JPH01204366A - Manufacture of electrolyte retaining matrix for fuel cell - Google Patents
Manufacture of electrolyte retaining matrix for fuel cellInfo
- Publication number
- JPH01204366A JPH01204366A JP63026910A JP2691088A JPH01204366A JP H01204366 A JPH01204366 A JP H01204366A JP 63026910 A JP63026910 A JP 63026910A JP 2691088 A JP2691088 A JP 2691088A JP H01204366 A JPH01204366 A JP H01204366A
- Authority
- JP
- Japan
- Prior art keywords
- electrolyte
- phosphoric acid
- matrix
- electrolyte retention
- weight
- 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.)
- Pending
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
- H01M8/0293—Matrices for immobilising electrolyte solutions
-
- 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
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)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明はリン酸を電解質とする燃料電池に関し、特に
上記電解質を保持する電解質保持マトリックスの製造方
法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a fuel cell using phosphoric acid as an electrolyte, and particularly to a method for manufacturing an electrolyte retention matrix that retains the electrolyte.
リン酸を電解質とする燃料電池は、通常、第1図の分解
斜視図に示すように導電性のカーボンベーパー等を用い
た電極基材(la)、(lb)の上に、白金を担持させ
たカーボンを撓水性のポリテトラフルオロエチレン(P
TFE)を結合剤として塗工した触媒jliJ (2a
) * (2b )から成る一対のガス拡散電極の間
に、電解質であるリン酸を保持させた電解質保持マトリ
ックス(3)を介在させて単位電池(4)を構成し、さ
らに、ガスを供給するための溝(5)を設けた隔離板(
6)を介して上記単位電池を複数枚積層して構成されて
いる。A fuel cell using phosphoric acid as an electrolyte usually has platinum supported on electrode base materials (la) and (lb) made of conductive carbon vapor, etc., as shown in the exploded perspective view of Figure 1. Water-repellent polytetrafluoroethylene (P)
Catalyst jliJ (2a
) * An electrolyte holding matrix (3) holding phosphoric acid as an electrolyte is interposed between a pair of gas diffusion electrodes consisting of (2b) to form a unit cell (4), and gas is further supplied. A separator plate (5) with a groove (5) for
6) is constructed by stacking a plurality of the above-mentioned unit batteries with each other interposed therebetween.
上記リン酸型燃料電池は、ガス拡散電極の一方に燃料ガ
スとして純水素あるいは水素混合ガスを供給し、他方に
酸化剤ガスとして純酸素あるいは空気を供給することに
より電気化学反応プロセスを経て電力を得るものである
。The phosphoric acid fuel cell described above generates electricity through an electrochemical reaction process by supplying pure hydrogen or hydrogen mixed gas as a fuel gas to one of the gas diffusion electrodes and supplying pure oxygen or air as an oxidant gas to the other. It's something you get.
上記リン酸型燃料電池において電解質であるリン酸を保
持するマトリックスは、電池特性の向上およびその長期
安定性を図る上で非常に重要な役割を担うため、次のよ
うな特性を保有することが要求される。In the above-mentioned phosphoric acid fuel cell, the matrix that holds the phosphoric acid electrolyte plays a very important role in improving the cell characteristics and ensuring its long-term stability, so it must have the following characteristics. required.
(1)燃料電池の運転条件である180〜230℃の温
度で、濃度95%以上のリン酸に対して熱的及び化学的
に安定であること。(1) It should be thermally and chemically stable to phosphoric acid with a concentration of 95% or more at a temperature of 180 to 230°C, which is the operating condition of a fuel cell.
(2)電解質であるリン酸との親和性が高く、リンン酸
を良く浸透させると共に保持力が高いこと。(2) It has a high affinity with the electrolyte phosphoric acid, allows phosphoric acid to penetrate well, and has a high retention power.
(3)水素イオンの良導体であると同時に電子の絶縁体
であること。(3) It is a good conductor of hydrogen ions and at the same time an insulator of electrons.
(4)燃料ガスと酸化剤ガスがマトリックスを透過し、
直接接触して反応することを防ぐため、十分な泡出圧力
(バブリング圧)を有すること。(4) Fuel gas and oxidant gas permeate the matrix,
Must have sufficient bubbling pressure to prevent direct contact and reaction.
(5)電池としての内部抵抗をできるだけ小さくするた
めにマトリックスの膜厚は機械強度の許す範囲内ででき
るだけ薄いこと。(5) In order to minimize the internal resistance of the battery, the thickness of the matrix should be as thin as possible within the range allowed by mechanical strength.
従来のリン酸型燃料電池用電解質保持マトリックスには
耐熱リン酸性に優れる炭化珪素(SiG)が電解質保持
剤として、また、フッ素系樹脂が結合剤として一般的に
用いられ、焼成工程を経て製造されていた。Conventional electrolyte retention matrices for phosphoric acid fuel cells generally use silicon carbide (SiG), which has excellent heat resistance to phosphoric acid, as an electrolyte retention agent and fluorine resin as a binder, and are manufactured through a firing process. was.
しかし、従来のリン酸型燃料電池用電解質保持マトリッ
クスは、焼成工程を経て製造されるために抗水性が高く
、リン酸の浸透性及び保持性に関しては未だ十分に満足
の行くものがないという問題点があった。However, conventional electrolyte retention matrices for phosphoric acid fuel cells have high water resistance because they are manufactured through a calcination process, and the problem is that they are still not fully satisfactory in terms of permeability and retention of phosphoric acid. There was a point.
なお、特開昭59−171472 、59−17147
3号公報に、耐リン酸性を高め、電池の寿命特性向上を
図るため、電解質保持剤として炭化珪素と耐リン酸性物
質を主成分とする複合酸化物を用いた電解質保持マトリ
ックスが提案開示されているが、この電解質保持マトリ
ックスも上記課題を解消することができなかった。In addition, Japanese Patent Application Laid-open No. 59-171472, 59-17147
Publication No. 3 proposes and discloses an electrolyte retention matrix using a composite oxide whose main components are silicon carbide and a phosphoric acid resistant substance as an electrolyte retention agent in order to increase phosphoric acid resistance and improve battery life characteristics. However, this electrolyte retention matrix could not solve the above problems.
