JPS6285031A - Melt-spinning of pitch - Google Patents

Melt-spinning of pitch

Info

Publication number
JPS6285031A
JPS6285031A JP22364085A JP22364085A JPS6285031A JP S6285031 A JPS6285031 A JP S6285031A JP 22364085 A JP22364085 A JP 22364085A JP 22364085 A JP22364085 A JP 22364085A JP S6285031 A JPS6285031 A JP S6285031A
Authority
JP
Japan
Prior art keywords
pitch
spinning
melt
degassed
discharged
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
JP22364085A
Other languages
Japanese (ja)
Inventor
Tadayuki Matsumoto
忠之 松本
Tomonori Iwami
知典 岩見
Michihiro Shiokawa
塩川 満弘
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP22364085A priority Critical patent/JPS6285031A/en
Publication of JPS6285031A publication Critical patent/JPS6285031A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:Pitch is melted, degassed and extruded, as the heat history which the pitch undergoes is being controlled, at specific conditions, to obtain carbon fiber stably without yarn breakage and void formation. CONSTITUTION:At first pitch is melted and degassed usually by treating it with reduced pressure. Then, the pitch is extruded out of the nozzles as the heat history the pitch undergoes is being controlled so that the amount of gas formed by pyrolysis becomes less than 0.2ml per 1g of pitch. The spinning of the pitch is preferably effected using a vented extruder.

Description

【発明の詳細な説明】 [産業上の利用分野1 本発明はピッチの溶融紡糸方法に関する。更に詳しくは
発泡による糸切れ、ボイドの発生等が改良されたピッチ
の溶融紡糸方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application 1] The present invention relates to a pitch melt spinning method. More specifically, the present invention relates to a pitch melt-spinning method in which yarn breakage and void generation due to foaming are improved.

[従来技術] ピッチを溶融紡糸して炭素繊維を得る方法としては、例
えば特開昭59−157309号記載の方法等がよく知
られている。
[Prior Art] As a method for obtaining carbon fibers by melt spinning pitch, for example, the method described in JP-A-59-157309 is well known.

しかしながら、溶融紡糸に用いられるピッチは、加熱に
より熱分解・重縮合等の反応を起こすため紡糸中に発泡
する。特に高強度・高弾性率の炭素繊維を得るために使
用されるメソフェーズピッチは、通常紡糸温度が300
 ’Cを越えるため紡糸温度において上記反応による発
泡が起こりやすく紡糸時のトラブルを起こしやすい。
However, the pitch used in melt spinning causes reactions such as thermal decomposition and polycondensation when heated, so it foams during spinning. Mesophase pitch, which is used to obtain particularly high-strength and high-modulus carbon fibers, is usually spun at a spinning temperature of 300°C.
Since the temperature exceeds 'C, foaming due to the above reaction is likely to occur at the spinning temperature, which tends to cause problems during spinning.

さらに、紡糸用ピッチはピッチを調整する際に吸着・溶
解した有機ガス成分やハンドリング時に吸着して水分お
よび表面酸化物に起因する二酸化炭素などの無機ガスな
どのため紡糸時に溶融すると発泡する。
Furthermore, pitch for spinning foams when melted during spinning due to organic gas components adsorbed and dissolved during pitch adjustment and inorganic gases such as carbon dioxide caused by water and surface oxides adsorbed during handling.

上記の理由で生じた泡は系中のボイドとなったり、紡糸
時の糸切れの原因になる。
Bubbles generated for the above reasons may cause voids in the system or cause yarn breakage during spinning.

[発明が解決しようとする問題点] 従って本発明の目的は、発泡による問題のないピッチの
溶融紡糸方法を提供することにおる。
[Problems to be Solved by the Invention] Accordingly, an object of the present invention is to provide a pitch melt-spinning method that is free from problems caused by foaming.

[問題点を解決するための手段] 本発明は、ピッチを溶融後、脱ガス処理を行ない、次い
で処理されたピッチを口金から吐出させる際に、脱ガス
後吐出されるまでにピッチが受ける熱履歴を、熱分解ガ
ス発生ψがピッデー10当り0.2m+以五とへ64よ
うにすることを特徴とするビツヂの溶融紡糸方法である
[Means for Solving the Problems] The present invention is designed to reduce the heat that the pitch receives after it is degassed and before it is discharged, when the pitch is degassed after being melted and then the treated pitch is discharged from the die. This is Bituji's melt-spinning method, which is characterized in that the pyrolysis gas generation φ is 0.2 m+5 or more per 10 piddays.

