JPS59199810A - Production of polyamide fiber - Google Patents

Production of polyamide fiber

Info

Publication number
JPS59199810A
JPS59199810A JP6878083A JP6878083A JPS59199810A JP S59199810 A JPS59199810 A JP S59199810A JP 6878083 A JP6878083 A JP 6878083A JP 6878083 A JP6878083 A JP 6878083A JP S59199810 A JPS59199810 A JP S59199810A
Authority
JP
Japan
Prior art keywords
yarn
winding
filament yarn
atmosphere
filaments
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
JP6878083A
Other languages
Japanese (ja)
Inventor
Takuji Sato
卓治 佐藤
Masaharu Yamamoto
雅晴 山本
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 JP6878083A priority Critical patent/JPS59199810A/en
Publication of JPS59199810A publication Critical patent/JPS59199810A/en
Pending legal-status Critical Current

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  • Artificial Filaments (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)

Abstract

PURPOSE:To obtain the titled fibers for knitted and woven fabrics, etc. having a high strength, heat stability and improved dyeability, by quenching filaments melt extruded through spinneret extrusion holes to the solidifying point or below, passing the quenched filaments through a heated atmosphere, adjusting the spinning tension of the resultant filament yarn just after passing through the atmosphere, oiling the filament yarn, and winding the resultant oiled filament yarn at a high speed. CONSTITUTION:Filaments of a thermoplastic polyamide, e.g. nylon 6, melt extruded through spinneret extrusion holes are quenched to the solidifying point of the polyamide, passed through an atmosphere at a temperature (T deg.C) within the range satisfying formula I [T is the temperature ( deg.C); Tm is the melting point of the polyamide ( deg.C)] and formula II [D is the fineness per filament of the wound filament yarn (deniers); V is the winding speed (m/min)] at the same time for 0.01-0.03sec, adjusting the spinning tension (Gg) of the resultant filament yarn just after passing through the atmosphere within the range expressed by formula III [G is the spinning tension (g); F is the number of filaments in the wound filament yarn (filaments)], oiling the fialment yarn, and winding the oiled filament yarn at 4,500-5,500m/min speed to give the aimed fibers.

Description

【発明の詳細な説明】 本発明(は、高速紡糸法により、機械的性質。[Detailed description of the invention] The mechanical properties of the present invention are improved by high-speed spinning method.

熱安定性、染色特性に優れた編織物用に適するポリアミ
ド繊維を製造する方法に関するものである。
The present invention relates to a method for producing polyamide fibers having excellent thermal stability and dyeing properties and suitable for use in knitted fabrics.

従来のポリアミド繊維の直接紡糸延伸方法は、例えば特
公昭48−20268号公報、特公昭46−22886
号公報などに示されるように、第1引取ローラ対と第2
づ[取ローラ対とで糸条を延伸し、加熱された第2引取
ローラ対で該糸条を熱固定するという方法が一般的であ
る。この方法により得られる繊維の゛物性は好ましいも
のであるが、第2引取ローラ対を5,000〜6,00
0 ’ % のような高速にした時、糸条の揺れが大き
く、特に前記ローラ対に8〜16糸条の多糸条を多数周
回させた場合には、糸条間での重なりが生じ糸切れとな
ったり、あるいはそれを避けるため糸条間隔を大きくと
ろうとすると、ローラ長が長くなり、装置的に高速回転
が不可能になるなどの間顕点があった。
Conventional methods for direct spinning and drawing of polyamide fibers are disclosed, for example, in Japanese Patent Publication No. 48-20268 and Japanese Patent Publication No. 46-22886.
As shown in the publication, the first pair of take-up rollers and the second
A common method is to draw the yarn with a pair of take-up rollers, and heat-set the yarn with a heated second pair of take-up rollers. Although the physical properties of the fibers obtained by this method are favorable, it is preferable to
When the speed is set to 0'%, the yarn sways greatly, and especially when the pair of rollers rotates a large number of yarns of 8 to 16 yarns, overlapping occurs between the yarns, causing the yarn to sway. If an attempt was made to increase the yarn spacing to avoid breakage, the length of the roller would become longer, making it impossible to rotate the roller at high speed.

