JPH09273043A - Spontaneously extensible polyester filament yarn, method for producing the same, and blended yarn containing spontaneously extensible polyester filament yarn - Google Patents

Spontaneously extensible polyester filament yarn, method for producing the same, and blended yarn containing spontaneously extensible polyester filament yarn

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Publication number
JPH09273043A
JPH09273043A JP10645096A JP10645096A JPH09273043A JP H09273043 A JPH09273043 A JP H09273043A JP 10645096 A JP10645096 A JP 10645096A JP 10645096 A JP10645096 A JP 10645096A JP H09273043 A JPH09273043 A JP H09273043A
Authority
JP
Japan
Prior art keywords
filament yarn
polyester filament
yarn
spontaneously
shw
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
JP10645096A
Other languages
Japanese (ja)
Inventor
Yoshihiko Sano
芳彦 佐野
Juichi Takeda
重一 武田
Hiroki Udo
裕樹 宇土
Yasuo Takada
靖夫 高田
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.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Rayon 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 Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Rayon Co Ltd
Priority to JP10645096A priority Critical patent/JPH09273043A/en
Publication of JPH09273043A publication Critical patent/JPH09273043A/en
Pending legal-status Critical Current

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  • Chemical Or Physical Treatment Of Fibers (AREA)
  • Artificial Filaments (AREA)
  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)

Abstract

(57)【要約】 【課題】 異収縮混繊糸に好適に用いられる自発伸長性
ポリエステルフィラメント糸及びその自発伸長性ポリエ
ステルフィラメント糸を含み織編物に嵩高性、ソフト感
を与え、ふかつき感、ヌメリ感を与えない混繊糸を提供
する。 【解決手段】 沸水処理後の160℃での乾熱処理で伸
長し、かつアルカリ減量の際に繊維軸方向に幅0.1〜
3μm、長さ5μm以上の筋状溝が繊維表面に形成され
る自発伸長性ポリエステルフィラメント糸、及びこの糸
を有機スルホン酸金属塩を含有する高配向ポリエステル
未延伸フィラメント糸を、ヒーターにてガラス転移温度
〜130℃の温度で0.02〜0.12g/dの張力下
で接触熱処理することにより得る。またこの自発伸長性
ポリエステルフィラメント糸と高収縮性ポリエステルフ
ィラメント糸とを混繊して混繊糸とする。
(57) 【Abstract】 PROBLEM TO BE SOLVED: To provide a woven or knitted fabric with bulkiness and softness, and to give a feeling of fuzzy, which includes a spontaneously extensible polyester filament yarn suitably used for a heterogeneous shrinkage mixed filament yarn and a spontaneously extensible polyester filament yarn. Provides a mixed yarn that does not give a slimy feel. SOLUTION: This is elongated by dry heat treatment at 160 ° C after boiling water treatment, and has a width of 0.1 to 0.1 in the fiber axis direction during alkali weight loss.
A glass transition of a spontaneously stretchable polyester filament yarn in which streak grooves with a length of 3 μm and a length of 5 μm or more are formed on the fiber surface, and a highly oriented polyester unstretched filament yarn containing the metal salt of an organic sulfonic acid. It is obtained by performing a contact heat treatment under a tension of 0.02 to 0.12 g / d at a temperature of from 130 ° C to 130 ° C. Further, the spontaneously stretchable polyester filament yarn and the high-shrinkage polyester filament yarn are mixed into a mixed yarn.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、自発伸長性ポリエ
ステルフィラメント糸及びその製造方法並びにその自発
伸長性ポリエステルフィラメント糸を含む混繊糸に関す
る。
TECHNICAL FIELD The present invention relates to a spontaneously extensible polyester filament yarn, a method for producing the same, and a mixed fiber containing the spontaneously extensible polyester filament yarn.

