JPH01264917A - Production of impermeable carbon material - Google Patents
Production of impermeable carbon materialInfo
- Publication number
- JPH01264917A JPH01264917A JP63092532A JP9253288A JPH01264917A JP H01264917 A JPH01264917 A JP H01264917A JP 63092532 A JP63092532 A JP 63092532A JP 9253288 A JP9253288 A JP 9253288A JP H01264917 A JPH01264917 A JP H01264917A
- Authority
- JP
- Japan
- Prior art keywords
- mesophase
- resin
- weight
- powder
- thermosetting resin
- 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
- 239000003575 carbonaceous material Substances 0.000 title claims abstract description 25
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- 239000000843 powder Substances 0.000 claims abstract description 32
- 229920005989 resin Polymers 0.000 claims abstract description 30
- 239000011347 resin Substances 0.000 claims abstract description 30
- 239000000835 fiber Substances 0.000 claims abstract description 29
- 229920001187 thermosetting polymer Polymers 0.000 claims abstract description 23
- 239000000203 mixture Substances 0.000 claims abstract description 14
- 239000012298 atmosphere Substances 0.000 claims abstract description 4
- 238000010304 firing Methods 0.000 claims description 11
- 238000000465 moulding Methods 0.000 claims description 4
- 230000001590 oxidative effect Effects 0.000 claims description 3
- 238000003763 carbonization Methods 0.000 abstract description 15
- 239000005011 phenolic resin Substances 0.000 abstract description 8
- 239000000126 substance Substances 0.000 abstract description 5
- 239000007849 furan resin Substances 0.000 abstract description 4
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 abstract description 3
- 239000011300 coal pitch Substances 0.000 abstract description 3
- 239000011301 petroleum pitch Substances 0.000 abstract description 3
- 229920001568 phenolic resin Polymers 0.000 abstract description 3
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 abstract description 2
- 239000003822 epoxy resin Substances 0.000 abstract description 2
- 229920000647 polyepoxide Polymers 0.000 abstract description 2
- 239000008096 xylene Substances 0.000 abstract description 2
- 238000001354 calcination Methods 0.000 abstract 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 38
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 19
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 17
- 229910052799 carbon Inorganic materials 0.000 description 12
- 239000000463 material Substances 0.000 description 11
- 238000002156 mixing Methods 0.000 description 11
- 239000007789 gas Substances 0.000 description 8
- 230000000704 physical effect Effects 0.000 description 8
- 239000000446 fuel Substances 0.000 description 7
- 239000002245 particle Substances 0.000 description 7
- 239000002994 raw material Substances 0.000 description 7
- 239000011159 matrix material Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 229920002239 polyacrylonitrile Polymers 0.000 description 4
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 239000004005 microsphere Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 229910003481 amorphous carbon Inorganic materials 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 229920003986 novolac Polymers 0.000 description 2
- 239000011295 pitch Substances 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 230000004580 weight loss Effects 0.000 description 2
- 229920003043 Cellulose fiber Polymers 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 239000012300 argon atmosphere Substances 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000007833 carbon precursor Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 229910003460 diamond Inorganic materials 0.000 description 1
- 239000010432 diamond Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- HDNHWROHHSBKJG-UHFFFAOYSA-N formaldehyde;furan-2-ylmethanol Chemical compound O=C.OCC1=CC=CO1 HDNHWROHHSBKJG-UHFFFAOYSA-N 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 229910021397 glassy carbon Inorganic materials 0.000 description 1
- 238000005087 graphitization Methods 0.000 description 1
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 150000001247 metal acetylides Chemical class 0.000 description 1
- 239000012778 molding material Substances 0.000 description 1
- 229910021382 natural graphite Inorganic materials 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000011417 postcuring Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 239000002470 thermal conductor Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/71—Ceramic products containing macroscopic reinforcing agents
- C04B35/78—Ceramic products containing macroscopic reinforcing agents containing non-metallic materials
- C04B35/80—Fibres, filaments, whiskers, platelets, or the like
- C04B35/83—Carbon fibres in a carbon matrix
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Composite Materials (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Carbon And Carbon Compounds (AREA)
- Ceramic Products (AREA)
Abstract
Description
【発明の詳細な説明】
〈産業上の利用分野〉
この発明は、熱伝導性、電気伝導性及び耐薬品性に優れ
ると共に、高い機械的強度を備えたガス不浸透性炭素材
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 method for producing a gas-impermeable carbon material having excellent thermal conductivity, electrical conductivity, and chemical resistance as well as high mechanical strength. It is something.
