JPH0663136B2 - Pitch-based carbon fiber manufacturing method - Google Patents
Pitch-based carbon fiber manufacturing methodInfo
- Publication number
- JPH0663136B2 JPH0663136B2 JP9697385A JP9697385A JPH0663136B2 JP H0663136 B2 JPH0663136 B2 JP H0663136B2 JP 9697385 A JP9697385 A JP 9697385A JP 9697385 A JP9697385 A JP 9697385A JP H0663136 B2 JPH0663136 B2 JP H0663136B2
- Authority
- JP
- Japan
- Prior art keywords
- pitch
- spinning
- carbon fiber
- based carbon
- spinning nozzle
- 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.)
- Expired - Lifetime
Links
- 229920000049 Carbon (fiber) Polymers 0.000 title claims description 23
- 239000004917 carbon fiber Substances 0.000 title claims description 23
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims description 20
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- 238000009987 spinning Methods 0.000 claims description 83
- 239000002245 particle Substances 0.000 claims description 8
- 238000012856 packing Methods 0.000 claims description 7
- 239000000843 powder Substances 0.000 claims description 7
- 238000003763 carbonization Methods 0.000 claims description 5
- 230000003287 optical effect Effects 0.000 claims description 5
- 235000014653 Carica parviflora Nutrition 0.000 claims description 4
- 241000243321 Cnidaria Species 0.000 claims description 4
- 229910010272 inorganic material Inorganic materials 0.000 claims description 4
- 239000011147 inorganic material Substances 0.000 claims description 4
- 239000007769 metal material Substances 0.000 claims description 4
- 238000005087 graphitization Methods 0.000 claims description 3
- 238000011144 upstream manufacturing Methods 0.000 claims 1
- 239000011295 pitch Substances 0.000 description 63
- 239000000835 fiber Substances 0.000 description 27
- 239000002994 raw material Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 11
- 239000000463 material Substances 0.000 description 10
- 238000010008 shearing Methods 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 6
- 239000011302 mesophase pitch Substances 0.000 description 6
- 238000009826 distribution Methods 0.000 description 5
- 239000000945 filler Substances 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 239000003245 coal Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000001747 exhibiting effect Effects 0.000 description 3
- LBUJPTNKIBCYBY-UHFFFAOYSA-N 1,2,3,4-tetrahydroquinoline Chemical compound C1=CC=C2CCCNC2=C1 LBUJPTNKIBCYBY-UHFFFAOYSA-N 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- SMWDFEZZVXVKRB-UHFFFAOYSA-N Quinoline Chemical compound N1=CC=CC2=CC=CC=C21 SMWDFEZZVXVKRB-UHFFFAOYSA-N 0.000 description 2
- 239000010692 aromatic oil Substances 0.000 description 2
- 239000011280 coal tar Substances 0.000 description 2
- 239000011294 coal tar pitch Substances 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000002074 melt spinning Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 230000010287 polarization Effects 0.000 description 2
- 241000894007 species Species 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 239000011269 tar Substances 0.000 description 2
- 238000006027 Birch reduction reaction Methods 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 235000016678 Erythrina glauca Nutrition 0.000 description 1
- 240000008135 Piscidia piscipula Species 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000011337 anisotropic pitch Substances 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 239000012300 argon atmosphere Substances 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000010000 carbonizing Methods 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000013307 optical fiber Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000011301 petroleum pitch Substances 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- 229920002239 polyacrylonitrile Polymers 0.000 description 1
- 238000006068 polycondensation reaction Methods 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Landscapes
- Filtering Materials (AREA)
- Inorganic Fibers (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明はピツチ系炭素繊維の製造法に関するものであ
り、より詳しくは、改善された強度を発現するピツチ系
炭素繊維を安定して製造する方法に関するものである。TECHNICAL FIELD The present invention relates to a method for producing a Pitch-based carbon fiber, and more specifically, to stably produce a Pitch-based carbon fiber exhibiting improved strength. It is about the method.
炭素繊維は、比強度、比弾性率が高い材料で、高性能複
合材料のフイラー繊維として最も注目されており、中で
もピツチ系炭素繊維は原料が潤沢である、炭化工程の歩
留が大きい、繊維の弾性率が高い、等ポリアクリロニト
リル系炭素繊維に比べて様々な利点を持つている。Carbon fiber is a material with a high specific strength and a high specific elastic modulus, and has received the most attention as a filler fiber for high-performance composite materials. Among them, Pitch-based carbon fiber has abundant raw materials and has a high yield in the carbonization process. It has various advantages over polyacrylonitrile-based carbon fiber, which has a high elastic modulus.
