JPS6245718A - Polyester yarn - Google Patents

Polyester yarn

Info

Publication number
JPS6245718A
JPS6245718A JP18642985A JP18642985A JPS6245718A JP S6245718 A JPS6245718 A JP S6245718A JP 18642985 A JP18642985 A JP 18642985A JP 18642985 A JP18642985 A JP 18642985A JP S6245718 A JPS6245718 A JP S6245718A
Authority
JP
Japan
Prior art keywords
yarn
polyester
fibers
aromatic
diameter
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
JP18642985A
Other languages
Japanese (ja)
Inventor
Hiroaki Sugimoto
杉本 宏明
Kazuo Hayatsu
早津 一雄
Toshiyuki Kobashi
小橋 利行
Seiji Takao
高尾 精二
Jun Takagi
潤 高木
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.)
Japan Exlan Co Ltd
Sumitomo Chemical Co Ltd
Original Assignee
Japan Exlan Co Ltd
Sumitomo Chemical 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 Japan Exlan Co Ltd, Sumitomo Chemical Co Ltd filed Critical Japan Exlan Co Ltd
Priority to JP18642985A priority Critical patent/JPS6245718A/en
Priority to EP86111184A priority patent/EP0216109A3/en
Publication of JPS6245718A publication Critical patent/JPS6245718A/en
Pending legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/78Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products
    • D01F6/84Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products from copolyesters
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D4/00Spinnerette packs; Cleaning thereof
    • D01D4/02Spinnerettes
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/58Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/62Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyesters

Landscapes

  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Artificial Filaments (AREA)

Abstract

PURPOSE:To obtain polyester yarn having high modulus of elasticity and improved wear resistance, by subjecting a polyester showing anisotropy in melting to melt spinning. CONSTITUTION:An aromatic polyester showing anisotropy in melting is subjected to melt spinning and prepared yarn has >=0.1mm, preferably >=0.3mm, more preferably >=0.5mm diameter when the thickness of the yarn is calculated as a section of circle and >=300g/d modulus of elasticity in tension. To make the yarn more elastic, the spun yarn can be heat-treated and/or drawn. USE:Useful for rope, cable, FRP, FRTP, speaker cone, safety clothes, tension member, etc.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は通常の繊維に比べ、太い直径を有し高弾性率を
有するポリ:ステル繊維に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to poly:stell fibers having a larger diameter and higher modulus than ordinary fibers.

(従来の技術) 合成繊維は天然繊維と並び、衣料用、産業用途に欠くべ
からざる素材であり、各種用途に用いられている0中で
もポリエステ/l/(代表的なものとしてポリエチレン
テレフタレートがある)は、8000 m/minを超
える紡糸速度、紡糸の安定性および価格の低さなどから
、ナイロン。
(Prior art) Synthetic fibers, along with natural fibers, are indispensable materials for clothing and industrial applications, and among the materials used for various purposes, polyester/l/ (a typical example is polyethylene terephthalate) Nylon is preferred due to its spinning speed of over 8000 m/min, stability of spinning, and low price.

アクリルを含めた8大繊維の中でも最も用いられている
。このポリエステルは強度が8〜10?/d9弾性率が
25〜150 r/dといった物性を有するが未だ十分
とはいえない。
It is the most used of the eight major fibers including acrylic. This polyester has a strength of 8-10? Although it has physical properties such as /d9 elastic modulus of 25 to 150 r/d, it is still not sufficient.

すなわち産業界においてはケーブルやロープの芯、架線
、ワイヤー代替等に、高強度又は高弾性率の太い繊維が
望まれていた。例えば、金属線を用いた場合には導電性
のため、計器にノイズや過電流を流したり、複合材料を
用いた場合には、母材と強化材の界面での接着が間ガ!
でありたり、細いデニールの糸九らロープを作る場合、
加工工程の手間、加工時における摩耗といった問題があ
った。
That is, in the industrial world, thick fibers with high strength or high elastic modulus have been desired for cores of cables and ropes, overhead wires, wire substitutes, etc. For example, when metal wires are used, their conductivity causes noise and overcurrent to flow through the instrument, and when composite materials are used, the adhesion at the interface between the base material and the reinforcing material can be difficult!
or when making a thin denier rope,
There were problems with the processing process and wear during processing.