〈従来技術とその課題〉
近年、軽量である上、寸法安定性、耐熱性、電気伝導性
、熱伝導性並びに耐薬品性に優れた素材として炭素成形
材が注目されるようになり、半導体製造の治工具、原子
炉材或いは電極等、多方面の分野においてその利用が推
進されている。<Prior art and its challenges> In recent years, carbon molding materials have attracted attention as materials that are lightweight, and have excellent dimensional stability, heat resistance, electrical conductivity, thermal conductivity, and chemical resistance, and are used in semiconductor manufacturing. Its use is being promoted in many fields such as jigs and tools, nuclear reactor materials, and electrodes.
中でも、特に“ガス不浸透性炭素材”は、ガスの透過遮
断物性のほか、低電気抵抗や良好な耐薬品性を示すこと
から、“リン酸型燃料電池の分離板”としての適用が注
目を集めている。なぜなら、リン酸型燃料電池の分離板
は、燃料として供給される水素と燃料用の空気との仕切
りの役目を果たすものであることから両者の混和を防止
する機能が必要であり、また、発生した電気や熱の良導
体であることや、更には約200℃のリン酸に対する優
れた耐触性が要求されていたが、ガス不浸透性炭素材の
有する物性はこれらの要求特性に極めて近いものだった
からである。Among these, "gas-impermeable carbon materials" in particular are attracting attention for their application as "separator plates for phosphoric acid fuel cells" because they exhibit low electrical resistance and good chemical resistance in addition to gas permeation blocking physical properties. are collecting. This is because the separator plate in a phosphoric acid fuel cell serves as a partition between the hydrogen supplied as fuel and the fuel air, so it must have a function to prevent the two from mixing. Gas-impermeable carbon materials were required to be good conductors of electricity and heat, and to have excellent resistance to phosphoric acid at temperatures of about 200°C, but the physical properties of gas-impermeable carbon materials are extremely close to meeting these requirements. Because it was.
それ故、これまでにも“リン酸型燃料電池の分離板”等
としても十分に満足できる特性を備えたガス不浸透性炭
素材を実現すべく様々な提案がなされてきた。Therefore, various proposals have been made to realize gas-impermeable carbon materials with sufficiently satisfactory characteristics as "separation plates for phosphoric acid fuel cells" and the like.
例えば、特公昭56−22836号公報には、硬化し得
る樹脂(熱硬化性樹脂)と硬化フェノール樹脂繊維との
混和物を成形・硬化した後、これを800℃以上の温度
で焼成して成る炭素材が示されている。ところが、該公
報に示された炭素材は、無定形炭素質であるので黒鉛質
の炭素材に比べ電気や熱の伝導性や耐リン酸性に劣ると
いう問題点に加えて、機械加工性(例えばリブ付の分離
板に加工する場合の溝の加工性)の点で十分に満足でき
るものではなかった。For example, Japanese Patent Publication No. 56-22836 discloses that after molding and curing a mixture of a curable resin (thermosetting resin) and cured phenol resin fibers, the mixture is fired at a temperature of 800°C or higher. Carbon material is shown. However, since the carbon material disclosed in the publication is an amorphous carbonaceous material, it has problems such as inferior electrical and thermal conductivity and phosphoric acid resistance compared to graphite carbonaceous materials, as well as poor machinability (e.g. The workability of the grooves when processing into a ribbed separation plate was not fully satisfactory.
そこで、上記の電気伝導性、熱伝導性、耐リン酸性並び
に機械加工性を改善した炭素材として、熱硬化性樹脂に
黒鉛粉を混合した原料を焼成したものが提案された(特
開昭57−72273号、特開昭59−195514号
、特開昭59−232906号等)。Therefore, as a carbon material with improved electrical conductivity, thermal conductivity, phosphoric acid resistance, and machinability, a material prepared by firing a raw material of thermosetting resin mixed with graphite powder was proposed (Japanese Unexamined Patent Application Publication No. 57-197). -72273, JP-A-59-195514, JP-A-59-232906, etc.).
