JPS6022085B2 - Melt spinning method for nylon-6 fibers - Google Patents

Melt spinning method for nylon-6 fibers

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Publication number
JPS6022085B2
JPS6022085B2 JP57114474A JP11447482A JPS6022085B2 JP S6022085 B2 JPS6022085 B2 JP S6022085B2 JP 57114474 A JP57114474 A JP 57114474A JP 11447482 A JP11447482 A JP 11447482A JP S6022085 B2 JPS6022085 B2 JP S6022085B2
Authority
JP
Japan
Prior art keywords
yarn
fibers
godet roller
nylon
oil
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP57114474A
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Japanese (ja)
Other versions
JPS599208A (en
Inventor
知乏 青木
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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Filing date
Publication date
Application filed by Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP57114474A priority Critical patent/JPS6022085B2/en
Publication of JPS599208A publication Critical patent/JPS599208A/en
Publication of JPS6022085B2 publication Critical patent/JPS6022085B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明はナイロン−6繊維の溶融紙糸方法、特に高速製
糸方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a process for producing nylon-6 fibers into fused paper yarn, particularly a high-speed yarn spinning process.

ポリアミド繊維の溶融紡糸方法として、禾延伸糸を製造
する紙糸工程と該禾延伸糸を延伸して有用な繊維を製造
する延伸工程に分割した方法(コンベンショナル方式)
が多く実施されてるが、池方紡糸工程と延伸工程を直結
して生産性を向上させる目的の高速製糸法の開発が活発
に進められ、実施されつつある。
As a melt-spinning method for polyamide fibers, a method is divided into a paper yarn process to produce a drawn yarn and a drawing process to produce useful fibers by stretching the drawn yarn (conventional method).
However, the development of high-speed spinning methods for the purpose of directly connecting the Ikekata spinning process and the drawing process to improve productivity is being actively pursued and implemented.

しかし、高速製糸法で得られた糸はコンベンショナル法
で得られた糸に比較し内部構造がルーズでありト染色時
の均梁性はすぐれている反面洗濯等の湿潤堅ロウ性に劣
るという欠点を有している。特にスポーツ用途に多く供
給されているポリアミド繊維にとって致命的な欠点とな
る。この欠点をカバーするため種々の検討がされている
However, yarns obtained by high-speed spinning methods have a looser internal structure than yarns obtained by conventional methods, and while they have better uniformity during dyeing, they have poor wet waxing properties when washed, etc. have. This is a fatal drawback especially for polyamide fibers, which are widely supplied for sports applications. Various studies have been made to overcome this drawback.

その例として■タンニン酸をブレンドして製糸する方法
(特開昭5−6672び号)、■多価アミンをブレンド
して製糸する方法(椿関昭52−124927)、■ア
ミ/末端基量を規制して製糸する方法(持関昭54一2
3717号)等の提案がなされている。しかし、高速製
糸方法の狙いは工程省略による合理化で製造コストを下
げる事にあり、染色時の糸切れが多く発生すれば、収率
の低下、要員夕の増加となり合理化の効果がうすれてし
まう。すなわち、製糸性に悪影響のないようにするには
異種の物質をブレンドしたり、コンベンショナルと異な
った原料を使用する事なく染色堅ロウ性を向上させる必
要がある。0 一方、繊維には製糸工程で必要な油剤お
よび高次工程で必要な製糸時に付与させており、この油
剤が付着ムラとなっていれば製糸性および高次加工時の
トラブルとなり易い。
Examples include: ■ A method for spinning yarn by blending tannic acid (Japanese Unexamined Patent Publication No. 5-6672), ■ A method for spinning yarn by blending a polyvalent amine (Tsubaki Seki Sho 52-124927), ■ Amine/terminal group amount A method of spinning silk by regulating the
No. 3717) and other proposals have been made. However, the aim of the high-speed silk reeling method is to reduce manufacturing costs by streamlining processes by omitting processes, and if thread breakage occurs frequently during dyeing, the yield will drop and the number of personnel will increase, reducing the effectiveness of streamlining. That is, in order to avoid adverse effects on yarn-spinning properties, it is necessary to improve dyeing fastness without blending different substances or using raw materials different from conventional ones. 0 On the other hand, the fibers are applied with an oil agent required in the spinning process and during yarn spinning that is required in a higher-order process, and if this oil agent is applied unevenly, it is likely to cause problems in yarn-spinning performance and higher-order processing.