【0002】[0002]

【従来の技術】従来、織編物に嵩高性、ソフト感を付与
する方法として、低収縮性フィラメント糸と高収縮性フ
ィラメント糸とを組み合わせた異収縮混繊糸を用いるこ
とが知られているが、織編物組織の拘束により収縮差の
発現が阻害されて十分満足する風合いが得られなかっ
た。かかる欠点を改良する方法として、特開平1−25
0425号公報、特開平1−250433号公報等で低
収縮性フィラメント糸として自発伸長性フィラメント糸
を用い、自発伸長性フィラメント糸と高収縮性フィラメ
ント糸を組み合わせて混繊することが提案されている。
2. Description of the Related Art Conventionally, as a method of imparting bulkiness and softness to a woven or knitted fabric, it has been known to use a different shrinkage mixed fiber yarn in which a low shrinkage filament yarn and a high shrinkage filament yarn are combined. However, the restraint of the texture of the woven or knitted fabric impeded the development of the difference in shrinkage, so that a satisfactory texture was not obtained. As a method for improving such a defect, Japanese Patent Laid-Open No. 1-25
In Japanese Patent No. 0425, JP-A-1-250433, etc., it is proposed to use a spontaneously extensible filament yarn as the low-shrinkable filament yarn, and to mix the spontaneously extensible filament yarn and the highly-shrinkable filament yarn in combination. .

【0003】この方法で得られる異収縮混繊糸は、低収
縮性フィラメント糸/高収縮性フィラメント糸の混繊糸
と比べはるかに優れた嵩高性、ソフト感を織編物に与え
るが、染色仕上げ加工により混繊糸の鞘側に配置された
自発伸長性フィラメントによるループによってふかつき
感、ヌメリ感を与えるという点で好ましいものではなか
った。
The heterogeneous shrinkage mixed yarn obtained by this method gives the woven or knitted fabric a much better bulkiness and softness than the mixed yarn of the low shrinkage filament yarn / high shrinkage filament yarn. It is not preferable in that the loop formed by the spontaneously extensible filaments disposed on the sheath side of the mixed fiber by processing gives a feeling of stuffiness and a slimy feel.

【0004】[0004]

【発明が解決しようとする課題】本発明の目的は、異収
縮混繊糸に好適に用いられる自発伸長性ポリエステルフ
ィラメント糸及びその自発伸長性ポリエステルフィラメ
ント糸を含み織編物に嵩高性、ソフト感を与え、ふかつ
き感、ヌメリ感を与えない混繊糸を提供することにあ
る。
DISCLOSURE OF THE INVENTION An object of the present invention is to provide a self-expanding polyester filament yarn which is preferably used for a heterogeneous shrinkage mixed yarn and a woven or knitted fabric containing the self-expanding polyester filament yarn, which imparts bulkiness and a soft feeling. It is to provide a mixed yarn that does not give a feeling of stickiness, a feeling of stickiness, and a slimy feeling.

【0005】[0005]

【課題を解決するための手段】本発明は、下記(1)及
び(2)の要件を満足する収縮率を有し、かつアルカリ
減量の際に繊維軸方向に幅0.1〜3μm、長さ5μm
以上の筋状溝が隣接間隔5μm以下に繊維表面に形成さ
れることを特徴とする自発伸長性ポリエステルフィラメ
ント糸、 (1) SHD−SHW≦0% (2) SHW≦8% (但し、SHWは沸水収縮率(%)、SHDは沸水処理
後の160℃での乾熱収縮率(%)を示す)
The present invention has a shrinkage factor satisfying the following requirements (1) and (2), and has a width of 0.1 to 3 μm and a length in the axial direction of the fiber during alkali weight loss. 5 μm
Spontaneous stretchable polyester filament yarn, characterized in that the above-mentioned streak grooves are formed on the fiber surface at intervals of 5 μm or less, (1) SHD-SHW ≦ 0% (2) SHW ≦ 8% (where SHW is Boiling water shrinkage (%), SHD indicates dry heat shrinkage (%) at 160 ° C. after boiling water treatment)