(発明が解決しようとする問題点および問題点を解決す
るための手段) このような現状に鑑み本発明者らは、溶r’jA l’
Jに異方性を示す芳香族ポリニスデルを用い、鋭意検を
寸の結果、太い径で高弾性率を有する210餉に関する
本発明に至った〇 すなわち、本発明は、溶融時に異方性を示す芳香族ポリ
エステルを溶融紡糸することによυ得られる繊維であっ
て、その断面積を真円で表わしだときの真円の直径が0
.111m以上であり、引張シ弾性率が80 Of/d
以上であることを特徴とするポリエステル繊維に関する
ものである0本発明における溶融時に異方性を示すポリ
エステルとをよ、りO直交した2枚の偏光板の間にある
加熱試料台上にポリエステ)VgJ料粉末を置いて昇温
していった時に流動可能な温度域において、光を透過し
うる性質を有するものを意味している。
(Problems to be Solved by the Invention and Means for Solving the Problems) In view of the current situation, the present inventors have
As a result of extensive investigation using aromatic polynisdel which exhibits anisotropy in J, we have arrived at the present invention relating to 210 wire having a large diameter and high elastic modulus〇In other words, the present invention exhibits anisotropy when melted. A fiber obtained by melt-spinning aromatic polyester, whose cross-sectional area is expressed as a perfect circle, and the diameter of the perfect circle is 0.
.. 111 m or more, tensile modulus is 80 Of/d
This relates to a polyester fiber characterized by the above characteristics.In the present invention, the polyester exhibiting anisotropy when melted is placed on a heated sample stand between two orthogonal polarizing plates. It means something that has the property of being able to transmit light in the temperature range where it can flow when the powder is placed and heated.

このような芳香族ポリエステルとしては、特公昭56−
18016号や同55−20008号等に示される芳:
If族シカyボン酸、芳香族ジオール及び/又は芳香族
ヒドロキジカルボン酸やこれらの誘導体から成るもので
、場合によシ、これらと指環族ジカルボン酸、5旨環族
ジオ−、I’L’ 、脂肪族ジオールやこれらの誘4体
との共重合体も含まれるO ここで芳香族ジカルボン酸としてはテレフタル酸、イソ
フタル酸、4 、4’−ジカルボキシジフェニ/’% 
2.6−ジカ〜ポキシナフタレン、1.2−ビス(4−
カルボキクフェノキV)エタン等や、これらのアルキル
、アリール、アルコキシ、ハロゲン基の核置換体があげ
られる。
As such aromatic polyester,
The aroma shown in No. 18016 and No. 55-20008, etc.:
If group dicarboxylic acids, aromatic diols and/or aromatic hydroxydicarboxylic acids, or derivatives thereof, optionally combined with ring dicarboxylic acids, pentacyclic dicarboxylic acids, I'L' , aliphatic diols and copolymers with these derivatives are also included. Here, the aromatic dicarboxylic acids include terephthalic acid, isophthalic acid, 4,4'-dicarboxydipheny/'%
2.6-dica-poxynaphthalene, 1.2-bis(4-
Examples thereof include carboxylic phenolic V) ethane, and derivatives thereof with alkyl, aryl, alkoxy, and halogen groups substituted on the nucleus.

