JPH05310471A - Production of impenetrative carbonaceous plate - Google Patents
Production of impenetrative carbonaceous plateInfo
- Publication number
- JPH05310471A JPH05310471A JP4143165A JP14316592A JPH05310471A JP H05310471 A JPH05310471 A JP H05310471A JP 4143165 A JP4143165 A JP 4143165A JP 14316592 A JP14316592 A JP 14316592A JP H05310471 A JPH05310471 A JP H05310471A
- Authority
- JP
- Japan
- Prior art keywords
- plate
- pressure
- carbonaceous
- under
- pressurization
- 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
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/96—Carbon-based electrodes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0213—Gas-impermeable carbon-containing materials
-
- 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
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Ceramic Products (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、燃料電池や塩素−亜鉛
系二次電池のセパレータ部材などの用途に好適な不透過
性炭素質プレートの製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing an impermeable carbonaceous plate suitable for use as a separator member for fuel cells and chlorine-zinc secondary batteries.
【0002】[0002]
【従来の技術】気体および液体に対して高度の不透過性
を備え、同時に優れた耐蝕性と導電性を有する炭素質プ
レートは、燃料電池とくに燐酸型燃料電池のセパレータ
部材として有用されている。該セパレータ部材を目的と
する不透過性炭素質プレートの製造技術に関しては従来
から多様なプロセスが提案されているが、実用的には最
終的にマトリックス部分がガラス状カーボンに転化する
ような熱硬化性樹脂を原料成分とする方法が優れてい
る。2. Description of the Related Art Carbonaceous plates having a high degree of impermeability to gases and liquids and, at the same time, excellent corrosion resistance and conductivity are useful as separator members for fuel cells, particularly phosphoric acid fuel cells. Although various processes have been proposed in the past for the production technology of the impermeable carbonaceous plate intended for the separator member, practically, it is thermosetting so that the matrix part is finally converted into glassy carbon. The method of using a hydrophilic resin as a raw material component is excellent.
【0003】例えばこの種の製造技術としては、熱硬化
性樹脂プレポリマーと炭素質フィラーの混練物をプレー
トに成形し、成形プレートを樹脂シートの離型性材料を
介して多段に積層し50〜100℃で10時間以上加熱
する工程と、150〜200℃の加熱下で1〜10kgf/
cm3 の圧力を加えながら1〜30分間処理する工程と、
180〜300℃で5時間以上加熱したのち非酸化性雰
囲気中で焼成炭化する工程からなる方法(特公平3−35
262 号公報) 、あるいは熱硬化性樹脂を含浸したセルロ
ース質の紙を積層圧着し、硬化、焼成する方法(特開昭
60−161144号公報)などが知られている。For example, as a manufacturing technique of this type, a kneaded product of a thermosetting resin prepolymer and a carbonaceous filler is molded into a plate, and the molded plates are laminated in multiple stages with a mold-releasing material of a resin sheet interposed therebetween. Heating at 100 ° C for 10 hours or more, and heating at 150 to 200 ° C for 1 to 10 kgf /
a step of treating for 1 to 30 minutes while applying a pressure of cm 3 ;
A method comprising a step of heating at 180 to 300 ° C for 5 hours or more and then firing and carbonizing in a non-oxidizing atmosphere (Japanese Patent Publication No. 3-35).
No. 262) or a method in which cellulosic paper impregnated with a thermosetting resin is laminated and pressure-bonded, and then cured and fired (Japanese Patent Laid-Open No. Sho 62-242, No.
No. 60-161144) is known.
