JPH0333801B2 - - Google Patents

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Publication number
JPH0333801B2
JPH0333801B2 JP58208385A JP20838583A JPH0333801B2 JP H0333801 B2 JPH0333801 B2 JP H0333801B2 JP 58208385 A JP58208385 A JP 58208385A JP 20838583 A JP20838583 A JP 20838583A JP H0333801 B2 JPH0333801 B2 JP H0333801B2
Authority
JP
Japan
Prior art keywords
roller
yarn
spinning
entanglement
melt
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 - Lifetime
Application number
JP58208385A
Other languages
Japanese (ja)
Other versions
JPS60104512A (en
Inventor
Masahiro Matsui
Kikuo Hori
Masakazu Fujita
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.)
Teijin Ltd
Original Assignee
Teijin 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 Teijin Ltd filed Critical Teijin Ltd
Priority to JP20838583A priority Critical patent/JPS60104512A/en
Publication of JPS60104512A publication Critical patent/JPS60104512A/en
Publication of JPH0333801B2 publication Critical patent/JPH0333801B2/ja
Granted legal-status Critical Current

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  • Artificial Filaments (AREA)
  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

<産業上の利用分野> 本発明は単糸デニールが1.5デニール以下と小
さくかつ強度が3.5g/de以下と低い溶融紡糸繊
維を製造する方法に関するものである。 <従来技術> 従来から、単糸デニールの小さな糸の製造は、
工程調子が不良で、極めて困難であることが知ら
れている。 特に、紡糸工程調子もさることながら、延伸工
程で断糸やローラー捲付等が発生し易く、これが
最大の問題点である。 その上低強度糸ともなると、益々断糸やローラ
ー捲付等が発生し易く、製造のむずかしさは倍加
され、単糸デニール1.5デニール以下、強度3.5
g/de以下の繊維を工業的に安定に生産するこ
とは事実上不可能であつた。その為、従来単糸デ
ニールの小さな糸の製造方法としては、延伸工程
のない製造技術に開発の重点が移され、高速紡糸
技術(紡速3000m/分以上)が採用されていた。
即ち、高速紡糸+細デニール化+急速冷却化によ
り紡糸工程での配向結晶化を促進させ、延伸なし
で伸度40%以下の繊維を製造していた訳である。 しかるに従来の方法では単糸デニールが0.6デ
ニール以上、特に1デニール近辺となると、紡糸
過程での配向結晶化が充分に進まないため、製品
伸度が高くなりすぎる等、完全な延伸状態の糸と
はなり得ず、正常な製品糸としては使用できな
い。 更に延伸工程のない高速紡糸方法では製品糸の
強伸度、熱収縮率等の調整を紡糸条件で行うこと
が困難、即ち一旦設備が決まれば、ほとんど成行
の状態とならざるを得ない等の問題点がある。 又、単糸デニールが小さく、かつ低強度糸の製
造で技術的に最も困難な点は、前述の如く、延伸
工程での断糸、ローラー捲付の発生であり、この
点の克服が最大の技術検討主眼である。 本発明者案は、その解決案として、延伸前に単
糸に交絡処理を施し、各単糸を単独にではなく、
集団で挙動させることにより、単糸のみかけの太
さ及び糸強力を増加させて延伸過程に於ける単糸
の破断や延伸ローラー捲付を防止することを考え
た。 しかるに、通常採用されている条件下で、延伸
前に単糸に交絡処理を施し、しかる後に延伸する
と、未延伸部が発生し、いわゆるThick and
Thin糸が製造される。これは、交絡処理を施し
た後延伸する方法が、Thick and Thin糸の製造
方法として公知であることからも明らかである。 発明の目的および構成 そこで本発明者案は、未延伸糸の発生が起こら
ぬ様な単糸の絡ませ方法について鋭意検討した結
果、驚くべきことに、交絡処理時の糸の張力を
0.5g/de以上に増加させ、かつ交絡処理強度を
延伸後の糸で測定し、3ケ/m以上、10ケ/m以
下とすると共に、一旦捲取ることなく直ちに延伸
する(紡糸直延伸)ことにより未延伸糸の発生が
なく、かつ工程調子的に安定である(延伸断糸や
ローラー捲付がない)ことを見出し、本発明に到
達したものである。 すなわち、本発明は溶融紡糸後、一旦巻取るこ
となく引続いて延伸し、単糸繊度が1.5デニール
以下でかつ強度が3.5g/de以下の繊維を製造す
るに際し、第1ローラ(引取ローラー)前で油剤
を付与し、該油剤付与装置と第1ローラー間の張
力を0.5g/de以上にするとともにこの間で流体
交絡処理を施し、そのときの交絡度を延伸後の糸
で測定し3ケ/m以上、10ケ/m以下とすること
を特徴とするポリエステルの溶融紡糸方法であ
る。 本発明においては、張力が0.5g/de未満の場
合、延伸断糸やローラー捲付がない程度の交絡処
理を施すと、未延伸糸の発生が防止できない。 張力が0.5g/de以上では未延伸糸が発生しな
いことを見出したが、この原因は明確化された訳
ではないけれども、交絡処理後の糸の絡み状態の
観察から次の様に推定される。 即ち、低張力下で交絡処理を施すと、局部的に
強い絡みが発生し、第1図に示すようないわゆる
ちようちん状の交絡形態となる。 これに対し、高張力下で交絡処理を施すと、第
2図に示すように長く、ゆるい絡み形態となるこ
とから、前者では交絡の強いちようちん状のくび
れ部分で未延伸が集中的に発生するのに対し、後
者では未延伸が発生しないものと推定される。 又、延伸断糸やローラー捲付の発生しない交絡
度は、延伸後の糸で測定して3ケ/m以上、10
ケ/m以下が適当で、10ケ/mを越えると交絡処
理時の糸の張力を高めても未延伸が発生し、3
ケ/m未満では交絡効果が小さく、延伸断糸、ロ
ーラー捲付が発生する。更に、交絡処理を施した
未延伸糸を一旦捲取り放置した後に延伸すると、
一旦捲取ることなく直ちに延伸する場合に比較
し、延伸断糸やローラー捲付が多くなる。 この原因は判然としないが、本発明方法に於け
る交絡形態は通常の交絡形態とは大巾に異なり、
いわゆるちようちん状ではなく、長くゆるい絡み
であるため長時間の放置により繊維の収縮等がお
こり、この際絡みが弱まる様になるものと考えら
れる。 いずれにせよ、延伸前に適正な交絡処理を施す
こと、その時の張力を高くすること及び紡糸後一
旦捲取ることなく直ちに延伸することの3つの要
因があわさつて、初めて1.5デニール以下という
単糸デニールが小さく、3.5g/d以下と強度の
小さな糸の安定した製造が可能となつたのであ
る。 ここで、交絡処理時の張力、即ち油剤付与装置
と第1ローラー間の張力を増加させる方法として
は種々の方法が考えられるが、紡糸速度の増加
(1600m/分以上、好ましくは1700m/分以上)、
口金孔径の増大、即ち紡糸ドラフト率の増加
(150以上、好ましくは180以上)、冷却の強化(口
金下距離の短縮、冷却風線速度の増加等)等の方
法が特に有効である。 又、交絡処理装置としては特に限定されず、通
常の空気を使用したインターレースノズル又は仮
撚ノズル等の流体交絡処理装置が使用できる。 本発明方法では延伸前に交絡処理を施す事がポ
イントであるが、後工程での取扱い性を向上させ
るために延伸ローラーの後で、捲取前に更に交絡
処理を施してもよい。 但し、この時は延伸性を向上させるために延伸
前に施した交絡度の測定には捲取直前に施した交
絡度を考慮に入れてはいけないことはいうまでも
ない。 本発明方法が適用される繊維としては、ポリエ
ステルやポリアミド等、溶融紡糸で製造される繊
維にはすべて適用可能であるが、特に比較的ヤン
グ率が高く、交絡処理のし難いエチレンテレフタ
レートを主たる繰返し単位とするポリエステル繊