しかしながら、これらの炭素材は、無定形炭素質(所謂
“グラッシーカーボン質”)のマトリックス中に電気や
熱の良導体でかつ耐リン酸性や機械加工性の良好な黒鉛
質粉末が分散したものであることから、確かに無定形炭
素質単独の場合に比べて電気伝導性、熱伝導性、耐リン
酸性及び機械加工性に優れた特性を有してはいたが、一
方で、熱硬化性樹脂を原料とした上記炭素材は、その炭
化焼成過程において「熱硬化性樹脂が著しく収縮するの
に対して黒鉛は全く収縮せず、そのため収縮率の差に起
因して両者の界面に亀裂が発生するのを防止できない」
との問題を抱えるものであり、従ってガス不浸透性に対
する信頼性が乏しいのを否めなかった。However, these carbon materials are made by dispersing graphite powder, which is a good electrical and thermal conductor and has good phosphoric acid resistance and machinability, in a matrix of amorphous carbon (so-called "glassy carbon"). Therefore, it certainly had better electrical conductivity, thermal conductivity, phosphoric acid resistance, and machinability than amorphous carbon alone, but on the other hand, thermosetting resin During the carbonization and firing process of the above-mentioned carbon material used as a raw material, ``thermosetting resin shrinks significantly, but graphite does not shrink at all, and as a result, cracks occur at the interface between the two due to the difference in shrinkage rate.'''cannot be prevented'
Therefore, it was undeniable that the reliability of gas impermeability was poor.
〈課題を解決するための手段〉
本発明者等は、上述のような観点から、ガス遮断性に優
れることは勿論、申し分のない電気伝導性、熱伝導性、
耐リン酸性並びに機械加工性を備え、リン酸型燃料電池
の分離板に適用しても十分に満足できる不浸透性炭素材
を提供すべく研究を行ったところ、[易黒鉛化物質であ
るメソフェーズ小球体やメソフェーズ粉は、その炭化焼
成の過程で収縮する」点に強い関心が向くこととなり、
「炭化焼成の過程で著しい収縮を見せる熱硬化性樹脂に
メソフェーズ小球体又はメソフェーズ粉を混合した場合
には、該メソフェーズ小球体又はメソフェーズ粉が熱硬
化性樹脂と同じく炭化焼成の際に収縮することから、マ
トリックスの熱硬化性樹脂との界面に収縮率差に基づく
亀裂の生成が抑制されるはずである」との推測の下に、
熱硬化性樹脂とメソフェーズ小球体又はメソフェーズ粉
との混合物を出発物質とする炭素材について更に研究を
重ねた結果、[該混合物を炭化焼成したものは、“メソ
フェーズ小球体又はメソフェーズ粉由来の炭化物”と“
熱硬化性物質由来の炭化物”の両者の界面に亀裂が認め
られず、不浸透性に優れた炭素材となっている上、電気
伝導性、熱伝導性。<Means for Solving the Problems> From the above-mentioned viewpoints, the present inventors have developed a technology that not only has excellent gas barrier properties but also has impeccable electrical conductivity, thermal conductivity,
We conducted research to provide an impermeable carbon material that has phosphoric acid resistance and machinability and can be used as a separator plate in phosphoric acid fuel cells. There was a strong interest in the fact that small spheres and mesophase powders contract during the carbonization and firing process.
``If mesophase small spheres or mesophase powder are mixed with a thermosetting resin that shows significant shrinkage during carbonization and firing, the mesophase small spheres or mesophase powder will shrink during carbonization and firing in the same way as the thermosetting resin. Based on this assumption, the formation of cracks due to the difference in shrinkage rate at the interface with the matrix thermosetting resin should be suppressed.
As a result of further research on carbon materials that use a mixture of thermosetting resin and mesophase spherules or mesophase powder as a starting material, we found that [the mixture obtained by carbonization and firing is "carbide derived from mesophase spherules or mesophase powder"] and"
There are no cracks at the interface between the two carbides derived from thermosetting substances, making it a carbon material with excellent impermeability, as well as electrical and thermal conductivity.
耐リン酸性並びに機械加工性の面でも十分に満足できる
ものであり、更に、これに熱硬化性樹脂と同程度の炭化
収縮率を有する不融化繊維を混合すると、上記好ましい
特性がそのまま維持された上で機械的強度が一段と向上
するようになる」との知見を得るに至ったのである。It was fully satisfactory in terms of phosphoric acid resistance and machinability, and furthermore, when infusible fibers having a carbonization shrinkage rate comparable to that of the thermosetting resin were mixed, the above-mentioned favorable characteristics were maintained. This led to the discovery that the mechanical strength of the material is further improved.
