JPS6079674A - Manufacture of electrolyte tile for fuel cell - Google Patents

Manufacture of electrolyte tile for fuel cell

Info

Publication number
JPS6079674A
JPS6079674A JP58188053A JP18805383A JPS6079674A JP S6079674 A JPS6079674 A JP S6079674A JP 58188053 A JP58188053 A JP 58188053A JP 18805383 A JP18805383 A JP 18805383A JP S6079674 A JPS6079674 A JP S6079674A
Authority
JP
Japan
Prior art keywords
sheet
resin
lithium
aluminate
temperature
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
Application number
JP58188053A
Other languages
Japanese (ja)
Inventor
Junji Nakamura
中村 淳次
Ikumasa Nishimura
西村 生真
Goro Saito
悟朗 斉藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toppan Inc
Original Assignee
Toppan Printing Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toppan Printing Co Ltd filed Critical Toppan Printing Co Ltd
Priority to JP58188053A priority Critical patent/JPS6079674A/en
Publication of JPS6079674A publication Critical patent/JPS6079674A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0289Means for holding the electrolyte
    • H01M8/0295Matrices for immobilising electrolyte melts
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Fuel Cell (AREA)

Abstract

PURPOSE:To obtain electrolyte tile for fuel cell having large porosity and fine pores by adding flocculation agent and surface active agent to slurry prepared by mixing gamma-lithium aluminate, wood pulpe, and thermoplastic resin, and making paper-like sheet and burning it. CONSTITUTION:Lithium hydroxide, lithium salt, and gamma-Al2O3 are heated at 1,000 deg.C for 1hr, cooled, and crushed to powder having a particle size of 1mu or less to prepare gamma-lithium aluminate. This aluminate is used as inorganic material. 3-40% Of wood pulpe as fiber material to total dry weight of sheet and 3-4% of thermoplastic resin are mixed to inorganic material to prepare slurry. The water slurry is adjusted to pH7, then flocculation agent and surface active agent are added to the slurry. After alocculation, it is prepared to a sheet by a paper making process. It is burned in such a condition that temperature is increased from room temperature at the rate of 30-8 deg.C/h, and kept at 500-700 deg.C for 1- 3hr, and increased at a rate of 100-300 deg.C/h, and kept at 1,000-1,300 deg.C for 1- 3hr. By this process, sheet-shaped electrolyte tiles having uniform thickness is continuously manufactured.

Description

【発明の詳細な説明】 本発明は燃料電池用電解質タイルの製造方法疋関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for manufacturing electrolyte tiles for fuel cells.

従来の燃料電池用電解質タイルのセラミックス多孔質体
としては、各々気孔の性状は異なるが、素焼きの陶器や
発泡性ガラスのセラミックスやセラミックスフオームが
ある、しかし、これらは燃料電池用電解質タイルとして
使用するセラミックスとして、セラミックスに要求され
る硬さや緻密さに欠けている。また、気孔部に各種の無
機物潰や電解質を充填して使用する場合に、イオンコ1
n過性、電子伝導性が不足するものがかなりある。また
、イオン通過性、電子伝導性は満足しても、気孔に充填
した各種の無機物質や電解質が気孔部から流失してしま
う欠点あるいはセラミックスの骨格だけでは、十分な強
度がでないという欠点を持つものが多かった。
Conventional ceramic porous bodies for electrolyte tiles for fuel cells include unglazed pottery, foamed glass ceramics, and ceramic foam, although each type has different pore properties.However, these are used as electrolyte tiles for fuel cells. As a ceramic, it lacks the hardness and precision required of ceramics. In addition, when filling the pores with various inorganic substances or electrolytes, Ion Co.
There are quite a few that are n-transparent and lack electron conductivity. In addition, even if the ion permeability and electron conductivity are satisfied, there are drawbacks such as the various inorganic substances and electrolytes filled in the pores being washed away from the pores, or the fact that the ceramic skeleton alone does not have sufficient strength. There were many things.