【0004】ところが、上記の方法にはそれぞれに問題
点がある。すなわち、前者の方法によれば材質がカーボ
ン粉/ガラス状カーボン複合材となるため、燃料電池セ
パレータに要求される高強度、高耐蝕性、低電気抵抗性
等の材質特性の面では満足するが、成形および硬化の工
程が複雑で製造に長期間を要するほか、製造コストが高
騰する欠点がある。これに対し、後者の方法は製造工程
が比較的単純であるために前者のような製造プロセス面
での欠点はないものの、製造される材質が実質的にガラ
ス状カーボン単味になる関係で、電気抵抗が高く、かつ
破壊靭性が低くなって燃料電池用セパレータとしての要
求特性を満足しなくなる材質面での問題がある。However, each of the above methods has problems. That is, according to the former method, since the material is carbon powder / glassy carbon composite material, it is satisfactory in terms of material properties such as high strength, high corrosion resistance and low electrical resistance required for the fuel cell separator. In addition to the complicated molding and curing steps, it takes a long time to manufacture, and the manufacturing cost rises. On the other hand, the latter method does not have the drawbacks in terms of the manufacturing process like the former because the manufacturing process is relatively simple, but the material to be manufactured is substantially glassy carbon alone, There is a problem in terms of material that electrical resistance is high, fracture toughness is low, and the characteristics required as a fuel cell separator are not satisfied.
【0005】[0005]
【発明が解決しようとする課題】このように、熱硬化性
樹脂を原料成分として不透過性炭素質プレートを製造す
るための従来技術においては、製造工程あるいは製品材
質のいずれかの面に解決すべき課題が残されている。As described above, in the prior art for producing an impermeable carbonaceous plate using a thermosetting resin as a raw material component, either the manufacturing process or the product material is solved. There are remaining issues to be solved.
【0006】本発明者らはこのような実情に鑑み、熱硬
化性樹脂を原料成分とする場合のプレート成形ならびに
硬化処理の工程に着目して鋭意研究を重ねた結果として
本発明の開発に至ったもので、その目的は燃料電池や塩
素−亜鉛系二次電池用のセパレータ部材に要求される材
質特性を満足する不透過性炭素質プレートを比較的簡単
な工程を介して生産性よく得るための製造方法を提供す
ることにある。In view of such circumstances, the inventors of the present invention have conducted intensive research focusing on the steps of plate molding and curing treatment in the case of using a thermosetting resin as a raw material component, and as a result, have led to the development of the present invention. The purpose is to obtain an impermeable carbonaceous plate satisfying the material characteristics required for a separator member for a fuel cell or a chlorine-zinc secondary battery with high productivity through a relatively simple process. It is to provide a manufacturing method of.
【0007】[0007]
【課題を解決するための手段】上記の目的を達成するた
めの本発明による不透過性炭素質プレートの製造方法
は、炭素質粉末と熱硬化性樹脂を主体とする原料成分を
真空下で混練処理して一次成形し、一次成形体を80〜
200℃に保持された平面板に載置して加圧・降圧のサ
イクルを反復してプレート化し、ついで20〜250kg
f/cm2 の加圧下でプレートを硬化させたのち、非酸化性
雰囲気中で焼成炭化処理を施すことを構成上の特徴とす
る。In order to achieve the above object, the method for producing an impermeable carbonaceous plate according to the present invention comprises kneading a carbonaceous powder and a raw material component mainly composed of a thermosetting resin under vacuum. 80-
Place on a flat plate kept at 200 ° C, repeat the pressurization and depressurization cycle to form a plate, and then 20 to 250 kg.
The structural feature is that the plate is cured under a pressure of f / cm 2 and then calcined and carbonized in a non-oxidizing atmosphere.
【0008】本発明の原料成分のうち炭素質粉末はフィ
ラーとなるもので、コークス、黒鉛、ガラス状カーボン
等の粉末あるいはカーボンブラックが用いられる。これ
らの炭素質粉末は好ましくは平均粒径50μm 以下の微
粉末として使用に供される。熱硬化性樹脂としては、例
えばフェノール樹脂、キシレン樹脂、フラン樹脂、ポリ
イミド樹脂など焼成炭化処理によってガラス状カーボン
に転化する炭素化率の高い樹脂類が挙げられ、プレポリ
マー状態の粉末および/または液状として適用される。
本発明の原料成分はこれら炭素質粉末と熱硬化性樹脂が
主体となるが、このほかに必要に応じて混練助剤、成形
助剤などの添加物を配合することができる。これらの添
加物は焼成炭化工程で揮散する性質の有機物質が好まし
く、例えば混練助剤としてメチルセルロース、カルボキ
シメチルセルロース、リグニンスルホン酸ナトリウム等
が、また成形助剤としてはグリセリンのような高級アル
コール類が好適に用いられる。原料成分の配合割合は得
られる材質の目標特性によって定められるが、主体原料
の配合比率としては炭素質粉末100重量部に対し熱硬
化性樹脂成分50〜200重量部の範囲が適当である。Among the raw material components of the present invention, carbonaceous powder serves as a filler, and powder of coke, graphite, glassy carbon or carbon black is used. These carbonaceous powders are preferably used as fine powders having an average particle size of 50 μm or less. Examples of the thermosetting resin include phenol resins, xylene resins, furan resins, polyimide resins and the like, which have a high carbonization rate and are converted into glassy carbon by a firing carbonization treatment, and powders and / or liquids in a prepolymer state. Applied as.