芳香族ジオールとしては、ヒドロキノン、レゾルシン、
 4 、4’−ジヒドロキシジフェニ〃、4.4−ジヒ
ドロキンベンゾフェノン、4.4−ジヒドロキシジフェ
ニルエタン、4 、4’−ジヒドロキシジフェニルエタ
ン、2.2−ビス(4−ヒドロキVフェニ/L/)プロ
パン、4.4′−ジヒドロキシジフェニルエーテル、4
.4−ジヒドロキシジフェニルスルホン、4.4−ジヒ
ドロキシフェニルスルフィド、2.6−ジヒドロキシナ
フタレン、1,5−ジヒドロキシナフタレン等やこれら
のアルキ〜、アリール、アルコキシ、ハロゲン基の核置
換体があげられる02−ヒドロキシナフタレン−6−カ
μボン酸、1−ヒドロキシナフタレン−5−カルボン酸
等やこれらのアルキル、アリ−〜、アルコキシ、ハロゲ
ン基の核1d換体がめげられる。
Aromatic diols include hydroquinone, resorcinol,
4,4'-Dihydroxydipheny, 4,4-dihydroquine benzophenone, 4,4-dihydroxydiphenylethane, 4,4'-dihydroxydiphenylethane, 2,2-bis(4-hydroxyVpheny/L/) Propane, 4,4'-dihydroxydiphenyl ether, 4
.. 02-Hydroxy, including 4-dihydroxydiphenylsulfone, 4,4-dihydroxyphenylsulfide, 2,6-dihydroxynaphthalene, 1,5-dihydroxynaphthalene, etc., and nuclear substituted products of these with alkyl, aryl, alkoxy, and halogen groups. Naphthalene-6-carboxylic acid, 1-hydroxynaphthalene-5-carboxylic acid, etc., and conversion of their alkyl, aryl to alkoxy, or halogen groups into the nucleus 1d are unsuccessful.

脂環族ジカルボン酸としてはtrans−1,4−ジカ
ルボキシシクロヘキサン、eis−1,4−!’カルポ
ギシシクロヘキサン等やこれらのアルキル・、アリール
、ハロゲン基の16′換体があげられるO nη脂環族び脂肪族ジオ−/しとしては、trams−
1,4−ジヒドロキシシクロヘキサン、eim−1,4
−ジヒドロキシシクロヘキサン、エチレングリコール、
1.4−ブタンジオール、キシリレンジオール等があけ
られる。
As the alicyclic dicarboxylic acid, trans-1,4-dicarboxycyclohexane, eis-1,4-! 'carpogysicyclohexane, etc. and 16' conversion of their alkyl, aryl, and halogen groups are mentioned.
1,4-dihydroxycyclohexane, eim-1,4
-dihydroxycyclohexane, ethylene glycol,
1.4-butanediol, xylylene diol, etc. are available.

これらの組合せの内で本発明の対象として好゛ましい芳
香族ポリエステルとしては、例えば(1)p−ヒドロキ
シ安息香酸残糸40〜7Qモ)V座と上記芳香族ジカル
ボン酸残基15〜30モル%と芳香族ジオール残基15
〜80−Tニル%から成ルコポリエステル、(2)テレ
フタル酸及ヒ/又はイソフタル酸とクロルヒドロキノン
、フェニルヒドロキノン及び/又はヒドロキノンカラ成
るコポリエステ#、(3)p−ヒドロキシ安息香酸残基
20〜80モμ%と2−ヒドロキシナフタレン−6−カ
ルボン酸残基20〜80モル%から成るコポリエステル
などがあげられる。
Among these combinations, preferred aromatic polyesters as objects of the present invention include (1) p-hydroxybenzoic acid residues 40 to 7Q; Mol% and aromatic diol residues 15
(2) copolyester consisting of terephthalic acid and/or isophthalic acid and chlorohydroquinone, phenylhydroquinone and/or hydroquinone color, (3) p-hydroxybenzoic acid residues 20 to 80%; Examples include copolyesters comprising 20 to 80 mol% of 2-hydroxynaphthalene-6-carboxylic acid residues.

これらの出発原料を用い、本発明の目的とするポリエス
テルに至るには、そのままであるいは脂肪族もしくは芳
香族モノカルボン酸又はそれらの誘導体、脂肪族7〜コ
ールもしくはフェノール類又はそれらの誘導体等による
エステル化により重縮合反応を行う。
These starting materials can be used as they are or as esters with aliphatic or aromatic monocarboxylic acids or their derivatives, aliphatic 7-coles, phenols or their derivatives, etc. A polycondensation reaction is carried out by chemical reaction.