更に、セラミックスのシートを作る場合に、抄紙方法を
用いないで作る方法が、射出成形法、押出成形法、静水
圧プレス法としである。しかし、これらの方法では、6
0Crn平方以上の大面積のセラミックスンートを作る
と、表面が、割れたり、歪んだりして均一なものとなら
ない。
Furthermore, when producing ceramic sheets, there are injection molding methods, extrusion molding methods, and isostatic pressing methods that do not use papermaking methods. However, with these methods, 6
If a ceramic suture with a large area of 0 Crn square or more is made, the surface will be cracked or distorted and will not be uniform.

また、従来、燃料電池用電解質タイルの作り方で、焼結
性物質の粉体として、α−アルミナを、繊維質として木
材パルプを51〜70重量%添加して、湿式混練し、凝
集させた後、抄造して得たソート状物を焼成することに
より、−薄くて緻密な多孔質体を得る方法がある。しか
し、この方法では、高い気孔率を得るために、木材ノく
パルプの含有量が多く、しかも、α−アルミナを使用し
ているため、焼結物質を得るのに、1.500〜1.6
00℃の高温で焼成する必要があった。
Conventionally, in the method of making electrolyte tiles for fuel cells, α-alumina is added as a sinterable material powder and 51 to 70% by weight of wood pulp is added as a fibrous material, and after wet kneading and agglomeration, There is a method of obtaining a thin and dense porous body by firing a sorted material obtained by papermaking. However, in this method, in order to obtain a high porosity, the content of wood pulp is high, and since α-alumina is used, it takes 1.500 to 1.50% to obtain a sintered material. 6
It was necessary to bake at a high temperature of 00°C.

本発明では、前記のような欠点を除去し、あるいはこれ
らの欠点を補なうのに十分1ハ緻密で強度があり、気孔
率が高く、細孔が迷路のようになっているセラミツぐス
の多孔質体を製造する方法として、焼結性無機物質とし
て、r−リチウムアルミネートで平均粒径が1μ以下の
ものを使用し、アルミナを使用する方法より低温で焼M
1可能とし、木材パルプの添加量を3〜15重量%と少
量にし、樹脂としては熱硬化性のプラスティックで、粉
末、望ましくはエマルジョン化されたものを3〜40重
量%添加し、気孔率が、焼結物の全体積の40〜80%
になるような燃料電池用電解質タイルの製造方法である
The present invention uses a ceramic material that is sufficiently dense and strong, has high porosity, and has labyrinth-like pores to eliminate or compensate for the above-mentioned drawbacks. As a method for manufacturing a porous body, r-lithium aluminate with an average particle size of 1 μm or less is used as the sinterable inorganic material, and sintering is performed at a lower temperature than the method using alumina.
1, the amount of wood pulp added is as small as 3 to 15% by weight, and the resin is a thermosetting plastic, powder, preferably emulsion, is added to 3 to 40% by weight, and the porosity is reduced. , 40-80% of the total volume of the sintered product
This is a method for manufacturing electrolyte tiles for fuel cells.

燃料電池用電解質タイルとしては、アルミナが緻密質で
電気絶縁性等に優れている。しかしながら、アルミナは
電解質として使用する炭酸塩の中で、特に炭酸リチウム
と反応し、リチウムアルミネートに変ってしまう。そこ
で、本発明においては、そのリチウムアルミネートの中
で一番安定な構造であろr−リチウムアルミネートを水
酸化リチウムあるいはリチウム塩類とアルミナを反応さ
せてあらかじめ製造しておき、これを焼結性無機物質と
して使用する。
As an electrolyte tile for fuel cells, alumina is dense and has excellent electrical insulation properties. However, among the carbonates used as electrolytes, alumina reacts particularly with lithium carbonate and turns into lithium aluminate. Therefore, in the present invention, r-lithium aluminate, which has the most stable structure among lithium aluminates, is produced in advance by reacting lithium hydroxide or lithium salts with alumina, and this is sintered. Use as an inorganic substance.