一方、上記直接紡糸延伸方法のような引取ローラ間延伸
せずに6,000〜8,000 ”、hの高速で引取る
いわゆる高速紡糸法が知られている。しかしこの方法で
機械・的1な・糸物性として好ましい水準である40%
程度の残留伸度を得ようとするとs、ooor4+以上
の高速で引取る必要があり、糸切れが多発したり、強度
が低下したりして、工業的生産には適していないもので
あった。
On the other hand, a so-called high-speed spinning method is known in which the yarn is taken up at a high speed of 6,000 to 8,000'' without drawing between take-up rollers like the above-mentioned direct spinning and drawing method. 40%, which is a preferable level for yarn physical properties.
In order to obtain a certain degree of residual elongation, it was necessary to take it off at a high speed of s, ooor 4+ or higher, which resulted in frequent yarn breakage and decreased strength, making it unsuitable for industrial production. .

こうした方法の改良として、特公昭57−25644号
公報などに、ポリアミド糸条を固化後加熱雰囲気中を通
過させるという方法が提案されている。この方法は、ポ
リアミド繊維の残留伸度を減少させ、熱安定性を向上さ
せるうえでかなり効果的ではあるが、B、000〜4.
00Or4程度の巻取速度で高速紡糸して得られた繊維
は、加熱雰囲気内での熱延伸が大きく、フィラメント間
で延伸ムラが生じるため、繊度ムラ、染色ムラなどの糸
構造ムラが目立つといった間顆が生じるのであった。
As an improvement on this method, a method has been proposed in Japanese Patent Publication No. 57-25644, etc. in which the polyamide thread is passed through a heated atmosphere after solidification. Although this method is quite effective in reducing the residual elongation and improving the thermal stability of polyamide fibers, B, 00-4.
Fibers obtained by high-speed spinning at a winding speed of about 00Or4 undergo a large amount of hot stretching in a heated atmosphere, causing uneven stretching between filaments, resulting in noticeable uneven yarn structure such as uneven fineness and uneven dyeing. A condyle was formed.

この糸ムラを減少させるためには、巻取速度を4,50
0〜5,500萎とすることが有効であることを見出し
たが、このような高い巻取速度にすると、前記加熱雰囲
気での熱処理を十分に行なうことがむずかしく、機械的
特性改善効果が不十分であるなどの新たな問題が生じる
のであった。
In order to reduce this yarn unevenness, the winding speed should be increased to 4.50.
It has been found that setting the winding speed to 0 to 5,500 mm is effective, but at such a high winding speed, it is difficult to perform sufficient heat treatment in the heating atmosphere, and the effect of improving mechanical properties is insufficient. New questions arose, such as sufficiency.

そこで、この問題の解消について検討した結果、前記加
熱雰囲気通過直後の紡糸張力を下記(3)式で示される
特定範囲内とするとと゛により、上記問題は解消される
こと、およびこの紡糸張力を(3)式の範囲内とした場
合は、前記加熱雰囲気温度は下記(1)・(2)式を同
時に満足する範囲内とし、かつ、通過時間を0.01〜
0.03秒間とすることが最も有効であることを見出し
、本発明をなすに至ったものである。
Therefore, as a result of studying how to solve this problem, we found that if the spinning tension immediately after passing through the heating atmosphere is set within a specific range shown by the following equation (3), the above problem is solved by ``, and this spinning tension is 3) When the heating atmosphere temperature is within the range of formula (1) and (2) below, the heating atmosphere temperature is within the range that satisfies the following formulas (1) and (2) at the same time, and the passing time is 0.01 to 0.
It has been found that setting the time to 0.03 seconds is most effective, and the present invention has been completed.

