JPS5976923A - Manufacture of carbon fiber - Google Patents

Manufacture of carbon fiber

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Publication number
JPS5976923A
JPS5976923A JP18528082A JP18528082A JPS5976923A JP S5976923 A JPS5976923 A JP S5976923A JP 18528082 A JP18528082 A JP 18528082A JP 18528082 A JP18528082 A JP 18528082A JP S5976923 A JPS5976923 A JP S5976923A
Authority
JP
Japan
Prior art keywords
fibers
pitch
fiber
liquid
air
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP18528082A
Other languages
Japanese (ja)
Inventor
Isao Kimura
功 木村
Tsuyoshi Nakamori
中森 強
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.)
Kanebo Ltd
Original Assignee
Kanebo 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 Kanebo Ltd filed Critical Kanebo Ltd
Priority to JP18528082A priority Critical patent/JPS5976923A/en
Publication of JPS5976923A publication Critical patent/JPS5976923A/en
Pending legal-status Critical Current

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  • Inorganic Fibers (AREA)

Abstract

PURPOSE:To obtain continuous carbon fiber by the melt-spinning of a pitch-based raw material, by attaching a liquid to the spun fibers under specific condition, collecting the fibers, making the fibers infusible, and thermally carbonizing in an inert gas atmosphere. CONSTITUTION:Fibers obtained by the melt-spinning of a pitch-based raw material, preferably made of coal or petroleum pitch, are passed through two or more rollers made of e.g. metal and one or more destaticizers of preferably corona-discharge type, and taken up with an air sucker. The fibers are imparted with a liquid such as water, urea etc. in the air sucker or immediately after the sucker, and collected. The collected fibers are made infusible by oxidizing with air, and thermally carbonized in an inert gas atmosphere to obtain the objective continuous carbon fibers. The liquid is preferably the one inert to the fiber and capable of giving collectability and antistaticity to the pitch-based fibers.

Description

【発明の詳細な説明】 本発明はピッチ系原料を使用した長繊維状の炭素繊維の
製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing long carbon fibers using pitch-based raw materials.

従来ピッチ類はコークス、炭素材料の出発原料として大
量に消費されており、この原料全使用して跋素繊維を製
造する事が考案され、今日工業的に多量生産されている
。炭素繊維は大別してアクリロニトリル系合成繊維から
作る方法とピッチ系原料の溶融紡糸から作る方法とがあ
り、前者#:を長繊維状の湿式紡糸した原料kMP+繊
維として目的物を作るがため、その製造工程はニジドレ
ス繊維全連続的に処理する、形郷をとり、製品の姿も長
繊維状の巻き形状が標準である。面かしなからピンチ系
炭素用1ユr5’r aPIチョツプドファイバー(短
繊維)の形かそれ全原料にし゛て加工し2t−繊維製品
即ち撚り糸、フェルト、布、紙等であり、mq 11:
の長さ方向にそろった製品としてはせいぜいトつかスラ
イバーの形状比りである。これはピッチ系1駅料ケ溶融
紡糸して炭素繊維用原糸を採収する場合、kj P+の
溶明粘度のdi、1度依?r性か余りに急勾t℃である
がため紡糸VCおける糸切れのない安全操業温度域が礒
めて狭く、僅かな温度制御のむら、或は場合によれば紡
糸作業域にあ・ける不i」抗力的な変動因子、例えは微
小な気流の襄化の川き要因によっても糸切れの危険が伴
ない、それ故実1g、上アクリルニトリル繊維ヲ含め、
ナイロン、ポリエステルの4り1き溶融紡糸によって生
産される合成繊維の如くエンドレス状態で長繊維* n
<収する事が困県なのである。更に又紡糸した炭素押目
1a +u ht給自1本も僚めて脆弱であるがため、
通常の溶融紡糸仕業の方法では糸j7Jれ全頻発せしめ
、到底長繊維υ、ピッチ系繊維が探′取出米ない。、#
免一般の合成繊維における如き巻きかえしの様な通輩行
なわれている繊維の取扱いか全く出来ないと云って過言
ではない。それ故実際には長繊維状の炭素繊維の生産を
欲するにも拘らずやむを得ず短繊維の形状にらまんじて
いるのが実状でるる。現在とられている極く一般的な製
法としては溶融状台上紡糸ノズルより吐出したピッチ原
着?繊維状にして一旦は回転ボビンの上に巻き収るもa
f1記した如く原糸自体が脆弱なため所謂開巻きにも出
来す、極く僅かの薄巻きにして適宜ボビンを収りかえ、
得られた薄巻きの原糸を例えば2分割に9ノ断しスライ
バー状となすか、或は又所副遠心紡糸汰にて溶融体をノ
ズルより遠心力で振り切りバスケットに採収した後、通
常のピッチ系炭素繊維の製造工程で行われている所謂加
熱酸化による不融化処理をほどこしてから不活性ガス雰
囲気下炭化処理全行い、#望の繊維長に切断して製品と
するが如きでるり、変化があるとしてもこの最終製品に
するチョップ化段階を不融化の前、又は後に変える程度
である。
Conventionally, pitches have been consumed in large quantities as starting materials for coke and carbon materials, and it has been devised to use all of these raw materials to produce locust fibers, which are now industrially produced in large quantities. Carbon fiber can be roughly divided into two methods: one is made from acrylonitrile-based synthetic fibers, and the other is made from melt-spinning pitch-based raw materials.The former involves wet-spinning long fibers of kMP+ fibers to produce the desired product. The process involves continuous processing of rainbow-dressed fibers, and the standard shape of the product is that of long fibers. 1Ur5'rAPI chopped fiber (short fiber) for face or pinch type carbon, or it is processed into 2T-fiber products such as twisted yarn, felt, cloth, paper, etc. as raw materials, mq 11:
As a product that is aligned in the length direction, the shape is at best that of a sliver. This means that when collecting yarn for carbon fiber by melt-spinning pitch system, the melting viscosity di of kj P+ depends on 1 degree? Due to the extremely steep slope of t°C, the safe operating temperature range without yarn breakage in the spinning VC is increasingly narrow, resulting in slight irregularities in temperature control or, in some cases, defects in the spinning work area. ``There is a risk of thread breakage due to drag-related fluctuation factors, for example, factors such as the flow of minute air currents.
Endless long fibers like synthetic fibers produced by four-way melt spinning of nylon and polyester * n
<It is a prefecture that has difficulty in collecting income. Furthermore, since the spun carbon stitches 1a + u ht are also fragile,
In the usual melt spinning method, yarn j7j is generated frequently, and long fibers υ and pitch fibers cannot be found. ,#
It is no exaggeration to say that he is completely incapable of handling fibers that are conventionally used, such as rewinding, as is the case with general synthetic fibers. Therefore, even though it is desired to produce carbon fibers in the form of long fibers, the actual situation is that the shape of short fibers has to be avoided. One of the most common manufacturing methods currently in use is pitch dyeing, which is discharged from a molten table spinning nozzle. Once it is made into a fiber and wound onto a rotating bobbin, a
As mentioned in f1, since the yarn itself is fragile, it can be wound open, so it is possible to wind it very thinly and replace the bobbin as appropriate.
The obtained thinly wound raw yarn is cut into 9 pieces, for example, into two parts to form a sliver, or alternatively, the melt is shaken off by centrifugal force from a nozzle in a secondary centrifugal spinner and collected in a basket, and then usually After applying the so-called heat oxidation infusibility treatment that is carried out in the manufacturing process of pitch-based carbon fibers, the entire carbonization treatment is performed in an inert gas atmosphere, and the product is produced by cutting to the desired fiber length. The only difference, if any, is that the chopping step to form this final product is performed before or after infusibility.