繊維の走行速度がおそいコンベンショナル方法の場合は
油剤の均一付タ与が比較的簡単になされていたが、高速
製糸方法の場合は繊維の走行速度が遠いため油剤の均一
付与が難しくなるばかりか、繊維に付与した油剤が高速
走行しているためふりきられて雰囲気中に飛散するとい
う問題点がある。本発明はかかる従来技術の諸欠点に鑑
み創案されたもので、その目的は高速走行中の繊維に油
剤を均一にかつ極力雰囲気中に飛散しないように付着可
能であると共に得られた糸の染色堅ロウ性を向上させる
ことの出釆る溶融紡糸方法を提供することにある。
In the conventional method, where the fiber running speed is slow, it is relatively easy to uniformly apply an oil agent, but in the case of a high-speed spinning method, the fiber traveling speed is far, which makes it difficult to uniformly apply an oil agent. There is a problem in that the oil applied to the fibers is blown off and scattered into the atmosphere because it is traveling at high speed. The present invention was devised in view of the various drawbacks of the prior art, and its purpose is to make it possible to apply an oil agent uniformly to fibers running at high speed and to prevent it from scattering into the atmosphere as much as possible, and to dye the resulting yarn. The object of the present invention is to provide a melt spinning method that improves fastness.

かかる本発明の目的は、 ‘1’ 溶融紡出されたナイロン−6繊維を冷却固化し
た後、水分率が1.5〜3.仇X%になるようにオィリ
ングを施し、次いで該糸条に第1ゴデーローラーと第2
ゴデーローラー間で20〜60%の伸張を与えた後、3
500の/分以上の速度で巻き上げることを特徴とする
ナイロン−6繊維の溶融* 紡糸方法。
The object of the present invention is to cool and solidify melt-spun nylon-6 fibers so that the moisture content is 1.5 to 3. Oiling is applied to the yarn so that it becomes X%, and then the first Godet roller and the second
After giving a stretch of 20-60% between Godet rollers, 3
A method for melt spinning* of nylon-6 fibers, characterized by winding up at a speed of 500 mm/min or more.

‘21 溶融縦出されたナイロン一6繊維を冷却固化し
た後、水分率が1.5〜3.仇九%になるように第1段
オィリングを施し、次いで該糸条に第1ゴデーローラー
と第2ゴデーローラー間で20〜60%の伸長を与えた
後、第2ゴデーローラー直下に設置したエアー交給装置
によって1段目で付与した油剤をマィグレーションさせ
、しかる後に加工糸用油剤を付与し、3500m/分以
上の速度で巻き上げることを特徴とするナイロン−6繊
維の溶融紙糸方法。
'21 After cooling and solidifying the molten nylon 16 fibers, the moisture content was 1.5 to 3. After applying the first stage oiling so that the fiber density is 9%, and then elongating the yarn by 20 to 60% between the first Godet roller and the second Godet roller, an air supply device installed directly below the second Godet roller is applied. A method for melting paper yarn of nylon-6 fibers, characterized in that the oil applied in the first stage is migrated, then the oil for processed yarn is applied, and the yarn is wound at a speed of 3500 m/min or more.

但しここでいう伸長とは次式で表わしたものである。However, the expansion mentioned here is expressed by the following formula.

傷由2ゴデーローラーの間遠)−(第1ゴデーローラー
の同速)xl。
Damage (distant distance between the 2nd Godet roller) - (same speed of the 1st Godet roller) xl.

〇第1ゴデーローラーの周速により達成される。〇Achieved by the peripheral speed of the first Godet roller.