ビッヂを溶融する際に発生する11機ガス、水、二酸化
炭素等(、二起因する泡は溶融ピッチに脱ガス処理を施
すことにより除かれる。脱ガス処理としては通常溶融し
たピッチを減圧処理づ−る方法が用いられる。例えば、
溶融したビッヂの貯槽を減)土にして、脱泡したり、ベ
ントエクストルーダを用いて脱ガス処理を行なうことか
できるが、脱ガス処理時の比表面積を可能な限り大ぎく
iノでおくのが好ましい。
Bubbles caused by gases, water, carbon dioxide, etc. (2) generated when melting pitch are removed by degassing the molten pitch. Degassing is usually done by treating the molten pitch under reduced pressure. For example,
It is possible to degas the molten bits by turning the storage tank into soil and degassing them, or by using a vent extruder, but it is important to keep the specific surface area as large as possible during the degassing process. is preferred.

しかしながら、ピッチは加熱により前記した様に熱分解
、重縮合等の反応に起因するメタン、丁タン、王ヂレン
等の有機ガスを発生ずるIこめ、脱泡処理を行なった後
ピッチを紡糸孔から吐出させるまでの熱履歴が重要とな
る。熱分解、重縮合等の反応は第1図に示V様に350
〜370℃以上で顕著となるが、第1図に示す様にピッ
チの種類によりガス発生量の温度依存性がわずかづつ異
なっている。
However, as described above, pitch generates organic gases such as methane, methane, and chlorine due to reactions such as thermal decomposition and polycondensation as described above.After defoaming treatment, the pitch is removed from the spinning hole. The thermal history up to discharge is important. Reactions such as thermal decomposition and polycondensation are carried out as shown in Figure 1.
This becomes noticeable at temperatures above 370 DEG C., and as shown in FIG. 1, the temperature dependence of the amount of gas generated differs slightly depending on the type of pitch.

一方溶融紡糸を行なう際に、発泡による糸切1′1.、
ボイド等の問題を起こさない様(こJるため14二は、
ピッチ1g当りのガス発生量が062m1」ス下どイf
る様に、脱ガス処理後、吐出孔から吐出り−る土ての熱
履歴を制御3n ty ′)つ紡糸する必要がある。
On the other hand, when performing melt spinning, thread cutting 1'1 due to foaming. ,
In order to avoid problems such as voids, 142 is
The amount of gas generated per 1g of pitch is 062m1.
After the degassing treatment, it is necessary to control the thermal history of the clay discharged from the discharge hole so that the yarn can be spun.

ピッチ1g当りのガス発生量は、ピッチを所定温度の窒
素中1.m10分間保持(1,た後、雰囲気を再び窒素
と交換し、溶融時【4二発生するガスの脱ガス処理を行
ない、次いで所定温度で所定時間保持し、その際発生し
たC1〜C3Q)6機ガスをガスクL1を用いて測定し
・合計覆゛る方法で求める。
The amount of gas generated per gram of pitch is 1. After holding for 10 minutes, the atmosphere was replaced with nitrogen again, and the gases generated during melting were degassed, and then held at a specified temperature for a specified period of time, C1 to C3Q generated at that time.6 Measure the machine gas using gask L1 and find it using the total overlapping method.

ガス発生芋と熱履1楚どの関係は第1図に示す様にピッ
チにより異なっているので、紡糸時の脱ガス後ピッチを
吐出づ゛るまでの間の熱履歴は、用いるピッチ毎に限界
を決定する必要がある。
As shown in Figure 1, the relationship between the gas-generating potato and the heat pump differs depending on the pitch, so the thermal history after degassing during spinning until the pitch starts to be discharged has a limit depending on the pitch used. need to be determined.