すなわち、本発明の主な目的は、得られたポリアミド繊
維の染色ムラ、繊度ムラを減少Δせること、紡糸糸切れ
を生じることなく加熱雰囲気中での熱処理を十分に行な
うことにあり、こ    1の目的を達成するために、
本発明40金吐出孔より溶融吐出された熱可塑性ポリア
ミド紡出糸条を、該ポリアミドの固化点温度以下に冷却
した後、下記(1)・(2)式を同時に満足する範囲内
の温度(T ℃)に加熱した雰囲気中を0.01〜00
3秒−間通過させ、通過直後の紡糸張力CG%)を下記
(3ン式に示す範囲内とし、給油した後に、4,500
〜Tm−10.0≦T≦Tm+60         
 (1)20D+0.07V+Tm−500≦T≦10
D+0.04V+Tm−170 (2)5J≦G≦17
 、/T             (3)本発明によ
れば、4,500〜5,500 %で高速巻取すること
により生じた繊維軸方向非晶部分の配向の乱れは、上記
(1)・(2)式の温度条件、上記(3)式の紡糸張力
条件および上記の通過時間条件下で加熱雰囲気中を通過
させることにより十分に解消することができるので、そ
の結果得られたポリアミド繊維は、機械的性質、熱的性
質、染色特性に優れ、衣料用編織物に好適な物である。
That is, the main objects of the present invention are to reduce uneven dyeing and uneven fineness of polyamide fibers obtained, and to sufficiently perform heat treatment in a heated atmosphere without causing yarn breakage. In order to achieve the purpose of
The thermoplastic polyamide spun yarn melted and discharged from the 40-karat gold discharge hole of the present invention is cooled to below the solidification point temperature of the polyamide, and then heated to a temperature ( 0.01-00 in an atmosphere heated to T °C)
After passing for 3 seconds, the spinning tension (CG%) immediately after passing was within the range shown in the 3-ton formula, and after oiling, 4,500
~Tm-10.0≦T≦Tm+60
(1) 20D+0.07V+Tm-500≦T≦10
D+0.04V+Tm-170 (2) 5J≦G≦17
, /T (3) According to the present invention, the disorder in the orientation of the amorphous portion in the fiber axis direction caused by high-speed winding at 4,500 to 5,500% is expressed by the above equations (1) and (2). This can be sufficiently resolved by passing it through a heated atmosphere under the temperature conditions of , the spinning tension conditions of equation (3) above, and the passing time conditions of above, so that the resulting polyamide fibers have good mechanical properties. It has excellent thermal properties and dyeing properties, and is suitable for knitted fabrics for clothing.

以下、本発明法について詳細に説明する。The method of the present invention will be explained in detail below.

熱可塑性ポリアミドを通常の方法で口金吐出孔より溶融
吐出して得られる紡出直後の糸条は、冷却風吹きつけあ
るいは空冷のような通常の冷却装置により前記ポリアミ
ドの固化点温度以下にいったん冷却される。この冷却を
行なう前の紡出糸条にポリアミド融点以上の高温加熱域
を通すことは、繊維の太さ斑を生じるので好ましくない
。次いで、上部集束ガイドで集束して、加熱雰囲気を通
過させる。
The yarn immediately after spinning obtained by melting and discharging thermoplastic polyamide from the nozzle discharge hole in a conventional manner is once cooled to below the solidifying point temperature of the polyamide using a conventional cooling device such as cooling air blowing or air cooling. Ru. It is not preferable to pass the spun yarn before cooling through a heating range at a high temperature higher than the melting point of the polyamide because it causes unevenness in the thickness of the fibers. It is then focused by an upper focusing guide and passed through a heated atmosphere.

加熱雰囲気の入口の位置は、糸条が固化点に達する位置
より下方であればよいが、糸条に対する空気抵抗を下げ
る意味で固化点位置に近い方が好ましい。
The position of the inlet of the heating atmosphere may be below the position where the yarn reaches the solidification point, but it is preferably closer to the solidification point in order to reduce air resistance to the yarn.

加熱雰囲気通過直後の紡糸張力(Gり)が5F≦G≦1
5./”F (Fは糸条のフィラメント数である) の範囲内とすることが重要である。
The spinning tension (G) immediately after passing through the heating atmosphere is 5F≦G≦1
5. /”F (F is the number of filaments in the yarn).

(5J了−)り以下の紡糸張力では、糸条に対する熱延
伸効果が少なく、従って繊維の機械的特性を十分に改善
することができない。また、(15σ)9−以上の紡糸
張力にすると、糸の残留伸度が低くなりすぎて糸切れ多
発につながる。
If the spinning tension is less than 5J, the effect of hot stretching on the yarn is small, and therefore the mechanical properties of the fiber cannot be sufficiently improved. Furthermore, if the spinning tension is (15σ)9 or more, the residual elongation of the yarn becomes too low, leading to frequent yarn breakage.

好ましくは、(8F〜12ゲ町りの範囲である。Preferably, it is in the range of (8F to 12 games).