重縮合反応としては、既知の塊状重合、溶液重合、懸濁
重合法等を採用することができ、150〜860℃で常
圧又は10〜0.1 torr の減圧下にSb 、T
I 、Ge 化合物等の重合触媒、リン系化合物等の安
定剤、TiO2、CaC0) 、タルク等の充てん剤等
を場合により添加して行なうことができるO 得られたポリマーはそのままで、あるいけ粉体状で不活
性気体中、又は減圧下に熱処理して紡糸用試料とする。
As the polycondensation reaction, known bulk polymerization, solution polymerization, suspension polymerization, etc. can be adopted, and Sb, T, etc.
The polymerization can be carried out by adding polymerization catalysts such as I, Ge compounds, stabilizers such as phosphorus compounds, TiO2, CaC0), fillers such as talc, etc. O The obtained polymer can be used as is or as a powder. The sample is heat-treated in body form in an inert gas or under reduced pressure to prepare a sample for spinning.

あるいは、一度押出機((より造粒して用いることもで
きる0 本発明における芳香族ポリエステルには紡糸に適した分
子量範囲が存在すると考えられるが、組成や構造によっ
ては、均一に溶解しうる溶剤がなかったり、分子量測定
法の精度がないという問題がちり、本発明に適した芳香
、挨ポリエステルの規格としては使えない0 そこで本発明者らは、溶〃膚紡糸条件に適する分子量に
対応する物性値として「流動温度」というものを導入し
た。島津製作所製のフローテスターCFT−500を用
い、径1諺、長さ10鴎のノズルで圧力100 Kv’
crAの状態で、芳香族ポリエステル試料を4℃/mi
nで昇彊し7、試料がノズルを通って流動し、かつ48
.000pois@の見かけ粘度を与える温度として「
流動温度」を定義した。
Alternatively, the aromatic polyester used in the present invention may have a molecular weight range suitable for spinning, but depending on the composition and structure, a solvent that can be uniformly dissolved may be There are many problems such as lack of molecular weight measurement method and lack of accuracy of molecular weight measurement method, and it cannot be used as a specification for aromatic and dusty polyester suitable for the present invention. We introduced "flow temperature" as a physical property value. Using a flow tester CFT-500 manufactured by Shimadzu Corporation, a pressure of 100 Kv' was used with a nozzle with a diameter of 1 and a length of 10 mm.
The aromatic polyester sample was heated at 4°C/mi in the crA state.
7, the sample flows through the nozzle, and 48
.. As the temperature that gives an apparent viscosity of 000 pois@,
"flow temperature" was defined.

本発明者らは各種の組成の芳香族ポリエステルを今成し
、その流動温度を変化させてみたところ、本発明の目的
とする高強度、高弾性率繊維の紡糸に適した芳香族ポリ
ニス5−ルの流動温度は280〜880℃であることが
わかった。
The present inventors have now produced aromatic polyesters of various compositions and have tried varying their flow temperatures, and have found that aromatic polyester 5- The flow temperature of the mol was found to be 280-880°C.

・この温度域よシ低い流動温度の場合には、納畠時の反
応がおこりやすかったυ、IB、維伸度が出にくいとい
った問題があp1高いと加工(紡糸)温度が高くなるた
め、分解−′P架橋反応をおこしやすく、又装置への負
荷が大きくなるとい9問題を生じる〇 本発明における溶融紡糸のための装置11としては、既
知のプフンジャー型又はスクリュー型押出機を利用する
ことができる0紡゛糸温度としては、280〜420℃
、好ましくは300〜400℃が良い。この温度範囲よ
シ低いと装置への負荷が大きくなった9、試料溶虐体が
均一でなかったシする0また逆にこの温度範囲より高い
と、ポリマーの分解を引きおこしたりする〇本発明にお
ける、要件の1つである太い僅の糸を得る方法としては
、0.5〜5■、好ましくは1〜8IIllのノズルを
用いて紡糸するのが良い0溶融時に異方性を示すポリエ
ステルはせん断による配向性が大きいので、ノズルのラ
ンド長と径の比は好塘しくけ0.5以上、よシ好ましく
は1以上のものがよく、さらに、ノ、ズyの径の大きい
ものを用いるときは、8以上のものを用いることが望ま
しい。
・When the flow temperature is lower than this temperature range, there are problems such as υ, IB, and fiber elongation which are difficult to obtain due to the tendency of reactions during storage. -'P crosslinking reaction is likely to occur, and the load on the device increases, which causes problems. As the device 11 for melt spinning in the present invention, a known Pfunger type or screw type extruder can be used. The possible zero spinning temperature is 280 to 420℃.
, preferably 300 to 400°C. If the temperature is lower than this range, the load on the apparatus becomes large9, and the sample agglomerates are not uniform0.Conversely, if the temperature is higher than this range, it may cause decomposition of the polymer.This invention As a method of obtaining a thick yarn, which is one of the requirements in Since the orientation due to shearing is large, the ratio of the land length to the diameter of the nozzle should be 0.5 or more, preferably 1 or more, and the nozzle should have a large diameter. In some cases, it is desirable to use a number of 8 or more.