以下さらに詳細に説明すれば、焼結性無機物質の製造で
は、f、10H5L L2 COs 、L i C石、
L 12SO−等のリチウム塩類とアルミナの中で粒径
が細か(、表面か活性なr−アルミナを1.000℃で
1時間以上服焼して反応させ、放冷して、IJチウムア
ルミネートの反応焼成物を製造し、この冷却物をボール
ミル中で粉砕して粒径な1μ以下にして使用する。
To explain in more detail below, in the production of sinterable inorganic materials, f, 10H5L L2 COs, Li C stone,
Lithium salts such as L12SO- are reacted with R-alumina, which has a small particle size among alumina (and surface active R-alumina), by baking at 1.000℃ for more than 1 hour, and then allowed to cool to form IJ lithium aluminate. A reaction calcined product is produced, and this cooled product is pulverized in a ball mill to obtain a particle size of 1 μm or less for use.

ボールミル中で、IJチウムアルミネートの粒径を1μ
以下にすることは、セラミックスの焼結の時と同様に、
燃料電池用電解質タイルにおいても、焼結温度が粒径も
細かにするほど焼結温度を下げて、省エネルギーにする
とともに、焼結物の強度を上げる目的のためである。ま
た、粒径の細かい、IJチウムアルミネートを使用して
、燃料電池用電解質タイルを製造した場合、このタイル
にL 12COs 、K2 COaのような炭酸塩を含
浸させなければならない。そして、このタイルが炭酸塩
を気孔に充填して保持しているためには、気孔の径が0
1〜1μ程度の細孔である必ザがある。r−リチウムア
ルミネートの粒径をより細かくずろことは、電解質タイ
ルの細孔をより細かくすく)ことである。
In a ball mill, the particle size of IJ thium aluminate was reduced to 1μ.
The following steps are the same as when sintering ceramics:
In electrolyte tiles for fuel cells as well, the sintering temperature is lowered as the particle size becomes finer to save energy and increase the strength of the sintered product. Further, when an electrolyte tile for a fuel cell is manufactured using IJ tium aluminate having a fine particle size, the tile must be impregnated with a carbonate such as L 12 COs or K 2 COa. In order for this tile to fill and retain carbonate in its pores, the pore diameter must be 0.
The pores must be about 1 to 1 μm in size. Making the particle size of the r-lithium aluminate finer makes the pores of the electrolyte tile finer.

補強剤としての機能と40〜80%の気孔率を得る目的
で、各種の繊維質の中から木材パルプな選択し、木材パ
ルプの添加量を焼結前の乾燥時のシート状物の全重量に
対して6〜15%としている。しかし、木材パルプの添
加だけでは、40〜80%の気孔率で、01〜1μの細
孔を得るのは無理である。そこで、この気孔率と細孔径
とするために樹脂を添加する。樹脂としては、熱硬化ゼ
1のプラスティック樹脂で、その一形態としては粉末状
でも良いが望ましくはエマルジョン化したものを焼成前
のシート状物の乾燥全車量に対して6〜40%添加する
In order to function as a reinforcing agent and obtain a porosity of 40 to 80%, wood pulp is selected from among various types of fibers, and the amount of wood pulp added is adjusted to the total weight of the sheet when dry before sintering. 6% to 15%. However, it is impossible to obtain pores of 01 to 1 μm with a porosity of 40 to 80% only by adding wood pulp. Therefore, a resin is added to achieve the desired porosity and pore size. The resin is a plastic resin of thermosetting resin 1, which may be in the form of a powder, but preferably in the form of an emulsion, and is added in an amount of 6 to 40% based on the total dry weight of the sheet material before firing.