The raw material components of the present invention are mainly composed of these carbonaceous powders and thermosetting resins, but in addition to these, additives such as kneading aids and molding aids can be added as necessary. These additives are preferably organic substances that volatilize in the firing and carbonization step, for example, methyl cellulose, carboxymethyl cellulose, sodium lignin sulfonate and the like as a kneading aid, and higher alcohols such as glycerin as a molding aid are suitable. Used for. The mixing ratio of the raw material components is determined by the target characteristics of the material to be obtained, but the mixing ratio of the main raw material is preferably in the range of 50 to 200 parts by weight with respect to 100 parts by weight of the carbonaceous powder.
【0009】これらの原料成分は真空下において混練処
理し、適宜な形状に一次成形する。工程条件としては、
真空度を100Torr以下とし、温度を30〜100℃に
設定することが好ましい。この工程では混練と成形をそ
れぞれ分離しておこなうこともできるが、混練機構と成
形機構とが一体となった混練成形機を用いると作業能率
が高まるほか、混入ガス成分が効果的に脱気されるので
材質特性の向上も図れる。本発明の目的に好適な処理手
段は、2軸スクリューからなる混練部と真空脱気室およ
び1軸スクリューの成形部からなる構造の混練押出成形
装置を用い、予備的に混練した原料成分を投入して連続
的に混練と押出成形をおこなうことである。該工程にお
いて、混練段階で炭素質粉末フィラーと熱硬化性樹脂プ
レポリマーは均一に相互分散し、同時に樹脂がバインダ
ーとなってフィラーを十分に濡らし、成形段階では混練
時に混入する空気および原料に含有される揮発成分が円
滑に除去される。These raw material components are subjected to a kneading treatment in a vacuum and primary molding into an appropriate shape. As process conditions,
It is preferable to set the degree of vacuum to 100 Torr or less and set the temperature to 30 to 100 ° C. In this process, kneading and molding can be performed separately, but using a kneading and molding machine with an integrated kneading mechanism and molding mechanism improves work efficiency and effectively degass mixed gas components. As a result, the material characteristics can be improved. The processing means suitable for the purpose of the present invention is a kneading extrusion molding apparatus having a structure including a kneading section consisting of a twin screw, a vacuum deaeration chamber and a molding section of a single screw, and the raw material components kneaded in advance are added. Then, the kneading and the extrusion molding are continuously performed. In the step, the carbonaceous powder filler and the thermosetting resin prepolymer are uniformly dispersed in the kneading step, and at the same time, the resin serves as a binder to sufficiently wet the filler, and in the molding step, it is contained in the air and raw materials mixed during kneading. The volatile components are smoothly removed.
