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JPH075767B2 - Method for producing carbon fiber reinforced thermoplastic resin - Google Patents
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JPH075767B2 - Method for producing carbon fiber reinforced thermoplastic resin - Google Patents

Method for producing carbon fiber reinforced thermoplastic resin

Info

Publication number
JPH075767B2
JPH075767B2 JP61104966A JP10496686A JPH075767B2 JP H075767 B2 JPH075767 B2 JP H075767B2 JP 61104966 A JP61104966 A JP 61104966A JP 10496686 A JP10496686 A JP 10496686A JP H075767 B2 JPH075767 B2 JP H075767B2
Authority
JP
Japan
Prior art keywords
pitch
carbon fiber
central axis
thermoplastic resin
gradually
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
Application number
JP61104966A
Other languages
Japanese (ja)
Other versions
JPS62263232A (en
Inventor
正 伊藤
恒彦 西村
雄次 松村
啓八郎 田中
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
DIC Corp
Nippon Sheet Glass Co Ltd
Osaka Gas Co Ltd
Original Assignee
Nippon Sheet Glass Co Ltd
Osaka Gas Co Ltd
Dainippon Ink and Chemicals Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Sheet Glass Co Ltd, Osaka Gas Co Ltd, Dainippon Ink and Chemicals Co Ltd filed Critical Nippon Sheet Glass Co Ltd
Priority to JP61104966A priority Critical patent/JPH075767B2/en
Publication of JPS62263232A publication Critical patent/JPS62263232A/en
Publication of JPH075767B2 publication Critical patent/JPH075767B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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  • Inorganic Fibers (AREA)
  • Nonwoven Fabrics (AREA)
  • Reinforced Plastic Materials (AREA)
  • Moulding By Coating Moulds (AREA)
  • Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
  • Working-Up Tar And Pitch (AREA)

Description

【発明の詳細な説明】 本発明は、炭素繊維で補強された熱可塑性樹脂の製造法
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a thermoplastic resin reinforced with carbon fibers.

軽量にして機械物性が良好であるばかりでなく耐熱性、
耐薬品性、電気伝導性及び摺動特性の良い炭素繊維を、
ナイロン、ポリエステル、ポリプロピレン、ノリル樹脂
など熱可塑性樹脂に配合させた複合材料は、各種工業材
料部品として既に汎用されている。
Not only is it lightweight and has good mechanical properties, it also has heat resistance,
Carbon fiber with good chemical resistance, electrical conductivity and sliding properties
Composite materials mixed with thermoplastic resins such as nylon, polyester, polypropylene, and noryl resins have already been widely used as various industrial material parts.

一方、炭素繊維そのものを安価な原料から製造する研究
も盛んとなり、特に近年、石油あるいは石炭系タールピ
ツチより高強度・高弾性の高性能炭素繊維を製造する研
究、あるいは、それ程の性能でなくとも経済的で汎用性
のある汎用型炭素繊維を製造する研究も行なわれてい
る。
On the other hand, research into producing carbon fiber itself from inexpensive raw materials has also become popular, and in recent years, in particular, research into producing high-performance and high-strength carbon fiber with higher strength and elasticity than petroleum or coal-based tarpits, or even if the performance is not so high, is economical. Studies have also been conducted to produce general-purpose carbon fibers that are general and versatile.

ピツチから得られる炭素繊維は、紡糸用ピツチの物性
(等方性、異方性)、溶融紡糸の方法及びピツチ繊維の
炭化温度により種々の物性になるが、特に溶融紡糸の方
法によつて炭素繊維の形態が決つて来るのである。
Carbon fibers obtained from pitches have various physical properties depending on the physical properties (isotropic or anisotropic) of spinning pitches, the method of melt spinning, and the carbonization temperature of the pitch fibers. In particular, carbon fibers are obtained by the method of melt spinning. The form of the fiber is fixed.