樹脂は、抄造したシート状物が乾燥、焼成中に溶解した
すせずに形状を維持する必要があり、そのためには、熱
硬化性プラスティック樹脂が:J Lている。また、熱
硬化性プラスティック樹脂の中ては、抄造の過程で、よ
り凝集し易(、抄造に適するようにエマルジョン化され
たものを選択するのが良い。添加量としては、焼成前の
シート状物の乾燥全重量に対して6〜40%と1−てい
る。この添加量が3%以下では、焼結物の気孔率が40
〜80%に達しないし、また、40%以上の添加量では
気孔率は80%以上となってしまい、焼結物の強度が低
下し、シート状物の形状が(ずれやすくブよる。そのた
め、熱硬化性プラスティック樹脂の添加量は3〜40重
量%としである。
It is necessary for the resin to maintain the shape of the paper-formed sheet without dissolving during drying and firing, and for this purpose, a thermosetting plastic resin is required. In addition, among thermosetting plastic resins, it is better to select one that is more likely to aggregate during the papermaking process (or one that has been emulsified to be suitable for papermaking). It is 6 to 40% of the total dry weight of the product.If this addition amount is 3% or less, the porosity of the sintered product will be 40%.
If the amount added is 40% or more, the porosity will be 80% or more, and the strength of the sintered product will decrease, and the shape of the sheet-like product will change (easily shift and warp. The amount of thermosetting plastic resin added is 3 to 40% by weight.

焼結物質の製造方法は先ず、3〜1″5重量%の水相バ
ルブと3〜40重量%の熱硬化性プラスティック樹脂と
焼結性無機物質である1μ以下の粒径のr−リチウムア
ルミネート粉体とからなる固形分に対して10〜50倍
程度の重量の水を加えて湿式混合し、抄造に適する水性
スラリーに調整する。この水性スラリーには、r−リチ
ウムアルミネート製造の際の過剰の水酸化リチウムある
いはリチウム塩類が溶出し、酸性あるいはアルカリ性を
カリ水溶液を加えてPIlを7に調整し、凝集剤1・9
よび界面活性剤を添加し凝集させ、抄造機にて抄造し、
シ・−ト状、あるいは板状に成形する。
The method for producing the sintered material is as follows: 3~1'' 5% by weight of an aqueous phase bulb, 3~40% by weight of a thermosetting plastic resin, and a sinterable inorganic material, r-lithium aluminum with a particle size of 1μ or less. Water is added in an amount of about 10 to 50 times the weight of the solid content consisting of aluminate powder and wet-mixed to prepare an aqueous slurry suitable for papermaking.This aqueous slurry contains Excess lithium hydroxide or lithium salts are eluted, acidic or alkaline solution is added to adjust PIl to 7, and flocculant 1.9
Add surfactant and coagulate, make paper using a paper making machine,
Form into a sheet or plate.

凝集剤の添加は、繊維質と樹脂と焼結性無機物質とが一
緒に凝集して抄造しゃすくするためである。また、界面
活性剤は繊維同志、樹脂同志、無機物質同志および繊維
質と樹脂質と無機物質とか一凝集するのを補助するとと
もに、抄造した/−ト状、板状のものの表面が均一で滑
らかになるようにするために添加する。
The reason for adding the flocculant is that the fibers, resin, and sinterable inorganic substance coagulate together to facilitate paper-making. In addition, surfactants help fibers, resins, inorganic substances, and fibers, resins, and inorganic substances coagulate together, and the surface of paper-shaped or plate-shaped objects is uniform and smooth. Add to make it.

この成形物を焼成炉に入れ、酸化雰囲気で焼成する。焼
成は室温から、1時間あたり60〜8゜’C(以下単[
30〜80℃/IIと略す)昇温し、500〜700℃
で1〜6時間保持する。これは、木材パルプおよび熱硬
化性プラスティック樹脂とが焼失気化されて、細孔で迷
路のような気孔を作るためである。昇温速度は3o’c
/II以上であると昇温に時間がかがりすぎ、また、s
o℃/I]以上ではパルプおよび樹脂が急速に膨張し、
抄造したシート状、板状の形状がふ(れて形が(ずれて
しまう。そのため昇温速度は30’〜80 ’C/Hが
適している。そして、5ow′O〜7oO°Cにおいて
パルプおよび樹脂を焼失気(IZせるため<soo〜7
00 ’Cで1〜3時間保持する。
This molded product is placed in a firing furnace and fired in an oxidizing atmosphere. Firing is performed from room temperature to 60-8°C per hour (hereinafter simply [
30-80℃/abbreviated as II), raise the temperature to 500-700℃
Hold for 1 to 6 hours. This is because the wood pulp and thermosetting plastic resin are burned and vaporized, creating a labyrinth of pores. The heating rate is 3o'c
/II or more, it takes too much time to raise the temperature, and
o℃/I], the pulp and resin expand rapidly;
The paper-made sheet or plate shape will swell and lose its shape. Therefore, a temperature increase rate of 30' to 80' C/H is suitable. and to burn out the resin (IZ) <soo ~ 7
Hold at 00'C for 1-3 hours.