ところで、このような地点を有するピツチ系炭素繊維の
原料である紡糸ピツチは種々検討されている。By the way, various spinning pitches, which are raw materials of the pitch-based carbon fiber having such a point, have been variously studied.
すなわち、従来紡糸ピツチとして使用していた等方質ピ
ツチの代りに、炭素質原料を加熱処理して、異方性が発
達し、配向しやすい分子種が形成されたピツチを使用す
ることにより、高特性のピツチ系炭素繊維が得られるこ
とが報告(特公昭49−8634号)されて以来、配向性の良
好な紡糸ピツチの調製について種々検討されてきた。That is, instead of the isotropic pitch that has been conventionally used as a spinning pitch, a carbonaceous raw material is heat-treated to develop anisotropy, and by using a pitch having a molecular species that is easily oriented, Since it was reported that a high-performance pitch-based carbon fiber could be obtained (Japanese Patent Publication No. Sho 49-8634), various studies have been conducted on the preparation of a spinning pitch having good orientation.
周知の様に、重質油、タール、ピツチ等の炭素質原料を
350〜500℃に加熱すると、それら物質中に粒径が数ミク
ロンから数百ミクロンの、偏光下に光学的異方性を示す
小球体が生成する。そして、さらに加熱するとこれらの
小球体は成長、合体し、ついには全体が光学的異方性を
示す状態となる。この異方性組織は炭素質原料の熱重縮
合反応により生成した平面状高分子芳香族炭化水素が層
状に積み重なり、配向したもので、黒鉛決勝構造の前駆
体とみなされている。As is well known, carbonaceous raw materials such as heavy oil, tar and pitch are used.
When heated to 350 to 500 ° C., small spheres having a particle size of several microns to several hundreds of microns and exhibiting optical anisotropy under polarized light are formed in the materials. Then, upon further heating, these small spheres grow and coalesce, and finally the whole becomes a state exhibiting optical anisotropy. This anisotropic structure is formed by layering and orienting planar polymeric aromatic hydrocarbons produced by the thermal polycondensation reaction of a carbonaceous raw material, and is regarded as a precursor of the graphite final structure.
この様な異方性組織を含む熱処理物は、一般的にはメソ
フエーズピツチと呼称されている。A heat-treated product containing such an anisotropic structure is generally called a mesophase pitch.
かかるメソフエーズピツチを紡糸ピツチとして使用する
方法としては、例えば、石油系ピツチを静置条件下で約
350〜450℃で加熱処理し、40〜90重量%のメソフエーズ
を含有するピツチを得て、これを紡糸ピツチとする方法
が提案されている(特開昭49−19127号)。As a method of using such a mesophase pitch as a spinning pitch, for example, a petroleum-based pitch may be used under a standing condition.
A method has been proposed in which heat treatment is performed at 350 to 450 ° C. to obtain a pitch containing 40 to 90% by weight of mesophase, which is used as a spinning pitch (JP-A-49-19127).
しかし、かかる方法により等方質の炭素質原料をメソ化
するには長時間を要するので、予め炭素質原料を十分量
の溶媒で処理してその不溶分を得、それを230〜400℃の
温度で10分以下の短時間加熱処理して、高度に配向さ
れ、光学的異方性部分が75重量%以上で、キノリン不溶
分25重量%以下の、所謂、ネオメソフエーズピツチを形
成し、これを紡糸ピツチとする方法が提案されている
(特開昭54−160427号)。However, since it takes a long time to mesomorphize an isotropic carbonaceous raw material by such a method, the carbonaceous raw material is previously treated with a sufficient amount of a solvent to obtain an insoluble matter thereof, which is heated at 230 to 400 ° C. By heat treatment at a temperature of 10 minutes or less for a short period of time, a so-called neomesophase pitch is formed, which is highly oriented and has an optically anisotropic portion of 75% by weight or more and a quinoline insoluble content of 25% by weight or less. A method of using this as a spinning pitch has been proposed (JP-A-54-160427).
その他、高特性炭素繊維製造用の配向性のよい紡糸ピツ
チとしては、例えば、コールタールピツチをテトラヒド
ロキノリン存在下に水添処理し、次いで、約450℃で短
時間加熱処理して得られる光学的に等方性で600℃以上
に加熱することによつて異方性に変わる性質を有するピ
ツチ、所謂、プリメソフエーズピツチ(特開昭58−1842
1号)、或いは、メソフエーズピツチをBirch還元法等に
より水素化処理して得られる光学的に等方性で外力を加
えるとその方向への配向性を示すピツチ、所謂、ドーマ
ントメソフエーズ(特開昭57−100186号)等が提案され
ている。In addition, as a spinning pitch having good orientation for producing high-characteristic carbon fibers, for example, an optical fiber obtained by hydrogenating coal tar pitch in the presence of tetrahydroquinoline, and then heating at about 450 ° C. for a short time is used. Isotropic and has a property of changing anisotropically by being heated to 600 ° C. or more, that is, a so-called premesophase pitch (Japanese Patent Laid-Open No. 58-1842).