この発明は上記のような課題を解消するためになされた
もので、電解質保持マトリックスのリン酸の浸透性及び
保持性を向上させ、電池特性の向上及びその長期安定性
を図ることを目的として行なったものである。This invention was made to solve the above-mentioned problems, and was carried out with the aim of improving the permeability and retention of phosphoric acid in the electrolyte retention matrix, improving battery characteristics and long-term stability. It is something that
この発明の燃料電池用電解質保持マトリックスの製造方
法は、炭化ホウ素および炭化珪素から成る電解質保持剤
、結合剤並びに可塑剤を混練して成形し、上記可塑剤を
溶媒抽出により除去するものである。The method for producing an electrolyte retention matrix for fuel cells of the present invention involves kneading and molding an electrolyte retention agent, a binder, and a plasticizer made of boron carbide and silicon carbide, and removing the plasticizer by solvent extraction.
この発明の別の発明の燃料電池用電解質保持マトリック
スの製造方法は、炭素粉および炭化珪素から成る電解質
保持剤、結合剤並びに可塑剤を混練して成形し、上記可
塑剤を溶媒抽出により除去するものである。A method for producing an electrolyte retention matrix for fuel cells according to another aspect of the present invention includes kneading and molding an electrolyte retention agent, a binder, and a plasticizer made of carbon powder and silicon carbide, and removing the plasticizer by solvent extraction. It is something.
この発明の電解質保持マトリックスは、電解質保持剤と
してSiCと、リン酸との親和性に優れる炭化ホウ素又
は炭素粉を含む混粒物を用いていることに加えて、焼成
工程を施さないため、混線工程でフィブリル化した結合
剤が電解質保持剤をフィブリルの絡まり合いで固定して
いるだけで、従来のように溶融した結合剤が電解質保持
剤の表面を覆っていないため、リン酸の浸透性及び保持
性が向上する。また、焼成工程を施さないため電解質保
持マトリックスはきわめて柔軟性に富んでおり、第1図
に示すように一対のガス拡散電極の間にリン酸を保持さ
せた電解質保持ヤトリックスを積層して面圧を加えた場
合、電極とマトリックスの密着性が高く、接触抵抗に基
づくオーム損失が大幅に低下する。The electrolyte retention matrix of the present invention uses mixed grains containing SiC and boron carbide or carbon powder that has excellent affinity with phosphoric acid as an electrolyte retention agent, and also has no sintering process. The fibrillated binder in the process only fixes the electrolyte retaining agent with entangled fibrils, and unlike conventional methods, the molten binder does not cover the surface of the electrolyte retaining agent, which reduces the permeability of phosphoric acid and Improves retention. In addition, since no firing process is performed, the electrolyte retention matrix is extremely flexible, and as shown in Figure 1, an electrolyte retention matrix containing phosphoric acid is laminated between a pair of gas diffusion electrodes. When pressure is applied, the adhesion between the electrode and matrix is high, and ohmic loss due to contact resistance is significantly reduced.
さらに、炭素粉を含む場合組成物をシート状にロール成
形する際に炭素粉が潤滑剤として働き、薄膜化が容易と
なる。Furthermore, when carbon powder is included, the carbon powder acts as a lubricant when the composition is roll-molded into a sheet, making it easier to form a thin film.
この発明に係わる炭化ホウ素(B4C)は炭化珪素(S
iC)と同様、共有結合性の炭化物であり、非常に硬く
、化学的に極めて安定であるという特長を有している。The boron carbide (B4C) according to this invention is silicon carbide (S
Like iC), it is a covalent carbide and has the characteristics of being extremely hard and chemically extremely stable.
密度は2.5f/crn”、融点は2450°Cで比電
気抵抗は0.仔−である。SiCの密度3.2に近いた
め混粒が容易であり、比電気抵抗もSiCのio。The density is 2.5 f/crn'', the melting point is 2450°C, and the specific electrical resistance is 0.9%.Since the density is close to 3.2 of SiC, it is easy to mix particles, and the specific electrical resistance is also io of SiC.
〜200Ω・函よりは低いが遷移金属元素の炭化物であ
る侵入型炭化物の10−5〜10−4Ω・αに比べると
比電気抵抗は十分高く、SiCを混粒することにより、
実用上問題とならない程度の電子絶縁性を発現すること
が期待される。炭化ホウ素の電解質保持剤に対する混粒
率は、10重量%以上であるのが望ましい。10重量%
以下ではリン酸との親和性の改善効果が小さい。~200Ω・The specific electrical resistance is lower than that of the box, but compared to 10−5 to 10−4Ω・α of interstitial carbides, which are carbides of transition metal elements, the specific electrical resistance is sufficiently high, and by mixing SiC grains,
It is expected that it will exhibit electronic insulating properties to a level that does not pose any practical problems. The mixing ratio of boron carbide to the electrolyte holding agent is preferably 10% by weight or more. 10% by weight
Below, the effect of improving the affinity with phosphoric acid is small.
この発明に係わる炭素粉としては例えば無定形のカーボ
ン結晶性のグラファイトの内の少なくとも一種が用いら
れるが、特に平均粒径が0.1〜10μmのグラファイ
トが好適に用いられる。グラファイトは電子電導性を有
す7るため、先にマトリックスの要求特性に示した電気
絶縁性の観点からはマトリックス材料としては好しくな
いと判断されるが、比電気抵抗が100〜200Ω・工
のSiCと混粒することにより実用上問題とならない程
度の電子絶縁性を発現することが期待される。炭素粉の
電解質保持剤に対する混粒率は10〜35重量%である
のが望ましい。10重量%以下ではリン酸との親和性の
改善効果が小さく、35重量%以上では抵抗が低くなる
。As the carbon powder according to the present invention, for example, at least one type of amorphous carbon crystalline graphite is used, and graphite having an average particle size of 0.1 to 10 μm is particularly preferably used. Since graphite has electronic conductivity7, it is judged to be unsuitable as a matrix material from the viewpoint of electrical insulation as shown in the required properties of the matrix above, but graphite has a specific electrical resistance of 100 to 200 Ω. By mixing grains with SiC, it is expected that electronic insulation properties to a level that does not pose a problem in practical use will be exhibited. The mixing ratio of carbon powder to the electrolyte holding agent is preferably 10 to 35% by weight. If it is less than 10% by weight, the effect of improving the affinity with phosphoric acid will be small, and if it is more than 35% by weight, the resistance will be low.