保持時間が1時間以下ではパルプおよび樹脂の焼失気化
が完了せず、6時間以上では焼成 に時間が長くなりす
ぎるため 1〜6時間が適当である。この間、空気(酸
素)を炉内に送り込んで酸化雰囲気とすることも有効で
ある、その後、 r IJチウムアルミネートが焼結す
るi、 000〜1,600 ℃までは10″0へ30
0’C/IIで昇温し、焼結が行なわれるi、00.0
〜1、300°Cで1〜6時間焼成を行なう、焼成はi
、 000℃以下では焼−結が完了ぜす、また、1. 
、!、 00 ’C以上では、焼結が進みすぎて、せっ
かくできた細孔がつふれてしまうので、焼結温度は1.
000〜i、 500℃が適当である。また、1、00
0〜1.300℃で1〜6時間保持するのは、コノ1.
000〜1.300°CVCおいて焼結が完了するため
には、保持時間が必要であり、その保持時間は1時間以
下では強度がです、形が(ずれてしまうし、3時間以上
では焼結が進みすぎてしまう。
If the holding time is less than 1 hour, the burning and vaporization of the pulp and resin will not be completed, and if the holding time is more than 6 hours, the baking time will be too long, so 1 to 6 hours is appropriate. During this time, it is also effective to send air (oxygen) into the furnace to create an oxidizing atmosphere. After that, the IJ lithium aluminate is sintered, from 000 to 1,600 °C, from 10" to 30
The temperature is raised at 0'C/II and sintering takes place i, 00.0
~1, Perform baking at 300°C for 1 to 6 hours, baking at i
, 1. Sintering is completed below 000°C.
,! , 00'C or higher, sintering progresses too much and the pores that have been created are clogged, so the sintering temperature is 1.
000-i and 500°C are suitable. Also, 1,00
0 to 1. Holding at 300°C for 1 to 6 hours is 1.
In order to complete sintering at 000~1.300°CVC, a holding time is required; if the holding time is less than 1 hour, the strength will deteriorate and the shape will shift, and if it is held for more than 3 hours, the sintering will fail. The knot ends up going too far.

それで1〜6時間が適当である。Therefore, 1 to 6 hours is appropriate.

以上のように、粒径が1μ以下の、IJチウムアルミネ
ートを使用することにより、より低温で焼結ができ、し
かも、木材パルプ量が3〜15%程度の添加および熱硬
化性プラ゛スティック樹脂で、望ましくはエマルジョン
化したものを3〜40%程度添加することにより、気孔
率が40〜80%と大きく、細孔が迷路のようになった
緻密質で強度の大きな燃料電池用電解質タイルが製造可
能となる、。
As described above, by using IJ tium aluminate with a particle size of 1μ or less, it is possible to sinter at a lower temperature, and moreover, it is possible to sinter at a lower temperature, and it is possible to add wood pulp of about 3 to 15% and to make thermosetting plastics. A dense and strong electrolyte tile for fuel cells with a large porosity of 40 to 80% and a labyrinth-like pore structure by adding 3 to 40% of a resin, preferably in the form of an emulsion. becomes possible to manufacture.

以下に本発明の具体的な実施例を述べる。Specific examples of the present invention will be described below.