No. 1), or a so-called dormant mesophase, which is obtained by hydrogenating a mesophase pitch by the Birch reduction method or the like and shows orientation in that direction when an external force is applied with optical isotropy. (JP-A-57-100186) and the like have been proposed.
この様な紡糸ピツチをノズルを通して溶融紡糸すること
によりピツチ繊維を得ることができる。次いで、このピ
ツチ繊維を不融化、炭化、さらに場合により黒鉛化する
事によつてピツチ系の高特性炭素繊維を得る事ができ
る。Pitch fibers can be obtained by melt spinning such a spinning pitch through a nozzle. Then, the Pitch-type high-performance carbon fiber can be obtained by infusibilizing, carbonizing, and optionally graphitizing the Pitch-type fiber.
従来の方法により、上記の様な配向性のよい紡糸ピツチ
を用いて紡糸した場合、得られるピツチ繊維中の平面状
高分子炭化水素の積層構造が繊維断面内でラジアル配向
となりやすく、その結果、その後の不融化処理、炭化処
理の際に炭化収縮に起因する引張応力が繊維断面の周方
向に作用するため、得られる炭素繊維の断面には繊維軸
方向に伸びるくさび状のクラツクが発生し、炭素繊維の
商品的価値を損なう欠点があつた。According to the conventional method, when spinning is performed using a spinning pitch having good orientation as described above, the laminated structure of the planar polymer hydrocarbon in the obtained pitch fiber tends to have radial orientation in the fiber cross section, and as a result, Subsequent infusibilization treatment, since tensile stress due to carbonization shrinkage during carbonization acts in the circumferential direction of the fiber cross section, a wedge-shaped crack extending in the fiber axis direction occurs in the cross section of the obtained carbon fiber, There was a drawback that impaired the commercial value of carbon fiber.
本発明者等は上記問題点に留意し、鋭意検討した経過、
紡糸ピツチを紡糸ノズルへ供給する前に剪断材層を通
過させることにより、上記欠点が克服されることを見い
出し、先に提案を行なつた(特願昭59−131641)。この
中で剪断材層を通過した紡糸ピツチを長時間溶融状態
で保持しておくと、微細化した紡糸ピツチの流動単位が
再度合体して、剪断材層通過前の状態に戻ると考えら
れているので、紡糸ピツチが剪断材層を通過後紡糸ノ
ズルに達するまでの所要時間が30分以内、好ましくは20
分以内、更に好ましくは10分以内のできるだけ短時間と
なるように剪断材層を設置するのが好ましいことを提
案した。The present inventors have paid attention to the above-mentioned problems, and have studied intensively,
It was found that the above drawbacks can be overcome by passing the spinning pitch through the shearing material layer before feeding the spinning pitch to the spinning nozzle, and the proposal was made earlier (Japanese Patent Application No. 59-131641). It is thought that if the spinning pitch that has passed through the shear layer is held in the molten state for a long period of time, the fluidized units of the refined spinning pitch will be re-united, and the state before passing through the shear layer will be restored. Therefore, the time required for the spinning pitch to reach the spinning nozzle after passing through the shearing material layer is within 30 minutes, preferably 20
It was proposed that it is preferable to place the shearing material layer so that the time is within a minute, more preferably within 10 minutes and as short as possible.
ここで紡糸ピツチが剪断材層を通過後紡糸ノズルに達
するまでの所要時間は剪断材層の下端から紡糸ノズル
入口上端までの内容積を紡糸ピツチの吐出量で除したも
のである。Here, the time required for the spinning pitch to reach the spinning nozzle after passing through the shearing material layer is the inner volume from the lower end of the shearing material layer to the upper end of the spinning nozzle inlet divided by the discharge amount of the spinning pitch.
