JPS6352128B2 - - Google Patents

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Publication number
JPS6352128B2
JPS6352128B2 JP55020398A JP2039880A JPS6352128B2 JP S6352128 B2 JPS6352128 B2 JP S6352128B2 JP 55020398 A JP55020398 A JP 55020398A JP 2039880 A JP2039880 A JP 2039880A JP S6352128 B2 JPS6352128 B2 JP S6352128B2
Authority
JP
Japan
Prior art keywords
yarn
denier
yarns
spinning
mixed
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
JP55020398A
Other languages
Japanese (ja)
Other versions
JPS56118915A (en
Inventor
Kenkichi Nose
Hiroyuki Nagai
Takumi Shimazu
Hiroyuki Iimuro
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 JP2039880A priority Critical patent/JPS56118915A/en
Publication of JPS56118915A publication Critical patent/JPS56118915A/en
Publication of JPS6352128B2 publication Critical patent/JPS6352128B2/ja
Granted legal-status Critical Current

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  • 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]

本発明は風合のよい異デニール混繊糸を安価に
製造する方法に関するものである。 従来から芯に単糸デニールの大きい糸条を、表
層部に単糸デニールの小さい糸条を配合した混繊
糸を使用して表面タツチの優れた腰のある織編物
を製造することは知られている。かかる織編物
は、通常単糸デニールの大きい糸条の収縮率を、
単糸デニールの小さい糸条の収縮率よりも大きく
して混繊した混繊糸を製編織して収縮処理するこ
とにより得ている。この方法は単糸デニールの異
なる糸条を別々に製造する必要があり、生産性が
低下し、コスト高となつている。しかも、別個に
紡糸又は延伸した糸条を加工中に均一に混繊させ
ることは難しく、このため風合も十分満足し得る
までに至つていない。 一方、かかる欠点を解消する目的で、ポリエス
テルの紡糸工程において紡糸孔径の異なる2以上
の紡糸孔群から溶融吐出し、各糸条群を合糸して
巻取る方法(特開昭50−24529号公報)が提案さ
れている。この方法によれば紡糸工程のみで単糸
デニール及び配向度の異なる2種以上の未延伸糸
を十分に混合させた混繊糸を製造することができ
るため、生産性が増し、コスト的に有利で、且つ
混繊状態も均一化される。しかしながらこの混繊
糸を織編物にすると表面タツチが悪く、腰のない
風合となる欠点がある。 即ち、上述の如き同時紡糸により製造した混繊
糸は、前記特開昭公報の実施例1から明らかな如
く、単糸デニールの大きい糸条が低配向となり、
単糸デニールの小さい糸条が高配向となるため
に、製織編加工すると、単糸デニールの小さい糸
条が芯部に存在し、単糸デニールの大きい糸条が
表層部に位置して表面タツチの悪い風合しか得ら
れない。 本発明者らは、かかる従来法の欠点を解消する
べく研究を重ねた結果、同時紡糸を採用する場合
でも、紡糸孔群ごとに紡糸孔1孔当りの吐出量を
異ならしめると共に各紡糸孔群より吐出された糸
条に張力差を与えることにより、分子配向(複屈
折率で表わされる)が調整され得ることを見出
し、本発明に到達したものである。 すなわち、本発明は 熱可塑性合成樹脂を2種の紡糸孔群から溶融紡
糸して単糸デニールの異なる2種の糸条を形成せ
しめ、次いで合糸して異デニール混繊糸を製造す
るに際し、各紡糸孔群の紡糸孔1孔当りの吐出量
を異ならしめると共に単糸デニールの大きい糸条
の複屈折率が、単糸デニールの小さい糸条の複屈
折率の1.3倍以上になるように、単糸デニールの
大きい糸条の集束長を単糸デニールの小さい糸条
の集束長より長くすることを特徴とする異デニー
ル混繊糸の製造方法 である。 本発明で言う集束長とは紡糸口金の吐出面から
集束ガイドまでの距離である。また、本発明を適
用する熱可塑性樹脂は溶融紡糸中の糸条張力が、
集束長を変更することによつて変化し得るもので
あれば、どんなものでもよく、特にポリエステル
やナイロン等が好適である。 本発明によれば、このような溶融紡糸可能な合
成樹脂を複数の紡糸孔群から各紡糸孔群ごとに紡
糸孔1孔当りの吐出量を異らしめて溶融吐出す
る。こゝで言う複数の紡糸孔群は、別個の紡糸口
金に設けたものでもよい。 各紡糸孔群は互いに紡糸孔1孔当りの吐出量が
異るように構成されておれば良く、この孔径、孔
数の何れを異らしめても、1孔当りの吐出量に差
を与え得るが、工業的に実施する場合には紡糸孔
径が同じで紡糸孔数の異なる複数個の紡糸口金を
使用するのが特に好適である。 各紡糸孔群の1孔当りの吐出量の差は、小さく
てもそれなりの風合が得られるが、本発明のよう
に紡糸孔群が2個の場合は、単糸デニールの大き
い糸条の単糸デニールが単糸デニールの小さい糸
条の単糸デニールの1.2倍以上になるのが好まし
い。 本発明にあつては、上述の如く複数の紡糸孔群
から複数の糸条を溶融吐出し、単糸デニールの大
きい糸条の集束長を単糸デニールの小さい糸条の
集束長より長くする。こうすることによつて、単
糸デニールの大きい糸条は、単糸デニールの小さ
い糸条に比較して、糸条の受ける空気抵抗が増大
して糸条張力が増大し、その結果その分子配向即
ち複屈折率が大になる。集束長を長くする程度
は、単糸デニールの大きい糸条の複屈折率が単糸
デニールの小さい糸条の複屈折率よりも大きくな
る必要があり、好ましくは単糸デニールの大きい
糸条の複屈折率を△n1、単糸デニールの小さい糸
条の複屈折率を△n2とすれば△n1/△n2≧1.3と
するのがよい。△n1≦△n2となると単糸デニール
の大きい糸条が芯に、単糸デニールの小さい糸条
が表層部に配置されなくなるので表面タツチが悪
くなる。また1<△n1/△n2<1.3となると一応
単糸デニールの大きい方の糸条が芯に、単糸デニ
ールの小さい方の糸条が表層部に配置されるけれ
ども充分とは言い難い。その上ボリユーム感も少
ない。 本発明は単糸デニールの異なる糸条群を別々に
集束した後オイリングして合糸するか、又は先に
集束合糸して集束部近傍にてオイリングする。合
糸はインターレースノズルを使用して混繊交絡処