ピッチ系の炭素繊維は大別して低強度、低弾性の所謂ロ
ーグレードの高強度、品弾性の・・イブレードかあり、
後inメソフ;、−ス又はブリメソフェースの液晶紡糸
による方法で・作られる。何れのタイプ共若しフィラメ
ント状態で最#藪品か得られるならは使用用途の拡大、
製造工程での製品収祉の増大による無駄の排除に貢献す
る所甚だ大きいものがある。Mえはローグレードの大き
な潜在的Wd要分ツ?であるItl #材、ブレーキ材
、断熱材、セメント建4,1等の分ツ)での石綿代替拐
トドや自動車を中心として車軸構造材−\の使用におい
て、例えはカラス繊維での代表的商品形跡であるロービ
ングが出来れば、製造工程での合理化は云うVC及ばず
、ピッチ系炭素繊維を使用する加工技術としても広範囲
なものが使えるようになる。
Pitch-based carbon fibers can be roughly divided into low-strength, low-elasticity, so-called low-grade, and high-strength, elasticity...eblades.
It is made by a method of liquid crystal spinning of in-metho-phase or brimethophane. If you can obtain the highest quality in either type or filament state, you can expand the usage.
There is a huge contribution to the elimination of waste by increasing product yield in the manufacturing process. M is a low-grade large potential Wd essential? For example, in the use of asbestos substitutes for asbestos materials, brake materials, insulation materials, cement building materials, etc., and axle structural materials mainly for automobiles, for example, glass fiber is a typical example. If roving, which is a product mark, can be created, the manufacturing process will be more rational than VC, and a wide range of processing techniques using pitch-based carbon fibers will become available.

零発す」者等はピッチ基原刺より長繊維払の炭素繊維を
得べく4νr究の結果不発り(jlr:完成した。
Those who want to obtain long-fiber carbon fiber from pitch-based raw material have failed as a result of 4νr research (jlr: completed).

本発明の目的は長繊維状のピッチ糸炭素繊維を提供する
にある。他の目的Fi斯かる繊維を工業的容易に製造す
る方法を提供するにある。
An object of the present invention is to provide pitch yarn carbon fibers in the form of long fibers. Another object of the present invention is to provide a method for manufacturing such fibers industrially and easily.

本発明方法は、ピッチ基原1’lk溶融紡糸するに除し
、少なくとも2個のロ一り一並びに少くとも1個の除電
装置111fI:介しエヤ′L”j’−1,カーを通し
て引取り、エギーサッカー内、乃至d工τ−サッカーを
通った直後に液体を付与して集束せしめ採取した糸条を
空気酸化して熱不融化し、次いで不活性気体雰囲気中で
加熱炭化せしめることケ特徴とする。
In the method of the present invention, the pitch base material 1'lk is melt-spun by at least two rotors and at least one static eliminator 111fI: air 'L''j'-1, which is taken up through the car. , Immediately after passing through the eggy sucker or the d-tech τ-sucker, a liquid is applied to collect and collect the yarn, which is oxidized in the air to make it thermally infusible, and then heated and carbonized in an inert gas atmosphere. shall be.

本発す1に適用するピッチ基原打上1.では石炭を代表
とする有機物質の乾溜によって得られるタール1に蒸留
するときに得られる黒色の炭素質固形残留物ばかりでな
くSRCと称する石゛炭液化過程或はタール採取過程で
溶剤muされた固形分、及び石AI]アスファルト類の
熱処理品が挙けられる。ポリ塩化ビニルの如きポリマー
及びテトクベンゾ7エナジンの如き低分子魁有機化合物
を熱分解せしめて作成したピッチ、更にはこれら何れの
ビ・フチ類をも不活性雰囲気上熱処理して光学的異方性
構mFMメソフェース、プリメソフェースを形成せしめ
たものも含まれる。
Pitch base launch applied to this launch 1 1. In this case, tar 1 is obtained by dry distillation of organic substances such as coal, and not only the black carbonaceous solid residue obtained during distillation, but also the carbonaceous solid residue obtained during distillation, as well as the carbonaceous solid residue that is removed as a solvent during the coal liquefaction process called SRC or the tar extraction process. Solid content and stone AI] Heat-treated products of asphalts can be mentioned. Pitches prepared by thermally decomposing polymers such as polyvinyl chloride and low-molecular weight organic compounds such as tetrabenzo7-enazine, as well as any of these bicarbonates, can be heat-treated in an inert atmosphere to produce optically anisotropic FM mesofaces. , those formed with pre-mesofaces are also included.

ピッチ系原料の@融紡糸において灯紡出原糸が脆弱なた
め通常の溶曽紡糸法合成繊維の如きボビン上への厚ひき
採取が出来ず、従って本発明方法で11長繊維状て糸条
を採収する為エヤーサッカーを使用し空気流の力を借り
て少なくとも2個のローラー並びに少くとも1個の除電
装置を介しエヤーrツカ−を通して繊維を損傷させる事
なく71イパーグンスへ収納する。こ\で使用するロー
ラーに鏡IIIJ什、ヒげ又Vi梨地仕上げの金属1J
ローラーが代表的+−,+質なるも、表面をゴム張り、
樹脂張りの物でも使用cIJ能である。1個のローラー
tユ通常紡糸ロ金より鉛直線下に#、10するのが好ま
しく、111のローラーの方は作業状況に応じて適宜位
置決めしてゆく。面しながら他のローラーの1個はファ
イバーケンスへの収納に対する引KK用りして使用する
ものであろうファイバーダンスは通常有孔円筒製で同心
状に床面で回転する円板上にe置する。
In @melt spinning of pitch-based raw materials, the lamp-spun raw yarn is fragile, so it is impossible to collect it thickly onto a bobbin like the usual melt-spinning synthetic fibers. An air sucker is used to collect the fibers, and the fibers are passed through the air sucker through at least two rollers and at least one static eliminator with the help of air flow, and stored in a 71 ipper gun without damaging the fibers. The rollers used here are Kagami IIIJ and Higemata Vi satin finish metal 1J.
Typical rollers are +- and +-quality, with rubberized surfaces,
Even those covered with resin can be used. It is preferable that one roller t is placed 10 degrees below the vertical line than the normal spinning wheel, and the roller 111 is positioned as appropriate depending on the working situation. One of the other rollers is used for pulling the fiber into the fiber can.The fiber dancer is usually made of a perforated cylinder and is mounted on a disc that rotates concentrically on the floor. place

ピッチ系原料はその楕成成分からして疎水性であり、そ
れを溶融して吐出した原糸も’i #、 、吸水性を示
さない。その為紡糸ノズルを離れて以降少くとも2個の
ローツーを介してエヤーサッカーを経由する過程におい
て#−i繊維間並びに繊維と他材料と走イ」接触する事
によりR維kまかなりの静電気を帯電し、そのま\の伏
態で作業を続ける限りロークーに巻きイ(1き、繊維切
断?起したり、たとえエヤーサッカーを経由してファイ
バーケンスに収納111米たとしても繊m束の状昨で採
取は田米ず、各単絨維毎からA合った蒙\になり到底次
の工程へ糸条形比で移行させる13!は全く不可能とな
る。
The pitch-based raw material is hydrophobic due to its ellipsoidal components, and the raw yarn produced by melting it and discharging it does not exhibit water absorption. Therefore, after leaving the spinning nozzle, during the process of passing through at least two low twos and an air sucker, a considerable amount of static electricity is generated between the R fibers and the R fibers due to contact between the #i fibers and between the fibers and other materials. As long as the work is electrically charged and the work is continued as it is, the fibers will not wind up in a low state. In recent years, the collection has been done without rice, and each single fiber has become A-matched, making it completely impossible to transfer it to the next process with the thread shape ratio.