よつて、すぐれた特性を持つ炭素繊維を得るには、ノズ
ル部直上に剪断材層すなわち、充填層を設けるのが好
ましいが、多ホールの紡糸口金の場合には、充填材を各
ホールに均質に挿入することが難しく、均質に挿入でき
ない場合、充填層を充填した各ホール毎の構成の差が各
紡糸ノズルから吐出される紡糸ピツチの流量の変動の原
因となり繊度ムラ(各紡糸ノズルから紡出される繊維の
直径の分布)を生ずる欠点がある。Therefore, in order to obtain carbon fibers with excellent characteristics, it is preferable to provide a shearing material layer, that is, a filling layer directly above the nozzle portion, but in the case of a multi-hole spinneret, the filling material is homogeneous in each hole. If it is difficult to insert it uniformly, and if it is not possible to insert it uniformly, the difference in the composition of each hole filled with the packing layer causes the fluctuation of the flow rate of the spinning pitch discharged from each spinning nozzle, and the unevenness of the fineness (spinning nozzle from each spinning nozzle is caused. There is a drawback that results in a distribution of the diameter of the fibers that are dispensed.
そこで本発明者らは更に検討を重ねた結果充填材とし
て、紡糸ノズル孔の直径の2〜3倍という非常に限られ
た範囲の粒径を有する珊瑚樹様の構造をした金属材料も
しくは無機材料の粉末を用いる場合は各ホールより紡出
される繊維径の分布が極めて小さくなることを見い出し
この知見に基づいて本発明に到達した。Therefore, as a result of further studies by the present inventors, as a filler, a metal material or an inorganic material having a coral tree-like structure having a particle diameter within a very limited range of 2 to 3 times the diameter of the spinning nozzle hole is used. When using powder, it was found that the distribution of fiber diameters spun from each hole was extremely small, and the present invention was reached based on this finding.
すなわち、本発明の目的は、繊維断面構造が実質的にラ
ジアル配向ではなく、繊維軸方向に伸びるくさび状のク
ラツクの発生が抑えられたピツチ系炭素繊維を繊度ムラ
なく安定的に製造することになる。That is, an object of the present invention is to stably produce a Pitch-based carbon fiber in which the generation of wedge-shaped cracks extending in the fiber axis direction is suppressed without the fiber cross-sectional structure being substantially in a radial orientation. Become.
すなわち、この目的は紡糸ピツチを紡糸ノズルから溶融
紡糸し、不融化処理を行ない、次いで炭化処理をし、さ
らに必要に応じて黒鉛化処理することによりピツチ系炭
素繊維を製造する方法において、該紡糸ノズルの直上部
に充填層として前記紡糸ノズル孔の直径の2〜3倍の粒
径を有する金属材料もしくは無機材料でできた珊瑚樹様
の構造をした粉体を充填し、該紡糸ピツチを該充填層お
よび該紡糸ノズルの願に流通させ、紡糸することにより
容易に達成される。That is, the purpose is to melt-spin a spinning pitch from a spinning nozzle, perform infusibilization treatment, then carbonize it, and then, if necessary, graphitize it to produce a pitched carbon fiber. A powder having a coral tree-like structure made of a metal material or an inorganic material having a particle diameter of 2 to 3 times the diameter of the spinning nozzle hole is filled as a filling layer immediately above the nozzle, and the spinning pitch is filled with the powder. It is easily achieved by circulating and spinning the layers and the spinning nozzles.
以下、本発明を詳しく説明するのに、本発明の紡糸ピツ
チとしては配向しやすい分子種が形成されており、光学
的に異方性のピツチを与えるものであれば特に制限はな
く、前述のような従来の種々のものを使用することがで
きる。Hereinafter, in order to explain the present invention in detail, as the spinning pitch of the present invention, a molecular species that is easily oriented is formed, and there is no particular limitation as long as it gives an optically anisotropic pitch. Various conventional types can be used.
しかし、それほど高度の比強度及び比弾性率が要求され
ない場合は、アモルフアスピツチを用いることもでき
る。これらの紡糸ピツチを得るための炭素質原料として
は、例えば、石炭系のコールタール、コールタールピツ
チ、石炭液化物、石油系の重質油、タール、ピツチ等が
挙げられる。これらの炭素質原料には通常フリーカーボ
ン、未溶解石炭、灰分などの不純物が含まれているが、
これらの不純物は過、遠心分離、あるいは溶剤を使用
する静置沈降分離などの周知の方法で予め除去しておく
事が望ましい。However, if a high specific strength and a high specific elastic modulus are not required, an amorphous aspitch can be used. Examples of the carbonaceous raw material for obtaining these spinning pitches include coal-based coal tar, coal tar pitch, coal liquefaction, petroleum heavy oil, tar, and pitch. These carbonaceous raw materials usually contain impurities such as free carbon, unmelted coal and ash,
It is desirable to remove these impurities in advance by a known method such as filtration, centrifugation, or static sedimentation using a solvent.