本発明においては、口金から溶融紙糸された糸条が十分
冷却されて第1ゴデーローラーに引取られる前に第1段
目の給油装置により、その水分率が1.5〜3.肌t%
になるようにオィリングを施す必要がある。
In the present invention, before the fused paper yarn is sufficiently cooled from the spinneret and taken up by the first Godet roller, the first stage oil supply device lowers the moisture content to 1.5 to 3. skin t%
It is necessary to apply oiling so that

この1段目で付着される水分率が3.0%を上廻る場合
は非晶部の鯨向が低下し、得られた糸の染色堅ロウ度が
著しく劣るものとなる。また同時に糸条が高速走行して
いるため雰囲気中に油剤が飛散し、生産設備としては環
境上好ましくない。一方、水分率が1.5%未満の場合
は染色堅ロウ性は問題ないが、第1ゴデーローラーおよ
び第2ゴデーローラー上で糸がスリップし易く、糸ムラ
が大きくなると同時に安定した製糸性を得る事が困難と
なる。上述の染色堅ロウ性、糸ムラおよび製糸性のそれ
ぞれを十分満足させるには、水分率が2.0%〜3.0
%の範囲が特に好ましい。所定の水分率を満足するよう
にオィリングされた糸条は、次いで第1ゴデーローラー
と第2ゴデーローラ−間で20〜60%の伸張を付与さ
れた後、3500の/分以上の速度で巻上げることによ
り、染色堅ロウ度の向上した糸ムラの少ない糸条を良好
な製糸性の下に得ることができる。この場合、第1ゴデ
ーローラーと第2ゴデ−ローラーの間伸長が20%を下
廻るような場合は残留伸度が大きくなり鯨向が低く染色
堅ロウ性が低下する。
If the moisture content deposited in the first stage exceeds 3.0%, the orientation of the amorphous portion will decrease, and the dye fastness of the resulting yarn will be significantly inferior. At the same time, since the yarn is running at high speed, oil is scattered in the atmosphere, which is not environmentally preferable for production equipment. On the other hand, if the moisture content is less than 1.5%, there is no problem with dyeing fastness, but the thread tends to slip on the first Godet roller and the second Godet roller, increasing yarn unevenness and making it difficult to obtain stable spinning performance. becomes difficult. In order to fully satisfy each of the above-mentioned dyeing fastness, yarn unevenness, and yarn spinnability, the moisture content should be 2.0% to 3.0%.
% range is particularly preferred. The yarn oiled to satisfy a predetermined moisture content is then stretched by 20 to 60% between the first Godet roller and the second Godet roller, and then wound at a speed of 3500 rpm or more. As a result, a yarn with improved dye fastness and less yarn unevenness can be obtained with good spinning properties. In this case, if the elongation between the first Godet roller and the second Godet roller is less than 20%, the residual elongation will be large, the grain orientation will be low, and the dye fastness will be reduced.

また、この伸長が60%を上廻るような場合は第1ゴデ
ーローラーのスピードが低下し糸の配向がルーズになる
。このルーズな状態で水分が付与されるため糸の表層付
近に球晶が発生すると同時にボィドも多く発生する。こ
のボイドの数が増すため平均的な染色の堅。ゥ度は低下
するので望ましくない。上述の状態で得られた糸は油剤
の付着量が少なく、また高速走行しているため油剤の付
着ムラも大きいためそのままでは高次加工向きに好適な
原糸とは云い難い。
Further, if this elongation exceeds 60%, the speed of the first Godet roller decreases and the orientation of the yarn becomes loose. Since water is added in this loose state, spherulites are generated near the surface layer of the yarn, and at the same time, many voids are also generated. This increases the number of voids due to the average staining hardness. This is undesirable because it lowers the degree of corrosion. The yarn obtained in the above condition has a small amount of oil attached, and since it is running at high speed, the oil adheres unevenly, so it is difficult to say that it is a raw yarn suitable for high-order processing as it is.

本発明において高次加工用として優れた糸を得るために
は、第1ゴデーローラーと第2ゴデー。
In the present invention, in order to obtain a yarn excellent for high-order processing, the first Godet roller and the second Godet roller are required.