維に対し、効果が顕著である。 又、これらの繊維には第3成分を共重合又は混
合してもよい。特にテレフタル酸成分とエチレン
グリコール成分とからなるポリエチレンテレフタ
レート繊維の場合には、金属スルホネート基を含
有すると強度低下が著しく、特に金属スルホネー
ト基を例えば1.5〜4.5モル%含有させた場合には
通常のポリマー固有粘度にて強度が3.5g/d以
下となり、本発明範囲を満足する繊維が得られ
る。 尚、交絡度は、市販のエンタングルメントテス
ター(ロツシエルド社製)にて、通常の方法にて
測定したものである。 測定は絡み個数40ケを測定し、交絡度としては
1m当りの個数に巻算して表わす。 次に本発明を図面によつて説明する。 第3図は本発明方法を実施するに適した工程の
説明図である。図において、1は紡糸筒、2は走
行糸条、3は油剤付与装置、4は流体交絡処理装
置、5は第1ローラー(引取りローラー)、6は
第2ローラー(延伸ローラー)、7は捲取装置で
ある。 本発明方法は油剤付与装置3と第1ローラー5
との間で糸の張力を0.5g/d以上とすると共に
ここで流体交絡処理を施し、一旦捲取ることな
く、第1ローラー5と第2ローラー6との間で引
続いて延伸するものである。 発明の効果 以上の如く、本発明方法によれば、単糸デニー
ルが小さく、かつ低強度の糸を良好な工程調子
で、即ち延伸断糸やローラー捲付がなく、かつ未
延伸糸の発生もない良好な品質の糸を安定して製
造することが可能となる。 次に、本発明方法をさらに実施例により説明す
る。 実施例 1 エチレンテレフタレートを主たる繰返し単位と
し、5−ソジウムスルホイソフタル酸成分を全酸
成分に対して2.6モル%共重合させたポリエステ
ルを、第3図に示す紡糸延伸装置を使用し、72ケ
の孔を有する口金より溶融吐出し、速度1800m/
分で引取り、一旦捲取ることなく直ちに2.1倍に
延伸し、製品繊度75デニール、単糸維度にして
1.04デニール、強度3.0g/dの製品糸を得た。
この時の紡糸張力は油剤付与装置と第1ローラー
の間で測定した値で冷却条件と口金孔径(紡糸ド
ラフト率)により、又流体交絡度は延伸後の糸で
測定したもので供給流体圧力を変更することによ
つて夫々変更し、下表(第1表)に示す結果を得
た。 又、比較のために紡糸後一旦捲取り、2日後に
延伸を実施するテストも行つた(水準No.6)。
<Industrial Application Field> The present invention relates to a method for producing melt-spun fibers having a small single filament denier of 1.5 denier or less and a low strength of 3.5 g/de or less. <Prior art> Traditionally, the production of small single denier yarns has been
It is known that the process is poor and extremely difficult. In particular, in addition to the spinning process conditions, yarn breakage and roller winding are likely to occur during the drawing process, which is the biggest problem. Moreover, when it comes to low-strength yarn, yarn breakage and roller winding are more likely to occur, and the difficulty of manufacturing is doubled.
It has been virtually impossible to stably industrially produce fibers with a g/de or less. For this reason, conventional methods for manufacturing small single-filament denier yarns have focused on manufacturing techniques that do not require a drawing process, and have adopted high-speed spinning techniques (spinning speeds of 3,000 m/min or higher).
That is, high-speed spinning + fine denier + rapid cooling promotes oriented crystallization in the spinning process, producing fibers with an elongation of 40% or less without drawing. However, in conventional methods, when the single yarn denier is 0.6 denier or more, especially around 1 denier, oriented crystallization does not proceed sufficiently during the spinning process, resulting in an excessively high elongation of the product, which results in problems with the fully drawn yarn. It cannot be used as a normal product thread. Furthermore, in high-speed spinning methods that do not involve a drawing process, it is difficult to adjust the strength and elongation of the product yarn, heat shrinkage rate, etc. in the spinning conditions. There is a problem. In addition, as mentioned above, the most technically difficult point in producing yarn with a small single yarn denier and low strength is the occurrence of yarn breakage and roller winding during the drawing process, and overcoming this point is the biggest challenge. The focus is on technical considerations. As a solution to this problem, the present inventor's proposal is to perform interlacing treatment on the single yarns before drawing, so that each single yarn is not treated individually.
The idea was to increase the apparent thickness and yarn tenacity of the single yarns by causing them to behave in groups, thereby preventing single yarns from breaking during the drawing process and from being wrapped around the drawing roller. However, under commonly used conditions, if the single yarn is subjected to interlacing treatment before drawing and then stretched, unstretched areas will occur, resulting in so-called thick and