本発明に従って紡糸し−II:、繊維はそのままで、又
は池斉、[を付着させ巻取る々シ、引落す〇巻取υ又は
引蕗しのj坐7空は得ようとするm維の太さから求める
。f計維の断面(寸、目的や用途によシ、¥4円、41
ff円、各種の凹凸を有するものを選ぶことができる。
According to the present invention, the fibers are spun as they are, or the fibers are attached and rolled up, and then the fibers are drawn down and the fibers to be obtained are Find it from the thickness. Cross section of f-meter fiber (depending on size, purpose and use, ¥4, 41
You can choose a ff circle or one with various unevenness.

これらの断面の繊維を作るには[側やr−」、 r六J
 、 r+1. rツ<J、「八」 といった各種の吐
出孔をもつノズルを使うことで達成できる。
To make fibers with these cross sections [side or r-'', r6J
, r+1. This can be achieved by using a nozzle with various discharge holes such as ``r〉<J, ``8''.

得られる繊維はその甘までも使用できるが、熱処理や延
伸やこれらの組合せの処理を施してやることにより、さ
らに高−性化することができる。
Although the resulting fiber can be used in its sweet form, it can be made even more resistant by heat treatment, stretching, or a combination of these treatments.

かくして本発明の41.t’維が得られる。なお糸の太
さとしてはに府γ幀真円以外の異形断面をもつ繊維の場
合には、真円の断面に換算して考えたとき)、その直径
が0,1w以上、好ましくは0.8畷以上、さらに好ま
しくけ0.5 m11以上のものが、特徴あるポリエス
テ/L’繊維を与オ、る。
Thus, 41. of the present invention. T' fibers are obtained. In addition, in the case of fibers with an irregular cross section other than a perfect circle, the diameter of the thread should be 0.1W or more, preferably 0.1W (when considered in terms of the cross section of a perfect circle). A fiber having a length of 8 or more, more preferably 0.5 m11 or more provides a characteristic polyester/L' fiber.

(作用および効果) かかる方法により得られた太い径を持つポリエステルv
lil維は高弾性率で、耐1?!耗性も太いがゆえにす
ぐれる。
(Function and Effect) Polyester v with a large diameter obtained by such method
lil fiber has a high elastic modulus and has a resistance of 1? ! It also has excellent abrasion resistance because it is thick.

そして本発明により得られる繊維よ、ローブ、ケーブル
、FRP、FRTP、スピーカーコーン、安全着、テン
シ町ンメンバー等に用いることができる。
The fibers obtained according to the present invention can be used for robes, cables, FRP, FRTP, speaker cones, safety clothing, city members, etc.

(実施例) 以下に本発明の詳細な説明するために実施例および比較
例を示すが、これらはあく壕で例示的なものであり、こ
れらに限定するものではない。
(Example) Examples and comparative examples are shown below to explain the present invention in detail, but these are merely illustrative and are not intended to be limiting.

なお、例中の繊維の引張シ試験は東洋ボールドウィン社
のオートグラフ7M−500を用い、試料間隔50■、
引張り速度51m1nで測定した。
In addition, the tensile test of the fiber in the example was carried out using Toyo Baldwin's Autograph 7M-500, with a sample interval of 50 cm,
The measurement was performed at a tensile speed of 51 m1n.