−ラ−との間で所定の伸長を付与された糸条に、該第2
ゴデーローラー直下に設置したエアー交路装置で糸条に
直交したエアーを噴き付けて、1段目で付与した油剤を
マィグレーションさせ、次いでエアー交絡装置を通過し
た糸条に、高次加工工程で必要な油剤を追濁して適正な
油分および水分付着量にして巻上げることが必要である
。尚マィグレーションに必要なエアーの圧力としてはl
k9/枕G〜6k9/〆Gあれば十分である。
- The second yarn is given a predetermined elongation between the
An air crossing device installed directly below the godet roller sprays air perpendicular to the yarn to migrate the oil applied in the first stage, and then the yarn that has passed through the air entangling device is processed in a higher processing step. It is necessary to add the necessary oil to the appropriate amount of oil and moisture and roll it up. The air pressure required for migration is l.
k9/pillow G to 6k9/〆G is sufficient.

次に本発明の効果を実施例により具体例に説明する。実
施例1〜3、比較例1〜4 ナイロン−6チップ(相対粘度2.6)を溶融紡糸し、
巻取後の織度が70デニールで24フィラメントになる
様に吐出させ冷却したのち1段目の給油装置でもつて、
水分付着量がそれぞれ1.0%,1.5%,2.0%,
3.0%、4.0%,5.0%,6.0%となるように
給油し、その後第2ゴデーローラーが4500肌/分で
第1ゴデーローラーと第2ゴデーローフー間で40%の
伸長を与えて巻上げた糸の染色堅ロ*ウ度、糸ムラ、油
剤の雰囲気中への飛散状態および製糸性を評価した。
Next, the effects of the present invention will be explained in detail using Examples. Examples 1 to 3, Comparative Examples 1 to 4 Nylon-6 chips (relative viscosity 2.6) were melt-spun,
After being discharged and cooled so that the weave after winding is 70 denier and 24 filaments, the first stage oil supply device is also used.
The amount of moisture attached is 1.0%, 1.5%, 2.0%, respectively.
Lubricating the oil to 3.0%, 4.0%, 5.0%, and 6.0%, then the second Godet roller elongates 40% between the first Godet roller and the second Godet roller at 4500 skins/min. The dyeing fastness, yarn unevenness, scattering of oil agent into the atmosphere, and yarn spinnability of the yarn that was fed and wound were evaluated.

結果を表−1に示す。表−1表−1から明らかなごとく
本発明を満足する実施例1〜3は比較例1〜4に比べて
製糸性、ウースタームラ、染色堅ロウ度が優れているう
え、油剤の飛散も皆無であった。
The results are shown in Table-1. Table 1 As is clear from Table 1, Examples 1 to 3 that satisfy the present invention are superior to Comparative Examples 1 to 4 in spinning properties, Worcester unevenness, and dye fastness, and there is no oil scattering. Met.

実施例4〜7、比較例5〜8 ナイロン−6チップ(相対粘度2.6)を溶融紡糸し、
巻取後の織度が70デニールで24フィラメントになる
様に吐出させ冷却したのち1段目の給油装置で水分付着
量が2.5%になるように給油し、その後第1ゴデーロ
ーラーと第2ゴデーローフー×間でそれぞれ0%,10
%,20%,30%,40%,60%,80%、および
100%の伸長を与えたのち4500の/分で巻上げた
糸の残留伸度、複屈折率および染色堅ロウ度を評価した
Examples 4 to 7, Comparative Examples 5 to 8 Nylon-6 chips (relative viscosity 2.6) were melt-spun,
After being discharged and cooled so that the weave after winding is 70 denier and 24 filaments, the first stage oil supply device supplies oil so that the moisture adhesion amount is 2.5%, and then the first Godet roller and the second 0% and 10 respectively between Gode Rofu ×
%, 20%, 30%, 40%, 60%, 80%, and 100% elongation and then winding at 4500/min, the residual elongation, birefringence, and color fastness were evaluated. .