Thin yarn is manufactured. This is clear from the fact that the method of drawing after the interlacing treatment is known as a method for producing thick and thin yarns. Purpose and Structure of the Invention The present inventor has made a proposal after intensively studying a method for entangling single yarns that does not generate undrawn yarns.
Increase the yarn to 0.5 g/de or more, and measure the intertwining strength of the yarn after stretching to make it 3 strands/m or more and 10 strands/m or less, and stretch it immediately without winding it up (direct spinning drawing). As a result, the present invention was achieved by discovering that there is no generation of undrawn yarns and the process is stable (no stretched yarn breakage or roller winding). That is, in the present invention, after melt-spinning, the first roller (take-up roller) The tension between the oil applying device and the first roller is set to 0.5 g/de or more, and a fluid entanglement process is performed between the two, and the degree of entanglement is measured on the stretched yarn. This is a method for melt-spinning polyester, characterized in that the spinning speed is at least /m and at most 10 /m. In the present invention, when the tension is less than 0.5 g/de, the generation of undrawn yarn cannot be prevented if the interlacing treatment is performed to the extent that there is no drawn yarn breakage or roller winding. It was found that undrawn yarn does not occur when the tension is 0.5 g/de or more, but although the cause of this has not been clarified, it is estimated as follows from observation of the entangled state of the yarn after the entangling treatment. . That is, when the entanglement treatment is performed under low tension, strong entanglement occurs locally, resulting in a so-called tangle-like form as shown in FIG. On the other hand, when the entanglement process is performed under high tension, the entanglement becomes long and loose as shown in Figure 2. However, it is presumed that unstretching does not occur in the latter case. In addition, the degree of entanglement that does not cause stretch yarn breakage or roller wrapping is 3 cases/m or more when measured with the yarn after stretching, and 10
The suitable value is less than 10 strands/m; if it exceeds 10 strands/m, unstretched yarn will occur even if the tension of the thread is increased during the intertwining process.
If it is less than x/m, the entangling effect will be small, and stretching and breakage and roller wrapping will occur. Furthermore, if the undrawn yarn that has been subjected to the interlacing treatment is wound up and then stretched,
Compared to the case where the yarn is immediately stretched without being wound up, the number of yarn breakage and roller winding increases. The cause of this is not clear, but the form of entanglement in the method of the present invention is vastly different from the usual form of entanglement.
Since the fibers are not so-called "chip-like" but long and loosely tangled, it is thought that if left for a long time, the fibers will shrink and the tangles will become weaker. In any case, the combination of three factors: performing appropriate entanglement treatment before drawing, increasing the tension at that time, and drawing immediately without winding after spinning, resulted in a single yarn denier of 1.5 denier or less. This made it possible to stably produce yarn with a low strength of less than 3.5 g/d. Here, various methods can be considered to increase the tension during the entangling process, that is, the tension between the oil application device and the first roller. ),