この発明は、上記知見に基づいてなされたものであり、
「メソフェーズ小球体又はメソフェーズ粉:5〜70M
量%、熱硬化性梼脂:10〜60重量%及び不融化繊維
:3〜60重量%の混合物を成形した後、その成形物を
非酸化性雰囲気下で焼成することにより、優れたガス遮
蔽性、電気伝導性、熱伝導性、耐リン酸性並びに機械加
工性を兼備し、しかも高い強度を示す不浸透性炭素材を
安定製造し得るようにした点」を特徴としている。This invention was made based on the above findings,
"Mesophase spherules or mesophase powder: 5-70M
After molding a mixture of thermosetting resin: 10 to 60% by weight and infusible fiber: 3 to 60% by weight, the molded product is fired in a non-oxidizing atmosphere to provide excellent gas shielding. It is characterized by the ability to stably produce an impermeable carbon material that exhibits high strength, electrical conductivity, thermal conductivity, phosphoric acid resistance, and machinability.
本発明において対象とする熱硬化性樹脂は、炭化焼成す
ることによって炭化物を与えることができる樹脂であり
、例えばフェノール樹脂、フラン樹脂、キシレン樹脂、
エポキシ樹脂等を挙げることができるが、炭化収率の高
いフェノール樹脂やフラン樹脂が好ましく、できれば5
0重量%以上の炭化収率のものを選ぶのが良い。このよ
うな樹脂が出発原料であれば、十分に優れた不浸透性の
炭素材が得られる。Thermosetting resins targeted in the present invention are resins that can be carbonized to provide a carbide by carbonization firing, such as phenol resins, furan resins, xylene resins,
Examples include epoxy resins, but phenol resins and furan resins with high carbonization yields are preferred, preferably 5
It is better to choose one with a carbonization yield of 0% by weight or more. If such a resin is used as a starting material, a sufficiently excellent impermeable carbon material can be obtained.
また、メソフェーズ粉は、石油系或いは石炭系等の何れ
のピッチから製造したものでも良い。ただ、耐リン酸腐
食性や電池反応の安定性の面から不純物の少ない炭素材
が要求されるので、石炭系メソフェーズ粉の場合にはメ
ソフェーズ製造川原料は精製しておいた方が好ましい。Further, the mesophase powder may be produced from any petroleum-based or coal-based pitch. However, from the viewpoint of phosphoric acid corrosion resistance and stability of battery reactions, a carbon material with few impurities is required, so in the case of coal-based mesophase powder, it is preferable to refine the mesophase production raw material.
通常、石油系または石炭系の重質油或いはピッチを35
0〜500℃で熱処理すると、熱処理の初期には球晶と
称する光学的に異方性の球体がピンチの母相中に生成し
、更に熱処理を続けて行くと球晶が合体・成長を繰り返
してピッチ全体が光学的に異方性の物質、所謂“バルク
メソフェーズ”となる。上記の球晶やバルクメソフェー
ズは、熱処理条件によっても異なるが、−船釣には軟化
点を示さない。つまり、不融性というコークス的な性質
がある反面、揮発分を数重量%含有するというピッチ的
な性質をも併せ持つ炭素前駆体である。Usually petroleum or coal based heavy oil or pitch
When heat treated at 0 to 500℃, optically anisotropic spheres called spherulites are generated in the pinch matrix at the beginning of the heat treatment, and as the heat treatment continues, the spherulites repeatedly coalesce and grow. The entire pitch becomes an optically anisotropic material, the so-called "bulk mesophase." The above-mentioned spherulites and bulk mesophases differ depending on the heat treatment conditions, but - they do not show a softening point in boat fishing. In other words, it is a carbon precursor that has coke-like properties of being infusible, but also pitch-like properties of containing several percent by weight of volatile matter.
本発明で対象とするメソフェーズ小球体とは前記“球晶
゛であり、メソフェーズ粉とは前記“バルクメソフェー
ズを粉砕したちの”である。The mesophase microspheres targeted by the present invention are the above-mentioned "spherulites", and the mesophase powder is the above-mentioned "pulverized bulk mesophase".
そして、例えば「炭素含有率が92重量%以上であり、
900℃までの揮発分が7〜20重量%。For example, "the carbon content is 92% by weight or more,
Volatile content up to 900°C is 7-20% by weight.