【0006】及び、エチレンテレフタレートを主たる繰
り返し単位とし、一般式R−SO3M(Rは炭素数3〜
30のアルキル基、炭素数7〜40のアリール基、Mは
アルカリ金属)で表される有機スルホン酸金属塩を0.
1〜10重量%含有する複屈折率Δnが0.03〜0.
08の高配向ポリエステル未延伸フィラメント糸を、ヒ
ーターにてガラス転移温度〜130℃の温度で0.02
〜0.12g/dの張力下で接触熱処理することを特徴
とする自発伸長性ポリエステルフィラメント糸の製造方
法、
In addition, ethylene-terephthalate is used as a main repeating unit, and the general formula R-SO 3 M (R is a carbon number of 3 to
30 is an alkyl group, an aryl group having 7 to 40 carbon atoms, and M is an alkali metal).
The birefringence Δn contained in the range of 1 to 10% by weight is 0.03 to 0.
The highly oriented polyester unstretched filament yarn of No. 08 was heated to 0.02 at a temperature of glass transition temperature to 130 ° C. with a heater.
A method for producing a spontaneously extensible polyester filament yarn, which comprises performing a contact heat treatment under a tension of 0.12 g / d,

【0007】並びに、前記の自発伸長性ポリエステルフ
ィラメント糸Aと、下記(3)及び(4)の要件を満足
する収縮率を有する高収縮性ポリエステルフィラメント
糸Bとを含み、自発伸長性ポリエステルフィラメント糸
Aと高収縮性ポリエステルフィラメント糸Bとが混繊さ
れたことを特徴とする自発伸長性ポリエステルフィラメ
ント糸含有混繊糸、にある。 (3) 10%≦SHW(B)≦30% (4) SHW(B)−SHW(A)≧10% (但し、SHW(A)は自発伸長性ポリエステルフィラ
メント糸Aの沸水収縮率(%)、SHW(B)は高収縮
性ポリエステルフィラメント糸Bの沸水収縮率(%)を
示す)
Further, the spontaneously stretchable polyester filament yarn A and the highly shrinkable polyester filament yarn B having a shrinkage ratio satisfying the following requirements (3) and (4) are included. A self-expanding polyester filament yarn-containing mixed fiber yarn in which A and a highly shrinkable polyester filament yarn B are mixed. (3) 10% ≤ SHW (B) ≤ 30% (4) SHW (B) -SHW (A) ≥ 10% (where SHW (A) is the boiling water shrinkage rate (%) of the spontaneously extensible polyester filament yarn A). , SHW (B) indicates the boiling water shrinkage rate (%) of the highly shrinkable polyester filament yarn B).

【0008】[0008]

【発明の実施の形態】本発明の自発伸長性ポリエステル
フィラメント糸は、エチレンテレフタレートを主たる繰
り返し単位とするポリエステルからなり、沸水処理した
ときに8%以下、好ましく0〜6%の収縮率を有し、沸
水処理したフィラメント糸を160℃以上で乾熱処理し
たときに乾熱収縮率と沸水収縮率の差の分だけ伸長し
て、非可逆的な伸長を示す。
BEST MODE FOR CARRYING OUT THE INVENTION The spontaneously stretchable polyester filament yarn of the present invention comprises a polyester having ethylene terephthalate as a main repeating unit, and has a shrinkage ratio of 8% or less, preferably 0 to 6% when treated with boiling water. When the filament yarn treated with boiling water is subjected to dry heat treatment at 160 ° C. or higher, the filament yarn is elongated by the difference between the dry heat shrinkage rate and the boiling water shrinkage rate, and exhibits irreversible extension.

【0009】さらに、本発明の自発伸長性ポリエステル
フィラメント糸は、アルカリ減量の際に繊維軸方向に幅
0.1〜3μm、長さ5μm以上の筋状溝が隣接間隔5
μm以下に繊維表面に形成されるという対アルカリ挙動
性能を有し、繊維表面に形成の筋状溝によりヌメリ感の
ないドライ感を呈する。
Further, in the spontaneously extensible polyester filament yarn of the present invention, when the alkali weight is reduced, a linear groove having a width of 0.1 to 3 μm and a length of 5 μm or more is adjacent to each other at an interval 5
It has an alkali-behavior performance of being formed on the fiber surface in the range of μm or less, and exhibits a dry feeling without sliminess due to the streak grooves formed on the fiber surface.