理する方が均一に混繊され、紡糸以降の工程にお
いてループや糸割れが防がれるのでより好まし
い。紡糸の引取速度は2000〜5500m/分の範囲に
するのが好ましい。紡糸引取速度が2000m/分よ
りも小さい場合、集束長による糸条張力の変化が
小さくなるので好適な範囲が狭くなる。 次に図面を用いて説明する。図面は本発明の好
適な実施態様を示す紡糸装置の概略側面図であ
り、1及び1′は紡糸口金、2は冷却風吹出部、
3及び4は集束ガイド、5はオイリングローラ、
6及び7はゴデツトローラ、8はインターレース
ノズル、9はワインダー、10はボビンを示し、
Y及びY′はそれぞれ単糸デニールの大きい糸条
及び単糸デニールの小さい糸条を示す。図におい
て紡糸口金1より吐出された単糸デニールの大き
い糸条Y及び紡糸口金1′より吐出された単糸デ
ニールの小さい糸条Y′は、冷却風吹出部2から
糸条と直交する方向に吹出される冷却風によつて
冷却される。冷却された両糸条Y及びY′は集束
ガイド3及び4でそれぞれ集束される。口金面か
ら集束ガイド3及び4までの距離即ち集束長L及
びL′はL>L′とする。一般に単糸デニールの小さ
い糸条の集束長L′は糸質に悪影響がない限り短く
し、単糸デニールの大きい糸条の集束長Lは紡糸
設備上可能な限り大きく取る方がボリユーム感の
ある表面タツチのよい織編物が得られる。我々の
実験ではL≧3mとし0.2m≦L′<2mとするのが好
適であつた。L′を短くし過ぎると繊度斑や密着が
発生する問題がある。 集束ガイド3及び4で集束された糸条Y及び
Y′はオイリングローラ5にてオイリングされた
後ゴデツトローラ6にて引取られる。ゴデツトロ
ーラ6にて引取られた糸Y及びY′はゴデツトロ
ーラ7との間に設けられたインターレースノズル
8にて混繊交絡処理される。インターレースノズ
ル8は特公昭36−12230号に記載されている公知
のノズルであり、インターレース度は通常30〜80
ケ/mの範囲に調整される。インターレースノズ
ルの位置はゴデツトローラ6及び7の間でもゴデ
ツトローラ7とワインダーの間でもよい。イン
ターレース処理された混繊糸はゴデツトローラ7
を経てワインダーによつてボビン10に巻取ら
れる。巻取後必要に応じて延伸される。 以上の如き方法で得られた混繊糸は、紡糸−工
程で一挙に製造することができるので極めて経済
的であり、しかも単糸デニールの小さい糸条は低
配向で低収縮性であるため織編物にした場合に表
層部に位置され、単糸デニールの大きい糸条は高
配向で高収縮性であるため織編物の芯部に位置さ
れ、腰があつて表面タツチが良く、しかもボリユ
ーム感のある優れた風合のものが得られるという
利点がある。 実施例 35℃オルソクロルフエノール溶液で測定した極
限粘度〔η〕が0.64のポリエチレンテレフタレー
ト(酸化チタン0.3重量%含有)の乾燥チツプを
図面に示す紡糸装置を使用し、口金として細単糸
用0.15φmm×72H、太単糸用0.15φmm×36Hを用い
て溶融温度298℃で吐出量を下表の条件で溶融吐
出した。吐出した2群の糸条は25℃の冷却風によ
つて通常の冷却を行つた後集束長をそれぞれ下表
の如く変更して通常のオイリングを施し、下表の
紡糸引取速度で引取り、巻取つてパツケージとし
た。 この際、図面に示す位置に糸道孔2.0φmm、圧空
孔0.8φmmのインターレース用ノズルを用いて圧空
圧4.5Kg/cm2Gで混繊処理した。 次に得られた混繊糸をメリヤス編にして100℃
20分間湿熱処理して風合を調べた。その結果を下
表に示す。
The present invention relates to a method for inexpensively producing mixed denier yarn with good texture. It has been known for a long time to produce woven and knitted fabrics with excellent surface touch and firmness by using a blended yarn with a large single-filament denier yarn in the core and a small single-filament denier yarn in the surface layer. ing. Such woven and knitted fabrics usually have a shrinkage rate of yarn with a large single denier,
It is obtained by weaving, weaving, and shrinking mixed yarns with a shrinkage rate higher than that of single yarns with a small denier. This method requires separate production of yarns with different single yarn deniers, resulting in lower productivity and higher costs. Moreover, it is difficult to uniformly mix separately spun or drawn yarns during processing, and for this reason, the texture has not yet been fully satisfied. On the other hand, in order to eliminate this drawback, in the polyester spinning process, the yarn is melted and discharged from two or more groups of spinning holes with different diameters, and each yarn group is combined and wound. Public bulletin) has been proposed. According to this method, it is possible to produce a blended yarn in which two or more types of undrawn yarns with different single filament deniers and degrees of orientation are sufficiently mixed only in the spinning process, which increases productivity and is advantageous in terms of cost. In addition, the mixed fiber state is also made uniform. However, when this mixed fiber yarn is made into a woven or knitted fabric, there is a drawback that the surface touch is poor and the texture is dull. That is, in the mixed fiber yarn produced by the above-mentioned simultaneous spinning, as is clear from Example 1 of the above-mentioned Japanese Patent Application Laid-Open No. 10-120001, yarns with a large single filament denier have a low orientation.