上記紡糸張力(09)を(5J″f〜15ゲロクとする
ためには、加熱雰囲気の前線に設けた集束ガイドによっ
て、加熱雰囲気内における糸の開繊状態を調節すること
により行なうことができる。
In order to set the spinning tension (09) to (5 J″f to 15 J″), this can be done by adjusting the opening state of the yarn in the heating atmosphere using a focusing guide provided at the front of the heating atmosphere.

例えば、紡糸張力を上げるためには、糸条とガイドとの
接触角度を増したり、あるいけ、接触摩擦係数の高い材
質のガイド音用いたりすればよい。また、紡糸張力2下
げるためには、上部ガイドに導電性物質のはいったガイ
ドを用いたり、糸条との接触ができるだけ小さくなるよ
うなガイド全役けたり、あるいは接触摩擦係数が低くか
つ摩耗強度の高い材質を用いたりすればよい。
For example, in order to increase the spinning tension, the contact angle between the yarn and the guide may be increased, or the guide sound of a material with a high contact friction coefficient may be used. In addition, in order to lower the spinning tension 2, it is possible to use a guide containing a conductive material in the upper guide, to use a guide that minimizes contact with the yarn, or to use a guide that has a low contact friction coefficient and high wear resistance. It is sufficient to use a material with high quality.

また、糸条の単糸繊度が小さいほど熱処理効果は十分に
行なえるので、単糸繊度は6デニール以下とすることが
好ましい。
Further, since the smaller the single yarn fineness of the yarn, the more sufficient the heat treatment effect can be, the single yarn fineness is preferably 6 denier or less.

なお、この加熱雰囲気入口上方で給油することは油剤の
蒸発潜熱に加熱エネルギーが消費されるため好ましくな
い。
Note that it is not preferable to supply oil above the inlet of the heated atmosphere because heating energy is consumed by the latent heat of vaporization of the oil agent.

加熱雰囲気を形成する装置としては、糸条の非接触加熱
装置であればいかなるものでもよいが、なかでも円形断
面の加熱管が好ましい。該加熱管の内径は糸条が管に接
触せずに通過するのに十分な大きさが必要であり、1糸
条あたり5〜20間の内径を有することが好ましい。管
の長さは、糸条の管通過時間が001〜0.03秒とな
る長さが必要である。好ましくは50〜800 cmで
ある。さらに望ましくは150〜250cmである。
As the device for forming the heating atmosphere, any device may be used as long as it is a non-contact heating device for yarn, but a heating tube with a circular cross section is particularly preferred. The inner diameter of the heating tube must be large enough to allow the yarn to pass through the tube without contacting it, and preferably has an inner diameter of between 5 and 20 mm per yarn. The length of the tube must be such that the thread passes through the tube for 0.01 to 0.03 seconds. Preferably it is 50-800 cm. More preferably, the length is 150 to 250 cm.

加熱雰囲気の温度は下記の(1)・(2)式の範囲内に
あることが必要である。
The temperature of the heating atmosphere needs to be within the range of equations (1) and (2) below.

□l Tm−100≦T≦Tm+60          (
1)20D+0.07V+Tm−500≦T≦10D+
0.04V+TTm−170(2)T:ボリアミドの融
点(℃) D:巻取糸の単糸繊度(デニール) ■:巻取速度()) (Tm−100)’O未満あるいは(20D + 0.
07V +Tm −500) ’C未満の温度では、熱
処理効果が十分でないため、得られる繊維の機械的性質
の向上が十分でなく、染色特性の向上も十分でない。
□l Tm-100≦T≦Tm+60 (
1) 20D+0.07V+Tm-500≦T≦10D+
0.04V+TTm-170 (2) T: Melting point of polyamide (°C) D: Single yarn fineness of wound yarn (denier) ■: Winding speed ()) Less than (Tm-100)'O or (20D + 0.
At temperatures below 07V +Tm -500) 'C, the heat treatment effect is not sufficient, so the mechanical properties of the resulting fibers are not sufficiently improved, and the dyeing properties are also not sufficiently improved.

また、(Tm+60)℃を越える温度では走行糸条間で
融着が発生し、安定巻取ができない。あるいは(10D
+0.04V+Tm−170 ) ’Cを越える温度で
は繊維の残留伸度が低くなりすぎて糸切れ多発につなが
る。
Furthermore, at temperatures exceeding (Tm+60)°C, fusion occurs between running yarns, making stable winding impossible. Or (10D
At temperatures exceeding +0.04V+Tm-170)'C, the residual elongation of the fiber becomes too low, leading to frequent yarn breakage.