Particularly effective are methods such as increasing the diameter of the spinneret hole, that is, increasing the spinning draft rate (150 or more, preferably 180 or more), and strengthening cooling (shortening the distance under the spinneret, increasing the cooling air velocity, etc.). Further, the entanglement treatment device is not particularly limited, and a fluid entanglement treatment device such as an interlace nozzle or a false twist nozzle using ordinary air can be used. The key point in the method of the present invention is to perform an interlacing treatment before stretching, but in order to improve handling in the subsequent process, an additional entangling treatment may be performed after the stretching roller and before winding up. However, in this case, it goes without saying that the degree of entanglement applied immediately before winding must not be taken into consideration when measuring the degree of entanglement applied before stretching in order to improve stretchability. The method of the present invention can be applied to all fibers manufactured by melt spinning, such as polyester and polyamide, but it is especially applicable to fibers produced by melt spinning, such as polyester and polyamide. The effect is remarkable for polyester fibers used as units. Further, a third component may be copolymerized or mixed with these fibers. In particular, in the case of polyethylene terephthalate fibers consisting of a terephthalic acid component and an ethylene glycol component, the strength decreases significantly when metal sulfonate groups are contained. A fiber having an intrinsic viscosity of 3.5 g/d or less and satisfying the range of the present invention can be obtained. The degree of entanglement was measured by a conventional method using a commercially available entanglement tester (manufactured by Rothsield). Measurements were made for 40 entangled pieces, and the degree of entanglement was
It is expressed by counting the number of pieces per 1m. Next, the present invention will be explained with reference to the drawings. FIG. 3 is an explanatory diagram of steps suitable for carrying out the method of the present invention. In the figure, 1 is a spinning tube, 2 is a running thread, 3 is an oil agent application device, 4 is a fluid entanglement treatment device, 5 is a first roller (take-up roller), 6 is a second roller (drawing roller), and 7 is a It is a winding device. The method of the present invention includes an oil applying device 3 and a first roller 5.
The tension of the yarn is set to 0.5 g/d or more between the yarn and the yarn is subjected to a fluid entanglement treatment, and the yarn is continuously stretched between the first roller 5 and the second roller 6 without being wound up. be. Effects of the Invention As described above, according to the method of the present invention, yarns with a small single yarn denier and low strength can be processed in good process condition, that is, without drawing breakage or roller winding, and without generating undrawn yarns. It becomes possible to stably produce yarn of good quality. Next, the method of the present invention will be further explained using examples. Example 1 A polyester containing ethylene terephthalate as the main repeating unit and a 5-sodium sulfoisophthalic acid component copolymerized at 2.6 mol% based on the total acid component was made into 72 pieces using the spinning/drawing apparatus shown in Figure 3. Melt is discharged from a nozzle with holes, speed of 1800m/
It is pulled out in minutes and immediately stretched to 2.1 times without being rolled up, resulting in a product with a fineness of 75 denier and a single fiber count.
A product yarn with a denier of 1.04 and a strength of 3.0 g/d was obtained.
The spinning tension at this time is the value measured between the oil application device and the first roller, and depends on the cooling conditions and spinneret hole diameter (spinning draft rate).The degree of fluid entanglement is the value measured on the yarn after drawing, and depends on the supply fluid pressure. By changing each, the results shown in the table below (Table 1) were obtained. For comparison, a test was also conducted in which the yarn was wound up once after spinning and then stretched two days later (Level No. 6).

