing judgment). There were other problems.
そこで、本発明は電解質板中の結合剤の除去を、悪臭を
発生させることなく常温下にて短時間で行えるようにし
、且つ脱脂状態の判定を簡単に行うことかできるように
しようとするものである。Therefore, the present invention aims to make it possible to remove the binder in the electrolyte plate in a short time at room temperature without generating any bad odor, and to make it possible to easily determine the degreased state. It is.
[課題を解決するための手段]
本発明は、上記課題を解決するために、製造時に用いた
結合剤を含む電解質板をカソードとアノードの両電極で
両面から挟むようにしてなるセルをセパレータを介し多
囮に積層して各セルのカソード側とアノート側にガス通
路を有する燃料電池スタックとし、該燃料電池スタック
の各セルごとの電解質板中から結合剤を除去する燃籾電
池における電解質板中の結合剤除去方法において、上記
燃料電池スタックの各セルごとのカソード側とアノード
側の各ガス通路に、運転前の段階で常温下にて有機溶剤
を流通させ、該有機溶剤中に上記電解質板中の結合剤を
溶出させることにより電解質板中の結合剤を除去づるこ
とを特徴とする燃料電池における電解質板中の結合剤除
去方法とする。[Means for Solving the Problems] In order to solve the above-mentioned problems, the present invention provides a cell in which an electrolyte plate containing a binder used during manufacturing is sandwiched between cathode and anode electrodes from both sides, with a separator in between. Bonding in an electrolyte plate in a fuel cell in which the binder is removed from the electrolyte plate of each cell of the fuel cell stack, which is stacked on a decoy to form a fuel cell stack having gas passages on the cathode side and the annotate side of each cell. In the method for removing the electrolyte, an organic solvent is passed through each gas passage on the cathode side and the anode side of each cell of the fuel cell stack at room temperature before operation, and the organic solvent in the electrolyte plate is introduced into the organic solvent. A method for removing a binder from an electrolyte plate in a fuel cell, characterized in that the binder from the electrolyte plate is removed by eluting the binder.
[作 用]
常温下で燃料電池スタック内に有機溶剤を流通させると
、電解質板中の結合剤が有機溶剤中に溶出するため、結
合剤の除去を悪臭を発生させることなく簡単に行うこと
ができる。又、脱脂状態の判定も有機溶剤中の結合剤の
溶出量を基に簡単に行うことができる。[Function] When an organic solvent is passed through the fuel cell stack at room temperature, the binder in the electrolyte plate is eluted into the organic solvent, making it possible to easily remove the binder without producing a bad odor. can. Furthermore, the degreased state can be easily determined based on the amount of binder eluted from the organic solvent.
[実 施 例] 以下、本発明の実施例を図面を参照して説明する。[Example] Embodiments of the present invention will be described below with reference to the drawings.
第1図は本発明の方法を実施するための工程の一実施例
を示すもので、第3図に示づ如く、電解質板1の両面に
カソード2とアノード3を配してなるセルCをセパレー
タ4を介し積層して各セルCごとにカソード2側及びア
ノード3側にガス通路9及び10が形成された構或とし
てある燃料電池スタックSに、電解質板製造時に使用し
たものと同様な有機溶剤12を、上記各ガス通路9,1
0を利用して電池運転前の段階で常温下にて流通させ、
該有機溶剤12に電解質板1中の枯合剤16を溶出させ
ることにより電解質板1中から結合剤16を除去するよ
うにし、且つ上記有機溶剤12中に溶出した結合剤16
の量を脱脂判定部20で検出して結合剤16の除去作業
終了の判定を行うようにし、又、電解質板1中の結合剤
16の除去に用いた上記有機溶剤12は再生部21で回
収した後、結合剤16を分離させて再び結合剤16の除
去のために循環使用させるようにする。FIG. 1 shows an embodiment of the process for carrying out the method of the present invention, and as shown in FIG. A fuel cell stack S has a structure in which gas passages 9 and 10 are formed on the cathode 2 side and the anode 3 side for each cell C by laminating them with a separator 4 interposed therebetween. The solvent 12 is passed through each of the gas passages 9, 1.
0 is used to distribute the battery at room temperature before battery operation,
The binder 16 is removed from the electrolyte plate 1 by eluting the deadening agent 16 in the electrolyte plate 1 into the organic solvent 12, and the binder 16 eluted into the organic solvent 12 is removed.
The amount of the organic solvent 12 used to remove the binder 16 from the electrolyte plate 1 is recovered by the regeneration unit 21. After that, the binder 16 is separated and recycled again for removal of the binder 16.