加熱雰囲気としては好ましくけ空気であるが窒素でもよ
′い。また、管内の加熱雰囲気は糸条による随伴気流お
よびそれに伴う乱流以外は静止雰囲気でもよいが、加熱
気体を糸条の上流から積極的に導入した方が好ましい。
Air is preferred as the heating atmosphere, but nitrogen may also be used. Further, the heated atmosphere inside the tube may be a static atmosphere except for the accompanying air flow caused by the yarn and the accompanying turbulence, but it is preferable to actively introduce the heated gas from upstream of the yarn.

“ 加熱雰囲気を通過させた後、給油ガイドで集束を与え、
給油を行ない、その後4,500−5,500)の速度
で巻取る。
“ After passing through the heated atmosphere, a refueling guide focuses the
After refueling, winding is performed at a speed of 4,500-5,500 mph.

給油する油剤としては、濃度2〜15重量%のエマルジ
ョン型油剤でもよく、また、鉱物油と界面活性剤との混
合物を主体とする非含水油剤でもよい。
The oil to be supplied may be an emulsion type oil having a concentration of 2 to 15% by weight, or may be a non-hydrous oil containing a mixture of mineral oil and a surfactant.

給油後に、インターレースなどの処理を行なってもよい
After refueling, processing such as interlacing may be performed.

巻取時の巻取張力は、0.05〜03この範囲内である
ことが好ましい。0.05%  未満では引取ローラな
どに巻き取られたり、トラバース装置から糸条がはずれ
たりしてドラムやボビンに巻き取ることが困難である。
The winding tension during winding is preferably within the range of 0.05 to 0.03. If it is less than 0.05%, the yarn may be wound up on a take-up roller or the like, or the yarn may come off from a traverse device, making it difficult to wind it onto a drum or bobbin.

また、03%全越えると繊維の残留歪が大きくなりすぎ
て良好なパッケージフオームが得られ難かったり、ある
いはパッケージの中央と端面とで繊維特性差が大きくな
りすぎて、製品不良を生じるなどの問題がある。さらに
0.1〜02%が好ましい。
Furthermore, if it exceeds 0.3%, the residual strain of the fibers becomes too large, making it difficult to obtain a good package form, or the difference in fiber properties between the center and end surfaces of the package becomes too large, resulting in problems such as product defects. There is. Further, 0.1 to 02% is preferable.

さらに、糸条の巻取に使用する巻取ボビンとしては、内
部にアルミなどの金属で補強したボビンが好ましい。本
発明によって得られる繊維は、加熱雰囲気内での熱延伸
によって生じる歪が巻取中に緩和するので、紙のみの巻
取ボビンで巻取った場合には、巻取糸の収縮によって細
管ボビンが直径方向につぶれて安定巻取が難しい。内部
にアルミなどの金属で補強されたボビン全使用した場合
は、ボビンの収縮はおこらず安定巻取が可能となる。ボ
ビンの表層部分としては紙、ABS樹脂などの合成樹脂
などが好ましい。
Furthermore, the winding bobbin used for winding the yarn is preferably a bobbin whose interior is reinforced with metal such as aluminum. In the fiber obtained by the present invention, the strain caused by hot drawing in a heated atmosphere is relaxed during winding, so when the fiber is wound on a winding bobbin made only of paper, the shrinkage of the winding yarn causes the thin tube bobbin to collapse. It collapses in the diameter direction, making stable winding difficult. If all bobbins are used that are internally reinforced with metal such as aluminum, the bobbin will not shrink and stable winding will be possible. The surface layer of the bobbin is preferably made of paper or synthetic resin such as ABS resin.

結晶部分の配向全十分に行ない、糸ムラが少なく、かつ
熱安定性、染色特性の優れた繊維を得るためには、巻取
速度は4,500r′4 以上が必要であり、4,60
0 %以上が好ましい。一方、巻取速度が5,500 
%を越えると、紡糸糸切れが多く発生するようになり、
また加熱域中での熱延伸が小さく、力学特性向上が小さ
くなるので不適当である。
In order to obtain fibers with sufficient orientation of the crystalline portions, minimal yarn unevenness, and excellent thermal stability and dyeing properties, the winding speed must be 4,500 r'4 or higher;
0% or more is preferable. On the other hand, the winding speed is 5,500
If it exceeds %, spun yarn breakage will occur frequently,
Further, the thermal stretching in the heating region is small, and the improvement in mechanical properties is small, which makes it unsuitable.