一般に、ピツチの溶融紡糸方法には3種類ある。その1
つは、ポリエステル繊維やポリプロピレン繊維のような
溶融紡糸方法と同様な方法であるが、エクストルーダー
で溶融ピツチをノズルからフイードし同時にドラフトを
かけ細糸として連続的に巻取る「連続紡糸法」である。
この方法で製造された炭素繊維は長いフイラメントの形
態を取る。
Generally, there are three types of melt spinning methods for pitch. Part 1
One is the same method as the melt spinning method for polyester fiber or polypropylene fiber, but it is the "continuous spinning method" in which the molten pitch is fed from the nozzle with an extruder, simultaneously drafted and continuously wound as fine yarn. is there.
The carbon fibers produced in this way take the form of long filaments.

さらに1つは、孔をうがつた高速回転体へ溶融ピツチを
フイードし、遠心力で細糸へと紡糸する「遠心紡糸法」
である。この方法で製造された炭素繊維は、連続的に巻
取れないので長さに限界があるが、比較的長い綿状の形
態を取る。
The first is the "centrifugal spinning method," in which the molten pitch is fed to a high-speed rotating body with holes and is spun into fine yarn by centrifugal force.
Is. The carbon fiber produced by this method has a limited length because it cannot be wound continuously, but takes a relatively long cotton-like form.

さらに1つの方法は、粘稠状態にあるピツチをオリフイ
スから流下させ、その流下軸に対し徐々に近接し且つ離
れて行く成分を有する3ケ以上の熱ガス流によつて繊維
化する方法、いわゆる「渦流法」(特公昭58-57374号)
である。この方法で製造された炭素繊維も、連続的に巻
取れないので長さに限界があり、やはり綿状の形態を取
る。
Further, one method is to make a viscous pit flow down from an orifice and fiberize it by three or more hot gas streams having components gradually approaching and leaving the down axis. "Vortex method" (Japanese Patent Publication No. 58-57374)
Is. The carbon fiber produced by this method also has a limit in length because it cannot be wound continuously, and also has a cotton-like shape.

遠心紡糸法と渦流法は、短かい炭素繊維しか製造できな
いが、紡糸工程が経済的であるから汎用型炭素繊維の製
造に適している。両法のうち渦流法は、より細い糸へ紡
糸でき、かつ、紡糸装置も安価である利点はあるものの
より短かいピツチ繊維しか紡糸できない欠点がある。
The centrifugal spinning method and the vortex method can produce only short carbon fibers, but they are suitable for producing general-purpose carbon fibers because the spinning process is economical. Among the two methods, the eddy current method has an advantage that it can spin finer yarns and that the spinning device is inexpensive, but has a drawback that only shorter pitch fibers can be spun.

さらに、渦流法で紡糸した糸は、その繊維化方法の特性
からベルトコンベア上に堆積し、連続的に不融化、次い
で炭化し、嵩高いマツト状で炭素繊維へ製造される方法
が最も技術的にも経済的にも有利である。しかし、遠心
紡糸法と比較するとより短かい繊維しか紡糸できないの
で、遠心紡糸法からなる炭素繊維のように紡いで一本の
トウとなし、切断してチヨツプにしたりブレードを編ん
だりする炭化後工程が技術的に困難である。従つて、通
常繊維強化熱可塑樹脂に使われるような炭素繊維のチヨ
ツプを取得するのは困難である。
Further, the most technical method is that the vortex-spun yarn is deposited on a belt conveyor, continuously infusibilized, and then carbonized in the form of a bulky matt into carbon fiber due to the characteristics of the fiberizing method. It is also economically advantageous. However, compared to the centrifugal spinning method, only shorter fibers can be spun, so it is spun like carbon fibers made by the centrifugal spinning method to form a single tow, which is then cut into chips or braided into a post-carbonization process. Is technically difficult. Therefore, it is difficult to obtain a carbon fiber chip that is usually used for fiber-reinforced thermoplastics.