静電気の除去とフィラメントの集束のため通常の合成繊
維で使用されている如き給油法、例えば油膜を表面に付
着させた回転ローラーの向に走行繊維全接触させるul
き方法はこの場合紡出原糸が4に喘に脆弱なため採用を
月末ない。各種油剤からなる成層中を紡出原糸が通過す
る時に受ける抵抗により原糸は殆ど紡糸/スル1tij
Vc応力が伝達され、七の個所で殆どの74う〆ントは
切断するに至る。
In order to eliminate static electricity and focus the filaments, an oiling method such as that used for ordinary synthetic fibers, such as UL, in which all running fibers are brought into contact with a rotating roller with an oil film attached to the surface.
In this case, this method will not be adopted at the end of the month because the spun yarn is fragile. Due to the resistance that the spun yarn receives when passing through stratified layers made of various oils, the yarn is mostly spun/slipped.
The Vc stress is transmitted and most of the 74 strands are cut at 7 points.

不発91方法ではエヤーサッカーを通じ又7アイパーケ
ンスに長繊維状糸条を収納する直前VCC液体付付与て
用東させる方法を採るため、紡糸ノズルより1す出され
た糸条か工A′−ダノカーに入る迄の過程でVユスト行
する繊維間の摩擦、必要により使用する集束カイト、そ
れに少く′とも2ケの【l−2−との接触時に発生ずる
静電気か繊維に蓄積し、その結果糸条の乱れ、ローシー
へのからみ寺子ν)れ原因とfz b bfゴしからさ
る現象が発生ヅる。これk iif’ Wする為、糸条
2ニー“C−→ノツカーへ4人−する迄のIll」少く
とも1りの除電装置6を設直し、糸条に蓄積した静電気
を積極0りに収り除きこれらトラブル発生原因耐消滅せ
しめる。本発明で使用する除電装置tゴ叩常Wb If
: V電(hLのコロナ放電式除電装置を用い、走行す
るピッチ系繊維の系釆に向けて設置?ffiせしめるも
のであり、lJ&雑の静電#A発生組に応じて或いね繊
11JIiの走行形白に心じて除+44装置の+i圧電
流容駕、除電装−の形状、数、及び設置位置等は簡亘選
択してよく、何等これン限走するものではない。
In the misfire 91 method, the long fibrous yarn is stored in the 7-eye percence through an air sucker, and immediately before it is stored, it is applied with VCC liquid and used. In the process of entering the fibers, the friction between the fibers as they move, the focusing kite used if necessary, and the static electricity generated when they come into contact with at least two [l-2-] accumulates on the fibers, and as a result, the thread The disorder of the rows, the entanglement with the low sea, and the phenomenon caused by fz b bf go occur. In order to do this, at least one static eliminator 6 for the yarn 2 knee "C-→Notsker to 4 people" is reinstalled to actively eliminate the static electricity accumulated in the yarn. Eliminate the causes of these troubles and eliminate them. Static eliminator used in the present invention Wb If
: This is a V-electric charge (using hL's corona discharge type static eliminator, which is installed towards the running pitch-based fiber system), and depending on the electrostatic #A generation group of lJ & miscellaneous, it is The +i voltage current capacity of the eliminator, the shape, number, installation position, etc. of the static eliminator may be easily selected keeping in mind the traveling type, and there is no limit to this.

通常除電装航の設置位置はピッチ糸繊維の集束ガイド通
過直後、各ロークー通過直後が好ましい。
Normally, the static eliminator is preferably installed immediately after the pitch yarn fibers pass through the convergence guide and immediately after each row passes.

かくしてピッチ系繊維はエヤーサッカーに欅大してファ
イバーケンスに収納するfi M)I VC霧吹きノズ
ルによる噴霧によるか、工τ−サッカーの糸条吸入孔乃
至エヤー導入孔近辺より液体を注入してピッチ系繊維糸
条表面に液体を付与する。
In this way, the pitch-based fibers are made into an air sucker and stored in a fiber can by spraying with a VC spray nozzle, or by injecting a liquid from the vicinity of the yarn suction hole or air introduction hole of the pitch-based fiber. Apply liquid to the yarn surface.

液体はエヤーサッカーを通過した直後にピッチ系繊維糸
条表向に噴霧によりイ1与するのが最適である。
It is best to apply the liquid by spraying it onto the surface of the pitch-based fiber yarns immediately after passing through the air sucker.

液体によって表面が滴らされたピッチ系繊維は液体全吸
収する事なく複数多数本のフィラメント同志が相互に付
着して集束する。そして集束したままの長繊維状糸条と
して回転しているファイバーケンスに収納される。
Pitch-based fibers whose surfaces are dripped with liquid do not completely absorb the liquid, but instead a large number of filaments adhere to each other and converge. The fibers are then stored in a rotating fiber can as long filament yarns that remain bundled.

こ\で使用する液体の目的は上記の如く疎水性のピッチ
系繊維の表向を濡らして複数多数本のフィクメンl−1
に1本の繊維束にする事にろるが、液体の役目は単にそ
れのみではない。即ちピッチ系繊維から最終目的の炭素
繊維を作るに当っては後記する如く該繊維を一旦酸化処
理する事にまり熱不融性に変換し、次いで不活性雰囲気
下所定温度に加熱して目的N&維−とするが、その工程
をとるに当っては溶融紡糸し九ピッチ系繊維を移動可能
な金属製或はセラミック製のコンベヤー上に直接振り落
すか、或は一度7アイパーケンス式所定量収納せしめて
から最終製品の商品形急に合うよう再び複数個の7アイ
バーケンスより大々一本の繊維束よりなるピッチ糸繊維
を収り出し合糸しなから酸化処理]1程に移す方法をと
る。何れの工程をとるにしても紡糸直後面体で品酵jし
た状態が時間と共に乾燥による液体含有散の質化を伴な
うので七の含有量の低下と共に集束性が低下し、&端な
場合、コンヘヤー上の移動又は7アイバーケンスより繊
維束を取出す過程において単糸間にきぼけが発生し、そ
れが単糸りj断にもつながりかねない。
As mentioned above, the purpose of the liquid used here is to wet the surface of the hydrophobic pitch-based fibers and to coat multiple pieces of fikumen l-1.
The role of the liquid is not simply to make a single fiber bundle. That is, when producing the final target carbon fiber from pitch fibers, as described later, the fibers are first oxidized to make them heat infusible, and then heated to a predetermined temperature in an inert atmosphere to produce the target N& However, in carrying out this process, the nine-pitch fibers are melt-spun and shaken directly onto a movable metal or ceramic conveyor, or they are once stored in a predetermined amount using a seven-eye percence system. After that, in order to fit the shape of the final product, the pitch fibers, which are made up of a single fiber bundle, are taken out again from the multiple 7-way fibers, and then the fibers are doubled and then oxidized. Take. No matter which process is taken, the state in which the product is fermented in the hedron immediately after spinning is accompanied by the quality of the liquid-containing dispersion due to drying over time, so as the content decreases, the cohesiveness decreases, and in extreme cases During movement on the conveyor or in the process of taking out the fiber bundle from the 7-way chain, fraying occurs between single yarns, which may lead to single yarn breakage.

丈に又か\る繊維束の移動の間に繊維相互のこすり合い
、或は繊維とローラー等の装置との接触摩擦によって静
電気が発生すれば、集束した繊維束は再びくずれ、単繊
維切断の原因となる事は勿論、所詮目的とする長繊維状
炭素繊維の作成は不iiJ能となる。かくの如く本発明
において使用する集束金目的とした面体にはたソ単に紡
糸直後の隼束性付与効果f、求めるだけに止まらず紡糸
以後不特定時間ピッチ系繊維を放置し又いる同も紡糸直
後同様の集束性効果會尭揮せしめるのと、史にνよ維束
の接動作業時に2いて静電気発生をおさえる訓電効果も
要求されるものである。
If static electricity is generated due to friction between the fibers or the contact friction between the fibers and a device such as a roller during the movement of the fiber bundle across the length, the bundled fibers will collapse again and the single fibers will be cut. Not only will this cause the problem, but it will also become impossible to create the desired long-fiber carbon fiber. As described above, the face piece intended for the binding material used in the present invention does not merely seek the effect of imparting bundle properties immediately after spinning, but also allows the pitch-based fibers to be left for an unspecified period of time after spinning. Immediately after, it is necessary to exert a similar focusing effect, and also to have a training effect to suppress the generation of static electricity when the fiber bundle is connected.