この発明に係わる結合剤としては、例えば耐熱性、耐薬
品性に優れるポリテトラフルオロエチレン(PTFE)
、四フッ化エチレン六フッ化プロピレン共重合体(FE
P)、ポリパーフルオロアルコキシエチレン(PFA)
、ポリフッ化エチレンプロピレンエーテル(PFEPE
)等のフッ素系樹脂が好適に用いられる。電解質保持
剤に対する結合剤の混合率は3重世%以下では機械的強
度が弱くシート状になり難く、15重量%以上では抗水
性が高くなりすぎるので、3〜15重量%が好適である
。The binder used in this invention is, for example, polytetrafluoroethylene (PTFE), which has excellent heat resistance and chemical resistance.
, tetrafluoroethylene hexafluoropropylene copolymer (FE
P), polyperfluoroalkoxyethylene (PFA)
, polyfluorinated ethylene propylene ether (PFEPE)
) and the like are preferably used. If the mixing ratio of the binder to the electrolyte holding agent is less than 3% by weight, the mechanical strength will be weak and it will be difficult to form a sheet, and if it is more than 15% by weight, the water resistance will become too high, so a ratio of 3 to 15% by weight is suitable.
この発明に係わる可塑剤としては、例えばジメチルフタ
レート、ジエチルフタレート、ジブチルフタレート、ジ
プロピルフタレート、ジアキルフタレート及びジオクチ
ルフタレート等のジアルキルフタレートが好適に用いら
れる。As the plasticizer according to the present invention, dialkylphthalates such as dimethyl phthalate, diethyl phthalate, dibutyl phthalate, dipropylphthalate, diacyl phthalate, and dioctyl phthalate are preferably used.
電解質保持剤と結合剤から成る凍結乾燥粉に対する可塑
剤の含有量は30〜50重量%が好ましい。The content of plasticizer in the freeze-dried powder consisting of an electrolyte holding agent and a binder is preferably 30 to 50% by weight.
30、重量%以下では粘土状になり難くバラバラになり
、50重量%以上では柔らかくなりすぎ、ともに成形性
が悪いので上記範囲が好適である。If it is less than 30% by weight, it will not become clay-like and will fall apart, and if it is more than 50% by weight, it will become too soft and the moldability will be poor in both cases, so the above range is preferable.
この発明に係わる溶剤としては、メチルアルコール、エ
チルアルコール及びプロピルアルコール等のアルコール
が好適に用いられる。Alcohols such as methyl alcohol, ethyl alcohol and propyl alcohol are preferably used as the solvent in this invention.
以下に、この発明の実施例の燃料電池用電解質保持マト
リックスの製造方法について説明する。A method for producing an electrolyte retention matrix for a fuel cell according to an embodiment of the present invention will be described below.
炭化珪素(SiC)と炭化ホウ素(B4C)又は炭素粉
(グラファイト)を含む混粒物の電解質保持剤を、結合
剤に対して10重量%となるように、結合剤として用い
るPTFHの水性ディスバージョンを所定量の純水で稀
釈した水溶液に分散させ、浅いバットに移してフリーザ
で凍結する。凍結した状態でトラップ付きの真空ポンプ
で吸引して乾燥し、上記電解質保持剤と結合剤が均一に
分散した凍結乾燥粉を調製した。Aqueous dispersion of PTFH using as a binder an electrolyte retaining agent of mixed particles containing silicon carbide (SiC) and boron carbide (B4C) or carbon powder (graphite) in an amount of 10% by weight based on the binder. Disperse it in an aqueous solution diluted with a predetermined amount of pure water, transfer it to a shallow vat, and freeze it in a freezer. The frozen state was suctioned and dried using a vacuum pump equipped with a trap to prepare a freeze-dried powder in which the electrolyte holding agent and binder were uniformly dispersed.
次に凍結乾燥粉に可塑剤としてジメチルフタレートを4
0重量%加え、加圧ニーダ−及びミキシングロールを用
いて混練した。混線条件によりPTFEのフィブリル化
の度合が異なるが、粘りのある粘土状の組成物が得られ
る。Next, add 4 ml of dimethyl phthalate as a plasticizer to the freeze-dried powder.
0% by weight was added and kneaded using a pressure kneader and a mixing roll. Although the degree of fibrillation of PTFE varies depending on the crosstalk conditions, a sticky clay-like composition can be obtained.
ミキシングロールで上記組成物を厚さ1〜2朋のシート
状に形成し、さらにカレンダーロールを用いて厚さ10
0〜300μmのシート状に成形した。Form the above composition into a sheet with a thickness of 1 to 2 mm using a mixing roll, and then use a calender roll to form a sheet with a thickness of 10 mm.
It was molded into a sheet having a size of 0 to 300 μm.
最後に混線及びシート化には不可欠ではあるが、電解質
保持マトリックスとして用いる場合には不要な可塑性を
メチルアルコールを溶剤として用いて抽出除去して乾燥
し、シート状のこの発明の実施例による電解質保持マト
リックスを得た。Finally, plasticity, which is essential for crosstalk and forming into a sheet, but unnecessary when used as an electrolyte retention matrix, is extracted and removed using methyl alcohol as a solvent and dried. I got the matrix.