500℃まで加熱した時の線収縮率が1%以上で、その
平均粒子径が40μm以下のメソフェーズ小球体」或い
は「上記メソフェーズ小球体と同一の性状を有するバル
クメソフェーズを平均粒径4゜μm以下に粉砕したメソ
フェーズ粉」が好ましい対象となる。"Mesophase microspheres with a linear shrinkage rate of 1% or more when heated to 500°C and an average particle size of 40 μm or less" or "Bulk mesophase having the same properties as the above mesophase microspheres with an average particle size of 4 μm or less" The preferred target is ``mesophase powder that has been ground into
ここで、炭素含有率が92%未満の場合は、炭素以外の
元素が焼成過程で分解・ガス化して重量減少量が増加す
ると共に、炭素以外の原子が黒鉛化性を阻害し、熱伝導
性、電気伝導性、耐リン酸性が向上しない恐れがある。If the carbon content is less than 92%, elements other than carbon will decompose and gasify during the firing process, resulting in increased weight loss, and atoms other than carbon will inhibit graphitization, resulting in poor thermal conductivity. , electrical conductivity and phosphoric acid resistance may not improve.
また、900℃までの揮発分が7重量%未満であると焼
成過程でマトリックスの熱硬化性樹脂との濡れ性が悪く
、メソフェーズ小球体又はメソフェーズ粉とマトリック
スとの界面に隙間(クランク)が発生し不浸透性の低下
を招く恐れがあり、一方、13重量%を超えると、メソ
フェーズ小球体又はメソフェーズ粉内部から多量に発生
する揮発分により発泡乃至は多孔体となって不浸透性が
低下する点が懸念されるようになる。In addition, if the volatile content up to 900°C is less than 7% by weight, wettability with the thermosetting resin of the matrix will be poor during the firing process, and a gap (crank) will occur at the interface between the mesophase spherules or mesophase powder and the matrix. On the other hand, if it exceeds 13% by weight, a large amount of volatile matter generated from inside the mesophase spherules or mesophase powder will result in a foamed or porous body, resulting in a decrease in impermeability. This is becoming a concern.
そして、500“Cまでに加熱した時の線収縮率とは、
メソフェーズ小球体又はメソフェーズ粉単独を2t/c
II1以上の圧力で加圧成形し、得られた成形体から試
片を採取して測定した値である。この線収縮率が1%未
満の場合には、炭化・焼成後のメソフェーズ小球体或い
はメソフェーズ粉由来の炭素粒子と熱硬化性樹脂由来の
マトリックス炭素との界面に隙間が発生し不浸透性が低
下しがちとなるので好ましくない。And what is the linear shrinkage rate when heated to 500"C?
2t/c of mesophase small spheres or mesophase powder alone
This is a value measured by taking a sample from the molded product obtained by pressure molding at a pressure of II1 or higher. If this linear shrinkage rate is less than 1%, a gap will occur at the interface between the carbon particles derived from the mesophase small spheres or mesophase powder after carbonization and firing and the matrix carbon derived from the thermosetting resin, resulting in a decrease in impermeability. This is not desirable because it tends to occur.
本発明が対象とする不融化繊維は、石油系及び石炭系の
ピッチ繊維、ポリアクリロニトリル(PAN)繊維、セ
ルロース繊維、フェノール樹脂繊維等の有機繊維を不融
化処理した繊維である。不融化処理の方法としては、有
機繊維の種類によっても異なるが、通常、200〜40
0℃の温度で空気酸化させる方法が採用される。The infusible fibers targeted by the present invention are fibers obtained by infusible treatment of organic fibers such as petroleum-based and coal-based pitch fibers, polyacrylonitrile (PAN) fibers, cellulose fibers, and phenol resin fibers. The method of infusibility treatment varies depending on the type of organic fiber, but usually 200 to 40
A method of air oxidation at a temperature of 0° C. is adopted.
なお、これらの不融化繊維は、長さ0.5〜10鶴の短
繊維、不織布、マット クロス等の何れの形態であって
も差し支えない。Note that these infusible fibers may be in any form such as short fibers with a length of 0.5 to 10 mm, nonwoven fabric, mat cloth, etc.
次に、かかる性状を有するメソフェーズ小球体又はメソ
フェーズ粉、熱硬化性樹脂、及び不融化繊維を用いた不
浸透性炭素材の製造条件について説明する。Next, conditions for manufacturing an impermeable carbon material using mesophase small spheres or mesophase powder having such properties, a thermosetting resin, and infusible fibers will be explained.