110しなから一方不発り4 K 2いて使用するピッ
チ原料#:を前記定義した如く、石炭系、石油系、それ
らの熱処理物、有機系ポリマー及び吐分子具有峨化合物
の熱分解物の1111れかよりなるか、それら物質に作
用し物理的、化学的に変質させる物質即ち活性物質を含
有する液体は当然の事なから使用出来ない。こ\で云う
作用とは紡糸直後室温下でピッチ系繊維表面を継部さぜ
る工程においてピッチ系繊維自体を膨部、膠着、且又橡
端には一部溶解せしめる如き現象1に惹起せしめる場合
に勿論のこと、紡糸以降の工程である不融化処理に2け
る空気中600℃前後の雰囲気、及び炭化処理における
不活性気体雰囲気中での最高温度800〜2000℃に
おける条件下においてもピッチ系繊維を膠着、部分溶解
せしめる如き作用のある物質紹避V)ねばならない。
110, while unexploded 4 K 2 Pitch raw materials used: As defined above, 1111 are coal-based, petroleum-based, heat-treated products thereof, organic polymers, and pyrolyzed products of emulsifying compounds. Naturally, liquids containing active substances that act on these substances and physically or chemically alter them cannot be used. The effect mentioned here is that in the process of touching the joints of the pitch fiber surface at room temperature immediately after spinning, the pitch fiber itself causes swelling and sticking, and also causes a phenomenon 1 such as partially dissolving at the ends of the pitch fiber. Needless to say, pitch-based materials can be used under the conditions of an atmosphere of around 600°C in the air during infusibility treatment, which is a process after spinning, and a maximum temperature of 800 to 2000°C in an inert gas atmosphere during carbonization treatment. Substances that have the effect of causing fibers to stick together or partially dissolve must be avoided.

不発り1に及いてピッチ系繊維に付与する液体は基本的
には(1)ピッチ系繊維に対°し不活性であり、且つ(
2)繊維に集束性及び制電性を付与すZ)ものであって
、しかも(ロ)炭化処理後灰分として残らないものであ
る。斯かる液体としては無機又は有機化合物の水溶液が
好適である。これらの化合物としては(1)水溶性であ
り且つ室温下で溶解性を旬し、(2)室気中丁吸湿性、
乃至潮解性會有し、(9空気中F4 n o℃前後の温
度において気化分解、ケ1華消滅する事が好ましい。尚
、ピッチ系繊維の不融化処理工程中に2いて繊維表面に
付着している溶質物の存在によってピッチの酸化促進に
も寄与出来れば更に望ましい。
The liquid applied to the pitch-based fibers in the misfire 1 is basically (1) inert to the pitch-based fibers, and (
2) Z) It imparts convergence and antistatic properties to the fibers, and (B) It does not remain as ash after carbonization. As such a liquid, an aqueous solution of an inorganic or organic compound is suitable. These compounds are (1) water-soluble and remain soluble at room temperature, (2) hygroscopic in room air,
It is preferable that it has a deliquescent to deliquescent property and that it evaporates and decomposes and disappears at temperatures around F4 in air (9 degrees Celsius).In addition, during the infusibility treatment process of pitch-based fibers, it is preferable that the particles adhere to the fiber surface. It would be even more desirable if the presence of solutes could also contribute to promoting pitch oxidation.

これらの諸条件を満たす化合物として有機化合物として
は原票、炭酸エチレン、カルバミン酸アンモン、クエン
酸第2アンモン、クエンm4Xsyンモン、皓石酸アン
モン、ギ酸アンモン、酢酸アンモン、シュク酸アンモン
、イソシアン酸)′ンモン、ピロガロール、レゾルシン
があり、無機化合物としては炭酸アンモノ、炭酸水素ア
ンモン、硝酸アンモン、チオシアン酸アン七ン、シアン
化アンモン、水酸化アンモニクムかある。
Organic compounds that meet these conditions include ethylene carbonate, ammonium carbamate, ammonium citrate, citric acid, ammonium oxalate, ammonium formate, ammonium acetate, ammonium succinate, isocyanic acid)' Inorganic compounds include ammonium carbonate, ammonium hydrogen carbonate, ammonium nitrate, ammonium thiocyanate, ammonium cyanide, and ammonium hydroxide.

これらの化合物d上記(1)〜(5)境目の条件?満足
し、その中でも例えば硝酸アンモンをま210℃で凡て
ガス体に分に〆し、史にその分解過程においてピッチを
空気酸化促進する触媒効果?有するので好適でるる。
Conditions for these compounds d above (1) to (5)? Among them, for example, ammonium nitrate is decomposed into a gaseous body at 210°C, and in the decomposition process there is a catalytic effect that promotes air oxidation of pitch. It is suitable because it has.

これら化合物は何れの場合も大々単独、iJ2は2神以
上の併用も可能であるが、凡て水tts r&にて使う
のか条件でろる。その場合の溶液濃度t/′i2.01
JL量以下%の範囲が好ましく、特KO,05〜10亜
量%の範囲が好呼しい。
In any case, these compounds can be used alone, and iJ2 can be used in combination of two or more, but it all depends on the conditions of use in water tts r&. Solution concentration t/'i2.01 in that case
A range of % below JL is preferred, and a range of KO, 05 to 10% is preferred.

本発明方法では上述の如くピッチ糸繊維にf、t 存す
る液体としては無機又は有機化合物の水溶6kが好適で
あるが、採収した糸条に1へ1与した液体?例えばケン
スを密封して水分蒸発?抑制する場合、又は引取り後直
ちに次工程へ送りける場合には水単独でもよい、 噴霧方式によって、ピッチ+lll1.維表面に付与す
る集束液の付首用はピッチ系酸#11に対し0.2〜4
重量%が好ましく、特に好ましくは05〜2重猷%であ
る。こVら集束液付着帳のコレトロ′−ルは噴璽へ1の
加減及び走行するピッチ系繊維に散布する噴霧ゾーンの
距離によって行う。
In the method of the present invention, as described above, the liquid present in the pitch yarn fibers is preferably an aqueous inorganic or organic compound. For example, can you seal the container and let the water evaporate? Water alone may be used when suppressing or when it can be sent to the next process immediately after collection. Depending on the spray method, pitch + lll1. For attaching the focusing liquid to the fiber surface, use 0.2 to 4 to pitch acid #11.
% by weight is preferred, particularly preferably 0.5 to 2% by weight. The core control of the focusing liquid adhesion sheet is determined by adjusting the amount of the spray and the distance of the spray zone to be sprayed onto the traveling pitch-based fibers.

不発す」方〃(VcIP、ける紡糸−引取りの一例全図
面紮もって説りjするが不発り]けこれによって何ら限
定されるもので&1ない。
(VcIP, an example of yarn spinning and take-up, will be explained with reference to all the drawings, but it will not occur) This is not intended to be limiting in any way.

即ち第1図に2いて雌1は紡糸装置に収り付けられた紡
糸用ノスルであり、原料ピッチは加熱溶融させてこのノ
ズルより空気中に吐出し、紡糸速度100〜+500m
/―で紡糸する。2け集束ガイド、ろは引取りローラー
、4#′i最終引収りローラー、5けエヤーサッカー、
6はe電気除電装置、7け液体噴′M/ズル、8は円筒
状ファイバーケンス、9は収納した長繊維状ピッチ系繊
維、10は回転円板を夫々示めす。
That is, in Fig. 1, the female 1 is a spinning nozzle housed in the spinning device, and the raw material pitch is heated and melted and discharged into the air from this nozzle at a spinning speed of 100 to +500 m.
/- to spin. 2-piece focusing guide, Roha take-up roller, 4#'i final take-up roller, 5-piece air sucker,
Reference numeral 6 designates an e-electrostatic eliminator, 7 a liquid jet M/zole, 8 a cylindrical fiber can, 9 a housed long fiber pitch fiber, and 10 a rotating disk.