光学異方性の測定は加熱ステージ上に試料を置いて、偏
光下、25℃/minで昇温して肉眼観察により行なっ
た。
The optical anisotropy was measured by placing the sample on a heating stage, raising the temperature at 25° C./min under polarized light, and observing it with the naked eye.

参考例1 p−アセトキシ安息香酸7.20 !llr (40七
μ)、テレフタル酸2.49〜(15モル)、イソフタ
Iv酸0.88b(5モ/L’)、4.4′−ジアセト
キンジフェニ/I15.45 Kf(20,2七〃)を
くし型攪拌翼をもつ重合槽に仕込み、窒素ガス雰囲気下
で攪拌しながら昇温し880℃で8時間重合した。この
間生成する酢酸を除去し、強力な攪拌で重合を行ない、
その後、徐々に冷却し、200℃で重合体を系外へ取出
した◎重合体の収量は10.88KFで理論収量の97
.8%であった□これを細用ミクロン社のハンマーミル
で粉砕し、2.5W以下の粒子とした0これをロータリ
ーキルン中で窒素雰囲気下に280℃で5時間処理した
ところ、「流動温度」が826℃となった0350℃以
上で光学異方性が観察された〇参考例2 参考例1と同じ装置6)を用い2,5−ジアセトキシビ
フェニルとテレフタル酸とから成るコポリエフ、チルを
合成し7た。「流動温度」は818℃であり840℃以
上で光学異方性が観察された0実施例1 tSS何例1ポリエステ/l/を用い、30納径のスク
リ二−型押出機によ邊溶謄紡糸を行なったOノスルは孔
径8II11、孔長86ILa1孔数1であるOなお吐
出口は貫円形状である。ポリエステルをホッパーから投
入し、365℃で紡糸した0吐出量と巻取り速度を変更
した。種々゛の糸径で、安定な紡糸が行なわれて淡黄色
の逝明級維が得られた。
Reference example 1 p-acetoxybenzoic acid 7.20! llr (407 μ), terephthalic acid 2.49-(15 mol), isophthalic acid 0.88 b (5 mol/L'), 4.4'-diacetoquine diphenyl/I 15.45 Kf (20,2 7) was charged into a polymerization tank equipped with a comb-shaped stirring blade, and the temperature was raised while stirring in a nitrogen gas atmosphere, and polymerization was carried out at 880° C. for 8 hours. During this time, the acetic acid produced is removed and polymerization is carried out with strong stirring.
After that, it was gradually cooled and the polymer was taken out of the system at 200°C. The yield of the polymer was 10.88KF, which was 97% of the theoretical yield.
.. 8% □ This was crushed with a hammer mill manufactured by Hosei Micron Co., Ltd. to produce particles of 2.5 W or less. □ When this was treated in a rotary kiln at 280°C under a nitrogen atmosphere for 5 hours, the "flow temperature" Optical anisotropy was observed above 0350°C, where the temperature was 826°C.Reference Example 2 Synthesis of copolyef, til consisting of 2,5-diacetoxybiphenyl and terephthalic acid using the same apparatus 6) as in Reference Example 1. It was seven years ago. The "flowing temperature" was 818°C, and optical anisotropy was observed above 840°C.Example 1 tSS Example 1 Using polyester/l/, melting was carried out using a screenie type extruder with a diameter of 30 mm. The O nostle used for mime spinning has a hole diameter of 8II11, a hole length of 86ILa, and a number of holes of 1.The discharge port has a circular shape. Polyester was charged from a hopper and spun at 365° C. The zero discharge amount and winding speed were changed. Stable spinning was carried out with various thread diameters, and pale yellow clear grade fibers were obtained.

この繊維を窒素中820℃で3時間処理したときの引張
り試験の結果およびこの繊維を直径80αのステンレス
製の車軸に5回巻き、車軸を60シ分で5分間回転し、
疲労試験をしたあとの引張シ試験結果とを表1に示す0 ポリエチレンテレフタレートの比較例1と比べ本発明の
繊維のすぐれていることがわかる。
The results of a tensile test when this fiber was treated in nitrogen at 820°C for 3 hours, and the fiber was wound 5 times around a stainless steel axle with a diameter of 80α, and the axle was rotated at 60 cm for 5 minutes.
The results of the tensile test after the fatigue test are shown in Table 1. It can be seen that the fiber of the present invention is superior to Comparative Example 1 of polyethylene terephthalate.