【表】【table】

【表】 ここで、延伸断糸率、ローラー捲付率は1doff5
Kg捲とし、1ton当りの生産量に換算した発生率
で、20%以下が不良、10%以下が良好である。 又、未延伸の発生は編地を染着し、判定した。 実施例 2 エチレンテレフタレートを主たる繰返し単位と
し、5−ソジウムスルホイソフタル酸成分を全酸
成分に対して3.5モル%共重合させたポリエステ
ルを、第3図に示す紡糸延伸装置を使用し、48ケ
の孔を有する口金より溶融吐出し、製品繊度50デ
ニール、単糸繊度にして、1.04デニール、強度2
〜2.5g/dの製品糸を得た。 この時、引取ローラー速度(紡糸速度)、引取
ローラーと延伸ローラーの速度比(延伸倍率)及
び紡糸ドラフト率、即ち口金径を種々変更し、下
表(第2表)に示す結果を得た。 尚、ここで、紡糸張力は実施例1と同様に油剤
付与装置と第1ローラーの間で測定した値、又、
流体交絡度は延伸後の糸で測定したもので、供給
流体圧力を変更することによつて調整した。
[Table] Here, the stretching breakage rate and roller winding rate are 1doff5
The occurrence rate is calculated based on production volume per 1 ton of kg, 20% or less is defective, and 10% or less is good. In addition, the occurrence of unstretchedness was determined by dyeing the knitted fabric. Example 2 A polyester containing ethylene terephthalate as the main repeating unit and a 5-sodium sulfoisophthalic acid component copolymerized in an amount of 3.5 mol% based on the total acid component was made into 48 pieces using the spinning/drawing apparatus shown in Figure 3. Melted and discharged from a nozzle with holes, the product fineness is 50 denier, the single yarn fineness is 1.04 denier, and the strength is 2.
A product yarn of ~2.5 g/d was obtained. At this time, the speed of the take-off roller (spinning speed), the speed ratio of the take-off roller and the stretching roller (stretching ratio), and the spinning draft ratio, that is, the diameter of the spinneret were variously changed, and the results shown in the table below (Table 2) were obtained. Here, the spinning tension is the value measured between the oil agent applying device and the first roller as in Example 1, and
The degree of fluid entanglement was measured on the yarn after drawing, and was adjusted by changing the supply fluid pressure.

【表】【table】

【表】 ここで、延伸断糸率、ローラー捲付率、未延伸
発生は実施例1と同一方法で判定した。 以上の結果より、本発明方法が単糸デニールが
小さく、低強度糸の製造に適した方法であること
が理解できる。
[Table] Here, the stretching yarn breakage rate, roller winding rate, and occurrence of unstretched yarn were determined by the same method as in Example 1. From the above results, it can be understood that the method of the present invention has a small single yarn denier and is suitable for producing low strength yarns.