Since the yarns with a small single filament denier are highly oriented, when weaving and knitting, the yarns with a small single filament denier are present in the core, and the yarns with a large single filament denier are located in the surface layer and touch the surface. You can only get a bad texture. As a result of repeated research in order to eliminate the drawbacks of such conventional methods, the present inventors have found that even when simultaneous spinning is adopted, the discharge amount per spinning hole is made different for each spinning hole group, and each spinning hole group The present invention was achieved based on the discovery that the molecular orientation (expressed by birefringence) can be adjusted by applying a tension difference to the yarns discharged from the yarn. That is, the present invention involves melt-spinning a thermoplastic synthetic resin through two types of spinning hole groups to form two types of yarns with different single filament deniers, and then combining the yarns to produce a mixed denier yarn. The discharge amount per spinning hole of each spinning hole group is made different, and the birefringence of the yarn with a large single filament denier is 1.3 times or more that of the birefringence of the yarn with a small single filament denier. This is a method for producing a mixed denier yarn, characterized in that the bundle length of yarns with a large single filament denier is made longer than the bundle length of yarns with a small single filament denier. The focusing length in the present invention is the distance from the discharge surface of the spinneret to the focusing guide. In addition, the thermoplastic resin to which the present invention is applied has a yarn tension during melt spinning that is
Any material may be used as long as it can be changed by changing the focusing length, and polyester, nylon, etc. are particularly suitable. According to the present invention, such a melt-spun synthetic resin is melt-discharged from a plurality of spinning hole groups by varying the discharge amount per spinning hole for each spinning hole group. The plurality of spinning hole groups mentioned here may be provided in separate spinnerets. It is sufficient that each spinning hole group is configured so that the discharge amount per spinning hole is different from each other, and even if the hole diameter or the number of holes is different, the discharge amount per hole can be different. However, in the case of industrial implementation, it is particularly suitable to use a plurality of spinnerets having the same spinning hole diameter but different numbers of spinning holes. Even if the difference in the discharge amount per hole in each spinning hole group is small, a certain texture can be obtained, but when there are two spinning hole groups as