ノズルより吐出したピッチ系繊維に対し必要にシbじ2
の嘔束ガイドを経由して5.4.の回転ローラーで引取
られつ\5のエヤーヴッ力−にて吸引され、噴霧ノズル
7全使用してCば捧にその繊維表ll11に付与せしめ
り一ファイバークンス8に収納する。
Squeeze the pitch fibers discharged from the nozzle as necessary.
5.4. The fibers are taken up by a rotating roller and suctioned with an air force of 5, applied to the fiber surface 11 by using all the spray nozzles 7, and stored in a fiber container 8.

この場合ファイバーケンス8は回転内板1o上に相互に
中心を合わせて設置されており、エヤーサッカー5のノ
ズル位Wtli回転円板1oの中心と7アイパーグンス
8の一端との向の他れかの位1mに鉛直線上に設置する
か、或いり又ファイバーケンス8上以外の空間位動にお
いてそのノズル方向を回転円板10の中心とファイバー
ケンス8の一端との間の何れかの位置になるように設定
せしめる。又エヤーサッカーノズル51j必要にわして
h++俊、左右、乃至円筒状に回転連動4加えてもかま
わない。
In this case, the fiber cans 8 are installed on the rotating inner plate 1o so that their centers are aligned with each other, and the nozzle of the air sucker 5 is located at one end of the center of the Wtli rotating disk 1o and one end of the 7-eye perguns 8. The nozzle may be installed at a height of 1 m on a vertical line, or the nozzle may be placed at a position between the center of the rotating disk 10 and one end of the fiber can 8 when the nozzle is moved in a spatial position other than above the fiber can 8. Set it to . Further, if necessary, the air sucker nozzle 51j may be provided with rotation interlocking 4 horizontally or cylindrically.

この場合使用する工A′−ザッカー5#ゴ糸条の総本数
、紡糸速度によりその吸引部孔径、長さ等適宜選択し、
史Vcはエヤーサッカー用の圧縮空気圧力、風量等もJ
宜選択する。尚この1程VCss−いて走行糸条の摩擦
により帯電した静電気iL6の除去装置にて積極的に取
り除く。
In this case, the suction hole diameter, length, etc. are selected as appropriate depending on the total number of A'-Zucker 5# threads used and the spinning speed.
History Vc also includes compressed air pressure, air volume, etc. for air soccer.
Choose as you like. It should be noted that the static electricity iL6 charged by the friction of the running yarn during this period of VCss is actively removed by a removal device.

繊維表面に対する妓体付与全例えは合成繊維の紡糸にお
ける如く巻取りローラー以前で行うと木兄Iダ1に係わ
るピッチ系繊維に2いては脆弱な繊維に対して液体の凝
集力が作用して糸条ifローラーに巻き付き、糸リノれ
無しに円滑にエイ−・ソーツカ−54紅山し7アイバー
ゲンス8に至らない。少くとも−Tヤーザッ力−5で繊
維糸条を吸引させる所で同時Vこ液体を滴トさせるか、
エヤーダツカ−5に吹き込む!を副空気に搬送させ′を
液体ケメイ状にしてノズル内Vl送り込むか、ノズル構
造の中で圧縮空気の入口直後に液体紮注加せしめるか、
さもなくば糸条がエヤーサッカ−5全 与する3,この様にしてファイバーケンス8に収納した
長繊維状ヒツチ糸繊維9は天々の単糸状への捌けに全く
無く完全に一本の糸条に集束きれて渦巻き形状でルーズ
に積み重なった状態で保持され、繊維の4t4傷も伺ら
娼められずに採取出来るの#′i篇くべき現象である。
For example, when applying a girdle to the fiber surface before a take-up roller, as in the case of spinning synthetic fibers, the cohesive force of the liquid acts on the brittle fibers of the pitch-based fibers involved in Kinoe Ida1. The yarn wraps around the roller and smoothly reaches A-Sotsuka-54 Beniyama 7 and 8. At the same time, drop the liquid at the point where the fiber yarn is suctioned with at least -5 force, or
Blow into Air Datsuka-5! Either by conveying it to the secondary air and sending it into the nozzle in the form of a liquid, or by injecting the liquid into the nozzle structure immediately after the inlet of the compressed air.
Otherwise, the yarn will be completely absorbed by the air sucker 5, and the long fiber hitch yarn fiber 9 thus stored in the fiber can 8 will not be separated into a single yarn at all, and will be completely formed into a single yarn. It is a remarkable phenomenon that the fibers are held in a loosely stacked state in a spiral shape, and the fibers can be collected without being exposed to 4T4 scratches.

極度に脆四で、疎水性の素材全集束された長繊維秋飽で
取得する紡糸方法は従来全く知られておらず本発明方法
において始めて実1怜に去施出米ることになった。丈に
驚くべき事に#i各車糸の脆弱さは何ら改善されたわけ
ではないが多数本の単糸が本発明に係わる液体を付着さ
せる事により一本の糸条に集束したものにはy通常の繊
維と同様の収扱いが可能なる事が1’lJ明した。
The method of spinning an extremely brittle, hydrophobic material using fully bundled long fibers has not been known in the past, and the method of the present invention is the first time that it has been successfully applied. Surprisingly, the fragility of each wheel yarn has not been improved in any way, but it has been found that the fragility of each thread has not been improved in any way, but it is It has become clear that it can be handled in the same way as ordinary fibers.

即ち必要あればファイバーケンス8に収帽したピッチ系
繊維9の喘糸奮持ちEけ他のB1<署′\$納も合糸も
出来るし、又回転状部の糸車にかけて1かせ」状態に巻
き上ける事も出来る。
That is, if necessary, it is possible to hold the pitch fibers 9 in the fiber can 8, and also to combine them with the other B1, and also to make one skein by passing them through the spinning wheel of the rotating part. It can also be rolled up.

上記の如く一旦フアイバーケンスに収納した純繊維状ピ
ッチ繊維は次いで酸化処理をtlとこして熱不融化状態
に変化せしめる。酸化処理としては主として空気を使用
する乾式と、酸化糸面体中にて行なう湿式とがあり、何
れの方法とも本発明に2いてはoJ能でちり,それを限
定するものではないが、22気中で加熱酸化する方法が
最も14便である。又それ金行う場合の長M!.維状ピ
ッチ系繊維の保持形態であるが、基本的に出来る限り繊
維表曲積を拡げて俊気と接触させるのか得策であるが、
それの実際的方法としては金属製の網状、又は有孔板上
に上記ピッチ系繊維をルーズな状態に移しかえ、そ71
を空気の存在する加熱雰囲気内を移動させなから敏維表
向より酸化を進めるのも−りの方法である。或いは又7
アイパ一ケンス自体が金網乃至4鵬性有孔筒よりなって
′2す、゛それに所定域の糸条を収納し、−U端糸をり
−rして、それを独立のロフトとなすか或は切;vfせ
ず別個のケンスと連続せしめてケンスこと、七のま\−
正気気酸化進めるのも一方法である。何れにしても酸化
に当っての8Ml+気中6JA度勾配Vユ0.6〜10
゛C/趨となし、光学的等方性m 3ttからなるヒツ
チの場合、原料ピッチの軟化温度よりも20〜150L
商い温度に迄到達せしめ、又光学的等方性格造からなる
ピッチの場合はその軟化点以下の温度に2いて各々その
最高温度域内において5分〜15時同保持する。
The pure fibrous pitch fibers once stored in the fiber cage as described above are then subjected to oxidation treatment to change them into a heat-infusible state. There are two types of oxidation treatment: a dry type that mainly uses air, and a wet type that is performed in an oxidized face. Of these, heating and oxidation is the most popular method. Long M when you do it again! .. Regarding the retention form of fibrous pitch-based fibers, it is basically a good idea to expand the fiber surface area as much as possible and bring it into contact with the agility.
A practical method for this is to loosely transfer the pitch-based fibers onto a metal mesh or perforated plate.
Another method is to proceed with oxidation from the surface of the fibers without moving the fibers in a heated atmosphere where air is present. Or 7
The eye pack itself consists of a wire mesh or a four-hole perforated tube, and the yarn in a predetermined area is stored in it, and the yarn at the end is threaded to form an independent loft. Or cut; connect it with a separate ken without vf, also known as ken, and seven ma\-
One way is to promote sanity oxidation. In any case, during oxidation, the gradient of 8Ml + 6JA in air is 0.6 to 10.
In the case of a hit consisting of ゛C/trend and optically isotropic m 3tt, the temperature is 20 to 150L lower than the softening temperature of the raw material pitch.
In the case of a pitch having an optically isotropic structure, the pitch is brought to a temperature below its softening point and maintained within its maximum temperature range for 5 minutes to 15 hours.