〈実施例1〉 (A ) r −IJチウムアルミネートの製造のため
r−アルミナ 50部 部を500m1程度のポリ袋に入れて、手で10分程振
り回して、乾式混合し、これを300m1+程度のルツ
ボに入れて、電気炉に入れる。酸化雰囲気で必要なら空
気を流しながら、室温から200℃肩で1. OO’ 
0°Cまで昇温する。1.000°Cで2時間保持して
服焼して反応させ、炉内放冷を行ない、室温まで冷却す
る。
<Example 1> (A) For the production of r-IJ thium aluminate, put 50 parts of r-alumina into a plastic bag of about 500 m1, shake it around by hand for about 10 minutes, dry mix it, and add it to about 300 m1+. Put it in a crucible and put it in an electric furnace. 1. In an oxidizing atmosphere, with air flowing if necessary, from room temperature to 200°C. OO'
Raise the temperature to 0°C. The mixture is held at 1.000°C for 2 hours to cause a reaction, and then allowed to cool in the furnace and cooled to room temperature.

冷却したr−リチウムアルミネートの服焼物を3oom
l程度のボールミルに入れて、24時間、粉砕し、平均
粒径を08部程度にする。
3 oom of cooled r-lithium aluminate
The mixture is placed in a ball mill of about 1.0 liters and pulverized for 24 hours to give an average particle size of about 0.8 parts.

(I3) 試料の組成 (C) 凝集剤と界面活性側 24程度の容器に水i、o o o部と木材パルプ5部
を入れ、20分はど攪拌して水に十分分散させて、そこ
へ、先はどボールミルで粉砕した。 IJチウムアルミ
ネートの服焼物60部およびフェノール樹脂20部を加
えて1分はど攪拌し、水性スラリーを作る。
(I3) Composition of the sample (C) Coagulant and surface active side Put 1,00 parts of water and 5 parts of wood pulp in a container with a size of about 24 cm, stir for 20 minutes to fully disperse it in the water, and then add Well, the tip was ground with a ball mill. Add 60 parts of baked IJ thium aluminate and 20 parts of phenol resin and stir for 1 minute to make an aqueous slurry.

この水性スラリーは過剰のリチウムイオンが水に溶出し
てPHが13以上の強アルカリとなる。
This aqueous slurry becomes a strong alkali with a pH of 13 or more as excess lithium ions are eluted into water.

そこであらかじめ作っておいた希硫酸(硫酸:水:20
:1)を滴加してP Hを7にする。その中へあらかじ
め作っておいた硫酸バンド(15%水溶液)を20部加
えて2分はど攪拌して、I) I−1が4以下になった
ことをP H試験紙で確認し、こり。
Therefore, we prepared dilute sulfuric acid (sulfuric acid: water: 20
:1) was added dropwise to bring the pH to 7. Add 20 parts of sulfuric acid band (15% aqueous solution) prepared in advance to the solution, stir for 2 minutes, and confirm with PH test paper that I) I-1 is 4 or less. .

もあらかじめ作っておいたポリアクリルアミド系高分、
子]凝ノ集(サンポリ−N−5,00の0.2%水溶液
) を60部と両性界面活性剤(リポミンLA、20%
水溶液を5部添加し、1分はど攪拌して凝集させる。
A polyacrylamide polymer prepared in advance,
60 parts of agglomerate (0.2% aqueous solution of Sunpoly-N-5,00) and an amphoteric surfactant (Lipomin LA, 20%
Add 5 parts of the aqueous solution and stir for 1 minute to coagulate.