結果を表−2に示す。表−2から明らかなごと〈本発明
で規定した伸長条件を外れる比較例5〜8の場合、染色
堅ロウ度が著しく低下することが分かる。又、この結果
は伸度、複屈折率だけでは説明できず、水分を付与する
時点の配向が染色堅ロウ度に影響があることを示してい
る。表−2 実施例8〜1い比較例9〜12 ナイロン−6チップ(相対粘度2.6)を溶融紡糸し、
巻取後の織度が70デニールで24フィラメントになる
様に吐出させ冷却したのち1段目の給油装置で水分付着
量が1%,2.5%,4.5%となるように給油し、そ
の後第1ゴデーローラーと第2ゴデーローラー間で40
%の伸長を与え、第2ゴデーローラーから4500肌/
分で送り出し、この直下に設けたエアー交絡装置でそれ
ぞれエアー圧ok9/嫌G,lk9/塊G,3k9/流
Gと変更し、その後2段給油装置でトータル水分が4.
5%、油分が1.0%となるように給油し巻上げた糸の
染色竪ロウ度および糸タテ方向の油剤の付着ムラ状態を
評価した。
The results are shown in Table-2. As is clear from Table 2, it can be seen that in the case of Comparative Examples 5 to 8, which deviate from the elongation conditions specified in the present invention, the color fastness is significantly reduced. Furthermore, this result cannot be explained by elongation and birefringence alone, but indicates that the orientation at the time of adding moisture has an effect on color fastness. Table 2 Examples 8 to 1 Comparative Examples 9 to 12 Nylon-6 chips (relative viscosity 2.6) were melt-spun,
After being discharged and cooled so that the weave after winding is 70 denier and 24 filaments, oil is supplied in the first stage oiling device so that the amount of moisture attached is 1%, 2.5%, and 4.5%. , then 40 between the first Godet roller and the second Godet roller
% elongation and 4500 skin/
The air pressure was changed to ok9/no G, lk9/lump G, and 3k9/flow G using the air entangling device installed directly below this, and then the total water content was adjusted to 4.
5% and the oil content was 1.0%, and the yarn was wound up and evaluated for dyeing waxiness and unevenness of oil adhesion in the longitudinal direction of the yarn.

結果を表−3に示す。付着水分率が多くなるほどエアー
圧力が高くな**るほど糸タテ方向の油剤付着ムラは少
なくなる。
The results are shown in Table-3. As the moisture content increases and the air pressure increases, the unevenness of oil adhesion in the yarn warp direction decreases.

しかし染色堅ロウ度は低下する。染色堅ロゥおよび糸タ
テ方向の付着ムラ両者を満足させる適正条件がそこに存
在することが分る。表−3 尚実施例及び比較例において染色堅ロゥ度及び油剤付着
ムラは次の方法で測定評価したものである。
However, the color fastness is reduced. It can be seen that there are appropriate conditions that satisfy both dyeing hardness and uneven adhesion in the yarn warp direction. Table 3 In Examples and Comparative Examples, dye fastness and oil adhesion unevenness were measured and evaluated using the following methods.

染色堅ロウ度について、筒縞地を作成し次の条件で染色
した。
Regarding the color fastness, a cylindrical striped fabric was prepared and dyed under the following conditions.

XyleneFastBlueP125%
2%owf錯酸 1%〃アミラ
ジンD 3%〃 を用い98℃で6び分 浴比1:100で染色後次のフ
イツクス処理を行なった。
XyleneFastBlueP125%
After dyeing using 2% owf complex acid 1% and 3% amylazine D at 98° C. and a bath ratio of 1:100, the following fixing treatment was performed.

ナイロンフイツクスTH 5%oWf蟻
酸 1%〃を用いて80午○で30
分。
Using nylon fixes TH 5% o Wf formic acid 1%〃, 30 pm at 80 pm
Minutes.

その後ザプ52/そを入れた40qCの温水で45分(
裕比1:100)間洗濯を行なった後、その洗濯液を肉
眼で判定し5級 全く染料の色の無いもの 4級 ごくわずか色の形跡のあるもの 3級 ほんの少し色がついたもの 2級 少し色のついたもの 1級 かなり色がついたもの の5段階の分別を行なった。
After that, soak in 40qC warm water containing Zapu 52/So for 45 minutes (
After washing for 1:100 minutes, the washing liquid was judged with the naked eye: 5th grade: no dye color at all 4th grade: very slight trace of color: 3rd grade: slight color: 2nd grade Class: 1st grade for slightly colored items and 5 levels for very colored items.