また、前記炭素質原料を、例えば、加熱処理した後特定
溶剤で可溶分を抽出するといつた方法、あるいは水素供
与性溶剤、水素ガスの存在下に水添処理するといつた方
法で予備処理を行なつておいても良い。Further, the carbonaceous raw material can be pretreated by, for example, a method in which soluble components are extracted with a specific solvent after heat treatment, or a method in which hydrogenation is performed in the presence of a hydrogen donating solvent or hydrogen gas. You can leave it.
本発明においては、前記炭素質原料あるいは予備処理を
行なつた炭素質原料を、通常350〜500℃、好ましくは38
0〜450℃で、2分〜50時間、好ましくは5分〜5時間、
窒素、アルゴン等の不活性ガス雰囲気下、或いは、吹き
込み下に加熱処理することによつて得られる40%以上、
特に70%以上の光学的異方性組織を含むピツチが紡糸ピ
ツチとして好適に使用できる。In the present invention, the carbonaceous raw material or the pretreated carbonaceous raw material is usually 350 to 500 ° C., preferably 38
At 0 to 450 ° C. for 2 minutes to 50 hours, preferably 5 minutes to 5 hours,
40% or more obtained by heat treatment under an inert gas atmosphere such as nitrogen or argon, or under blowing,
In particular, a pitch containing 70% or more of optically anisotropic structure can be preferably used as a spinning pitch.
本発明でいう紡糸ピツチの光学的異方性組織割合は、常
温下偏光顕微鏡での紡糸ピツチ試料中の光学的異方性を
示す部分の面積割合として求めた値である。The optically anisotropic structure ratio of the spinning pitch in the present invention is a value obtained as the area ratio of the portion showing the optical anisotropy in the spinning pitch sample under a polarization microscope at room temperature.
具体的には、例べばピツチ試料を数mm角に粉砕したもの
を常法に従つて直径約2cmの樹脂の表面のほぼ全面に試
料片を埋込み、表面を研磨後、表面全体をくまなく偏光
顕微鏡(100倍率)下で観察し、試料の全表面積に占め
る光学的異方性部分の面積の割合を測定する事によつて
求める。Specifically, for example, a Pitch sample crushed into a few mm square is embedded with a sample piece on almost the entire surface of the resin with a diameter of about 2 cm according to the usual method, and after polishing the surface, the entire surface is covered all over. It is determined by observing under a polarizing microscope (100 magnification) and measuring the ratio of the area of the optically anisotropic portion to the total surface area of the sample.
本発明においては、上記紡糸ピツチを充砕層を通過させ
た後、紡糸ノズルへ供給し紡糸する。In the present invention, the spinning pitch is passed through the crush layer and then supplied to the spinning nozzle for spinning.
ここで充填層とは、紡糸ピツチ流通路内であつて、紡糸
ノズルの直上部に充填されたものであり、溶融状態の紡
糸ピツチが該層を通過することにより、紡糸ピツチの流
れが細分化され、かつ該層を通過する間に紡糸ピツチの
メソフエーズの積層状態が乱され、その結果実質的にラ
ジアル配向でない繊維断面構造を有するピツチ繊維を与
えるものである。充填層を構成する充填材としては、具
体的には350〜400℃程度の温度に充分耐えられるよう
な、ステンレス鋼、銅、アルミニウム等の金属材料、ま
たはセラミツク、ガラス、黒鉛等の無機材料の珊瑚樹様
の構造をした粉体であつてその粒径が後記紡糸ノズルの
直径の2〜3倍の大きさを有するものである。充填材粒
径がこの範囲より小さい場合も大きい場合も各ホールよ
り紡出される繊維の径の分布が、均質にならず紡糸中に
糸切れが頻発し安定して所望の繊維を得ることができな
い。Here, the packed bed is one that is filled in the spinning pitch flow passage and immediately above the spinning nozzle, and the flow of the spinning pitch is subdivided by passing the molten spinning pitch through the layer. And the mesophases of the spinning pitch are disturbed while passing through the layer, resulting in a pitch fiber having a fiber cross-section that is not substantially radially oriented. As the filler constituting the filling layer, specifically, a metal material such as stainless steel, copper, or aluminum, which can sufficiently withstand a temperature of about 350 to 400 ° C., or a ceramic, glass, or an inorganic material such as graphite. It is a powder having a coral tree-like structure, and its particle size is 2-3 times the diameter of the spinning nozzle described later. Regardless of whether the filler particle size is smaller or larger than this range, the diameter distribution of the fibers spun from each hole is not uniform, and yarn breakage frequently occurs during spinning, and the desired fiber cannot be stably obtained. .