と配電解質保持マトリックスは、先に記述したように水
素イオン良導体であると同時に電子絶縁体である必要が
ある。即ち電解質であるリン酸がない状態での電気抵抗
は106Ω・の以上の電子絶縁体であることが必要であ
る。The electrolyte retention matrix must be a good conductor of hydrogen ions and an electronic insulator as described above. That is, it is necessary to be an electronic insulator with an electrical resistance of 10 6 Ω· or more in the absence of phosphoric acid, which is an electrolyte.
電子絶縁性評価試験
(1) SiCの混粒率が0.20,40,60.80
重量%即ちB、Cの混粒率が100.80,60.40
門20重量%の電解質保持剤を用いて電解質保持マトリ
ックスを作製し、また、比較のため上記と同様の方法で
SiCが10096の電解質保持剤を用いてシート状の
電解質保持マトリックスを作製し、電解質保持剤のSi
C混粒率と比電気抵抗の関係を調べた。上記電解質保持
マトリックスにリン酸を入れずに電極で挾み、4 kf
7cm2の面圧をかけた状態で比電気抵抗を測定した
。その結果を第2図の特性図中の(A1)に示す。縦軸
は比電気抵抗(Ω・cIrL)を、横軸はSiCの混粒
率(重量%)を表わす。第2図より明らかなようにSi
Cの混粒率が0重量%においても106Ω・α以上の電
子絶縁性を発現し、絶縁体領域に入ることを確認した。Electronic insulation evaluation test (1) SiC mixed particle ratio is 0.20, 40, 60.80
Weight%, that is, the mixed grain ratio of B and C is 100.80, 60.40
An electrolyte retention matrix was prepared using an electrolyte retention agent containing 20% by weight, and for comparison, a sheet-like electrolyte retention matrix was also prepared using an electrolyte retention agent with SiC of 10096 in the same manner as above. Retention agent Si
The relationship between C mixed particle ratio and specific electrical resistance was investigated. The above electrolyte retention matrix was sandwiched between electrodes without phosphoric acid, and 4 kf
The specific electrical resistance was measured with a surface pressure of 7 cm2 applied. The results are shown in (A1) in the characteristic diagram of FIG. The vertical axis represents the specific electrical resistance (Ω·cIrL), and the horizontal axis represents the SiC mixed particle ratio (wt%). As is clear from Figure 2, Si
It was confirmed that even when the mixed particle ratio of C was 0% by weight, electronic insulation of 10 6 Ω·α or more was exhibited, which fell into the insulator region.
上記電解質保持マトリックスにリン酸を入れた場合の電
気抵抗は水素イオンが電荷のキャリアとして働くため第
2図の曲線(13+)に示すように10−2〜10−1
Ω・αであり、SiCの混粒率が0重量%においても実
用上問題とならない程度の電子絶縁性を発現している。When phosphoric acid is added to the electrolyte retention matrix, the electrical resistance is 10-2 to 10-1 as shown in the curve (13+) in Figure 2 because hydrogen ions act as charge carriers.
Ω·α, and exhibits electronic insulating properties to the extent that it does not pose a practical problem even when the SiC mixed particle ratio is 0% by weight.
また、SiCの混粒率が多い場合にはリン酸との親和性
の改善効果が少ないため、上記結果を考慮するとB4C
の混粒率は10重量%以上の範囲にあることが好ましい
。In addition, when the mixed grain ratio of SiC is high, the effect of improving the affinity with phosphoric acid is small, so considering the above results, B4C
The mixed grain ratio is preferably in the range of 10% by weight or more.
(2)平均粒径1μmのグラファイトと平均粒径2μm
のSiCを用い、グラファイトの混粒率が20 、40
。(2) Graphite with an average particle size of 1 μm and an average particle size of 2 μm
using SiC with a graphite mixed grain ratio of 20 and 40
.
60及び80重量%の電解質保持剤を用いて電解質保持
マトリックスを作製し、また、比較のため上記と同様の
方法でグラファイトあるいはSiCがZo。Electrolyte retention matrices were prepared using 60 and 80 wt% electrolyte retention agents, and for comparison, graphite or SiC was used in the same manner as above.
%の電解質保持剤を用いてシート状の電解質保持マトリ
ックスを作製し、電解質保持剤のグラファイト混粒率と
比電気抵抗の関係を調べた。上記電解質保持マトリック
スにリン酸を入れずに電極で挾み、4 ky/crn2
の面圧をかけた状態で比電気抵抗を測定した。その結果
を第3図中の曲線(A2)に示す。縦軸は比電気抵抗(
Ω・C7rL)を、横軸はグラファイトの混粒率(重量
96)を表わす。第3図より明らかなようにグラファイ
トの混粒率が35重量%までの範囲で比電気抵抗は10
6Ω・ぼ以上の電子絶縁性を発現するが35重量%を越
えると106Ω・α以下と撚導体領域に入る。上記電解
質保持マトリックスにリン酸を入れた場合の比電気抵抗
は水素イオンか電荷のキャリアとして働くため第3図中
の曲線(B2)に示すように、10−2〜10−1Ω・
ぼであり、グラファイトの混粒率が35重量%以下であ
れば実用上問題とならない程度の電子絶縁性を発現して
いる。% electrolyte retention agent was used to prepare a sheet-like electrolyte retention matrix, and the relationship between graphite mixed particle ratio of the electrolyte retention agent and specific electrical resistance was investigated. The above electrolyte holding matrix was sandwiched between electrodes without phosphoric acid, and 4 ky/crn2
The specific electrical resistance was measured with a surface pressure of . The results are shown in curve (A2) in FIG. The vertical axis is the specific electrical resistance (
Ω·C7rL), and the horizontal axis represents the graphite mixed particle ratio (weight 96). As is clear from Figure 3, the specific electrical resistance is 10 when the graphite mixed particle ratio is up to 35% by weight.
It exhibits an electronic insulation property of more than 6 Ω·α, but when it exceeds 35% by weight, it becomes less than 10 6 Ω·α, which falls into the twisted conductor region. The specific electrical resistance when phosphoric acid is added to the electrolyte holding matrix is 10-2 to 10-1 Ω, as shown in curve (B2) in Figure 3, because it acts as a hydrogen ion or charge carrier.