溶融ビッヂを貯留し、ピッチ表面から減圧処理等を行な
って脱泡し、次いでこの溶融ピッチを旧最ポンプ等で排
出しながら口金から吐出させて紡糸する、いわゆるポッ
ト型の紡糸機の場合、減圧処理とピッチの計量排出を同
時に行なうのは圧力バランスの点て田難であり、また減
圧処理と計」排出とを交豆に行なうとピッチの滞留時間
が一定にならないため、これらの問題を生じないベント
タイプエクス1〜ルーダを使用するのが好ましい。
In the case of a so-called pot-type spinning machine, the molten pitch is stored and degassed by depressurizing the pitch surface, and then discharged from the spinneret while being discharged by a pump, etc., and spun. It is difficult to maintain the pressure balance when processing and discharging pitch at the same time, and if the depressurization treatment and discharging are carried out at the same time, the retention time of the pitch will not be constant, resulting in these problems. It is preferable to use vent type Ex 1 to Ruda.

本発明は光学的に等方l−異方斗のいずれのピッチにも
使用できるが、光学的異方i生のいわゆるメソツー丁−
ズピッチの場合紡糸温度が300°C以上と高温になり
発泡の問題か起こりヤずいので、本発明の効果が大きい
Although the present invention can be used for any optically isotropic l-anisotropic pitch, the so-called meso-to-isotropic pitch of the optically anisotropic i-pitch can be used.
In the case of spun pitch, the spinning temperature is as high as 300° C. or higher, which can lead to foaming problems, so the present invention is highly effective.

以上本発明を実施例へ挙げて更に訂細に′説明する。The present invention will be explained in more detail by referring to examples.

なお実施例中の測定方法は以下に示す方法による。In addition, the measurement method in the examples is based on the method shown below.

光学的異方性 試料をエポキシ系、樹脂に包埋したあと、常法により研
磨した。研摩面をl−e’itz社製0RTHOPLA
N:顕微鏡を用いて反射偏光法tこより観察した。光学
的異方性成分の存在帛は、前記した偏光下で観察した時
の等方性部分と異方性部分の面積化から求めた。。
After embedding the optically anisotropic sample in epoxy resin, it was polished by a conventional method. Polished surface with l-e'itz 0RTHOPLA
N: Observation was made using a reflective polarization method using a microscope. The presence structure of the optically anisotropic component was determined by calculating the area of the isotropic part and the anisotropic part when observed under polarized light as described above. .

キノリンネ溶分 J I S −に−2425に規定される遠心分離法と
;濾過法と8粗合けた方法で行なった。
The quinoline solution was carried out by a method that was a combination of the centrifugation method specified in JIS-2425 and the filtration method.

軟化点 温度勾配を昔する)フルミ(反。七に杓砕した1ゴツヂ
を置き、2分1着(こやわらかい筆でアルミ牛反−にの
ピッチ粉末を除き、溶融か開始し・た位置の温度から軟
化点を求める。
Place one piece of crushed gotsuji in a bowl and use a soft brush to remove the pitch powder from the aluminum bowl and place it at the point where it started melting. Determine the softening point from the temperature.

[実施例] コールタールd3よび」−・ルタールピップを表1に示
す条件で水素化したII 350℃で蒸溜し水素化ピッ
チを得た。次いで表1に示″リー条件℃熱処理し3種類
のメソノエーズピッヂを得た。得られたピッチの特性を
表2に示す。これらのピッチを表3に示1−条件でベン
トエクス1〜ルーダに通し60mmHgの減圧上で脱ガ
ス処理を行な−)だ後、表4に示す各種熱履歴を与えな
がら0.2戸、100ト(口金から吐出させ、450m
/minで引き取り直径14μのグリーンフフイパを1
1だ。結果を表4に示す。また同一ピッチを表4に示し
た熱履歴で明細書記載の方法で熱分解ガス発生量を測定
し、同じく表4に示した。実験N、1.3.5はいずれ
も熱分解ガス発生口が0. 2ml/gピッチ以下であ
り良好な紡糸性を示した。一方、実験N、2.4,6゜
7はいずれも熱履歴が大きく、熱分解ガス発生量が0.
2ml/gピッチを越えるため、紡糸時に泡による糸切
れを生じたり、系中にボイドを生じたりする問題が起っ
た。
[Example] Coal tar d3 and Lutar pip were hydrogenated under the conditions shown in Table 1. Hydrogenated pitch was obtained by distilling at 350°C. Next, three types of mesonoaze pitches were obtained by heat treatment under the conditions shown in Table 1. The characteristics of the obtained pitches are shown in Table 2. After degassing treatment at a reduced pressure of 60 mmHg through a ruder, 0.2 doors, 100 tons (discharged from the nozzle, 450 m while giving various thermal histories shown in Table 4)
1 green pipe with a diameter of 14μ is picked up at a rate of 1
It's 1. The results are shown in Table 4. Further, the amount of pyrolysis gas generated was measured using the method described in the specification using the thermal history shown in Table 4 for the same pitch, and the results are also shown in Table 4. In both experiments N and 1.3.5, the pyrolysis gas generation port was 0. The pitch was 2 ml/g or less, indicating good spinnability. On the other hand, experiments N, 2.4, and 6°7 all had large thermal histories, and the amount of pyrolysis gas generated was 0.
Since the pitch exceeds 2 ml/g, there were problems such as yarn breakage due to bubbles during spinning and voids in the system.