本発明者らは渦流法の優位性に着目し、この嵩高い炭素
繊維マツトを熱可塑性樹脂の補強材とすべく鋭意検討し
た結果、本発明に到達した。すなわち、本発明は、例え
ば特公昭58-57374号公報に記載された方法(粘稠状態に
あるピツチを流出オリフイスから流出させ、前記オリフ
イスの周りに周方向に間隔を置いて配置した少なくとも
3本の気体噴出ノズルから直線状に高速気体流を吹き出
させ、ここにおいて前記気体流の各々は前記物質の中心
軸線を横断する断面の外周に沿う接線方向の成分と前記
物質の流出方向に向つて先ず前記物質の中心軸線に徐々
に接近し次に前記中心軸線から徐々に離れてゆく成分と
を有しており、それにより前記粘稠状態にあるピツチの
流出流れが中心軸線の周りに自転しながら徐々に細ま
り、繊維状にされ、渦巻状に飛び出され、引き伸ばされ
て繊維化される、いわゆる渦流繊維化法)によつて繊維
化され堆積されたピツチ繊維を不融化、炭化してなる密
度が0.008〜0.08g/cm3の嵩高い炭素繊維マツトに熱可塑
性樹脂を含浸させてシート状になし、次いで成型加工す
ることを特徴とする炭素繊維強化熱可塑性樹脂の製造法
を提供する。尚、該渦流法では、熱ガス流として高圧空
気、高圧水蒸気、ガス燃焼廃ガス等が用いられる。
The present inventors have paid attention to the superiority of the eddy current method, and as a result of earnestly studying to use this bulky carbon fiber mat as a reinforcing material for a thermoplastic resin, they have reached the present invention. That is, the present invention relates to, for example, the method described in Japanese Patent Publication No. 58-57374 (at least three pipes that are in a viscous state are discharged from an outflow orifice and are circumferentially spaced around the orifice). A high-speed gas stream is linearly blown out from the gas jet nozzle, wherein each of the gas streams is first directed toward the outflow direction of the substance and the tangential component along the outer periphery of the cross section that crosses the central axis of the substance. A component that gradually approaches the central axis of the substance and then gradually separates from the central axis, whereby the outflow of the pitch in the viscous state rotates about the central axis. It is made into fibers by a so-called vortex fiberization method, in which fibers are gradually thinned, made into a fibrous shape, ejected in a spiral shape, stretched, and made into a fiber, which is infusibilized and carbonized. Density 0.008~0.08g / cm 3 bulky carbon fiber mat is impregnated with a thermoplastic resin without a sheet form, and then to provide a process for the preparation of carbon fiber reinforced thermoplastic resin, characterized by molding. In the swirl method, high pressure air, high pressure steam, gas combustion waste gas, etc. are used as the hot gas flow.

渦流法で繊維化したピツチ繊維は、通常長さ5mm〜50c
m、直径4〜20μmであり、例えばメツシユベルトコン
ベア上に堆積させる。堆積密度や量はコンベアの速度と
繊維化の速度を変えコントロールできる。続いて不融化
及び炭化するために堆積密度は空気や窒素ガスが十分流
通するように嵩高い堆積体である必要がある。一方、炉
の効率を考えれば密度が高い方が好ましいので、炭素繊
維マツトは密度で0.008〜0.08g/cm3が好ましい。この嵩
高い炭素繊維マツトは、炭化後場合によつては表面処理
さらにはサイジング処理される。かかるマツトは一般に
はロール状に巻いて保存されるか、あるいは、炭化炉か
ら連続的に含浸機へフイードし、場合によつては連続的
に乾燥してシートとして巻取り保存する。
Pitch fibers fiberized by the vortex method usually have a length of 5 mm to 50 c.
m, diameter 4 to 20 μm, deposited on a mesh belt conveyor, for example. The deposition density and amount can be controlled by changing the conveyor speed and the fiberization speed. In order to infusibilize and carbonize subsequently, the deposition density needs to be a bulky deposit so that air or nitrogen gas can sufficiently flow therethrough. On the other hand, considering the efficiency of the furnace, it is preferable that the density is high. Therefore, the density of the carbon fiber mat is preferably 0.008 to 0.08 g / cm 3 . After being carbonized, this bulky carbon fiber mat is optionally surface-treated and then sized. Such mats are generally rolled and stored in rolls, or continuously fed from a carbonization furnace to an impregnator and optionally continuously dried and stored as sheets.