ここで第1〜第4図の本発明の充填層を設けた紡糸装置
の種々の形態における紡糸ノズル部付近の拡大図を示し
たものである。1は紡糸口金、2は紡糸ノズル、3は導
入口、4は充填層を示す。充填層4の厚さは、後述する
結晶配向に対する効果の面では厚い方が好ましいが、そ
の効果を発現させるためにはノズル部直上に設置する場
合粒子数として5個程度もあれば十分であり、いたずら
に厚くするとピツチの流通抵抗が大きくなり設備上コス
ト高となる。よつて、充填層の厚みとしてはせいぜい20
mmである。各ホールに充填する充填層の厚みはなるべく
均一にすることが望ましいのは勿論である。本発明で用
いられる紡糸ノズルは孔径が0.05〜0.5mm、長さが0.01
〜5mmの範囲から選定するのが好ましいが、その形状は
特に限定されるものではなく、直管状のもの、紡糸ノズ
ルの中間部が拡大された形状のもの、あるいは紡糸ノズ
ル下部が拡大された形状のものなどのいずれの形状の紡
糸ノズルも使用できる。Here, it is an enlarged view of the vicinity of the spinning nozzle portion in various forms of the spinning device provided with the filling layer of the present invention in FIGS. 1 to 4. 1 is a spinneret, 2 is a spinning nozzle, 3 is an inlet, and 4 is a packed layer. The thickness of the filling layer 4 is preferably thick from the viewpoint of the effect on the crystal orientation described later, but in order to bring out the effect, it is sufficient if the number of particles is about 5 when it is installed directly above the nozzle portion. However, if it is unnecessarily thick, the distribution resistance of the pitch becomes large and the cost of the equipment becomes high. Therefore, the thickness of the packed bed is at most 20.
mm. Of course, it is desirable to make the thickness of the filling layer filling each hole as uniform as possible. The spinning nozzle used in the present invention has a pore size of 0.05 to 0.5 mm and a length of 0.01.
It is preferable to select from the range of ~ 5 mm, but the shape is not particularly limited, a straight tubular shape, a shape in which the intermediate portion of the spinning nozzle is enlarged, or a shape in which the lower portion of the spinning nozzle is enlarged. Spinning nozzles of any shape, such as those described above, can be used.
また、溶融状態の紡糸ピツチは充填層4を経て紡糸ノズ
ル2より吐出され紡糸されるが、充填層4を設けること
により紡糸ピツチの吐出に際し、紡糸ピツチに少なくと
も2kg/cm2・G以上、好ましくは5kg/cm2・G以上、
更に好ましくは10kg/cm2・G以上の圧力を加え紡糸を
行なう必要がある。In addition, the melted spinning pitch is discharged from the spinning nozzle 2 through the filling layer 4 and spun. When the spinning layer is discharged by providing the filling layer 4, the spinning pitch is at least 2 kg / cm 2 · G or more, preferably Is 5 kg / cm 2 · G or more,
More preferably, it is necessary to apply a pressure of 10 kg / cm 2 · G or more to perform spinning.
本発明においては、溶融状態の紡糸ピツチが充填層4を
通過することにより、紡糸ピツチの流れを細分化し、か
つ充填層4においてメソフエーズの積層状態が乱され、
繊維断面構造が実質的にラジアル配向でないピツチ繊維
ひいてはピツチ系炭素繊維が得られるものと考えられ
る。In the present invention, the melted spinning pitch passes through the packing layer 4 to subdivide the flow of the spinning pitch, and the stacked state of the mesophases is disturbed in the packing layer 4.
It is considered that the Pitch fibers having a substantially non-radial orientation in the fiber cross-sectional structure and further the Pitch-based carbon fibers can be obtained.
更に、本発明においては充填層として、紡糸ノズル部の
直径の2〜3倍と限定された粒径のものを用いることに
より、各ホール毎の圧力損失が最も均質となり多ホール
ノズルを用いて紡糸するに際し、各ホールより紡出され
る繊維径の分布が小さくなり安定的に紡糸される。Further, in the present invention, by using a packing layer having a particle diameter limited to 2 to 3 times the diameter of the spinning nozzle portion, the pressure loss for each hole is most uniform, and spinning is performed using a multi-hole nozzle. In doing so, the distribution of the diameter of the fibers spun from each hole becomes small, and the spinning is performed stably.
したがつて、充填層4により紡糸ピツチの流動性が改善
されるとともに、紡糸時における上記範囲の加圧操作に
より、紡糸温度で紡糸ピツチから発生するガスあるいは
気泡の生成が抑制される。更に、流出量の少ないホール
が少なくなるため、紡糸安定性が向上し、改善された特
性を有するピツチ繊維を長時間安定して製造できる。Therefore, the fluidity of the spinning pitch is improved by the packed bed 4, and the generation of gas or bubbles generated from the spinning pitch at the spinning temperature is suppressed by the pressurizing operation within the above range during spinning. Furthermore, since the holes with a small outflow amount are reduced, spinning stability is improved, and pitch fibers having improved characteristics can be stably manufactured for a long time.