表2 [発明の効果] 本発明の溶融紡糸方法によりピッチ紡糸時の発泡による
糸切れ、糸のボイド発生を防止することができ、炭素繊
維の強度式■を起こさずに安定して炭素繊維を得ること
ができる。
Table 2 [Effects of the invention] The melt spinning method of the present invention can prevent yarn breakage and yarn voids due to foaming during pitch spinning, and can stably produce carbon fibers without causing carbon fiber strength formula (■). Obtainable.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は実施例中の各種ピッチを10分間熱処理した時
の処理温度と熱分解ガス発生量どの関係図でおる。 2Eo     ’1lo5    12o    3
4t)     h&039゜処 叩 i!IJI(℃
1 iI′11  図
FIG. 1 is a diagram showing the relationship between the treatment temperature and the amount of pyrolysis gas generated when various pitches in Examples were heat-treated for 10 minutes. 2Eo '1lo5 12o 3
4t) h & 039° place hit i! IJI(℃
1 iI'11 Figure

Claims (1)

【特許請求の範囲】[Claims] ピッチを溶融後、脱ガス処理を行ない、次いで処理され
たピッチを口金から吐出させる際に、脱ガス後吐出され
るまでにピッチが受ける熱履歴を、熱分解ガス発生量が
ピッチ1g当り0.2ml以下となるようにすることを
特徴とするピッチの溶融紡糸方法。
After melting the pitch, degassing treatment is performed, and then when the treated pitch is discharged from the die, the thermal history that the pitch undergoes after degassing and before being discharged is determined by the amount of pyrolysis gas generated per 1 g of pitch. A method for melt spinning pitch, characterized in that the pitch is 2 ml or less.
JP22364085A 1985-10-09 1985-10-09 Melt-spinning of pitch Pending JPS6285031A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22364085A JPS6285031A (en) 1985-10-09 1985-10-09 Melt-spinning of pitch

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22364085A JPS6285031A (en) 1985-10-09 1985-10-09 Melt-spinning of pitch

Publications (1)

Publication Number Publication Date
JPS6285031A true JPS6285031A (en) 1987-04-18

Family

ID=16801358

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22364085A Pending JPS6285031A (en) 1985-10-09 1985-10-09 Melt-spinning of pitch

Country Status (1)

Country Link
JP (1) JPS6285031A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002040754A1 (en) * 2000-11-15 2002-05-23 Conoco Inc. Pre-spinning treatment process for solvated mesophase pitch

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58115120A (en) * 1981-12-28 1983-07-08 Nippon Oil Co Ltd Preparation of pitch type carbon fiber
JPS6134213A (en) * 1984-07-24 1986-02-18 Dainippon Ink & Chem Inc Manufacture of pitch fiber

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58115120A (en) * 1981-12-28 1983-07-08 Nippon Oil Co Ltd Preparation of pitch type carbon fiber
JPS6134213A (en) * 1984-07-24 1986-02-18 Dainippon Ink & Chem Inc Manufacture of pitch fiber

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002040754A1 (en) * 2000-11-15 2002-05-23 Conoco Inc. Pre-spinning treatment process for solvated mesophase pitch

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