この同容囲気内の空気は静止状態ても、男は又積極的に
撹拌、通風状態、何れでもかまわない。
Even if the air in this same volume of air is still, the man can actively stir it or ventilate it.

史に積極的にオゾンを酸化雰囲気内にノー人する事もo
J龜である。
It is also possible to actively introduce ozone into an oxidizing atmosphere.
It's J.

不融化処理を終えた長繊維状ヒツチ糸繊維は不活性ガス
″#囲気下の加熱領域へ導き入れて加熱炭化し、殻繊維
状脚素繊維となす。この場合、炭化処理工程中の糸条の
移動は無緊張F又は緊張下何れでも可能にして加熱領域
での昇温時をて2ける温度勾配#′11〜20 ’C7
mで最高温度800〜2000゛C1そのaS温度保持
時時間〜60分で炭化処理を完了する。処1!l!後の
繊維は引張強度を充分性する炭素繊維となっており、そ
れは通常の繊維取扱い方法に従って例えばロービング秋
愚に巻きあける!]1が0J能でろる。
After the infusibility treatment, the long filament fibers are introduced into a heating area under an inert gas atmosphere and heated and carbonized to form shell fibers. The temperature gradient #'11 to 20' C7 allows movement of the temperature either under tension or under tension, and increases the temperature in the heating region.
The carbonization process is completed in 60 minutes at a maximum temperature of 800 to 2,000 C1 and a holding time of 60 minutes. Place 1! l! The latter fiber is carbon fiber with sufficient tensile strength, and it can be rolled up into a roving bag, for example, according to normal fiber handling methods! ] 1 is 0J ability.

不発11は脆弱にして吸醒性、吸水性の全くない紡出糸
を引取ローラー會介してエヤーサッカーに導入し、その
直後繊維表面に液体を付与せしめる事にて各単繊維を集
束せしめ、ボビン上に巻き収らす、長縁組状に採取した
ものを炭化することにより、従来ピッチ糸原料からね得
ることのできなかった長繊維状炭素繊維を製造し得たも
のでちり、得られた炭素m維の利用分野は広範囲にする
ものである。
In case of dud 11, the spun yarn is made fragile and has no wicking or water absorbing properties, and is introduced into an air sucker via a take-up roller. By carbonizing the long strands of carbon fiber that could not be obtained from conventional pitch yarn raw materials, the carbon The fields of application of m-fibers are wide-ranging.

以下実施例にて具体的に説明するが不発りJtjこれに
限定されるものでhない。
A detailed description will be given below with reference to examples, but the failure is not limited to this.

実施例1 平均分子ht b o o 、軟化点220℃のコール
クールピッチをベッセル型メルク−に充填し、窒素ガス
封入上列部より加熱して内M 26 (+ ’Cとなし
、m rNQ Lπコールクールピッチをギヤポンプに
て定量的に送液しつ\孔径0.5fl、孔数56個の紡
糸ノズルより系外に吐出せしめ1表面速度300tシー
で回転しているロー:7−2個を介して工〒−サッカー
にJ(pいfc oこの場合ノズル直下には集束ガイド
を孜固し、それと@10−ラーとの聞、並びに9R1ロ
ーラーと第20−クーとの間に夫々コロナ放電式静電気
除去411!+(宍戸商会製エリミノスクット)を設置
し、長繊維状ピッチ糸繊維に帯電している静電気を除去
せしめた後エヤーサッカーに吸引せしめた。こ\で使用
したエヤーサッカーは吸引(」径8請、長さ150Mの
空気旋l型にてそのノズル面下においてD、2%lL鼠
の尿素水溶液をめ、wIl維表曲表向維重り当り15重
量%の付着短で握潤させた伏動でファイバーケンスに崎
巻き秋で収納した。
Example 1 Coal cool pitch with an average molecular weight ht b o o and a softening point of 220°C is filled in a Bessel type Merck-type vessel, and heated from the upper part filled with nitrogen gas to form an inner M 26 (+'C, m rNQ Lπ Coal Cool Pitch was quantitatively fed by a gear pump and discharged out of the system from a spinning nozzle with a hole diameter of 0.5 fl and a number of holes of 56. In this case, a focusing guide is installed directly below the nozzle, and a corona discharge is applied between it and the @10 roller, as well as between the 9R1 roller and the 20th roller. A Static Eliminator 411!+ (Erimino Scutt, manufactured by Shishido Shokai) was installed to remove the static electricity charged on the long pitch yarn fibers, and then the air sucker was used to suck it in. A 2% lL mouse urea aqueous solution was poured under the nozzle surface of a pneumatic rotary type with a diameter of 8 pipes and a length of 150 m, and the fiber was gripped with a 15 wt% adhesion length per fiber weight on the curved surface of the fibers. I laid it down and stored it in a fiber can with a sakimaki fall.

仁の場合7アイパーグンス6:i’/s rpmの速度
で同芯回転し、エヤーラッカーノズルはファイノ(−ケ
ンスの中心と周辺との172のrルにの鉛直線上に位置
せしめた。
The air lacquer nozzle was positioned on a vertical line between the center and the periphery of the fine can, which rotated concentrically at a speed of 7 i'/s rpm.

紡糸(継Ht時間]10分1/&I隔で複数個の7アイ
パーケンスに大々ピッチ系繊維を採収し、終r後5個の
ダンスより大々集束糸會取出し、それt1本に合糸した
後その端糸をステンレス製金明上に蛇行状に長繊維状糸
条を並べ最高m度500℃に保持した加熱炉の中を通し
アヒっこの場合糸条の移動は温度勾配置“C/#lI+
、 500℃保持時向20分になるようにした。加熱炉
から取った糸条は焔にさらしても不溶融状態になってい
た。この不融化処理した糸条をステンレスの金網の上に
無緊張状態に乗せたま\中心部温度1000℃で窒素ガ
ス′5I:流動させた電気p中r移励きぜた。仁の場合
、温度勾配5’C/Il’l!、最高IWK + 00
 T) ”Cの保持時間10分になるよう条件設定して
長繊維状糸条を炭化した。かくシ、てフールクールピッ
チを原料に開用し長1代維状の炭素繊維を採取した。こ
の繊維の物件は絨維径16I・、引張強度80ル(il
/a4、引張弾性率2900へq/−てあ−11ヒ。
Spinning (spinning Ht time) Collect large pitch fibers in multiple 7-eye percense at intervals of 10 minutes, 1/&I, and after the end, take out a large bundle of yarns from 5 dances and combine them into 1 thread. After threading, the end threads are arranged in a meandering pattern on a stainless steel metal plate and passed through a heating furnace maintained at a maximum temperature of 500°C. /#lI+
, 500°C was maintained for 20 minutes. The yarn taken from the heating furnace remained unmelted even when exposed to flame. The infusible yarn was placed on a stainless steel wire mesh in a non-tensioned state and agitated in an electrically flowing nitrogen gas '5I at a center temperature of 1000°C. In the case of Jin, the temperature gradient is 5'C/Il'l! , highest IWK + 00
T) The long fibrous yarn was carbonized under conditions such that the C retention time was 10 minutes.Fur Cool Pitch was then used as a raw material and long 1 generation carbon fiber was collected. This fiber material has a fiber diameter of 16I and a tensile strength of 80L.
/a4, tensile modulus of elasticity 2900q/-tea-11hi.