かくして、得られたピツチ繊維を不融化、炭化必要に応
じて黒鉛化することにより、ランダム配向あるいはオニ
オンライク配向の繊維断面構造を有し、繊維軸方向に伸
びるくさび状のクラツクのない、高特性でかつ繊度ムラ
の小さいピツチ系炭素繊維を得ることができる。Thus, the obtained pitch fibers are made infusible, and carbonized by graphitization if necessary, to have a fiber cross-section structure of random orientation or onion-like orientation, without a wedge-shaped crack extending in the fiber axis direction, and high characteristics. It is possible to obtain a Pitch-based carbon fiber having a small fineness unevenness.
ここでオニオンライク配向とは、繊維断面積の主たる部
分が同心円状の分子配向性を有するものであり、一部、
特に外周部が後続の炭化あるいは黒鉛化処理によりクラ
ツクを生じない程度のラジアル配向しているものも含
む。また、これらの繊維断面構造は偏光顕微鏡で測定し
たものである。Here, the onion-like orientation means that the main portion of the fiber cross-sectional area has concentric molecular orientation, and
In particular, the outer peripheral portion includes those having a radial orientation such that cracking does not occur due to the subsequent carbonization or graphitization treatment. Moreover, these fiber cross-sectional structures were measured with a polarization microscope.
以下実施例を挙げて本発明を具体的に説明する。 The present invention will be specifically described below with reference to examples.
なお、実施例における変動係数は下記の式を用いて計算
した値である。The coefficient of variation in the examples is a value calculated using the following formula.
x=個々の測定値 =個々の測定値の算術平均値 n=サンプル数 実施例1 60の反応器にコールタールピツチと、水添した芳香族
油を等量混合したものを50/hrの速度で供給し処理し
た。この時の反応器の温度は450℃であつた。この反応
器より得られた反応液を過した後、減圧蒸留して芳香
族油分を回収して残渣ピツチを得た。次いでこの残渣ピ
ツチに窒素ガスをパブリングしながら430℃で125分間加
熱処理してメソフエーズピツチを得た。得られたメソフ
エーズピツチの異方性割合は100%であつた。 x = individual measured value = arithmetic average value of individual measured values n = number of samples Example 1 A reactor of 60 was mixed with coal tar pit and an equal amount of hydrogenated aromatic oil at a rate of 50 / hr. And processed. At this time, the temperature of the reactor was 450 ° C. After passing the reaction solution obtained from this reactor, it was distilled under reduced pressure to recover the aromatic oil and obtain a residual pitch. Then, the residual pitch was heat-treated at 430 ° C. for 125 minutes while bubbling nitrogen gas to obtain a mesophase pitch. The anisotropy ratio of the obtained mesophase pitch was 100%.
次に、第1図に示すような紡糸ノズル(紡糸ノズル2の
孔径0.1mm、長さ0.1mm)を120ホール有する紡糸口金を
用い、その導入口3に60〜65メツシユの大きさ(0.208
〜0.246mm)に篩分された珊瑚樹様の形をしたステンレ
ス製のメタルパウダーを約10mmの厚さ充填した。Next, a spinneret having 120 holes of spinning nozzles (hole diameter 0.1 mm, length 0.1 mm of spinning nozzle 2) as shown in FIG. 1 was used, and a size of 60-65 mesh (0.208
~ 0.246 mm) and a metal powder made of stainless steel in the shape of a coral tree, which had been sieved, was filled to a thickness of about 10 mm.
次いで、この紡糸口金を用いて前記メソフエーズピツチ
を325〜360℃の温度範囲で溶融紡糸した。何れの場合も
最適の温度において糸の巻取り速度を変えることにより
糸径10μm迄のピツチ繊維を長時間にわたり安定的に得
ることができた。Next, using the spinneret, the mesophase pitch was melt-spun in the temperature range of 325 to 360 ° C. In either case, it was possible to stably obtain pitch fibers up to a diameter of 10 μm for a long time by changing the winding speed of the yarn at the optimum temperature.
336℃の条件で溶融紡糸して得られたピツチ繊維を空気
中310℃で不融化し、さらにアルゴン雰囲気下1400℃で
炭化して炭化繊維を得た。この炭素繊維の引張り強度及
び繊度ムラを測定しその結果を第1表に示す。Pitch fibers obtained by melt spinning at 336 ° C were infusibilized in air at 310 ° C and carbonized at 1400 ° C in an argon atmosphere to obtain carbonized fibers. The tensile strength and fineness unevenness of this carbon fiber were measured, and the results are shown in Table 1.