If the proportion of mixed graphite particles is 35% by weight or less, it exhibits electronic insulation to the extent that it does not pose a practical problem.
グラファイトの混粒率が高いと電子絶縁性を保持できな
くなり、SiCの混粒率が多い場合にはリン酸との親和
性の改善効果が少ないため、上記結果を考慮すると混粒
率は10〜35重量%の範囲にあることが好ましい。If the mixed grain ratio of graphite is high, electronic insulation properties cannot be maintained, and if the mixed grain ratio of SiC is high, the effect of improving the affinity with phosphoric acid is small. Considering the above results, the mixed grain ratio should be 10~ Preferably, it is in the range of 35% by weight.
次にこの発明の実施例のSiCにグラファイト又はB4
Cを混粒した電解質保持マトリックスのリン酸親和性の
向上効果および電池特性の向上およびその長期安定性の
改善効果を確認するためにSiCにグラファイト又はB
4Cを混粒したシート状の電解質保持マトリックスを作
製した。以下にその製造方法を実施例をあげて具体的に
述べる。Next, graphite or B4 is added to the SiC of the embodiment of this invention.
In order to confirm the effect of improving the phosphoric acid affinity of the electrolyte retention matrix mixed with C, the improvement of battery characteristics, and the improvement of its long-term stability, graphite or B was added to SiC.
A sheet-like electrolyte retention matrix containing 4C particles was prepared. The manufacturing method will be specifically described below by giving examples.
実施例1
11!の純水にPTFEの60重量%水性ディスバージ
ョン(三井フロロケミカル製) 16tyy (PTF
E量としては100F )を添加し、攪拌機で50Or
pmで攪拌しながら平均粒径1.5μmのB、C90J
を少量ずつ添加して均一に混合した後、ステンレスバッ
トに移して一40℃の超低温フリーザで凍結する。Example 1 11! 60% by weight aqueous dispersion of PTFE (manufactured by Mitsui Fluorochemicals) 16tyy (PTF
The amount of E is 100 F), and the mixture is heated to 50 Or
B, C90J with an average particle size of 1.5 μm while stirring at pm
After adding little by little and mixing uniformly, the mixture was transferred to a stainless steel vat and frozen in an ultra-low temperature freezer at -40°C.
凍結した状態でトラップ付きの真空ポンプで吸引して乾
燥し、上記電解質保持剤と結合剤が均一に分散した1k
fの凍結乾燥粉を調整した。上記凍結乾燥粉の組成はB
4Cから成る電解質保持剤が100重量%、結合剤が1
0重量%である。The frozen state is suctioned and dried using a vacuum pump with a trap, and the electrolyte retaining agent and binder are uniformly dispersed.
A freeze-dried powder of f was prepared. The composition of the above freeze-dried powder is B
100% by weight of electrolyte retention agent consisting of 4C, 1% of binder
It is 0% by weight.
上記凍結乾燥粉1kyに400 fのジブチルフタレー
トを加えて混合したものを加圧ニーダを用いて混練し、
粘りのある粘度状の組成物を得た。上記組成物をミキシ
ングロールを用いて厚さ約2711jlのシート状に成
形し、さらにカレンダーロールを用いて厚さ約200μ
mのシート状に成形した。A mixture of 1 ky of the freeze-dried powder and 400 f of dibutyl phthalate was kneaded using a pressure kneader.
A sticky viscous composition was obtained. The above composition was formed into a sheet with a thickness of about 2711 ml using a mixing roll, and then formed into a sheet with a thickness of about 200 μl using a calendar roll.
It was molded into a sheet shape of m.
次に上記シート状に成形されたマトリックスをエチルア
ルコールを入れたステンレスバットに2時間浸漬してジ
ブチルフタレートを完全に抽出除去した後乾燥し、シー
ト状のこの発明の一実施例の燃料電池用′庖解質保持マ
トリックスを得た。Next, the matrix formed into a sheet is immersed in a stainless steel vat containing ethyl alcohol for 2 hours to completely extract and remove dibutyl phthalate, and then dried. A spore retention matrix was obtained.
実施例2
添加する電解質保持剤としてB4C180gと平均粒径
2fimの5iC720Fを用いB4Cが20重量%、
SiCが80重量%の混粒比である以外は実施例1と同
様にして膜厚220μmのシート状のこの発明の他の実
施例の燃料電池用電解質保持マトリックスを得た。Example 2 180g of B4C and 5iC720F with an average particle size of 2fim were used as the electrolyte retention agent to be added, and B4C was 20% by weight.
A sheet-shaped electrolyte retention matrix for a fuel cell according to another example of the present invention having a film thickness of 220 μm was obtained in the same manner as in Example 1 except that the SiC content was 80% by weight.
実施例3
電解質保持剤としてB4Cが40重量%、平均粒径2μ
mのSiCが60重量%の混粒比である以外は実施例1
と同様にして膜厚200μmのシート状のこの発明の他
の実施例の燃料電池用電解質保持マトリックスを得た。Example 3 40% by weight of B4C as an electrolyte retention agent, average particle size 2μ
Example 1 except that the mixed grain ratio of m SiC was 60% by weight.
In the same manner as above, a sheet-like electrolyte retention matrix for a fuel cell according to another example of the present invention having a film thickness of 200 μm was obtained.
実施例4
電解質保持剤としてB4Cが60重量%、平均粒径2μ
mのSiCが40重量%の混粒比である以外は実施例1
と同様にして膜厚210μmのシート状のこの発明の他
の実施例の燃料電池用電解質保持マトリックスを得た。Example 4 60% by weight of B4C as an electrolyte retention agent, average particle size 2μ
Example 1 except that the mixed grain ratio of m SiC was 40% by weight.
In the same manner as above, a sheet-like electrolyte retention matrix for a fuel cell according to another example of the present invention having a film thickness of 210 μm was obtained.