【0010】得られた一次成形体は、80〜200℃に
保持された平面板に載置し、加圧・降圧のサイクルを反
復してプレート状に成形する。この工程は加圧によるプ
レート化と降圧による反応副生物の除去を繰り返すこと
によって素材の緻密化を図る段階で、平面板の保持温度
が80℃未満であると樹脂成分の軟化が不十分となり、
200℃を上廻ると樹脂の硬化反応が急速に進行し過ぎ
ていずれも円滑なプレート成形が困難となる。加圧・降
圧のサイクルは少なくとも2回、好ましくは3〜5回反
復しておこなう。加圧時の圧力は平面板の温度、一次形
成体の流動性等を考慮して設定されるが、通常10〜2
50kgf/cm2 の範囲内に調整される。降圧の度合は加圧
時の圧力より下げることで足りるが、反応副生物の揮散
を効果的に進行させるためには加圧時の圧力1に対して
降圧時の圧力を0.5以下に調整することが望ましい。
好適な降圧時の圧力は、0kgf/cm2 かそれに近似する範
囲である。The obtained primary compact is placed on a flat plate kept at 80 to 200 ° C., and a cycle of pressurization and pressure reduction is repeated to form a plate. This process is a stage to densify the material by repeating plate formation by pressurization and removal of reaction by-products by pressure reduction. If the holding temperature of the flat plate is less than 80 ° C, the softening of the resin component becomes insufficient,
If the temperature exceeds 200 ° C., the curing reaction of the resin will proceed too rapidly, making smooth plate molding difficult. The pressurization / depressurization cycle is repeated at least twice, preferably 3 to 5 times. The pressure at the time of pressurization is set in consideration of the temperature of the flat plate, the fluidity of the primary forming body, etc., but usually 10 to 2
It is adjusted within the range of 50 kgf / cm 2 . It is sufficient to lower the pressure lower than the pressure applied, but in order to promote the volatilization of reaction by-products, the pressure is adjusted to 1 or less and 0.5 or less. It is desirable to do.
A suitable pressure for pressure reduction is 0 kgf / cm 2 or a range close to it.
【0011】ついで、平面板上のプレートに20〜25
0kgf/cm2 の加圧力を付加しながら硬化する。プレート
は加圧下の硬化により全体の硬化状態が均一化して炭化
時の熱収縮差に起因する歪みの発生がなくなるので、後
工程の焼成炭化時における変形、割れ等の現象を防止す
ることができる。加圧硬化後のプレートは、必要に応じ
て150〜300℃の温度域に加熱して硬化を完結す
る。Then, the plate on the flat plate is placed on the plate 20-25.
It is cured while applying a pressure of 0 kgf / cm 2 . The plate is cured under pressure so that the entire cured state becomes uniform and the strain due to the difference in heat shrinkage during carbonization is eliminated, so that it is possible to prevent the phenomenon such as deformation and cracking during firing and carbonization in the subsequent step. .. The plate after pressure curing is heated to a temperature range of 150 to 300 ° C. as necessary to complete curing.
【0012】上記のプレート成形および硬化処理の工程
は、通常、平面板として熱盤を備えたプレス装置を用い
ておこなわれるが、一次成形体が熱盤に融着する現象を
防止するため、熱盤面に予めシリコーン系またはフッ素
系の離型剤を塗布しておくか、ポリエチレン、ポリプロ
ピレン、ポリフルオロエチレン等からなる離型シートも
しくはこれら樹脂成分を塗布した離型紙を一次成形体と
熱盤の間に敷いておくことが好ましい。また、熱盤には
所定の寸法精度を有するスペーサーを付設しておくと、
プレート厚の精度確保に有効である。The above-mentioned plate molding and hardening treatment steps are usually carried out by using a pressing device having a heating plate as a flat plate. However, in order to prevent the phenomenon that the primary molded body is fused to the heating plate, heat treatment is performed. A silicone or fluorine release agent is applied to the board surface in advance, or a release sheet made of polyethylene, polypropylene, polyfluoroethylene, etc. or release paper coated with these resin components is applied between the primary molding and the hot plate. It is preferable to lay it on. Also, if a spacer with a predetermined dimensional accuracy is attached to the hot platen,
It is effective for ensuring the accuracy of plate thickness.
【0013】硬化が完了したプレート成形体は、非酸化
性雰囲気中で焼成炭化処理を施し樹脂成分をガラス状カ
ーボンに転化させる。焼成炭化温度は、通常、800〜
2000℃であるが、必要により2000℃以上に加熱
して材質を黒鉛化することもできる。処理にはリードハ
ンマー炉、ガス置換炉等を用い、プレート成形体をコー
クス粉のようなパッキング材で被包して酸素を遮断する
か、あるいは炉内を窒素、アルゴン等の不活性ガスで置
換した状態でおこなう。The cured plate molded body is subjected to firing carbonization treatment in a non-oxidizing atmosphere to convert the resin component into glassy carbon. The firing carbonization temperature is usually 800 to
Although the temperature is 2000 ° C., the material can be graphitized by heating to 2000 ° C. or higher if necessary. A lead hammer furnace, gas replacement furnace, etc. are used for the treatment, and the plate molded body is covered with a packing material such as coke powder to block oxygen, or the inside of the furnace is replaced with an inert gas such as nitrogen or argon. It is done in the state where it did.