【0010】本発明の自発伸長性ポリエステルフィラメ
ント糸は、有機スルホン酸金属塩を含有する高配向ポリ
エステル未延伸フィラメント糸を、ヒーターにて接触熱
処理することにより製造される。高配向ポリエステル未
延伸フィラメント糸として、エチレンテレフタレートを
主たる繰り返し単位とし、前記一般式R−SO3Mで表
される有機スルホン酸金属塩を0.1〜10重量%、好
ましくは0.5〜5重量%含有する高配向ポリエステル
未延伸フィラメント糸を用いる。有機スルホン酸金属塩
は、アルカリ減量の際にアルカリ減量の活性点となり、
繊維表面に筋状溝を形成させる。有機スルホン酸金属塩
の含有量が0.1重量%未満では、筋状溝が形成され
ず、また10重量%を超えると、未延伸フィラメント糸
を良好に得ること自体が紡糸性の点で困難となる。
The spontaneously stretchable polyester filament yarn of the present invention is produced by subjecting a highly oriented polyester unstretched filament yarn containing an organic sulfonic acid metal salt to a contact heat treatment with a heater. As highly oriented polyester undrawn filament yarn, and the ethylene terephthalate as a main recurring unit, the general formula R-SO 3 organic sulfonic acid metal salt represented by M 0.1 to 10 wt%, preferably 0.5 to 5 Highly oriented polyester unstretched filament yarn containing wt% is used. The metal salt of organic sulfonic acid becomes an active point of alkali weight loss at the time of alkali weight loss,
Striations are formed on the fiber surface. If the content of the organic sulfonic acid metal salt is less than 0.1% by weight, streak-shaped grooves are not formed, and if it exceeds 10% by weight, it is difficult to obtain an unstretched filament yarn satisfactorily in terms of spinnability. Becomes

【0011】また、用いる高配向ポリエステル未延伸フ
ィラメント糸が、複屈折率Δnが0.03〜0.08、
好ましくは0.04〜0.06の高配向ポリエステル未
延伸フィラメント糸であることが必要である。複屈折率
Δnが0.03未満では、配向が不十分であり、得られ
るフィラメント糸のアルカリ減量の際の繊維表面の筋状
溝の形成が困難であり、複屈折率Δnが0.08を超え
ると、得られるフィラメント糸が乾熱処理での自発伸長
性がないものとなる。
The highly oriented polyester unstretched filament yarn used has a birefringence Δn of 0.03 to 0.08,
It is necessary that it is a highly oriented polyester undrawn filament yarn of preferably 0.04 to 0.06. When the birefringence Δn is less than 0.03, the orientation is insufficient, it is difficult to form streak grooves on the fiber surface when the alkali weight of the obtained filament yarn is reduced, and the birefringence Δn is 0.08. When it exceeds, the filament yarn obtained does not have spontaneous elongation in dry heat treatment.

【0012】かかる高配向ポリエステル未延伸フィラメ
ント糸を用い、ヒーターにて高配向未延伸フィラメント
糸のガラス転移温度〜130℃の温度で、0.02〜
0.12g/dの張力下で接触熱処理する。接触熱処理
には、公知の任意のヒーターが用いられるが、熱効率、
コストの面で接触式ヒーターが特に好ましく用いられ
る。温度がガラス転移温度未満では、繊維内部の分子歪
みの緩和が起こらず、沸水処理による収縮が大きくな
り、また130℃を超えると、繊維の結晶化及び配向が
進みすぎ、自発伸長の発現が困難となる。
Using such a highly oriented polyester unstretched filament yarn, 0.02 to 0.02 at a temperature of the glass transition temperature to 130 ° C. of the highly oriented unstretched filament yarn with a heater.
Contact heat treatment is performed under a tension of 0.12 g / d. A known arbitrary heater is used for the contact heat treatment, but thermal efficiency,
A contact heater is particularly preferably used in terms of cost. If the temperature is lower than the glass transition temperature, the relaxation of the molecular strain inside the fiber does not occur and the shrinkage due to boiling water treatment becomes large, and if it exceeds 130 ° C, the crystallization and orientation of the fiber proceed too much, and it is difficult to express spontaneous elongation. Becomes