実施例5
電解質保持剤としてB4Cが80重量%、平均粒径2μ
mのSiCが20重量%の混粒比である以外は実施例1
と同様にして膜厚210μmのシート状のこの発明の他
の実施例の燃料電池用′七解質保持マトリックスを得た
。Example 5 80% by weight of B4C as electrolyte retention agent, average particle size 2μ
Example 1 except that the mixed grain ratio of m SiC was 20% by weight.
In the same manner as above, a 210 .mu.m thick sheet-like 7 solyte retaining matrix for fuel cells according to another embodiment of the present invention was obtained.
実施例6
電解質保持剤として90Fの平均粒径1μmのグラファ
イトと81ofの平均粒径2μmのSiCを用い、凍結
乾燥粉の組成をグラファイト10重量%、5iC90重
量%とする以外は実施例1と同様にして膜厚的220μ
mのシート状のこの発明の他の実施例の燃料電池用電解
マトリックスを得た。Example 6 Same as Example 1 except that graphite of 90F with an average particle size of 1 μm and SiC of 81of with an average particle size of 2 μm were used as electrolyte retention agents, and the composition of the freeze-dried powder was 10% by weight of graphite and 90% by weight of 5iC. The film thickness is 220μ
An electrolytic matrix for a fuel cell according to another example of the present invention was obtained in the form of a sheet of m.
実施例7
電解質保持剤としてグラファイト20重量%、SiC7
0重量%の混粒比である以外は実施例6と同様にして膜
厚210μmのシート状のこの発明の他の実施例の燃料
電池用電解質保持マトリックスを得た。Example 7 20% by weight of graphite and SiC7 as electrolyte retention agent
A sheet-shaped electrolyte retention matrix for a fuel cell according to another example of the present invention having a film thickness of 210 μm was obtained in the same manner as in Example 6 except that the mixed grain ratio was 0% by weight.
実施例3
電解質保持剤としてグラファイト30重量%、SiC7
0重量%の混粒比である以外は実施例6と同様にして膜
厚200μmのシート状のこの発明の他の実施例の燃料
電池用電解質保持マトリックスを得た。Example 3 Graphite 30% by weight, SiC7 as electrolyte retention agent
A sheet-shaped electrolyte retention matrix for a fuel cell according to another example of the present invention having a film thickness of 200 μm was obtained in the same manner as in Example 6 except that the mixed grain ratio was 0% by weight.
比較例
電解質保持剤としてSiCを90of添加して5iC1
00重量%とする他は実施例1と同様にして、膜厚23
0μmのシート状の従来の燃料電池用電解質保持マトリ
ックスを得た。Comparative example 5iC1 with 90 of SiC added as an electrolyte holding agent
The film thickness was 23% by weight in the same manner as in Example 1 except that the
A sheet-like conventional electrolyte retention matrix for fuel cells with a thickness of 0 μm was obtained.
上記実施例及び比較例において、電解質保持剤として用
いたB、Cの混粒率および作製した電解質表 1
表 2
それによると、B、CおよびグラファイトとSiCの平
均粒径が近いため、ポアサイズ、ポロシティともに10
0%のSiCを用いた比較例の電解質保持マトリックス
とほぼ同程度であると言える。In the above Examples and Comparative Examples, the mixed particle ratio of B and C used as electrolyte holding agents and the prepared electrolyte Table 1 Table 2 According to it, since the average particle diameters of B, C and graphite and SiC are close to each other, the pore size, Both porosity are 10
It can be said that it is almost the same as the electrolyte retention matrix of the comparative example using 0% SiC.
リン酸親和性試験
上記この発明の実施例の燃料電池用電解保持マトリック
ス(実施例1〜8)のリン酸の接触角を測定する。即ち
、室温から200℃の温度範囲で所定の温度をこ保たれ
た試料加熱台に上記この発明の実施例による電解質マト
リックス(実施例1〜8)を水平に置き、濃度105%
のリン酸を滴下した後の接触角の経時変化を観測した。Phosphoric Acid Affinity Test The contact angle of phosphoric acid of the electrolytic retention matrices for fuel cells (Examples 1 to 8) of the above embodiments of the present invention is measured. That is, the electrolyte matrices (Examples 1 to 8) according to the above embodiments of the present invention were placed horizontally on a sample heating table maintained at a predetermined temperature in the temperature range of room temperature to 200°C, and
The change in contact angle over time after dropping phosphoric acid was observed.
その結果を滴下5分後の接触角の温度変化を示す特性図
の第4図(実施例1〜5)および接触角の経時変化を示
す特性図の第5図(実施例6〜8)に示す。The results are shown in Figure 4 (Examples 1 to 5) of the characteristic diagram showing the temperature change in contact angle 5 minutes after dropping and Figure 5 (Examples 6 to 8) of the characteristic diagram showing the change in contact angle over time. show.
図において縦軸は接触角C度)を、横軸は試料温度(0
又は経過時間(分)を表わし、特性曲線囚は実施例1の
特性曲線(B)は実施例5の、特性曲線(Qは比較例の
、特性曲線■は実施例6の、特性曲線(ト)は実施例の
、特性曲線(F’lは実施例8の特性を示す。In the figure, the vertical axis represents the contact angle (C degrees), and the horizontal axis represents the sample temperature (0
The characteristic curve (B) of Example 1 is the characteristic curve (B) of Example 5, the characteristic curve (Q is of the comparative example), and the characteristic curve (■) is the characteristic curve (T) of Example 6. ) shows the characteristic curve of Example 8 (F'l shows the characteristic of Example 8).
実施例2は特性曲線囚に重なり、実施例3,4は特性曲
線(んと特性曲線(B)の間にあった。Example 2 overlapped with the characteristic curve, and Examples 3 and 4 were between the characteristic curve (and characteristic curve (B)).