【0014】[0014]
【作用】本発明のプロセスによれば、まず真空下による
原料成分の混練と一次成形化の工程で原料成分が十分に
混練されると同時に混入する空気や原料中の揮発性ガス
成分が除去され、素材が緻密化する。緻密質の一次成形
体は引き続く平面板上での加圧・降圧サイクルの反復工
程で、加圧により成形体が軟化してプレート状に成形さ
れる。この際、樹脂成分は急速に硬化して多量の水等の
反応副生物を生成し、これが組織を多孔質化させるが、
次の降圧段階で反応副生物は組織内から円滑に揮散除去
される。したがって、加圧・降圧のサイクルを反復する
過程で組織が一層緻密化しながらプレート状に成形され
る。ついで、プレートは加圧下の硬化処理により歪みの
ない均一な硬化状態が得られるから、最終的な焼成炭化
処理において変形や割れ現象を伴うことなく正常な炭素
質プレートが製造される。According to the process of the present invention, first of all, the raw material components are sufficiently kneaded in the steps of kneading the raw material components under vacuum and the primary molding process, and at the same time, air and volatile gas components contained in the raw materials are removed. , The material becomes more compact. The dense primary molded product is formed into a plate by softening the molded product by pressurization in the repeated process of pressurizing and depressurizing cycles on the subsequent flat plate. At this time, the resin component rapidly hardens to generate a large amount of reaction by-products such as water, which makes the tissue porous,
In the next step of reducing the pressure, reaction by-products are smoothly removed from the tissue by volatilization. Therefore, in the process of repeating the pressurization / depressurization cycle, the tissue is further compacted and formed into a plate shape. Then, since the plate is cured under pressure to obtain a uniform cured state without distortion, a normal carbonaceous plate is manufactured without deformation or cracking phenomenon in the final firing carbonization treatment.
【0015】このような各工程の作用が相乗して、従来
技術に比べ簡略化された成形・硬化工程を介して炭素粉
末/ガラス状カーボン複合系の組織を有し、優れた不透
過性、材質強度ならびに耐蝕性を具備する炭素質プレー
トを生産性よく製造することが可能となる。Due to the synergistic effects of the respective steps, the carbon powder / glassy carbon composite structure is formed through the molding / curing process which is simplified as compared with the prior art, and the excellent impermeability, A carbonaceous plate having material strength and corrosion resistance can be manufactured with high productivity.
【0016】[0016]
【実施例】以下、本発明の実施例を比較例と対比して説
明する。EXAMPLES Examples of the present invention will be described below in comparison with comparative examples.
【0017】実施例1〜3 平均粒径12μm の黒鉛微粉末100重量部をプレポリ
マー状態の粉末フェノール樹脂〔住友デュレズ(株)
製、PR311〕60重量部と共にV型混合機を用いて
5分間混合した。この混合物に液状のフェノール樹脂プ
レポリマー〔住友デュレズ(株)製、PR940〕60
重量部を配合し、Z型混練翼を有するニーダーで予備混
練をおこなったのち、これを混練部と成形部が真空脱気
室を介して一体化された構造の混練押出成形装置に投入
して、温度40℃、真空度50Torrの条件で混練押出成
形をおこなって一次成形した。Examples 1 to 3 100 parts by weight of graphite fine powder having an average particle diameter of 12 μm was used as a powdery phenol resin in a prepolymer state [Sumitomo Dures Co., Ltd.].
Manufactured by PR311] and mixed for 5 minutes using a V-type mixer. Liquid phenol resin prepolymer [PR940] manufactured by Sumitomo Dures Co., Ltd. was added to this mixture.