本発明における炭素繊維マツトは平面的に二次元的に堆
積しているので、マツト平面の垂直方向から圧縮しても
糸の折れ損傷が少なく、1/15位までも圧縮が可能であ
る。圧縮はマツトに樹脂を含浸する前でも後でも良い
が、糸の損失がなく圧縮操作がより容易になる樹脂を含
浸させたシート状体を圧縮する含浸後圧縮の方が好まし
い。圧縮操作は加圧ロールが好ましい。
Since the carbon fiber mat according to the present invention is two-dimensionally accumulated in a plane, even if compressed from the direction perpendicular to the mat plane, the yarn is less likely to be broken and the compression is possible up to about 1/15. The compression may be carried out before or after the mat is impregnated with the resin, but the post-impregnation compression is preferred in which the resin-impregnated sheet-like body which does not cause loss of yarn and facilitates the compression operation is compressed. A pressure roll is preferable for the compression operation.

本発明のマツトに熱可塑樹脂を含浸させる工程は、マツ
トが十分な破断強度を有する場合には、フイードロー
ル、絞りロール、乾燥機、含浸浴あるいはメルター巻取
りロールなどを備えた含浸装置あるいはホトメルト装置
に通して連続的に行なえる。破断強度が不足の場合に
は、テフロンあるいは金属シート及びメツシユフイルム
を支持ベルトにして同様な装置で行える。また、含浸の
方法も、溶液や融液に浸す方法の他に必要量をパウダー
としてふりかけ含浸する方法は、キスリングロールから
付着含浸する等の方法がある。
The step of impregnating the mat of the present invention with a thermoplastic resin is, if the mat has sufficient breaking strength, an impregnating device or a photomelt device equipped with a feed roll, a squeezing roll, a dryer, an impregnation bath or a melter winding roll, etc. Can be done continuously through. When the breaking strength is insufficient, it can be carried out by a similar device using Teflon or a metal sheet and a mesh film as a supporting belt. Further, as the method of impregnation, in addition to the method of immersing in a solution or melt, the method of sprinkling and impregnating a necessary amount as a powder includes the method of adhering and impregnating from a kiss ring roll.

本発明でいう熱可塑性樹脂とは、熱軟化温度が室温以上
の高分子化合物である。例えば、ポリエチレンテレフタ
レート、ポリブチレンテレフタレート、ポリアセター
ル、ポリスチレン、6−ナイロン、6−6ナイロン、ポ
リスルホン、ポリカーボネート、ポリフエニレンオキサ
イド、ポリフエニレンスルフイド、ポリウレタン、ポリ
プロピレン、ポリエチレン、ポリブチレン、ポリメチル
メタクリレート、ポリエーテルエーテルケトン、ポリテ
トラフルオロエチレン、ポリフエノール樹脂、ABS、ジ
アリルフエノールおよびこれらの混合物がある。この樹
脂中に潤滑材、顔料、ガラスや無機フイラーなど配合し
ても何ら支障ない。これら熱可塑性樹脂中に前記炭素繊
維は、0.5〜60重量%となるように配合されるのが好ま
しい。
The thermoplastic resin referred to in the present invention is a polymer compound having a thermal softening temperature of room temperature or higher. For example, polyethylene terephthalate, polybutylene terephthalate, polyacetal, polystyrene, 6-nylon, 6-6 nylon, polysulfone, polycarbonate, polyphenylene oxide, polyphenylene sulfide, polyurethane, polypropylene, polyethylene, polybutylene, polymethyl methacrylate, poly There are ether ether ketone, polytetrafluoroethylene, polyphenol resin, ABS, diallyl phenol and mixtures thereof. There is no problem even if a lubricant, a pigment, glass, an inorganic filler or the like is added to this resin. The carbon fibers are preferably blended in these thermoplastic resins in an amount of 0.5 to 60% by weight.

本発明でいう炭素繊維は、石油系、石炭系を問わず、ま
た等方性、異方性を問わず、ピツチを原料として得られ
る。炭化温度は800℃〜2800℃と変えられ、その結果、
炭素繊維も黒鉛繊維も本発明に有用である。従つて、本
発明の炭素繊維とは、黒鉛繊維をも含むものである。
The carbon fiber referred to in the present invention is obtained from pitch as a raw material regardless of whether it is petroleum-based or coal-based, isotropic or anisotropic. The carbonization temperature can be changed from 800 ° C to 2800 ° C, resulting in
Both carbon fibers and graphite fibers are useful in the present invention. Therefore, the carbon fiber of the present invention also includes graphite fiber.