なお、本発明に言う「ポリアミド」とは、ナイロン6あ
るいはナイロン66を主に指すが、これらに少量の他の
ポリアミド形成性成分を共重合したコポリアミドでもよ
い。また、これらのポリアミドは艶消剤2着色剤、耐熱
安定剤。
The term "polyamide" used in the present invention mainly refers to nylon 6 or nylon 66, but it may also be a copolyamide obtained by copolymerizing these with a small amount of other polyamide-forming components. In addition, these polyamides are matting agents, 2 colorants, and heat stabilizers.

紫外線吸収剤、充填剤、吸湿剤、その他の添加物を含有
してもさしつかえない。ナイロン6の場合、融点(Tm
)は約215°Cである。
It may contain ultraviolet absorbers, fillers, moisture absorbers, and other additives. In the case of nylon 6, the melting point (Tm
) is approximately 215°C.

本発明法によると、結晶部分の配向が十分に進んでいて
、かつ、非晶部分の配向の乱れも十分に解消された優れ
たポリアミド繊維が得られるのであり、すなわち、機械
的特性、熱的特性かつ染色特性に優れ、衣料用繊維とし
て好適な繊維が得られるのである。
According to the method of the present invention, excellent polyamide fibers can be obtained in which the orientation of the crystalline portions is sufficiently advanced and the disordered orientation of the amorphous portions is sufficiently eliminated. This makes it possible to obtain fibers that have excellent properties and dyeing properties and are suitable for use as clothing fibers.

本発明法で得られたポリアミド繊維は、例えば、トリコ
ント用、織物用、加工糸用などに有用である。
The polyamide fibers obtained by the method of the present invention are useful for, for example, trichomes, textiles, textured yarns, and the like.

以下の実施例で本発明を詳述する。The following examples illustrate the invention in detail.

・ 実施例1 ナイロン6チップ(硫酸相対粘度ηr−2,6)を溶融
温度265℃で溶融後、直径o、 a mm (孔数2
4=+)の吐出孔から吐出した。吐出量は各巻取速度に
おいて巻取系繊度が70Dとぶ    ・lるように調
整した。紡出糸条全温度18℃。
- Example 1 After melting a nylon 6 chip (relative viscosity of sulfuric acid ηr-2,6) at a melting temperature of 265°C,
4=+) was discharged from the discharge hole. The discharge amount was adjusted so that the winding system fineness increased by 70D at each winding speed. The total temperature of the spun yarn was 18°C.

風速30)の冷却横風で冷却後、上部集束ガイドを経て
、吐出口金から3mの位置に入口をもつ加熱管(温度2
00℃、管長さ120Cm。
After cooling with a cooling cross-wind at a wind speed of 30), it passes through an upper focusing guide and is heated to a heating tube (temperature 2
00℃, tube length 120cm.

管内径1.5 cm )に糸条全案内した。加熱管には
上流から200℃に加熱した空気を50 N%。
The entire yarn was guided through a tube with an inner diameter of 1.5 cm. The heating tube is filled with 50N% air heated to 200℃ from the upstream.

流量で流した。加熱管通過直後の紡糸張力は表1に示す
値であった。その後、給油ガイドによって濃度lO%の
エマルジョン型油剤を5%付与した後、ゴデツトロール
を経て表1に示す各巻取速度で巻取張力7りで巻き取っ
た。
It flowed at a flow rate. The spinning tension immediately after passing through the heating tube was the value shown in Table 1. Thereafter, 5% of an emulsion-type oil agent having a concentration of 10% was applied using a refueling guide, and then the material was wound up through a godet roll at each winding speed shown in Table 1 with a winding tension of 7.

加熱管の前後に設けた集束ガイドを調節することにより
、紡糸張力を変更した以外は、上記同様の条件で製糸を
行ない、比較例とした。
A comparative example was prepared by spinning yarn under the same conditions as above, except that the spinning tension was changed by adjusting the focusing guides provided before and after the heating tube.