After mixing parts by weight and pre-kneading with a kneader having a Z-type kneading blade, this is put into a kneading extrusion molding device having a structure in which the kneading part and the molding part are integrated via a vacuum deaeration chamber. The mixture was kneaded and extruded under the conditions of a temperature of 40 ° C. and a vacuum degree of 50 Torr for primary molding.
【0018】得られた一次成形体をテフロンシートを敷
いたプレス機の加熱盤(平面板)上に載置し、プランジ
ャーにより加圧・降圧のサイクルを3回反復してプレー
ト化した。ついで、プレートを100kgf/cm2 に加圧し
ながら硬化して縦横850mm、厚さ1mmのプレート成形
体を得た。このプレート成形体を電気乾燥器で180℃
に加熱して硬化を完結したのち、両面を黒鉛板で挟み付
けた状態で電気炉に詰め、周囲をコークス粉で被包して
から20℃/時の昇温速度で1300℃に加熱して焼成
炭化処理を施した。製造された炭素質プレートは、変形
や亀裂が認められない緻密組織を呈するものであった。
この不透過性炭素質プレートの各種特性を測定し、その
結果を混練成形および加圧・降圧サイクルの条件と対比
させて表1に示した。The obtained primary molded body was placed on a heating plate (flat plate) of a press machine on which a Teflon sheet was laid, and a pressurizing / pressurizing cycle was repeated three times by a plunger to form a plate. Then, the plate was cured while being pressurized to 100 kgf / cm 2 to obtain a plate molded body having a length and width of 850 mm and a thickness of 1 mm. This plate molded body is heated at 180 ° C with an electric dryer.
After heating to complete the curing, put it in an electric furnace with both sides sandwiched by graphite plates, wrap the surrounding area with coke powder, and heat to 1300 ° C at a heating rate of 20 ° C / hour. A firing carbonization process was performed. The produced carbonaceous plate had a dense structure with no deformation or cracks.
Various properties of this impermeable carbonaceous plate were measured, and the results are shown in Table 1 in comparison with the conditions of kneading molding and pressurization / pressurization cycle.
【0019】比較例1 混練成形を常圧でおこない、加圧・降圧のサイクル条件
を加圧時の圧力80kgf/cm2 、降圧時の圧力40kgf/cm
2 としたほかは、実施例と同一条件により炭素質プレー
トを製造した。得られた炭素質プレートの外観は表面組
織が粗いものであった。その各種特性を製造条件と対比
させて表1に併載した。Comparative Example 1 Kneading and molding were carried out under normal pressure, and the pressurization / reduction cycle conditions were 80 kgf / cm 2 when pressure was applied and 40 kgf / cm when pressure was decreased.
A carbonaceous plate was produced under the same conditions as in Example except that the number was changed to 2. The obtained carbonaceous plate had a rough surface structure. The various characteristics are also listed in Table 1 in comparison with the manufacturing conditions.
【0020】比較例2 実施例と同一の条件で真空下で混練成形した一次焼成体
を加圧・降圧サイクル処理を施さずに、直接に100kg
f/cm2 で加圧しながら硬化し、その後の条件は実施例と
同様にして炭素質プレートを製造した。得られた炭素質
プレートの組織には無数の孔が存在していることが認め
られた。その各種特性を製造条件と対比させて表1に併
載した。Comparative Example 2 A primary fired body, which was kneaded and molded under vacuum under the same conditions as in Example, was directly subjected to a pressure / pressure reduction cycle treatment of 100 kg.
A carbonaceous plate was manufactured by curing under pressure of f / cm 2 under the same conditions as in Example. It was confirmed that the texture of the obtained carbonaceous plate had numerous holes. The various characteristics are also listed in Table 1 in comparison with the manufacturing conditions.