詳述づると、先ず、燃料電池スタックSに形戊ざれてい
る酸化ガスと燃籾ガスの各供給側流路孔5,7(第3図
参照)に、電池運転前に常温下にて有機溶剤12を同時
に供給する。これにより、有機溶剤12は各セルCごと
のカソード2側のガス通路9とアノード3側のガス通路
10を通って各排出側流路孔6,8(第3図参照)から
排出されるが、この際、第2図に示づ如く、有機溶剤1
2はガス通路9,10を流通する間にカソード2及びア
ノード3を通過して電解質板1中にしみ込んで行くため
、電解質板1中の結合剤16は有機溶剤12中に徐々に
溶出することになり、この結果、電解質板1中から結合
剤16が除去される。このようにして結合剤16の除去
に供した有機溶剤12が燃料電池スタックS外に排出さ
れると、次に、脱脂判定部20にあいて、たとえば、液
体クロマトグラフを用いて有機溶剤12中の結合剤16
の量を検出したり、あるいは、有機溶剤12の電気伝導
率を調べることにより、除去作業終了の判定を行う。こ
の場合、当初は結合剤16の溶出量は多いが次第に少な
くなってくるので、モニター等で監視し、量が少なくな
ってきて電池運転上支障の起らない8〜9割程度除去で
きた時点で終了とする。又、除去作業終了の判定が行わ
れるまでは、燃料電池スタックS外へ排出ざれた有機溶
剤12を再生部21で回収して結合剤16を分離し、結
合剤16を分離除去した後の有機溶剤12を燃料電池ス
タックSに供給させて再び結合剤16の除去に循環使用
させるように寸る。To be more specific, first, before cell operation, an organic material is introduced into each of the supply-side passage holes 5 and 7 (see Fig. 3) for oxidizing gas and combustion gas formed in the fuel cell stack S at room temperature. Solvent 12 is supplied at the same time. As a result, the organic solvent 12 passes through the gas passage 9 on the cathode 2 side and the gas passage 10 on the anode 3 side of each cell C, and is discharged from each discharge side passage hole 6, 8 (see Fig. 3). , At this time, as shown in Figure 2, organic solvent 1
2 passes through the cathode 2 and anode 3 and soaks into the electrolyte plate 1 while flowing through the gas passages 9 and 10, so that the binder 16 in the electrolyte plate 1 gradually dissolves into the organic solvent 12. As a result, the binder 16 is removed from the electrolyte plate 1. When the organic solvent 12 used to remove the binder 16 in this manner is discharged outside the fuel cell stack S, the organic solvent 12 is then subjected to a degreasing determination section 20 using, for example, a liquid chromatograph. binder 16
The completion of the removal work is determined by detecting the amount of organic solvent 12 or by checking the electrical conductivity of the organic solvent 12. In this case, the amount of binder 16 eluted is large at first, but it gradually decreases, so monitor it with a monitor, etc., and when the amount decreases and about 80 to 90% has been removed without causing any problems in battery operation. It ends with. Furthermore, until it is determined that the removal work is complete, the organic solvent 12 discharged outside the fuel cell stack S is recovered by the regeneration unit 21 and the binder 16 is separated, and the organic solvent 12 after the binder 16 has been separated and removed is The solvent 12 is supplied to the fuel cell stack S and recirculated to remove the binder 16.
なお、この場合、循環使用させる有機溶剤12は、結合
剤16を完全に除去したものでなくてもよい。In this case, the organic solvent 12 to be recycled does not have to have the binder 16 completely removed.
上記ガス通路9と10に同時に有機溶剤12を流すこと
により電池反応部での電解質板1中の結合剤を除去する
際、周辺部のウエットシール部でも徐々に電解質板1中
の結合剤は抜け出で来る。When the binder in the electrolyte plate 1 in the battery reaction section is removed by simultaneously flowing the organic solvent 12 into the gas passages 9 and 10, the binder in the electrolyte plate 1 gradually escapes even in the wet seal area at the periphery. I'm coming.
このように、本発明においては、電解質板1中の結合剤
の除去を、電池を運転する前の段南で熱を使わずに常温
下にて有機溶剤12中に溶出させることにより行うので
、従来の如き悪臭を発生させることはなく、数時間にて
行うことができ、又、脱脂状態の判定も、有機溶剤12
中に溶けている結合剤16の量から液体クロマトグラフ
や電気伝導率等により検出できるので、簡単に行うこと
ができる。As described above, in the present invention, the binder in the electrolyte plate 1 is removed by dissolving it into the organic solvent 12 at room temperature without using heat in the step south before the battery is operated. The degreasing process can be carried out in a few hours without producing any bad odor like conventional methods, and the degreasing state can also be determined using an organic solvent 12
The amount of binder 16 dissolved therein can be detected by liquid chromatography, electrical conductivity, etc., so it can be easily carried out.