in the present invention, yarns with a large single denier It is preferable that the single yarn denier is 1.2 times or more the single yarn denier of the yarn with a small single yarn denier. In the present invention, as described above, a plurality of yarns are melted and discharged from a plurality of spinning hole groups, and the bundled length of the yarns with a large single filament denier is made longer than the bundled length of the yarns with a small single filament denier. By doing this, yarns with a large single filament denier experience more air resistance and yarn tension, compared to yarns with a small single filament denier, and as a result, the molecular orientation of the yarn increases. That is, the birefringence becomes large. The degree to which the focusing length is increased is such that the birefringence of the yarn with a large single filament denier is larger than that of the yarn with a small single filament denier, and preferably the birefringence of the yarn with a large single filament denier is If the refractive index is △n 1 and the birefringence of a yarn with a small denier is △n 2 , it is preferable that △n 1 /△n 2 ≧1.3. When △n 1 ≦△n 2 , the yarn with a large single filament denier will not be placed in the core and the yarn with a small single filament denier will not be placed in the surface layer, resulting in poor surface touch. Also, when 1 < △n 1 / △n 2 < 1.3, the yarn with a larger single yarn denier is placed in the core and the yarn with a smaller single yarn denier is placed in the surface layer, but this cannot be said to be sufficient. . Moreover, there is little sense of volume. In the present invention, groups of yarns with different single filament deniers are bundled separately and then oiled and combined, or the yarns are bundled and combined first and then oiled near the bundled part. It is more preferable to use an interlace nozzle to mix and entangle the yarns, since the fibers are mixed uniformly and loops and yarn breakage are prevented in the steps after spinning. The spinning speed is preferably in the range of 2000 to 5500 m/min. When the spinning take-off speed is less than 2000 m/min, the change in yarn tension due to the convergence length becomes small, so the suitable range becomes narrow. Next, it will be explained using drawings. The drawing is a schematic side view of a spinning device showing a preferred embodiment of the present invention, in which 1 and 1' are spinnerets, 2 is a cooling air blowing part,
3 and 4 are focusing guides, 5 is an oiling roller,
6 and 7 are godet rollers, 8 is an interlace nozzle, 9 is a winder, 10 is a bobbin,
Y and Y' represent a yarn with a large single denier and a yarn with a small single denier, respectively. In the figure, the yarn Y with a large single denier discharged from the spinneret 1 and the yarn Y' with a small single denier discharged from the spinneret 1' are directed from the cooling air blowing part 2 in a direction perpendicular to the yarns. It is cooled by the cooling air blown out. Both of the cooled yarns Y and Y' are focused by focusing guides 3 and 4, respectively. The distances from