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

第1図は低紡糸張力下で流体交絡処理を施した
場合の交絡形態を示す図、第2図は本発明方法に
示す高張力下で流体交絡処理を施した場合の交絡
形態を示す図、第3図は本発明を実施するに適し
た溶融紡糸巻取工程の説明図である。 1は紡糸筒、2は糸条、3は油剤付与装置、4
は流体交絡処理装置、5は第1ローラー(引取ロ
ーラー)、6は第2ローラー(延伸ローラー)、7
は巻取装置である。
FIG. 1 is a diagram showing the form of entanglement when fluid entanglement treatment is performed under low spinning tension, and FIG. 2 is a diagram showing the form of entanglement when fluid entanglement treatment is performed under high tension according to the method of the present invention. FIG. 3 is an explanatory diagram of a melt spinning winding process suitable for carrying out the present invention. 1 is a spinning tube, 2 is a yarn, 3 is an oil application device, 4
5 is a fluid entanglement processing device, 5 is a first roller (take-up roller), 6 is a second roller (stretching roller), 7
is a winding device.

Claims (1)

【特許請求の範囲】 1 溶融紡糸後、一旦巻取ることなく引続いて延
伸し、単糸繊度が1.5デニール以下でかつ強度が
3.5g/de以下のポリエステル繊維を製造するに
際し、第1ローラー(引取ローラー)前で油剤を
付与し、該油剤付与装置と第1ローラーの間の張
力を0.5g/de以上にするとともにこの間で流体
交絡処理を施し、そのときの交絡度を延伸後の糸
で測定し3ケ/m以上、10ケ/m以下とすること
を特徴とするポリエステルの溶融紡糸方法。 2 第1ローラーの引取り速度が1600m/分以上
である特許請求の範囲第1項記載のポリエステル
の溶融紡糸方法。 3 紡糸ドラフトが150以上である特許範囲第1
項若しくは第2項記載のポリエステルの溶融紡糸
方法。 4 溶融紡糸繊維が、エチレンテレフタレートを
主たる繰返し成分とし、金属スルホネート基を
1.5〜4.5モル%含有したポリエチレンテレフタレ
ートである特許範囲第1項もしくは第2項もしく
は第3項記載のポリエステルの溶融紡糸方法。
[Claims] 1. After melt spinning, the fiber is drawn without being wound up, and the single fiber fineness is 1.5 denier or less and the strength is
When producing polyester fibers of 3.5 g/de or less, an oil agent is applied in front of the first roller (take-up roller), the tension between the oil agent application device and the first roller is set to 0.5 g/de or more, and during this time 1. A method for melt spinning polyester, which comprises subjecting the yarn to a fluid entanglement treatment, and measuring the degree of entanglement of the drawn yarn to be 3 strands/m or more and 10 strands/m or less. 2. The polyester melt spinning method according to claim 1, wherein the take-up speed of the first roller is 1600 m/min or more. 3 Patent scope 1 where the spinning draft is 150 or more
A method for melt spinning polyester according to item 1 or 2. 4 Melt-spun fibers contain ethylene terephthalate as the main repeating component and metal sulfonate groups.
A method for melt-spinning a polyester according to the patent scope item 1, 2 or 3, which is polyethylene terephthalate containing 1.5 to 4.5 mol%.
JP20838583A 1983-11-08 1983-11-08 Melt-spinning process Granted JPS60104512A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20838583A JPS60104512A (en) 1983-11-08 1983-11-08 Melt-spinning process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20838583A JPS60104512A (en) 1983-11-08 1983-11-08 Melt-spinning process

Publications (2)

Publication Number Publication Date
JPS60104512A JPS60104512A (en) 1985-06-08
JPH0333801B2 true JPH0333801B2 (en) 1991-05-20

Family

ID=16555386

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20838583A Granted JPS60104512A (en) 1983-11-08 1983-11-08 Melt-spinning process

Country Status (1)

Country Link
JP (1) JPS60104512A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2768675B2 (en) * 1987-12-25 1998-06-25 東レ株式会社 Direct spinning and drawing method for polyester yarn

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6052615A (en) * 1983-08-31 1985-03-25 Toray Ind Inc Direct spinning, drawing, and winding of polyamide yarn

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6052615A (en) * 1983-08-31 1985-03-25 Toray Ind Inc Direct spinning, drawing, and winding of polyamide yarn

Also Published As

Publication number Publication date
JPS60104512A (en) 1985-06-08

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