本発明のシートは、このまゝスタンピングシートとして
スタンピングプレスなど熱圧成型機で成型できる。数mm
のチヨツプを配合したスタンピングシートとは異なり、
より長い炭素繊維が配合されているので、長い繊維によ
るメリツト、例えば補強効果、導電効果などが認められ
る。
The sheet of the present invention can be molded as a stamping sheet by a thermocompression molding machine such as a stamping press. Several mm
Unlike the stamping sheet that is mixed with
Since the longer carbon fibers are blended, the merits of the longer fibers, such as the reinforcing effect and the conductive effect, are recognized.

また、本発明のシートは、破断して粒体や粉体となし、
押出成形機あるいは射出成型機によつても種々の形に成
形できる。
Further, the sheet of the present invention is broken into particles or powder,
An extrusion molding machine or an injection molding machine can be used to form various shapes.

嵩高いマツトへ樹脂を含浸させるため、炭素繊維の含有
量は概して低いものになる。従つて、十分な補強効果を
持たせるためには、既に炭素繊維を含有している粉体や
粒体に必要量の炭素繊維を配合しても良い。配合手段に
は、押出成形機や各種ニーダーがある。
Since the resin is impregnated into the bulky mat, the carbon fiber content is generally low. Therefore, in order to provide a sufficient reinforcing effect, a necessary amount of carbon fibers may be mixed with the powder or granules already containing carbon fibers. The compounding means includes an extruder and various kneaders.

また、本発明によれば熱可塑性樹脂の物理的強度を上げ
るのみならず、電気電導度や摺動特性を上げることもで
きる。
Further, according to the present invention, not only the physical strength of the thermoplastic resin can be increased, but also the electric conductivity and sliding characteristics can be improved.

次に、本発明を実施例に従つて具体的に説明する。Next, the present invention will be specifically described with reference to Examples.

実施例1 コールタールピツチを調整して得た等方性ピツチを渦流
法で繊維化後、ベルトコンベア上で堆積して操続的に不
融化、次いで1000℃で炭化し、高さ42mm、幅300mmの嵩
高いマツト状炭素繊維を得た。密度は0.02g/cm3、繊維
長さは10〜100mm(中心は約60mm)、糸径は10〜15μ
(中心は13μ)であつた。また、糸の引張強度は80Kg/m
m2、引張弾性率は4Ton/mm2、伸度は1.9%であつた。
Example 1 An isotropic pitch obtained by adjusting a coal tar pitch was fibrillated by a vortex method, and then deposited on a belt conveyor to continuously make it infusible, then carbonized at 1000 ° C., height 42 mm, width Bulky matte carbon fibers of 300 mm were obtained. Density is 0.02g / cm 3 , fiber length is 10-100mm (center is about 60mm), thread diameter is 10-15μ
(Center is 13μ). In addition, the tensile strength of the yarn is 80 Kg / m
m 2 , the tensile elastic modulus was 4 Ton / mm 2 , and the elongation was 1.9%.

このマツトを1/2厚さにロールで圧縮後、6,6−ナイロン
をメルトさせたメルター中に通し、絞りロールでさらに
1/2厚さに圧縮し、約10mm厚のシートを得た。このナイ
ロンシート中には約10重量%の炭素繊維が含有されてい
た。
After compressing this mat to 1/2 thickness with a roll, it is passed through a melter in which 6,6-nylon is melted, and further squeezed roll
It was compressed to 1/2 thickness to obtain a sheet having a thickness of about 10 mm. This nylon sheet contained about 10% by weight of carbon fiber.