本発明法(扁1〜3・5・6)で得られた繊維は、機械
的特性、染色特性が優れており、かつ、製糸性も良好で
あった。一方、紡糸張力が低すぎる場合(A4)l”i
、熱処理効果が不十分であるため機械的特性、染色特性
が不満足であった。紡糸張力が高すぎる場合(A7)は
、紡糸糸切れが多く製糸性不良であり、染色ムラも生じ
た。
The fibers obtained by the method of the present invention (Flats 1 to 3, 5, and 6) had excellent mechanical properties and dyeing properties, and also had good spinning properties. On the other hand, if the spinning tension is too low (A4) l”i
, mechanical properties and dyeing properties were unsatisfactory due to insufficient heat treatment effect. When the spinning tension was too high (A7), there were many spun yarn breakages, resulting in poor spinning properties and uneven dyeing.

なお、繊維の機械的特性および複屈折はJIS法により
測定したが、染色堅牢度は針数320本 77%−7の
筒編をXylene FastBlue Pの2%ow
fで98℃、So分間染色した物についての洗濯色落ち
をJ工S法で測定した値であり、5級が最良で、通常使
用可能なレベルtfi8級である。tた染色ムラは、上
記筒編をParatine Fast Black W
ANの0.2%owfで60℃、30分間染色したもの
について目視判定した。製糸性は紡糸糸切れ回数で評価
した。
The mechanical properties and birefringence of the fibers were measured according to the JIS method, and the color fastness was measured using 320 needles.
This is a value measured by the J Engineering S method for washing color fading of an item dyed at 98° C. and So for minutes at f, and the best grade is 5th grade, which is the normally usable level TFI 8th grade. To avoid uneven dyeing, use Paratine Fast Black W for the tube knit above.
Visual judgment was made on those stained with 0.2% OWF of AN at 60°C for 30 minutes. The spinning property was evaluated by the number of spun yarn breaks.

拳  比  較  例 実施例1において、巻取速度を変更し、もしくは加熱管
の加熱を行なわず、加熱空気も流さない以外は、実施例
1と同じ条件で製糸を行ない、その結果を表2に示した
Fist Comparison Example Silk spinning was carried out under the same conditions as in Example 1, except that the winding speed was changed, the heating tube was not heated, and heated air was not flown. The results are shown in Table 2. Indicated.

巻取速度が低すぎる場合(扁8)は、染色ムラがあり、
かつ機械的特性、染色特性が不満足であり、一方、高す
ぎる場合(扁9)は、製糸性が不良で、かつ機械的特性
が不満足であった。また、加熱全行なわなかった場合(
A i o〜12)は、残留伸度が高すぎ、強度。
If the winding speed is too low (flat 8), there will be uneven dyeing.
Moreover, the mechanical properties and dyeing properties were unsatisfactory.On the other hand, when it was too high (flat 9), the spinning properties were poor and the mechanical properties were unsatisfactory. Also, if heating is not completed (
Aio~12) has too high residual elongation and poor strength.

モジュラス、配向が低すぎ、かつ染色特性も悪く不満足
なものであった。
The modulus and orientation were too low, and the dyeing properties were also poor and unsatisfactory.

・( ・ 実施例2 加熱管、加熱空気の温度および加熱空気流量を表3に示
す各条件に変更した以外は、実施例1の扁2と同一の条
件で製糸を行ない、その結果を表3に示した。
・( ・ Example 2 Silk spinning was carried out under the same conditions as in Example 1, except that the temperature of the heating tube, the temperature of the heated air, and the flow rate of the heated air were changed to the conditions shown in Table 3. The results are shown in Table 3. It was shown to.

上表かられかるように、加熱雰囲気温度範囲として、単
糸繊度3dで5.ooor4+巻取の場。、150〜2
50’Oが良好であった。すなわち加熱温度の低すぎる
場合(應13・14)は、得られた繊維の特性が不満足
であり、一方、高すぎる場合は、単糸融着が生じ、巻き
取ることができなかった。
As can be seen from the above table, the heating atmosphere temperature range is 5. ooor4+ winding place. , 150-2
50'O was good. That is, when the heating temperature was too low (Nos. 13 and 14), the characteristics of the obtained fibers were unsatisfactory, while when it was too high, single filament fusion occurred and the fiber could not be wound.