比較例1 充填層として100〜150メツシユの大きさ(0.104〜0.147
mm)に篩分された珊瑚樹様のメタルパウダーを充填する
以外は実施例1と全く同様にして紡糸したが、各ホール
からの流出量の均質性が劣り、流量の少ないノズルが原
因となり安定に紡糸することが困難であつた。Comparative Example 1 The size of the filling layer is 100 to 150 mesh (0.104 to 0.147).
mm) was spun in exactly the same manner as in Example 1 except that the sieved coral-like metal powder was charged, but the homogeneity of the outflow rate from each hole was inferior, and the nozzle with a small flow rate caused a stable It was difficult to spin.
第1図〜第4図は本発明で用いられる紡糸装置の種々の
態様における紡糸口金付近部の拡大断面概略図である。 第5図および第6図は本発明に用いられる剪断材の一
例の拡大略図である。 1;紡糸口金、2;紡糸ノズル 3;導入孔、4;充填層1 to 4 are schematic enlarged cross-sectional views of the vicinity of the spinneret in various aspects of the spinning device used in the present invention. 5 and 6 are enlarged schematic views of an example of the shearing material used in the present invention. 1; Spinneret, 2; Spinning nozzle 3; Introduction hole, 4; Packing layer
Claims (4)
不融化処理を行ない、次いで炭化処理し、さらに必要に
応じて黒鉛化処理することによりピツチ系炭素繊維を製
造する方法において、該紡糸ノズルの上流部に前記紡糸
ノズル孔の直径の2〜3倍の粒径を有する金属材料また
は無機材料の珊瑚樹様の構造をした粉体よりなる充填層
を充填し、該紡糸ピツチを該充填層および該紡糸ノズル
の順に流通させ紡糸することを特徴とするピツチ系炭素
繊維の製造法。1. A spinning pitch is melt-spun from a spinning nozzle,
In a method for producing a Pitch-based carbon fiber by performing infusibilization treatment, then carbonization treatment, and further graphitization treatment if necessary, in the upstream portion of the spinning nozzle, the diameter is 2 to 3 times the diameter of the spinning nozzle hole. A metal material or an inorganic material having a particle diameter of a packing layer made of a powder having a coral tree-like structure, and the spinning pitch is circulated through the packing layer and the spinning nozzle in this order for spinning. -Based carbon fiber manufacturing method.
すピツチであることを特徴とする特許請求の範囲第1項
記載のピツチ系炭素繊維の製造法。2. The method for producing a pitch-based carbon fiber according to claim 1, wherein the spinning pitch is a pitch having an optical anisotropy of 40% or more.
ことを特徴とする特許請求の範囲第1項記載のピツチ系
炭素繊維の製造法。3. The method for producing a pitch-based carbon fiber according to claim 1, wherein the diameter of the spinning nozzle hole is 0.05 to 0.5 mm.
で溶融紡糸することを特徴とする特許請求の範囲第1項
記載のピツチ系炭素繊維の製造法。4. The method for producing a pitch-based carbon fiber according to claim 1, wherein the spinning pitch is melt-spun under a pressure of 2 kg / cm 2 · G or more.
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9697385A JPH0663136B2 (en) | 1985-05-08 | 1985-05-08 | Pitch-based carbon fiber manufacturing method |
| DE8585107676T DE3584693D1 (en) | 1984-06-26 | 1985-06-21 | METHOD FOR THE PRODUCTION OF CARBON FIBERS OF THE LEFT TYPE. |
| EP85107676A EP0166388B1 (en) | 1984-06-26 | 1985-06-21 | Process for the production of pitch-type carbon fibers |
| US07/039,679 US4818612A (en) | 1984-06-26 | 1987-04-20 | Process for the production of pitch-type carbon fibers |
| US07/245,564 US4923648A (en) | 1984-06-26 | 1988-09-19 | Process for the production of pitch-type carbon fibers |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9697385A JPH0663136B2 (en) | 1985-05-08 | 1985-05-08 | Pitch-based carbon fiber manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61258022A JPS61258022A (en) | 1986-11-15 |
| JPH0663136B2 true JPH0663136B2 (en) | 1994-08-17 |
Family
ID=14179160
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9697385A Expired - Lifetime JPH0663136B2 (en) | 1984-06-26 | 1985-05-08 | Pitch-based carbon fiber manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0663136B2 (en) |
-
1985
- 1985-05-08 JP JP9697385A patent/JPH0663136B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61258022A (en) | 1986-11-15 |
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