このシートをクラツシヤーにかけ、直径7mmのメツシユ
のふるいにかけ、炭素繊維含有量が約10重量%の粒体を
得た。次に、この粒体2.0Kgと前もつて上記マツトを平
均長8mmにカツトしたチヨツプ570gとをよくタンブラー
で混合し、押出成型機で混練押出しし、チヨツパーで、
長さ4mm、直径1.3mmのペレツトを得た。このペレツトを
射出成型して各種試験片を得た。表−1に結果を示し
た。
The sheet was crushed and passed through a mesh sieve having a diameter of 7 mm to obtain granules having a carbon fiber content of about 10% by weight. Next, 2.0 kg of these granules and 570 g of the above mat that was cut to an average length of 8 mm were mixed well with a tumbler, kneaded and extruded with an extrusion molding machine, and with a chipper.
A pellet having a length of 4 mm and a diameter of 1.3 mm was obtained. This pellet was injection-molded to obtain various test pieces. The results are shown in Table-1.

実施例2 実施例1とまつたく同様にして、嵩高い炭素繊維マツト
を得た。密度は0.04g/cm3、厚さは3.0mm、幅は300mm、
繊維長さは20〜60mm(中心は約40mm)、糸径は8〜11μ
(中心は9μ)であつた。糸の物性は実施例1にほゞ等
しかつた。
Example 2 A bulky carbon fiber mat was obtained in the same manner as in Example 1. Density 0.04 g / cm 3 , thickness 3.0 mm, width 300 mm,
Fiber length is 20-60mm (center is about 40mm), thread diameter is 8-11μ
(Center is 9μ). The physical properties of the yarn were almost the same as in Example 1.

このマツトを1/3厚さにニードルパンチングして調整
後、縦、横幅共に300mmのマツトとして切出した。一
方、ポリフエニレンスルフイド(フイリツプスペトロー
リアム製)72gを微粉末にして、平滑に敷いたパレツト
にこのマツトをのせ、ステンレス板で押えて、420℃で
2時間加熱した。シートを取出してプレス成型機にか
け、5mmの厚さに熱圧した。このシートからASTM試験方
法の試片を切り出し、物性を測定した結果は、表−2の
通りである。
This mat was adjusted by needle punching to a thickness of 1/3 and cut into a mat having a length and width of 300 mm. On the other hand, 72 g of polyphenylene sulfide (manufactured by Philippe Petroleum) was made into a fine powder, and the mat was placed on a smooth pallet, which was pressed with a stainless steel plate and heated at 420 ° C. for 2 hours. The sheet was taken out, put on a press molding machine, and hot pressed to a thickness of 5 mm. Table 2 shows the results of measuring the physical properties by cutting out a test piece of the ASTM test method from this sheet.

実施例3 コールタールピツチを調整して得られた異方性ピツチを
渦流性で繊維化後、ベルトコンベア上で堆積して連続的
に不融化、次いで1100℃で炭化し、高さ30mm、幅300mm
の嵩高いマツト状炭素繊維を得た。密度は0.03g/cm3
繊維長さは20〜60mm(中心は40mm)、糸径は7〜10μ
(中心は8μ)であつた。また、糸の引張強度は220Kg/
mm2、引張弾性率は11Ton/mm2、伸度は1.3%であつた。
Example 3 Anisotropic pitch obtained by adjusting coal tar pitch was vortexed to form fibers, and then deposited on a belt conveyor to continuously make it infusible, then carbonized at 1100 ° C., height 30 mm, width 300 mm
A bulky matte carbon fiber was obtained. Density is 0.03g / cm 3 ,
Fiber length is 20-60mm (center is 40mm), thread diameter is 7-10μ
(Center is 8μ). The tensile strength of the yarn is 220 kg /
mm 2 , the tensile elastic modulus was 11 Ton / mm 2 , and the elongation was 1.3%.