上記第4図および第5図より、明らかなように、100
96のSiCを用いた従来の電解質保持マトリックスと
比較して、グラファイト又はB4CとSiCを混粒した
試料はリン酸との親和性が向上した結果、リン酸の接触
角が低くなることを確認した。特に、グラファイトとS
iCを混粒した試料は、表面より内部に浸透し易いため
に時間経過に従って接触角がより速やかに低下すること
がわかる。As is clear from FIGS. 4 and 5 above, 100
Compared to a conventional electrolyte retention matrix using 96 SiC, it was confirmed that the sample containing graphite or B4C mixed with SiC had an improved affinity with phosphoric acid, resulting in a lower contact angle with phosphoric acid. . In particular, graphite and S
It can be seen that in the sample mixed with iC particles, the contact angle decreases more quickly over time because the iC particles penetrate more easily into the interior than the surface.
リン酸保持性試験
次に電解質であるリン酸の保持性の指環として、第1図
のような単位電池を構成したマトリックス内のリン酸量
の経時変化よりリン酸移動量を測定した。その結果を第
6図と第7図のリン酸移動量の経時変化を示す特性図に
示す。図において縦軸はリン酸移動量(m17cm”)
を、横軸は経過時間(h)を表わし、特性曲線■は実施
例1の、特性曲線(L)は実施例3の、特性曲線(財)
は実施例5の、特性曲線閃は比較例の、特性曲線(へ)
は実施例6の、特性曲線(0)は実施例7の、特性曲線
(P)は実施例8のリン酸移動量の経時変化を示してい
る。第6図および第7図より明らかなように、B4C又
はグラファイトにSiCを混粒した電解質保持マトリッ
クスはリン酸移動量が少なく、リン酸保持性が向上した
ことがわかる。また、マトリックスのリン酸保持性が向
上したことにより泡出圧力も向上した。Phosphoric Acid Retention Test Next, as a measure of the retention of phosphoric acid, which is an electrolyte, the amount of phosphoric acid transferred was measured based on the change over time in the amount of phosphoric acid in the matrix constituting a unit cell as shown in FIG. The results are shown in FIGS. 6 and 7, which are characteristic diagrams showing changes over time in the amount of phosphoric acid transferred. In the figure, the vertical axis is the amount of phosphoric acid transferred (m17cm”)
, the horizontal axis represents the elapsed time (h), the characteristic curve ■ is for Example 1, the characteristic curve (L) is for Example 3, and the characteristic curve (goods) is
is the characteristic curve of Example 5, and the characteristic curve is of Comparative Example.
Characteristic curve (0) shows the change over time in the amount of phosphoric acid transferred in Example 6, characteristic curve (P) in Example 7, and characteristic curve (P) in Example 8. As is clear from FIGS. 6 and 7, the electrolyte retention matrix in which B4C or graphite is mixed with SiC particles has a small amount of phosphoric acid transfer, and it can be seen that the phosphoric acid retention property is improved. Furthermore, the foaming pressure was also improved due to the improved phosphoric acid retention of the matrix.
さらに、この発明による電解質保持マトリックスは焼成
しておらず、そのため極めて柔軟なため電極との密着性
に優れ、電池の内部抵抗をマトリックスの膜厚がOpm
に外挿した接触抵抗も約5vと従来(SiC100%、
PTFE 3〜10%、焼成品)の接触抵抗の1/3〜
1/2に改善された。Furthermore, the electrolyte retention matrix according to the present invention is not fired and is therefore extremely flexible, so it has excellent adhesion to the electrodes, and the internal resistance of the battery is reduced by the thickness of the matrix.
The contact resistance extrapolated to the conventional (100% SiC,
1/3 to 1/3 of the contact resistance of PTFE 3 to 10%, fired product)
Improved to 1/2.
電池特性および寿命試験
次に電池特性および寿命の改善効果を確認するために第
1図のような単位電池を構成し、セル電圧と内部抵抗に
基づくオーム損の経時変化を測定した。その結果を第8
図および第9図に示す。Battery Characteristics and Lifetime Test Next, in order to confirm the improvement effect on battery characteristics and lifespan, a unit battery as shown in FIG. 1 was constructed, and changes over time in ohmic loss based on cell voltage and internal resistance were measured. The results are shown in the 8th section.
9 and 9.
図において縦軸はセル電圧(mV )およびオーム損(
mV )を表わし、横軸は運転時間(h)を表わす。In the figure, the vertical axis is the cell voltage (mV) and the ohmic loss (
mV), and the horizontal axis represents operating time (h).
また実線のプロット(qr) (yl) (R1)はセ
ル電圧を、破線のプロット(Q2) (Y2) (R2
)はオーム損に対応する。特性曲線(Ql) (Q2)
は実施例3、特性曲線(R1) (R2)は実施例8、
特性曲線(Yl) (Y2)は比較例の電解質保持マト
リックスを用いた場合を示す。第8図および第9図より
明らかなように、B、C又はグラファイトにSiCを混
粒した電解質マトリックスはリン酸保持性が向上した結
果オーム損は1000時間経過しても変化せず、セル電
圧も1000時間経過で10mV以下の低下であった。Also, the solid line plot (qr) (yl) (R1) is the cell voltage, and the broken line plot (Q2) (Y2) (R2
) corresponds to ohmic loss. Characteristic curve (Ql) (Q2)
is Example 3, characteristic curve (R1) (R2) is Example 8,
Characteristic curve (Yl) (Y2) shows the case where the electrolyte retention matrix of the comparative example was used. As is clear from Figures 8 and 9, the electrolyte matrix containing B, C, or graphite mixed with SiC has improved phosphoric acid retention, and as a result, the ohmic loss does not change even after 1000 hours, and the cell voltage Also, the decrease was less than 10 mV after 1000 hours.
これに対して比較例では600時間経過後より徐々にオ
ーム損が増加し始め、セル電圧も1000時間経過で2
’OmV以上の低下を示した。従って、B4C又はグラ
ファイトをSiCに混粒したマトリックスを用いること
により、電池特性が向上しし、その長期安定性を実現す
ることができた。On the other hand, in the comparative example, the ohmic loss gradually started to increase after 600 hours, and the cell voltage also increased by 2 after 1000 hours.
'It showed a decrease of more than OmV. Therefore, by using a matrix in which B4C or graphite is mixed with SiC, the battery characteristics were improved and long-term stability could be achieved.