以上のようにして凝集した試料は、抄造機で抄造し、5
0cm角で2配厚のシート状にする。これを乾燥した後
に電気炉に入れて、酸化雰囲気で、必要ならば炉内に空
気を流しながら、室温から、50°C/ I−1の速度
で加熱し、木材パルプおよびフェノール樹脂が焼失気化
されて、細孔で迷路のような気孔ができる温度の600
’(:、で2時間保持する。その後1. IJチウムア
ルミネートが焼結する1、 200℃まで200°C/
Hで昇温し、電気炉の温度が1.200℃になったら、
この温度で2時間保持して、r−リチウムアルミネート
を焼結さぜ、燃料電池用電解質タイルを製造した。
The sample agglomerated in the above manner is made into a paper using a paper making machine, and
Form into a 0cm square sheet with two thicknesses. After drying, it is placed in an electric furnace and heated from room temperature at a rate of 50°C/I-1 in an oxidizing atmosphere, with air flowing through the furnace if necessary, until the wood pulp and phenolic resin are burned off and vaporized. At a temperature of 600°C, a maze-like pore is formed.
'(:, held for 2 hours. Then 1. IJ tium aluminate is sintered 1. 200 °C / 200 °C
When the temperature of the electric furnace reaches 1.200℃ by increasing the temperature with H,
This temperature was maintained for 2 hours to sinter the r-lithium aluminate and produce an electrolyte tile for a fuel cell.

〈実施例2〉 (B) 試料の調整 (C) 凝集剤と界面活性剤 (ライオン(陶製商品名「リポミ/ 、L+ 11 J
 /以上のような組成(5)(131(Q を用いて、
以下は実施例1と同様にしてシート状の燃料7L池用’
lJf IW質メタイル得られた。
<Example 2> (B) Sample preparation (C) Flocculant and surfactant (Lion (ceramic product name: "Lipomi/", L+ 11 J
/The above composition (5) (131 (using Q,
The following is the same as in Example 1 for a sheet-shaped fuel 7L pond.
lJf IW quality metal was obtained.

このようにして得らり、たセラミックス多孔9体は燃料
電池で用いられる電解質タイルとしての11―能に優J
1、耐久性にも優れているものである、本発明によれば
、薄型で、緻密質で、気孔率が高く、細孔が迷路のよう
に連続的になったセラミックス多孔質体が製造される。
The ceramic porous body thus obtained has excellent properties as an electrolyte tile used in fuel cells.
1. According to the present invention, a ceramic porous body which is excellent in durability, is thin, dense, has high porosity, and has continuous pores like a labyrinth. Ru.

本発明では、従来の薄型で、気孔のない、緻密質の金属
酸化物を作る方法と発泡性多孔質体を作る方法の両方法
の長所を取入れており、気孔率の調整も木材パルプと熱
硬化性プラスティック樹脂の添加量によって自由に変え
ら)する。しかも、セラミックスフオーム製造知おける
問題の、ポリウレタンによる発泡を施した後の複雑な処
理工程が、本発明では除去されるので、製造工程が簡略
化される。また、粒径1μ以下のr−リチウムアルミネ
ートを使用する事と、木材パルプと熱硬化性プラスティ
ック樹脂の添加で、より低温で、緻密で強度の高いセラ
ミックス多孔質体が得られるため、省エネルギーの効果
も生ずる。
The present invention incorporates the advantages of both the conventional method of making a thin, pore-free, dense metal oxide and the method of making a foamable porous material, and the porosity can also be adjusted using wood pulp and heat. (can be freely changed depending on the amount of curable plastic resin added). In addition, the present invention eliminates the complicated processing steps after foaming with polyurethane, which is a known problem in ceramic foam manufacturing, so the manufacturing process is simplified. In addition, by using r-lithium aluminate with a particle size of 1μ or less and adding wood pulp and thermosetting plastic resin, a dense and strong ceramic porous body can be obtained at lower temperatures, resulting in energy savings. Effects also occur.

その上、従来使用できなかった熱による膨張、収縮を繰
返ず場所や応力のかがる場所および特に、燃料電池用電
解質タイルのように、熱応力、電気的応力、機械的応力
が繰返しかかる場所への使用が十分可能になる。
In addition, it can be used in places where thermal stress does not repeatedly expand or contract due to heat, or places where stress is applied, and in particular, places where thermal stress, electrical stress, or mechanical stress is applied repeatedly, such as electrolyte tiles for fuel cells. It becomes fully possible to use it.