なお、上記実施例では、有機溶剤12を燃料電池スタッ
クS内に送り込んで排出させるようにした場合を示した
が、たとえば、有機溶剤12を入れておいたタンク内に
スタック全体を浸づようにし、fi機溶剤12を自然流
動的に流通させて結合剤16を除去するようにしてもよ
いこと、その他本発明の要旨を逸脱しない範囲内におい
て種々変更を加え得ることは勿論である。In the above embodiment, the organic solvent 12 is fed into the fuel cell stack S and discharged. However, for example, the entire stack may be immersed in a tank containing the organic solvent 12. It goes without saying that the binder 16 may be removed by flowing the fi solvent 12 in a natural flow manner, and that various other changes may be made without departing from the gist of the present invention.
[発明の効果]
以上述べた如く、本発明の燃料電池における電解質板中
の結合剤除去方法によれば、電池運転前に、燃料電池ス
タック内に常温下にて有機溶剤を流通させて、該有機}
容剤中に電解質板中の結合剤を}容出させるようにづる
ので、結合剤の除去を悪臭を発生させることなく短時間
にて行うことができ、又、脱脂状態の判定も、有機溶剤
中に溶けている結合剤の里から簡単に行うことができる
、等の優れた効果を発揮寸る。[Effects of the Invention] As described above, according to the method for removing a binder from an electrolyte plate in a fuel cell of the present invention, an organic solvent is passed through the fuel cell stack at room temperature before cell operation, and the organic solvent is removed from the fuel cell stack at room temperature. organic}
Since the binder in the electrolyte plate is discharged into the container, the binder can be removed in a short time without producing a bad odor, and the degreasing state can also be determined using an organic solvent. It can be easily done from the binder dissolved in it, and has excellent effects such as:
第1図は本発明の燃料電池における電解質板中の結合?
411除去方法の一実施例を示す工程図、第2図は本発
明の方法により結合剤を除去している状態を示寸燃料電
池スタックの部分拡大断面図、第3図は燃料電池の一例
を示すN要図、第4図はテープ或形法による電riI−
質板の製造方法を示づ工程図である。
1・・・電解賀板、2・・・カソード、3・・・アノー
ド、9・・・カソード側のガス通路、10・・・アノー
ド側のガス通路、12・・・有機溶剤、16・・・結合
剤、20・・・脱脂判定部、21・・・再生部、C・・
・セル、S・・・燃料電池スタック。Figure 1 shows the bonds in the electrolyte plate in the fuel cell of the present invention.
FIG. 2 is a partially enlarged cross-sectional view of a fuel cell stack showing a state in which the binder is removed by the method of the present invention, and FIG. 3 is an example of a fuel cell. The N diagram shown in Figure 4 is an electrical connection made using a tape method.
It is a process diagram showing the manufacturing method of quality board. DESCRIPTION OF SYMBOLS 1... Electrolysis plate, 2... Cathode, 3... Anode, 9... Gas passage on the cathode side, 10... Gas passage on the anode side, 12... Organic solvent, 16...・Binder, 20... Degreasing determination section, 21... Regeneration section, C...
・Cell, S...Fuel cell stack.
Claims (1)
とアノードの両電極で両面から挟むようにしてなるセル
をセパレータを介し多層に積層して各セルのカソード側
とアノード側にガス通路を有する燃料電池スタックとし
、該燃料電池スタックの各セルごとの電解質板中から結
合剤を除去する燃料電池における電解質板中の結合剤除
去方法において、上記燃料電池スタックの各セルごとの
カソード側とアノード側の各ガス通路に、運転前の段階
で常温下にて有機溶剤を流通させ、該有機溶剤中に上記
電解質板中の結合剤を溶出させることにより電解質板中
の結合剤を除去することを特徴とする燃料電池における
電解質板中の結合剤除去方法。(1) A fuel that has gas passages on the cathode side and the anode side of each cell, in which cells are stacked in multiple layers with a separator in between, in which an electrolyte plate containing the binder used during production is sandwiched between cathode and anode electrodes from both sides. In a method for removing a binder from an electrolyte plate in a fuel cell in which a binder is removed from an electrolyte plate in each cell of the fuel cell stack, the method includes removing a binder from a cathode side and an anode side of each cell of the fuel cell stack. The binder in the electrolyte plate is removed by flowing an organic solvent through each gas passage at room temperature before operation, and eluting the binder in the electrolyte plate into the organic solvent. A method for removing binder from an electrolyte plate in a fuel cell.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1154461A JP2855662B2 (en) | 1989-06-19 | 1989-06-19 | Method for removing binder from electrolyte plate in fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1154461A JP2855662B2 (en) | 1989-06-19 | 1989-06-19 | Method for removing binder from electrolyte plate in fuel cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0320970A true JPH0320970A (en) | 1991-01-29 |
| JP2855662B2 JP2855662B2 (en) | 1999-02-10 |
Family
ID=15584749
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1154461A Expired - Fee Related JP2855662B2 (en) | 1989-06-19 | 1989-06-19 | Method for removing binder from electrolyte plate in fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2855662B2 (en) |
-
1989
- 1989-06-19 JP JP1154461A patent/JP2855662B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JP2855662B2 (en) | 1999-02-10 |
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