油剤付着ムラについて 紙糸油剤中に市販の赤インクを10%濃度になる様に加
え付与後巻取った糸を筒編となしムラの状態を肉眼で判
定し、ムラの大きいもの、中ぐらいのもの、小さいもの
の3つに分別評価した。
Regarding uneven oil adhesion, add commercially available red ink to the paper yarn oil agent to a concentration of 10%, then wind up the yarn to make a tube knit, and judge the unevenness with the naked eye. Items were evaluated separately into three categories: large items and small items.

Claims (1)

【特許請求の範囲】 1 溶融紡糸されたナイロン−6繊維を冷却固化した後
、水分率が1.5〜3.0wt%になるようにオイリン
グを施し、次いで該糸条に第1ゴデーローラーと第2ゴ
デーローラー間で20〜60%の伸張を与えた後、35
00m/分以上の速度で巻き上げることを特徴とするナ
イロン−6繊維の溶融紡糸方法。 2 溶融紡出されたナイロン−6繊維を冷却固化した後
、水分率が1.5〜3.0wt%になるように第1段オ
イリングを施し、次いで該糸条に第1ゴデーローラーと
第2ゴデーローラー間で20〜60%の伸長を与えた後
、第2ゴデーローラー直下に設置したエアー交絡装置に
よつて1段目で付与した油剤をマイグレーシヨンさせ、
しかる後に加工糸用油剤を付与し、3500m/分以上
の速度で巻き上げることを特徴とするナイロン−6繊維
の溶融紡糸方法。
[Claims] 1. After cooling and solidifying the melt-spun nylon-6 fibers, oiling is applied so that the moisture content becomes 1.5 to 3.0 wt%, and then the yarn is passed through a first Godet roller and a first Godet roller. After giving a stretch of 20-60% between two Godet rollers, 35
1. A method for melt spinning nylon-6 fibers, which comprises winding up at a speed of 00 m/min or more. 2. After cooling and solidifying the melt-spun nylon-6 fibers, the first stage oiling is applied so that the moisture content becomes 1.5 to 3.0 wt%, and then the yarn is passed through a first Godet roller and a second Godet roller. After giving an elongation of 20 to 60% in between, the oil agent applied in the first stage is migrated by an air entangling device installed directly under the second Godet roller.
A method for melt-spinning nylon-6 fibers, which comprises subsequently applying a processed yarn oil and winding the fibers at a speed of 3,500 m/min or more.
JP57114474A 1982-07-01 1982-07-01 Melt spinning method for nylon-6 fibers Expired JPS6022085B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57114474A JPS6022085B2 (en) 1982-07-01 1982-07-01 Melt spinning method for nylon-6 fibers

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57114474A JPS6022085B2 (en) 1982-07-01 1982-07-01 Melt spinning method for nylon-6 fibers

Publications (2)

Publication Number Publication Date
JPS599208A JPS599208A (en) 1984-01-18
JPS6022085B2 true JPS6022085B2 (en) 1985-05-31

Family

ID=14638637

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57114474A Expired JPS6022085B2 (en) 1982-07-01 1982-07-01 Melt spinning method for nylon-6 fibers

Country Status (1)

Country Link
JP (1) JPS6022085B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ATE67799T1 (en) * 1985-04-22 1991-10-15 Basf Corp PROCESS FOR HIGH-SPEED SPINNING POLYAMIDE FIBERS.

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4896809A (en) * 1972-03-14 1973-12-11
JPS5083519A (en) * 1973-11-28 1975-07-05
JPS5738685B2 (en) * 1974-06-11 1982-08-17
DD124391A5 (en) * 1975-03-13 1977-02-16
JPS5838528B2 (en) * 1975-07-22 1983-08-23 帝人株式会社 Oiling Hohou
JPS5828370B2 (en) * 1975-08-28 1983-06-15 東レ株式会社 Polyamide spinning method
NL7702555A (en) * 1976-03-12 1977-09-14 Bayer Ag FAST MELT SPIN DRAWING METHOD FOR MANUFACTURE OF YARN FROM TAPE THREADS.
JPS6039761B2 (en) * 1977-05-06 1985-09-07 ユニチカ株式会社 Melt spinning method
JPS5418921A (en) * 1977-07-12 1979-02-13 Teijin Ltd Production of polyamide multifilament yarn

Also Published As

Publication number Publication date
JPS599208A (en) 1984-01-18

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