さらに言えば、焼成用のシート状物を成形するのに、抄
造技術を用いるので、均一な厚さのノート状物を連続製
造することが可能であり、その厚さも様々な範囲で実施
可能である。
Furthermore, since papermaking technology is used to form sheet-like objects for firing, it is possible to continuously manufacture notebook-like objects of uniform thickness, and the thickness can also be varied within a variety of ranges. be.

特許出願人 凸版印刷株式会社 代表者鈴木和夫patent applicant Toppan Printing Co., Ltd. Representative Kazuo Suzuki

Claims (1)

【特許請求の範囲】[Claims] ull外性無機物質粉体と繊維質と樹脂を混合して水性
スラリーとし、凝集、抄造して得たシート状物質を焼成
することにより前記繊維質および樹脂を焼失気化させ、
焼結性無機物質の粉体な焼結させて、薄くて緻密な多孔
質体を製造する際に、無機物質どして、水酸化リチウム
およびまたはリチウム塩類とr−Aff120.をi、
 o o o ℃で1時間以上服焼して、放冷した焼成
物をボールミルで粉砕し、平均粒径を1μ以下にしたi
 IJチウムアルミネートを使用し、繊維質としては木
材パルプを、焼成前のシート状物の乾燥全重量に対して
3〜15%を、樹脂としては熱硬化性のプラスティック
樹脂を焼成前のシート状物の乾燥全重量に対して3〜4
0%添加して、混合した水性スラIJ−に、無機の酸ま
たはアルカリ水溶液でpHを7に調整し、その後、凝集
剤と界面活性剤を添加して凝集、抄造し、焼成は、室温
から60〜8゛′C/IIで昇温し、500〜700’
Cで1〜6時間保持し、その後ioo〜300°C/ 
I−Iで昇温し、1.00 []〜1.5 D 0℃で
1〜3時間保持することを特徴とする燃料電池用電解質
タイルの製造方法。
Aqueous slurry is obtained by mixing an extraneous inorganic substance powder, fibrous material, and resin, and the sheet-like material obtained by agglomeration and papermaking is fired to burn off and vaporize the fibrous material and resin,
When producing a thin and dense porous body by sintering a powder of a sinterable inorganic substance, the inorganic substance is mixed with lithium hydroxide and/or lithium salts and r-Aff120. i,
o o o The baked product was baked at ℃ for more than 1 hour and then allowed to cool.The baked product was ground in a ball mill to reduce the average particle size to 1μ or less.
IJ thium aluminate is used, wood pulp is used as the fiber material, 3 to 15% of the total dry weight of the sheet before firing is used, and thermosetting plastic resin is used as the resin before firing. 3 to 4 for the total dry weight of the item
The pH of the mixed aqueous slurry IJ- is adjusted to 7 with an inorganic acid or alkaline aqueous solution, and then a flocculant and a surfactant are added to flocculate and form paper, and the firing starts from room temperature. Raise the temperature at 60-8'C/II, 500-700'
Hold at ℃ for 1-6 hours, then ioo~300°C/
A method for producing an electrolyte tile for a fuel cell, which comprises raising the temperature at I-I and holding it at 1.00 [ ] to 1.5 D 0°C for 1 to 3 hours.
JP58188053A 1983-10-07 1983-10-07 Manufacture of electrolyte tile for fuel cell Pending JPS6079674A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58188053A JPS6079674A (en) 1983-10-07 1983-10-07 Manufacture of electrolyte tile for fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58188053A JPS6079674A (en) 1983-10-07 1983-10-07 Manufacture of electrolyte tile for fuel cell

Publications (1)

Publication Number Publication Date
JPS6079674A true JPS6079674A (en) 1985-05-07

Family

ID=16216859

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58188053A Pending JPS6079674A (en) 1983-10-07 1983-10-07 Manufacture of electrolyte tile for fuel cell

Country Status (1)

Country Link
JP (1) JPS6079674A (en)

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