尚比較実験として、尿素水溶面の噴霧勿しない以外tj
几て同じ条件下で紡糸した所、エギーツ゛ツカ−から噴
S#された繊維kま中糸リノれ奮起しつ\単糸相転にか
らA右い、時にね粉化し、部分的に繊維状倉とソめると
しても塊状になったま\で長繊維状糸条形部の収り田し
は全く出来なか。た、。
As a comparative experiment, tj
When the fibers were spun under the same conditions, the fibers spouted from the egg twister were stirred up, and the single yarn phase change occurred. Even if it were to be soaked, it would remain in the form of a lump, and the long fiber-like filamentous part could not be collected at all. Ta,.

実施例 平均か子厭800、軟化点245 ”Cの溶剤精岐炭(
略称5RC)′に実施例1と同じ紡糸装置ftに充填し
、4!t$、封入上内温を270 ’Cに加熱して溶融
し、u、15m径の孔11111個全有するノズルより
吐出し、表1111速度500 MI/Mで回転してい
るローラー2個全ブトしてエギーザノ力−に導いたっ繊
維の走行途中に実施例1と向しく2個の静電気除去機k
 2 +&した。エヤーサッカーノズルはファイバーケ
ンス頭上性向辺より20cn1隔れた場所に置き。
Examples: Solvent refined charcoal with an average molecular weight of 800 and a softening point of 245"C.
Abbreviation 5RC)' was filled into the same spinning device ft as in Example 1, and 4! t $, heated the inner temperature of the sealed top to 270 'C to melt it, u, discharged from a nozzle with 11111 holes of 15 m diameter, Table 1111 2 rollers rotating at a speed of 500 MI / M all but During the running of the fibers, two static electricity eliminators were installed in the same direction as in Example 1.
2 +&. Place the air sucker nozzle at a distance of 20 cm from the fiber can overhead side.

そのノズル方向をケンス周辺位1−jより中心に回。Rotate the nozzle direction from 1-j around the can.

てケンス半径の176fζなる角度で設置した。面して
エヤーサッカーノズルの直下に鳴動装置を置き、硝酸ア
ンセン0.5亀量%水溶液をもってエヤーサッカーノズ
ルより吐出して来るピッチ系−維に回って散布した。こ
の場合集束面の付着、m、け0.6本量%になるよう噴
tittikk調節した。
It was installed at an angle of 176fζ of the can radius. A ringing device was placed directly below the air sucker nozzle, and a 0.5 weight percent aqueous solution of anthene nitrate was sprayed around the pitch fibers discharged from the air sucker nozzle. In this case, the injection amount was adjusted so that the adhesion on the focusing surface was 0.6%.

かくして集束液で繊維表面?湿潤させる事により100
フイラメントを1木の集束糸となして渦巻状に71イバ
ーケンス内に収納した。ファイバーケンス10個より大
々1木の集束糸計10本を収り出し、それを1本に合糸
しつ\その長繊維状糸条全実施例1と同一条件下、先ず
移動式で空気中最高温度270℃に迄加熱し九所、各繊
維向の膠着なしに熱不融化出来、更に最高湯度1100
℃迄昇酷速度7℃/罐で加ピ〆〜し、+ l OrじC
で15分保持しつ\炭化処理した所、繊維径14μ、引
張強度90kQ/、4、引張弾性帯521〕口Af/−
の長繊維状糸条に&維が得られた。得られた繊維tユロ
ーピング形状に巻き触る皇が出来/と。
Thus, fiber surface with focusing liquid? 100 by moistening
The filament was made into a single bundled thread and housed in a spiral shape in a 71 Iverkens. A total of 10 bundled yarns of one tree were collected from 10 fiber cans, and they were combined into one long fiber-like yarn. Under the same conditions as in Example 1, first, they were heated in a mobile air conditioner. It can be heated to a maximum temperature of 270℃ in nine places, making it heat infusible without sticking to each fiber direction, and furthermore, the maximum hot water temperature is 1100℃.
℃ ramp rate 7℃/can, + l OrjiC
After being held for 15 minutes and carbonized, the fiber diameter was 14 μ, the tensile strength was 90 kQ/, 4, the tensile elastic band 521] mouth Af/-
& fibers were obtained in the long fibrous filaments. The resulting fiber can be rolled into a roping shape and touched.

尚この場合、放電式静電気除去機を設置しないで上記集
束液のみを工六′−ワッカーノズル1u下でnQ71j
する方式を採った所、vJ糸ノズルから吐出したビ・ノ
チ砿41! Fi静電気発生か著しく、゛走イ]糸は」
L糸4Uに拡かり、第10−ラー表面においで巻き付き
、エヘ′−・サッカーの位161 K迄繊維の移動か困
難となり、到底長繊維状糸条としてピッチ系繊維を採収
する41 tit、 Ill来なか、た。
In this case, without installing a discharge-type static electricity remover, only the above-mentioned focusing liquid was applied under the Wacker nozzle 1u.
When we adopted this method, 41 pieces of bi-nochi was discharged from the vJ thread nozzle! Fi static electricity was generated, and the thread ran.
The L yarn spreads to 4U, wraps around the surface of the 10th layer, and it becomes difficult to move the fibers up to the 161K position, making it impossible to collect pitch-based fibers as long fibrous yarns. Ill never come.

実施例 炭素含有量90.2亀蓋%、キノリンネ溶分1j重祉%
のグロシアスファルトを4ツロフシスコに充填し、窒素
ガス気流下十分撹拌しなから内TMヲ420’Cに保っ
て6時間熱分解、重縮合をλ11め軟化点280℃、キ
ノリンネ溶分411<if%の光学的異方性構造を有す
るメソフェースピッチを得た。
Example carbon content 90.2%, quinolinium solubles 1j%
of Glossia asphalt was packed into a 4-tube container, stirred thoroughly under a nitrogen gas flow, and then thermally decomposed for 6 hours while keeping the internal temperature at 420'C. The polycondensation was carried out at λ11, the softening point was 280°C, and the quinoline solubility was 411<if A mesoface pitch with an optically anisotropic structure of % was obtained.

このピッチを内温ろ70℃に保つて溶融し1.孔径01
禦1孔&2’io個の紡糸ノズルよりノズル表面温度5
511 ℃に保持して吐出せしめ、集束カイト、及び静
電気除去機全径由して表面1京度600m/X?+I+
の回転ローシーに接触せしめ、更に静電気除去機を介し
て同じ表面速度の引取りローラーを経てエヤーサッカー
ノズルに吸引せしめた。エキ−ザラ力・−ノズルの位I
Mは実施例1と同じにした。
This pitch is melted by keeping it at an internal temperature of 70°C.1. Hole diameter 01
Nozzle surface temperature 5 from 1 hole &2'io spinning nozzles
Maintain the temperature at 511 degrees Celsius and discharge it, use a focusing kite, and a static eliminator to remove the surface at 1 trillion degrees 600 m/x? +I+
The sample was brought into contact with a rotating roller sheath, and was then sucked into an air sucker nozzle via a static electricity remover and a take-up roller with the same surface speed. External force - Nozzle position I
M was the same as in Example 1.

集束液としては酢酸アンモン0.5粗麺%と水酸化アン
モニウム[J、 4重量%の混合水溶液ケ用いた。
As the focusing liquid, an aqueous mixed solution of 0.5% by weight of ammonium acetate and 4% by weight of ammonium hydroxide was used.