実施例3 ナイロン66チップ(硫酸相対粘度ηr−26を溶融温
度290℃で溶融後、孔数24つの吐出孔から吐出した
。その後の冷却、加熱2巻取条件は実施例1と同様にし
て行なった。
Example 3 Nylon 66 chips (sulfuric acid relative viscosity ηr-26) were melted at a melting temperature of 290°C and discharged from 24 discharge holes.The subsequent cooling, heating and winding conditions were the same as in Example 1. Ta.

その結果を表4に示す。The results are shown in Table 4.

表4に示すように、ナイロン66でもナイロン6同様に
本発明法は効果があることがわかった。
As shown in Table 4, the method of the present invention was found to be effective for nylon 66 as well as nylon 6.

・ 実施例4 ナイロン6チップ(硫酸相対粘度ηr−2,6)全溶融
温度265℃で溶融後、直径0.2 am (孔数68
コ)または直径0.4 mm (孔数]2コ)の吐出孔
から吐出した。吐出量は各巻取速度において巻取系繊度
が70ctとなるように調整した。その後の冷却、加熱
雰囲気等は実施例1と同一の条件をとり、結果を表5に
示したO 表5に示したように、単糸繊度が小さいほど熱処理効果
が大きいことがわかった。
- Example 4 Nylon 6 chip (sulfuric acid relative viscosity ηr-2,6) after melting at a total melting temperature of 265°C, diameter 0.2 am (number of holes 68
It was discharged from a discharge hole with a diameter of 0.4 mm (number of holes: 2). The discharge amount was adjusted so that the winding system fineness was 70 ct at each winding speed. The subsequent cooling, heating atmosphere, etc. were the same conditions as in Example 1, and the results are shown in Table 5. As shown in Table 5, it was found that the smaller the single yarn fineness, the greater the heat treatment effect.

特許出願人  東 し 株 式会社Patent applicant Higashishi Co., Ltd.

Claims (1)

【特許請求の範囲】 口金吐出孔より溶融紡出された熱可塑性ボ1ノアミド紡
出糸条を、該ポリアミドの固イヒ、売温度以下に冷却し
た後、下記(1)・(2)式を同時に満足する範囲内の
温度(T ’O)に加熱した雰囲気中を0.01〜0.
08秒間通過させ、通過直後の紡糸張力(G9)を下記
(3)式に示す範囲内とし、給油した後に、4,500
〜5,500%の速度で巻取ることを特徴とするポリア
ミド繊維の製造法。 Tm−100≦T≦Tm+60           
(1)20D+0.0TV+Tm−500≦T≦10D
+0.04V+Tm−170 (2)5σ≦G≦17σ
           (3)
[Claims] After cooling the thermoplastic boronamide spun yarn melt-spun from the nozzle discharge hole to below the solidification and selling temperature of the polyamide, the following formulas (1) and (2) are applied. At the same time, in an atmosphere heated to a temperature (T'O) within a satisfactory range of 0.01 to 0.
After passing for 08 seconds, the spinning tension (G9) immediately after passing was within the range shown by the following formula (3), and after refueling, 4,500
A method for producing polyamide fibers, characterized by winding at a speed of ~5,500%. Tm-100≦T≦Tm+60
(1) 20D+0.0TV+Tm-500≦T≦10D
+0.04V+Tm-170 (2) 5σ≦G≦17σ
(3)
JP6878083A 1983-04-19 1983-04-19 Production of polyamide fiber Pending JPS59199810A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6878083A JPS59199810A (en) 1983-04-19 1983-04-19 Production of polyamide fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6878083A JPS59199810A (en) 1983-04-19 1983-04-19 Production of polyamide fiber

Publications (1)

Publication Number Publication Date
JPS59199810A true JPS59199810A (en) 1984-11-13

Family

ID=13383584

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6878083A Pending JPS59199810A (en) 1983-04-19 1983-04-19 Production of polyamide fiber

Country Status (1)

Country Link
JP (1) JPS59199810A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5137666A (en) * 1989-07-10 1992-08-11 E. I. Du Pont De Nemours And Company Multifilament apparel yarns of nylon
JPH07159731A (en) * 1993-12-09 1995-06-23 Fuji Elelctrochem Co Ltd Optical isolator

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5137666A (en) * 1989-07-10 1992-08-11 E. I. Du Pont De Nemours And Company Multifilament apparel yarns of nylon
JPH07159731A (en) * 1993-12-09 1995-06-23 Fuji Elelctrochem Co Ltd Optical isolator

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