比較例1 東洋紡のポリエチレンテレフタレートRT−580を用
い、300Cで実施例1と同じ方法で紡糸した。但し、
この場合、ノズル下、5工の所で、吐出糸を水中に導き
、急冷した0150℃で4倍に延伸し、185℃で8時
間、緊張下に熱処理しだ0この繊維の引張り試験と、疲
労試験後の引張り試験の結果を示す0 実施例2
Comparative Example 1 Spinning was performed in the same manner as in Example 1 at 300C using Toyobo's polyethylene terephthalate RT-580. however,
In this case, at the 5th point under the nozzle, the discharged yarn was introduced into water, rapidly cooled, stretched 4 times at 0.150°C, and heat treated under tension at 185°C for 8 hours. 0 Example 2 showing the results of the tensile test after the fatigue test

Claims (1)

【特許請求の範囲】[Claims] 溶融時に異方性を示すポリエステルを溶融紡糸すること
により得られる繊維であって、その断面積を真円で表わ
したときの真円の直径が0.1mm以上であり、引張り
弾性率が300g/d以上であることを特徴とするポリ
エステル繊維。
A fiber obtained by melt-spinning polyester that exhibits anisotropy when melted, whose cross-sectional area is expressed as a perfect circle, and whose diameter is 0.1 mm or more, and whose tensile modulus is 300 g/ d or more.
JP18642985A 1985-08-23 1985-08-23 Polyester yarn Pending JPS6245718A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP18642985A JPS6245718A (en) 1985-08-23 1985-08-23 Polyester yarn
EP86111184A EP0216109A3 (en) 1985-08-23 1986-08-12 Polyester fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18642985A JPS6245718A (en) 1985-08-23 1985-08-23 Polyester yarn

Publications (1)

Publication Number Publication Date
JPS6245718A true JPS6245718A (en) 1987-02-27

Family

ID=16188274

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18642985A Pending JPS6245718A (en) 1985-08-23 1985-08-23 Polyester yarn

Country Status (2)

Country Link
EP (1) EP0216109A3 (en)
JP (1) JPS6245718A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008002041A (en) * 2006-06-26 2008-01-10 Kaneka Corp Fiber for artificial hair and method for producing the same

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6245751A (en) * 1985-08-26 1987-02-27 住友化学工業株式会社 Protective material
US5242645A (en) * 1989-11-15 1993-09-07 Toray Industries, Inc. Rubber-reinforcing polyester fiber and process for preparation thereof
FR2857984B1 (en) * 2003-07-25 2008-02-08 Rhodia Performance Fibres THREADS, FIBERS, ABRASION RESISTANT FILAMENTS
FR2864094B1 (en) 2003-12-19 2006-02-10 Rhodia Industrial Yarns Ag COMPOSITE MATERIALS COMPRISING A REINFORCING MATERIAL AND A THERMOPLASTIC MATRIX, PRECURSOR COMPOUND ARTICLE OF THESE MATERIALS AND PRODUCTS OBTAINED FROM THESE MATERIALS

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE633371A (en) * 1962-06-07
US3975487A (en) * 1973-08-20 1976-08-17 The Carborundum Company Process for spinning high modulus oxybenzoyl copolyester fibers
US4066620A (en) * 1975-04-29 1978-01-03 E. I. Du Pont De Nemours And Company Copolyester capable of forming anisotropic melt and shaped articles thereof
US4256624A (en) * 1979-07-02 1981-03-17 Celanese Corporation Polyester of 6-hydroxy-2-naphthoic acid, aromatic diol, and aromatic diacid capable of undergoing melt processing
US4370466A (en) * 1981-09-28 1983-01-25 E. I. Du Pont De Nemours And Company Optically anisotropic melt forming polyesters

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008002041A (en) * 2006-06-26 2008-01-10 Kaneka Corp Fiber for artificial hair and method for producing the same

Also Published As

Publication number Publication date
EP0216109A3 (en) 1987-11-19
EP0216109A2 (en) 1987-04-01

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