このマツトを1/2厚さにロールで圧縮後、ポリブチレン
テレフタレート(東洋紡製)をメルトさせたメルター中
に通し、絞りロールでさらに1/2厚さに圧縮し、約8mm厚
のシートを得た。このシートの電気抵抗は、体積固有抵
抗で、103〜105Ohm・cmであつた。このシートからASTM
試験方法の試片を切り出し、物性を測定した結果は、表
−3の通りであつた。
This mat is compressed to 1/2 thickness with a roll, then passed through a melter in which polybutylene terephthalate (manufactured by Toyobo) is melted, and further compressed to 1/2 thickness with a squeezing roll to obtain a sheet with a thickness of about 8 mm. It was The electrical resistance of this sheet was a volume resistivity of 10 3 to 10 5 Ohm · cm. From this sheet ASTM
The results of measuring the physical properties by cutting out the test pieces of the test method are shown in Table 3.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 D01F 9/14 7199−3B D04H 1/42 E 7199−3B 1/58 Z 7199−3B // B29C 70/10 (72)発明者 松村 雄次 兵庫県西宮市六軒町2−17−611 (72)発明者 田中 啓八郎 兵庫県伊丹市春日丘4−32−11─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Office reference number FI Technical display location D01F 9/14 7199-3B D04H 1/42 E 7199-3B 1/58 Z 7199-3B // B29C 70/10 (72) Inventor Yuji Matsumura 2-17-611 Rokugencho, Nishinomiya-shi, Hyogo Prefecture (72) Keiichiro Tanaka 4-32-11 Kasugaoka, Itami-shi, Hyogo Prefecture

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】粘稠状態にあるピツチを流出オリフイスか
ら流出させ、前記オリフイスの周りに周方向に間隔を置
いて配置した少なくとも3本の気体噴出ノズルから直線
状に高速熱気体流を吹き出させ、ここにおいて前記気体
流の各々は前記ピツチの中心軸線を横断する断面の外周
に沿う接線方向の成分と前記ピツチの流出方向に向つて
先ず前記ピツチの中心軸線に徐々に接近し次に前記中心
軸線から徐々に離れてゆく成分とを有しており、それに
より前記粘稠状態にあるピツチの流出流れが中心軸線の
周りに自転しながら徐々に細まり、繊維状にされ、渦巻
状に飛び出され、引き伸ばされて繊維化される、いわゆ
る渦流法で繊維化され堆積されたピツチ繊維を不融化、
炭化してなる密度が0.008〜0.08g/cm3の嵩高い炭素繊維
マツトに、熱可塑性樹脂を含浸させてシート状になし、
次いで成型加工することを特徴とする炭素繊維強化熱可
塑性樹脂の製造法。
1. A viscous pitch is discharged from an outflow orifice, and a high-speed hot gas stream is linearly blown out from at least three gas ejection nozzles arranged at intervals in the circumferential direction around the orifice. , Where each of the gas streams gradually approaches the central axis of the pitch and then gradually approaches the central axis of the pitch in the direction of the tangential component along the outer periphery of the cross-section crossing the central axis of the pitch and the outflow direction of the pitch. It has a component that gradually separates from the axis, whereby the outflow of the pitch in the viscous state gradually turns around the central axis while gradually thinning, becoming fibrous, and jumping out in a spiral shape. Is melted, stretched and fiberized, infusibilized Pitch fibers deposited by the so-called vortex method,
Carbonized densities of 0.008 to 0.08 g / cm 3 that are bulky carbon fiber mats impregnated with a thermoplastic resin to form a sheet,
Then, a method for producing a carbon fiber reinforced thermoplastic resin, characterized by molding.
JP61104966A 1986-05-09 1986-05-09 Method for producing carbon fiber reinforced thermoplastic resin Expired - Lifetime JPH075767B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61104966A JPH075767B2 (en) 1986-05-09 1986-05-09 Method for producing carbon fiber reinforced thermoplastic resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61104966A JPH075767B2 (en) 1986-05-09 1986-05-09 Method for producing carbon fiber reinforced thermoplastic resin

Publications (2)

Publication Number Publication Date
JPS62263232A JPS62263232A (en) 1987-11-16
JPH075767B2 true JPH075767B2 (en) 1995-01-25

Family

ID=14394844

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61104966A Expired - Lifetime JPH075767B2 (en) 1986-05-09 1986-05-09 Method for producing carbon fiber reinforced thermoplastic resin

Country Status (1)

Country Link
JP (1) JPH075767B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007084649A (en) * 2005-09-21 2007-04-05 Teijin Ltd Carbon fiber composite sheet and method for producing the same

Also Published As

Publication number Publication date
JPS62263232A (en) 1987-11-16

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