メソフェーズ小球体又はメソフェーズ粉は、熱硬化性樹
脂及び不融化繊維との混合物に対して5〜70重量%の
範囲の割合になるように配合される。この配合割合が5
重量%未満の場合には、メソフェーズ小球体又はメソフ
ェーズ粉の配合効果が得られず、熱伝導性、電気伝導性
、耐リン酸性並びに機械加工性が低下する。一方、70
重量%を超えて配合すると、メソフェーズ小球体又はメ
ソフェーズ粉の表面積が増えて、熱硬化性樹脂により均
一にメソフェーズ小球体又はメソフェーズ粉を結着でき
なくなって強度低下を招く。The mesophase spherules or mesophase powder are blended in a proportion ranging from 5 to 70% by weight with respect to the mixture with the thermosetting resin and infusible fiber. This blending ratio is 5
When the amount is less than % by weight, the effect of blending the mesophase spherules or mesophase powder cannot be obtained, and thermal conductivity, electrical conductivity, phosphoric acid resistance, and machinability deteriorate. On the other hand, 70
If the amount exceeds % by weight, the surface area of the mesophase spherules or mesophase powder will increase, and the thermosetting resin will not be able to bind the mesophase spherules or mesophase powder uniformly, resulting in a decrease in strength.
また、不融化繊維は、メソフェーズ小球体又はメソフェ
ーズ粉と熱硬化性樹脂との混合物に対して3〜60重量
%の範囲となるように配合される。Further, the infusible fiber is blended in an amount of 3 to 60% by weight with respect to the mixture of mesophase spherules or mesophase powder and thermosetting resin.
なぜなら、この配合割合が3重量%未満の場合には不融
化繊維の配合効果が得られないので十分な強度を確保で
きず、一方、60重量%を超えて配合すると、メソフェ
ーズ小球体又はメソフェーズ粉の配合割合にもよるが、
不融化繊維の表面積が増大して熱硬化性樹脂により均一
に不融化繊維を結着できなくなって、やはり強度低下を
招く。This is because if the blending ratio is less than 3% by weight, the blending effect of infusible fibers cannot be obtained and sufficient strength cannot be secured, whereas if the blending ratio exceeds 60% by weight, mesophase spherules or mesophase powder It depends on the blending ratio of
The surface area of the infusible fibers increases, making it impossible to bind the infusible fibers uniformly with the thermosetting resin, which also results in a decrease in strength.
上記素材原料から不浸透性炭素材を製造するには、まず
、前述の如くに配合した素材原料混合物を金型に仕込み
、通常は130〜200℃の温度下で5〜150 kg
/cm”の圧力を負荷して加圧成形する。次いで、この
成形体を必要に応じて130〜200℃で10〜30時
間加熱することによって“後硬化”させる。後硬化した
成形体は、非酸化性雰囲気(例えばN2ガスや計ガスの
流通下)で昇温速度二0.5〜50℃/hrにて少なく
とも800℃まで炭化焼成し、必要に応じて更に黒鉛化
して不浸透性炭素材とされる。In order to produce an impermeable carbon material from the above-mentioned raw materials, first, the raw material mixture blended as described above is charged into a mold, and 5-150 kg of the raw material mixture is usually placed at a temperature of 130-200°C.
The molded product is then pressure-molded by applying a pressure of 1.5 cm/cm. The molded product is then “post-cured” by heating at 130 to 200°C for 10 to 30 hours as necessary.The post-cured molded product is Carbonization is carried out in a non-oxidizing atmosphere (for example, under the flow of N2 gas or gauge gas) at a heating rate of 20.5 to 50°C/hr to at least 800°C, and if necessary, further graphitized to form impermeable carbon. It is considered as a material.
以下、実施例によってこの発明を更に具体的に説明する
。Hereinafter, the present invention will be explained in more detail with reference to Examples.
〈実施例〉
実施例 1
炭素含有率: 93.3重量%、900℃までの揮発分
: 10.3重量%、500℃までの線収縮率が3%で
平均粒子径が15μmのメソフェーズ粉、 1000°
Cにおける炭化収率が52重四%のフェノール・ノボラ
ック樹脂粉末、及びPANの不融化短繊維(長さ111
)を第1表に示す配合割合で混合した後(第1表ではメ
ソフェーズ粉と不融化繊維の配合割合のみを示したが、
残部は配合熱硬化性樹脂である)、lmX1mの平面積
を持つ金型に仕込み、温度:180℃、圧カニ 80
kg/cm2で30分間加熱・加圧成形して厚さl m
mの成形体を得、次いでこの成形体を20時間かけて2
00℃まで昇温してから、200℃で20時間保持して
“後硬化”させた。<Examples> Example 1 Mesophase powder with carbon content: 93.3% by weight, volatile content up to 900°C: 10.3% by weight, linear shrinkage rate up to 500°C of 3%, and average particle size of 15 μm. 1000°
Phenol/novolac resin powder with a carbonization yield of 52x4% in C and infusible short fibers of PAN (length 111
) at the blending ratio shown in Table 1 (Table 1 only shows the blending ratio of mesophase powder and infusible fiber,
The remainder is a blended thermosetting resin), placed in a mold with a planar area of 1m x 1m, temperature: 180°C, pressure crab 80
Heated and pressure molded at kg/cm2 for 30 minutes to a thickness of lm.