the mouthpiece surface to the focusing guides 3 and 4, that is, the focusing lengths L and L', satisfy L>L'. In general, it is better to shorten the bundle length L' of yarns with a small single filament denier as long as it does not adversely affect the yarn quality, and to make the bundle length L of yarns with a large single filament denier as large as possible based on the spinning equipment, to create a sense of volume. A woven or knitted fabric with a good surface texture can be obtained. In our experiments, it was preferable to set L≧3m and 0.2m≦L′<2m. If L′ is too short, there is a problem that uneven fineness and adhesion will occur. Yarn Y and
Y' is oiled by an oiling roller 5 and then taken up by a godet roller 6. The yarns Y and Y' taken off by the godet roller 6 are mixed and entangled in an interlace nozzle 8 provided between the godet roller 7 and the godet roller 7. The interlace nozzle 8 is a known nozzle described in Japanese Patent Publication No. 36-12230, and the degree of interlace is usually 30 to 80.
It is adjusted to a range of 6/m. The interlace nozzle may be located between the godet rollers 6 and 7 or between the godet roller 7 and the winder 9 . The interlaced mixed fiber yarn is Godet Roller 7.
After that, it is wound onto a bobbin 10 by a winder 9 . After winding, it is stretched as necessary. The mixed fiber yarn obtained by the above method is extremely economical because it can be produced in one step by spinning and spinning, and the yarn with a small single filament denier has low orientation and low shrinkage, so it can be woven easily. When made into a knitted fabric, it is located in the surface layer, and the yarn with a large single yarn denier is highly oriented and has high shrinkage, so it is located in the core of the woven or knitted fabric, giving it a firm waist and good surface touch, as well as a voluminous feel. It has the advantage of providing a certain excellent texture. Example Dry chips of polyethylene terephthalate (containing 0.3% by weight of titanium oxide) with an intrinsic viscosity [η] of 0.64 measured in an orthochlorophenol solution at 35°C were used in the spinning apparatus shown in the drawing, and a spindle of 0.15φmm for fine single yarn was used. ×72H and 0.15φmm×36H for thick single yarns were melted and discharged at a melting temperature of 298°C and a discharge amount under the conditions shown in the table below. The two groups of yarns that were discharged were cooled in the usual way with cooling air at 25°C, then the convergence length was changed as shown in the table below, and the yarns were oiled in the usual way, and taken up at the spinning take-off speed shown in the table below. It was rolled up and used as a package. At this time, the fibers were mixed at an air pressure of 4.5 Kg/cm 2 G using an interlacing nozzle having a thread passage hole of 2.0 φ mm and a pressure hole of 0.8 φ mm at the position shown in the drawing. Next, the obtained mixed fiber yarn is stockinette knitted at 100℃.
It was subjected to a moist heat treatment for 20 minutes and its texture was examined. The results are shown in the table below.