この水#′F液ケエヤーサッカーの空気導入孔の下部に
圧加ゼしめノズル孔内に吸引したピッチW&維の表面に
霧状で付着するように5なし繊維に対し1重i!96付
41−1シめてファイバークンス内に渦巻キ状で集束糸
2採取した。
This water #'F liquid is pressurized at the bottom of the air inlet hole of the air sucker and applied to the surface of the pitch W & fibers sucked into the nozzle hole so that it adheres in the form of a mist to the surface of the fibers. 96, 41-1, and two bundled yarns were collected in a spiral shape inside the fiber kunsu.

得られた繊維は60%qa、25℃の室内に1週向放九
した後合糸するため、ケンス4個より大々1木の集束糸
を取り出し巻上はガイドヶ経由して金網上に杉・しか、
t’を行った所1本1木の集束系は静電気発生V5よる
単糸Vj:なれ現象を全く発生せず紡糸時集束した状1
.・i2のチ\の形状にて合計1000フイラメント数
の合^1.た長繊維状糸条として収り扱う$が出来た。
The obtained fibers are 60% qa, and are left in a room at 25°C for one week before being combined. To do this, one piece of bundled yarn is taken out from four cans, and the yarn is wound onto a wire mesh via a guide. ·deer,
When t' was carried out, the convergence system of each tree was a single yarn Vj due to static electricity generation V5: a state of convergence during spinning without any curling phenomenon1
..・The total number of filaments is 1000 in the shape of i2. This resulted in the creation of $, which can be stored and handled as a long fibrous yarn.

この糸条を最高温度240 ”Cに保持した加熱炉の中
を空気の存在下級高温度保持時間1時間になるよつ通i
・亡しめて熱不融化せしめ、史に−f:の糸条に+80
11℃に床ワた窒素気流雰囲気中を移−υノ]j (、
めて艮繊刊状炭素繊維がイ(すられた。この繊維1」繊
径10μ、引張強度195んQ/a4 ’、引張弾性率
18.00 tl Kq/−の物性を有した。
This thread was passed through a heating furnace held at a maximum temperature of 240"C for 1 hour in the presence of air.
・Destroy it and make it heat infusible, +80 to the thread of -f: to the history
Transfer the mixture to 11°C under a nitrogen stream atmosphere.
For the first time, the fiber-like carbon fiber had physical properties of 1'' diameter of 10 μ, tensile strength of 195 mm Q/a4', and tensile modulus of 18.00 tl Kq/-.

尚この実願例にあ・いて放電式静電気除去機を設置〆1
ぜず、又エギーサッカーノズル内において集束蔽1ζ1
与?fjなわないで紡糸rした所、先ず第10−シーに
&−いてピッチ糸#R維の巻き付き?起こし純繊維状糸
条として採収する事は出来なか−Iた。
In addition, in accordance with this application example, we installed a discharge type static electricity remover.1
Also, in the egg sucker nozzle, the focusing shield 1ζ1
Give? When the yarn was spun without fj, first of all, the pitch yarn #R fiber was wrapped around the 10th sea. It was not possible to collect it as a pure fibrous thread.

4、 図i1o 〕17.+ fit i説す」第1図
二勲#集;訓は不発用の実施鍬様の一例?示す紡糸方法
の説り1図である。
4, Figure i1o ] 17. + Fit i explanation" Figure 1 Nihon #Collection; Kun is an example of a dud implementation hoe? FIG. 1 is a diagram illustrating the spinning method shown in FIG.

Claims (1)

【特許請求の範囲】 (1)  ヒツチ基原PI ’を溶融紡糸するにI祭し
、少なくとも2個のローラー並びに少くとも1個の除電
装置?介しエギープ1カー全通して引取り、エヤーサッ
カー内、乃至はエヤーサッカーを通った直後に(伐体紮
付与して集束せしめ採収した糸条を空気酸化して熱不融
化し、次いで不活性気体雰囲気中で加熱炭化せしめるこ
とを特徴とする長*維状ピッチ系炭素繊維の製造方法。 (2)  ピッチ系原料が石炭系又は石113系のもの
でろる特許請求の範囲第1項記載の方法。 (5)除電装置がコロナ放電式である特許請求の範囲第
1項記載の方法。 (4)液体がピッチ系繊維に不活性のものである特許請
求の範囲第1Jr4記載の方法。 (5)液体かピッチ系m維に集束性及び訓電性を付与す
るものである特許請求の範囲第1項記載の方法。 (6)液体が水系でろる特許請求の範囲第1項記載の方
法。 (71液体全噴霧により付与する特fI−請求の範囲第
1填記載の方法。 (8)熱不融化を0.5〜I O”C/ III/lの
昇温速度で行なうIF#IP請求のa間第1墳記載の方
法。 (9)炭化を800〜2000℃の温度で加熱する特許
請求の範囲第1項記載の方法。
[Claims] (1) Is it suitable for melt-spinning Hitachi base material PI', at least two rollers and at least one static eliminator? The entire eggyp car is picked up through the air sucker, or immediately after passing through the air sucker (the threads are bundled and collected by air oxidation to make them infusible, and then inert. A method for producing long* fibrous pitch-based carbon fibers, which is characterized by carbonizing the fibers by heating in a gas atmosphere. (2) The method according to claim 1, wherein the pitch-based raw material is a coal-based or stone-based material. Method. (5) The method according to Claim 1, wherein the static eliminator is a corona discharge type. (4) The method according to Claim 1, Jr. 4, wherein the liquid is inert to pitch-based fibers. ( 5) The method according to claim 1, in which a liquid imparts focusing properties and conductive properties to pitch-based m-fibers. (6) The method according to claim 1, in which the liquid is aqueous. (71 Feature fI applied by full liquid spraying - method according to claim 1. (8) IF#IP in which thermal infusibility is carried out at a heating rate of 0.5 to IO"C/III/l The method described in claim 1. (9) The method described in claim 1, wherein carbonization is performed by heating at a temperature of 800 to 2000°C.
JP18528082A 1982-10-20 1982-10-20 Manufacture of carbon fiber Pending JPS5976923A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18528082A JPS5976923A (en) 1982-10-20 1982-10-20 Manufacture of carbon fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18528082A JPS5976923A (en) 1982-10-20 1982-10-20 Manufacture of carbon fiber

Publications (1)

Publication Number Publication Date
JPS5976923A true JPS5976923A (en) 1984-05-02

Family

ID=16168069

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18528082A Pending JPS5976923A (en) 1982-10-20 1982-10-20 Manufacture of carbon fiber

Country Status (1)

Country Link
JP (1) JPS5976923A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60252722A (en) * 1984-05-30 1985-12-13 Idemitsu Kosan Co Ltd Production of carbon fiber
JPS6170016A (en) * 1984-09-10 1986-04-10 Idemitsu Kosan Co Ltd Production of carbon yarn
JPS62282025A (en) * 1986-05-26 1987-12-07 Osaka Gas Co Ltd Production of pitch carbon yarn
JPS63282314A (en) * 1987-05-14 1988-11-18 Mitsubishi Kasei Corp Method for taking off pitch fiber tow
CN103015154A (en) * 2012-12-03 2013-04-03 天津工业大学 Method for improving tensile strength of carbon fiber by utilizing carbon nano tubes
CN103046311A (en) * 2012-12-03 2013-04-17 天津工业大学 Method for improving carbon fiber tensile strength

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60252722A (en) * 1984-05-30 1985-12-13 Idemitsu Kosan Co Ltd Production of carbon fiber
JPS6170016A (en) * 1984-09-10 1986-04-10 Idemitsu Kosan Co Ltd Production of carbon yarn
JPS62282025A (en) * 1986-05-26 1987-12-07 Osaka Gas Co Ltd Production of pitch carbon yarn
JPS63282314A (en) * 1987-05-14 1988-11-18 Mitsubishi Kasei Corp Method for taking off pitch fiber tow
CN103015154A (en) * 2012-12-03 2013-04-03 天津工业大学 Method for improving tensile strength of carbon fiber by utilizing carbon nano tubes
CN103046311A (en) * 2012-12-03 2013-04-17 天津工业大学 Method for improving carbon fiber tensile strength

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