【0021】[0021]
【表1】 [Table 1]
【0022】表1の結果から、本発明の要件を満たす実
施例では高密度で強度、ガス不透過性に優れ、電気抵抗
の低い特性の炭素質プレートが得られることが認められ
る。特に加圧・降圧サイクル時の降圧圧力が0kg/cm2の
条件において良好な結果が得られた。これに対し、混練
成形工程を常圧下でおこなった比較例1および成形・硬
化工程に加圧・降圧サイクルを適用しない比較例2で
は、いずれも大幅に特性が低下した。From the results shown in Table 1, it is recognized that in the examples satisfying the requirements of the present invention, a carbonaceous plate having high density, excellent strength, gas impermeability and low electric resistance can be obtained. Particularly, good results were obtained under the condition that the pressure reduction pressure during the pressure / pressure reduction cycle was 0 kg / cm 2 . On the other hand, in Comparative Example 1 in which the kneading / molding step was performed under normal pressure and Comparative Example 2 in which the pressurizing / decreasing cycle was not applied to the molding / curing step, the characteristics were significantly deteriorated.
【0023】[0023]
【発明の効果】以上のとおり、本発明に従えば従来技術
に比べて簡略化された製造工程により組織が緻密で、高
強度、高耐蝕性、低電気抵抗の特性を備える優れた品質
の不透過性炭素質プレートを製造することができる。し
たがって、燃料電池や塩素−亜鉛系二次電池用のセパレ
ータ部材をはじめ、組織の緻密性と不透過性能が要求さ
れる各種の炭素部材の製造技術として有用である。As described above, according to the present invention, due to the manufacturing process simplified as compared with the prior art, the structure is dense, high strength, high corrosion resistance, low electrical resistance and excellent quality are obtained. A permeable carbonaceous plate can be manufactured. Therefore, it is useful as a manufacturing technique for various carbon members such as separator members for fuel cells and chlorine-zinc based secondary batteries, which are required to have a dense structure and impermeability.
Claims (2)
原料成分を真空下で混練処理して一次成形し、一次成形
体を80〜200℃に保持された平面板に載置して加圧
・降圧のサイクルを反復してプレート化し、ついで20
〜250kgf/cm2 の加圧下でプレートを硬化させたの
ち、非酸化性雰囲気中で焼成炭化処理を施すことを特徴
とする不透過性炭素質プレートの製造方法。1. A raw material component mainly composed of carbonaceous powder and a thermosetting resin is kneaded in a vacuum for primary molding, and the primary molded body is placed on a flat plate kept at 80 to 200 ° C. Repeated pressurization and depressurization cycle to plate, then 20
A method for producing an impermeable carbonaceous plate, which comprises curing the plate under a pressure of ˜250 kgf / cm 2 , and then subjecting the plate to firing carbonization in a non-oxidizing atmosphere.
を、加圧時の圧力1に対して降圧時の圧力を0.5以下
に設定する請求項1記載の不透過性炭素質プレートの製
造方法。2. The impermeable carbonaceous plate according to claim 1, wherein the pressure ratio during the pressurization / reducing cycle is set such that the pressure during depressurization is 0.5 or less with respect to the pressure during pressurization of 1. Production method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14316592A JP3342508B2 (en) | 1992-05-07 | 1992-05-07 | Method for producing impermeable carbonaceous plate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14316592A JP3342508B2 (en) | 1992-05-07 | 1992-05-07 | Method for producing impermeable carbonaceous plate |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH05310471A true JPH05310471A (en) | 1993-11-22 |
JP3342508B2 JP3342508B2 (en) | 2002-11-11 |
Family
ID=15332430
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14316592A Expired - Lifetime JP3342508B2 (en) | 1992-05-07 | 1992-05-07 | Method for producing impermeable carbonaceous plate |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3342508B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008127476A (en) * | 2006-11-21 | 2008-06-05 | Lignyte Co Ltd | Carbon/phenolic resin composite material production method, carbon/phenolic resin composite material, carbon/phenolic resin composite-carbonized material, fuel cell separator, electroconductive resin composition, secondary battery electrode, electrically double-layer capacitor |
-
1992
- 1992-05-07 JP JP14316592A patent/JP3342508B2/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008127476A (en) * | 2006-11-21 | 2008-06-05 | Lignyte Co Ltd | Carbon/phenolic resin composite material production method, carbon/phenolic resin composite material, carbon/phenolic resin composite-carbonized material, fuel cell separator, electroconductive resin composition, secondary battery electrode, electrically double-layer capacitor |
Also Published As
Publication number | Publication date |
---|---|
JP3342508B2 (en) | 2002-11-11 |
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