A molded body of m is obtained, and then this molded body is heated for 20 hours.
After raising the temperature to 00°C, it was held at 200°C for 20 hours for "post-curing".
次に、後硬化させた成形体を“粉コークスを詰めた容器
”内にて 4℃/hrの速度で1000℃まで昇温しで
炭化した後、アルゴン雰囲気中で4℃/minの速度で
2500°Cまで昇温し、厚さ0.8鶴の黒鉛化物を得
た。Next, the post-cured compact was carbonized by raising the temperature to 1000°C at a rate of 4°C/hr in a “vessel filled with coke powder”, and then carbonized at a rate of 4°C/min in an argon atmosphere. The temperature was raised to 2500°C to obtain a graphitized material with a thickness of 0.8 mm.
得られた黒鉛化物の物性を測定したが、この結果を第1
表に示す。The physical properties of the obtained graphitized material were measured, and these results were used in the first
Shown in the table.
なお、第1表における「通気度」は、差圧1 kg/c
m2のN2ガスの通過量を室温にて測定することによっ
て求めた。Note that "air permeability" in Table 1 is based on a differential pressure of 1 kg/c.
It was determined by measuring the amount of N2 gas passing through m2 at room temperature.
また、「耐リン酸性」は、200℃の100%リン酸液
に1000時間浸漬した後の初期重量に対する重量減量
率である。Moreover, "phosphoric acid resistance" is the weight loss rate with respect to the initial weight after being immersed in a 100% phosphoric acid solution at 200° C. for 1000 hours.
機械加工性は、直径200mm、J!J−さ2鶴のダイ
ヤモンドブレードを243Orpmの速度で回転し、黒
鉛化物を111m1nの送り速度で移動させて切断加工
を行い、このときの黒鉛化物のワレ発生の有無から判定
した。Machinability is 200mm in diameter, J! Cutting was performed by rotating a J-Sa2 Tsuru diamond blade at a speed of 243 rpm and moving the graphitized material at a feed rate of 111 m1n, and judgment was made based on the presence or absence of cracking of the graphitized material at this time.
実施例 2
炭素含有率: 92.8重量%、900℃までの揮発分
712.0重量%、500゛cまでの線収縮率が5%で
、平均粒子径が30μmのメソフェーズ小球体をメソフ
ェーズ粉の代わりに用い、硬化フェノール樹脂繊維の1
011長のチョップをPAN不融化繊維の代わりに用い
た以外は、実施例1と全く同じ方法で黒鉛化物を得た。Example 2 Mesophase spherules with a carbon content of 92.8% by weight, a volatile content of 712.0% by weight up to 900°C, a linear shrinkage rate of 5% up to 500°C, and an average particle size of 30 μm were made into mesophase powder. 1 of the cured phenolic resin fiber.
A graphitized material was obtained in exactly the same manner as in Example 1, except that a 011-length chopped fiber was used instead of the PAN infusible fiber.
得られた黒鉛化物の物性を測定し、その結果を同じく第
1表に示す。The physical properties of the obtained graphitized product were measured, and the results are also shown in Table 1.
実施例 3
炭素含有率: 93.3重量%、900℃までの揮発分
:9.8重量%、500’Cまでの線収縮率が2%で平
均粒子径が30μmのメソフェーズ粉:50重量部に、
フェノール・ノゾール樹脂液:25重量部とLoamの
長さのピンチ繊維の不融化繊維:25重量部を混練した
後、80℃で10分間乾燥した。Example 3 Mesophase powder with carbon content: 93.3% by weight, volatile content up to 900°C: 9.8% by weight, linear shrinkage rate up to 500°C of 2% and average particle size of 30 μm: 50 parts by weight To,
After kneading 25 parts by weight of the phenol/nozole resin liquid and 25 parts by weight of the infusible pinched fibers having a loam length, the mixture was dried at 80° C. for 10 minutes.
そして、このようにして得られた乾燥粉末を出発混合物
とした以外は、実施例1と同じ方法で黒鉛化物を製造し
た。A graphitized product was produced in the same manner as in Example 1, except that the dry powder thus obtained was used as the starting mixture.