以上説明したとおり、この発明は炭化ホウ素および炭化
珪素から成る電解質保持剤、結合剤並びに可塑剤を混練
して成形し、上記可塑剤を溶媒抽出により除去すること
により、リン酸の浸透性および保持性を向上させ、電池
特性の向とおよびその長期安定性に優れた燃料電池用電
解保持マトリックスの製造方法を得ることができる。As explained above, the present invention improves phosphoric acid permeability and retention by kneading and molding an electrolyte retention agent, a binder, and a plasticizer made of boron carbide and silicon carbide, and removing the plasticizer by solvent extraction. It is possible to obtain a method for producing an electrolytic retention matrix for a fuel cell, which has improved properties, improved cell properties, and excellent long-term stability.
この発明の別の発明は、炭素粉および炭化珪素から成る
電解質保持剤、結合剤並びに可塑剤を混練して成形し、
上記可塑剤を溶媒抽出により除去することにより、上記
効果に加えて薄膜化の容易な燃料電池用電解質保持マト
リックスの製造方法を得ることができる。Another invention of the present invention is to knead and mold an electrolyte holding agent, a binder, and a plasticizer made of carbon powder and silicon carbide,
By removing the plasticizer by solvent extraction, it is possible to obtain a method for producing an electrolyte retention matrix for a fuel cell that not only provides the above effects but also allows easy formation of a thin film.
第1図は一般的な燃料電池の分解斜視図、第2図はこの
発明の一実施例によるB、Cを混粒した電解質保持マト
リックスと従来のものとを比較するSiC混粒率(重量
%)比電気抵抗(Ω・crrL)変化を示す特性図、第
3図はこの発明の他の実施例によるグラファイトを混粒
した電解質保持マトリックスと従来のものとを比較する
グラファイト混粒率(重量96)による比電気抵抗(Ω
・it)変化を示す特性図、第4図はこの発明の実施例
によるB4Cを混粒した電解質保持マトリックスと従来
のものとを比較するリン酸接触角(0)の温度変化を示
す特性図、第5図はこの発明の実施例によるグラファイ
トを混粒した電解質保持マトリックスと従来のものとを
比較するリン酸接触角(つの経過時間変化を示す特性図
、第6図はこの発明の実施例によるB4Cを混粒した電
解質保持マトリックスと従来のものを比較するリン酸移
動B1 (my /Crf)の経過時間(時)変化を示
す特性図、第7図はこの発明の実施例によるグラファイ
トを混粒した電解質保持マトリックスと従来のものを比
較するリン酸移動量(my/crIL2)の経過時間C
時)変化を示す特性図、第8図はこの発明の実施例によ
るB4Cを混粒した電解質保持マトリックスと従来のも
のとを比較する電池特性図、第9図はこの発明の実施例
によるグラファイトを混粒した電解質保持マトリックス
と従来のものとを比較する電池特性図である。
図において、(3)は電解質保持マトリックスである。FIG. 1 is an exploded perspective view of a general fuel cell, and FIG. 2 is a comparison of the SiC mixed particle ratio (wt% ) A characteristic diagram showing the change in specific electrical resistance (Ω・crrL), and FIG. 3 shows the graphite mixed particle ratio (weight 96 ) by specific electrical resistance (Ω
・It) A characteristic diagram showing changes in the phosphoric acid contact angle (0) comparing an electrolyte retention matrix mixed with B4C according to an embodiment of the present invention with a conventional one, and FIG. Figure 5 is a characteristic diagram showing the change in phosphoric acid contact angle over time, comparing the graphite-mixed electrolyte retention matrix according to an embodiment of the present invention with a conventional matrix. A characteristic diagram showing the change in phosphoric acid transfer B1 (my/Crf) over time (hours) comparing an electrolyte retention matrix mixed with B4C and a conventional one. Elapsed time C of phosphoric acid transfer amount (my/crIL2) comparing the electrolyte retention matrix and the conventional one
Fig. 8 is a battery characteristic diagram comparing the electrolyte retention matrix mixed with B4C according to the embodiment of this invention and a conventional one, and Fig. 9 is a characteristic diagram showing the change in graphite according to the embodiment of this invention. FIG. 3 is a battery characteristic diagram comparing a mixed electrolyte retention matrix and a conventional one. In the figure, (3) is an electrolyte retention matrix.
Claims (2)
、結合剤並びに可塑剤を混練して成形し、上記可塑剤を
溶媒抽出により除去する燃料電池用電解質保持マトリッ
クスの製造方法。(1) A method for producing an electrolyte retention matrix for a fuel cell, which comprises kneading and molding an electrolyte retention agent, a binder, and a plasticizer made of boron carbide and silicon carbide, and removing the plasticizer by solvent extraction.
合剤並びに可塑剤を混練して成形し、上記可塑剤を溶媒
抽出により除去する燃料電池用電解質保持マトリックス
の製造方法。(2) A method for producing an electrolyte retention matrix for a fuel cell, which comprises kneading and molding an electrolyte retention agent, a binder, and a plasticizer made of carbon powder and silicon carbide, and removing the plasticizer by solvent extraction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63026910A JPH01204366A (en) | 1988-02-08 | 1988-02-08 | Manufacture of electrolyte retaining matrix for fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63026910A JPH01204366A (en) | 1988-02-08 | 1988-02-08 | Manufacture of electrolyte retaining matrix for fuel cell |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH01204366A true JPH01204366A (en) | 1989-08-16 |
Family
ID=12206372
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63026910A Pending JPH01204366A (en) | 1988-02-08 | 1988-02-08 | Manufacture of electrolyte retaining matrix for fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01204366A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100362284B1 (en) * | 2000-05-12 | 2002-11-23 | 삼성에스디아이 주식회사 | Manufaturing method of lithium polymer batteries |
-
1988
- 1988-02-08 JP JP63026910A patent/JPH01204366A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100362284B1 (en) * | 2000-05-12 | 2002-11-23 | 삼성에스디아이 주식회사 | Manufaturing method of lithium polymer batteries |
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