【表】【table】

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

図面は本発明の実施態様例を示す紡糸装置の概
略正面図を示す。 1及び1′は紡糸口金、3及び4は集束ガイド、
6及び7はゴデツトローラ、8はインターレース
ノズル、9はワインダー、Y及びY′はそれぞれ
単糸デニールの大きい糸条及び単糸デニールの小
さい糸条を示す。
The drawing shows a schematic front view of a spinning device illustrating an embodiment of the present invention. 1 and 1' are spinnerets, 3 and 4 are focusing guides,
6 and 7 are godet rollers, 8 is an interlace nozzle, 9 is a winder, and Y and Y' are a yarn with a large single yarn denier and a yarn with a small single yarn denier, respectively.

Claims (1)

【特許請求の範囲】 1 熱可塑性合成樹脂を2種の紡糸孔群から溶融
紡糸して単糸デニールの異なる2種の糸条を形成
せしめ、次いで合糸して異デニール混繊糸を製造
するに際し、各紡糸孔群の紡糸孔1孔当りの吐出
量を異ならしめると共に単糸デニールの大きい糸
条の複屈折率が、単糸デニールの小さい糸条の複
屈折率の1.3倍以上になるように、単糸デニール
の大きい糸条の集束長を単糸デニールの小さい糸
条の集束長より長くすることを特徴とする異デニ
ール混繊糸の製造方法。 2 単糸デニールの大きい糸条の単糸デニール
が、単糸デニールの小さい糸条の単糸デニールの
1.2倍以上である特許請求の範囲第1項記載の異
デニール混繊糸の製造方法。 3 溶融紡糸の引取速度が2000m/分以上である
特許請求の範囲第1項〜第2項のいずれか1項記
載の異デニール混繊糸の製造方法。
[Claims] 1. A thermoplastic synthetic resin is melt-spun through two types of spinning holes to form two types of yarns with different single filament deniers, and then the yarns are combined to produce a mixed denier yarn. In this process, the discharge amount per spinning hole of each spinning hole group is made different, and the birefringence of the yarn with a large single filament denier is 1.3 times or more that of the yarn with a small single filament denier. A method for producing a mixed denier yarn, characterized in that the bundle length of yarns with a large single yarn denier is made longer than the bundle length of yarns with a small single yarn denier. 2 The single yarn denier of the yarn with a large single yarn denier is the same as that of the yarn with a small single yarn denier.
A method for producing a mixed denier yarn according to claim 1, which is 1.2 times or more. 3. The method for producing a mixed denier yarn according to any one of claims 1 to 2, wherein the take-up speed of melt spinning is 2000 m/min or more.
JP2039880A 1980-02-22 1980-02-22 Production of different denier blended fiber yarn Granted JPS56118915A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2039880A JPS56118915A (en) 1980-02-22 1980-02-22 Production of different denier blended fiber yarn

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2039880A JPS56118915A (en) 1980-02-22 1980-02-22 Production of different denier blended fiber yarn

Publications (2)

Publication Number Publication Date
JPS56118915A JPS56118915A (en) 1981-09-18
JPS6352128B2 true JPS6352128B2 (en) 1988-10-18

Family

ID=12025907

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2039880A Granted JPS56118915A (en) 1980-02-22 1980-02-22 Production of different denier blended fiber yarn

Country Status (1)

Country Link
JP (1) JPS56118915A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS621003A (en) * 1985-06-26 1987-01-07 Amada Co Ltd Numerical controller capable of changing setting of memory contents
JPS621002A (en) * 1985-04-01 1987-01-07 セムトロニクス インク Digital pulse converted servo control system

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS621002A (en) * 1985-04-01 1987-01-07 セムトロニクス インク Digital pulse converted servo control system
JPS621003A (en) * 1985-06-26 1987-01-07 Amada Co Ltd Numerical controller capable of changing setting of memory contents

Also Published As

Publication number Publication date
JPS56118915A (en) 1981-09-18

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