得られた黒鉛化物の物性を測定し、その結果を同じく第
1表に示す。The physical properties of the obtained graphitized product were measured, and the results are also shown in Table 1.
比較例 1
固定炭素: 97.0重量%、灰分:2重量%、揮発分
:1重量%で、平均粒径:10μmの天然黒鉛をメソフ
ェーズ粉の代わりに用いた以外は、実施例1と全く同じ
方法で黒鉛化物を製造した。Comparative Example 1 Completely the same as Example 1 except that fixed carbon: 97.0% by weight, ash content: 2% by weight, volatile content: 1% by weight, and natural graphite with an average particle size of 10 μm was used instead of mesophase powder. A graphitized product was produced in the same manner.
得られた黒鉛化物の物性を測定し、その結果を同じく第
1表に示す。The physical properties of the obtained graphitized product were measured, and the results are also shown in Table 1.
比較例 2
実施例1で用いたのと同一の原料を用い、配合割合のみ
を変えて、実施例1と同じ方法で黒鉛化物を製造した。Comparative Example 2 A graphitized product was produced in the same manner as in Example 1, using the same raw materials as in Example 1 and changing only the blending ratio.
得られた黒鉛化物の物性を測定し、その結果を同じく第
1表に示す。The physical properties of the obtained graphitized product were measured, and the results are also shown in Table 1.
比較例 3
フェノール・ノボラック樹脂:50重量部と、硬化フェ
ノール樹脂繊維〔カイノール11010 :群栄化学に
、に、の商品名〕の10mm長のチヨ・7プ:50重量
部とを混合した後、実施例1と同じ方法で成形し、後硬
化し、炭化し、更に黒鉛化した。Comparative Example 3 After mixing 50 parts by weight of phenol novolac resin and 50 parts by weight of 10 mm long Chiyo 7 fiber of cured phenol resin fiber [Kynol 11010: Gunei Chemical Co., Ltd., product name], It was molded, post-cured, carbonized, and graphitized in the same manner as in Example 1.
得られた黒鉛化物の物性を測定し、その結果を同しく第
1表に示す。The physical properties of the obtained graphitized product were measured, and the results are also shown in Table 1.
なお、得られた1000°C焼成品、2500℃焼成品
とも機械加工は非常に困難であった。Note that machining was extremely difficult for both the obtained products fired at 1000°C and 2500°C.
〈効果の総括〉
以上に説明した如く、この発明によれば、ガス遮蔽性、
電気伝導性、熱伝導性、耐リン酸性1強度並びに機械加
工性が共に優れ、リン酸型燃料電池の分離板に適用した
としても十分に満足できる不浸透性炭素材を提供できる
など、産業上有用な効果がもたらされる。<Summary of Effects> As explained above, according to the present invention, gas shielding properties,
It has excellent electrical conductivity, thermal conductivity, phosphoric acid resistance, strength, and machinability, and can provide an impermeable carbon material that is fully satisfactory even when applied to the separation plate of phosphoric acid fuel cells. Useful effects are produced.
Claims (1)
%、熱硬化性樹脂:10〜60重量%及び不融化繊維:
3〜60重量%の混合物を成形した後、その成形物を非
酸化性雰囲気下で焼成することを特徴とする、不浸透性
炭素材の製造方法。Mesophase small spheres or mesophase powder: 5 to 70% by weight, thermosetting resin: 10 to 60% by weight, and infusible fiber:
A method for producing an impermeable carbon material, which comprises molding a 3-60% by weight mixture and then firing the molded product in a non-oxidizing atmosphere.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63092532A JPH01264917A (en) | 1988-04-14 | 1988-04-14 | Production of impermeable carbon material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63092532A JPH01264917A (en) | 1988-04-14 | 1988-04-14 | Production of impermeable carbon material |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01264917A true JPH01264917A (en) | 1989-10-23 |
Family
ID=14056970
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63092532A Pending JPH01264917A (en) | 1988-04-14 | 1988-04-14 | Production of impermeable carbon material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01264917A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010534306A (en) * | 2007-07-24 | 2010-11-04 | シエツフレル コマンディートゲゼルシャフト | Method for manufacturing a graphite cage for anti-friction bearings containing a plurality of rolling elements |
-
1988
- 1988-04-14 JP JP63092532A patent/JPH01264917A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010534306A (en) * | 2007-07-24 | 2010-11-04 | シエツフレル コマンディートゲゼルシャフト | Method for manufacturing a graphite cage for anti-friction bearings containing a plurality of rolling elements |
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