【0013】また、張力が0.02g/d未満では、接
触が不安定になり加熱効果が不均一となって全体的に沸
水収縮率が高くなり、0.12g/dを超えると、繊維
の配向が進みすぎ、自発伸長の発現が困難となる。
When the tension is less than 0.02 g / d, the contact becomes unstable and the heating effect becomes non-uniform, and the boiling water shrinkage ratio becomes high as a whole. When the tension exceeds 0.12 g / d, the fiber The orientation is too advanced and it becomes difficult to express spontaneous elongation.

【0014】図1に、本発明の自発伸長性ポリエステル
フィラメント糸の製造工程を示す。図1の工程では、高
配向未延伸フィラメント糸(1)をフィードローラー
(2)から供給し、ヒーター(3)に接触させながら熱
処理し、デリベリローラー(4)を経てワインダー
(5)により捲き取る。
FIG. 1 shows a process for producing the spontaneously extensible polyester filament yarn of the present invention. In the process of FIG. 1, highly oriented undrawn filament yarn (1) is supplied from a feed roller (2), heat-treated while being in contact with a heater (3), and wound by a winder (5) via a delivery roller (4). take.

【0015】本発明の自発伸長性ポリエステルフィラメ
ント糸は、沸水処理後の乾熱処理で伸長するものであ
り、自発伸長を発現させるためのこれらの沸水処理及び
乾熱処理は、織編物の形態でのアルカリ減量加工、染色
仕上げ等の後工程で施されてもよい。
The spontaneously stretchable polyester filament yarn of the present invention is stretched by dry heat treatment after boiling water treatment, and these boiling water treatment and dry heat treatment for expressing spontaneous stretching are carried out by alkali in the form of woven or knitted fabric. It may be applied in a subsequent step such as weight reduction processing or dyeing finishing.

【0016】特に本発明の自発伸長性ポリエステルフィ
ラメント糸は、高収縮性ポリエステルフィラメント糸と
混繊されたときに、その特徴が際立って発揮されること
から、混繊糸とされることが特に好ましく、本発明に
は、次の自発伸長性ポリエステルフィラメント糸含有混
繊糸をも含まれる。
Particularly, the spontaneously extensible polyester filament yarn of the present invention is particularly preferable when it is mixed with the high-shrinkage polyester filament yarn, because its characteristics are remarkably exhibited. The present invention also includes the following spontaneously extensible polyester filament yarn-containing mixed fiber yarn.

【0017】即ち、本発明の自発伸長性ポリエステルフ
ィラメント糸含有混繊糸は、前記の自発伸長性ポリエス
テルフィラメント糸Aと、沸水収縮率が10〜30%
で、フィラメント糸Aの沸水収縮率の差が10%以上で
ある高収縮率の高収縮性ポリエステルフィラメント糸B
とを含み、自発伸長性ポリエステルフィラメント糸Aと
高収縮性ポリエステルフィラメント糸Bとが混繊されて
なる混繊糸にある。
That is, the mixed filament yarn containing the spontaneously extensible polyester filament yarn of the present invention has a boiling water shrinkage ratio of 10 to 30% with the spontaneously extensible polyester filament yarn A.
And the difference in the boiling water shrinkage ratio of the filament yarn A is 10% or more
And a spontaneously extensible polyester filament yarn A and a highly shrinkable polyester filament yarn B.

【0018】高収縮性ポリエステルフィラメント糸Bの
沸水収縮率が10%未満では、自発伸長性ポリエステル
フィラメント糸Aとの収縮差の発現が不十分となり、織
編物に嵩高性を与えることができず、30%を超える
と、過度の収縮により織編物にソフト感を与えることが
できない。また、沸水収縮率の差が10%未満では、染
色仕上げ等においての収縮差の発現が不十分となり嵩高
性、ソフト感に劣る織編物となる。
When the boiling water shrinkage ratio of the highly shrinkable polyester filament yarn B is less than 10%, the difference in shrinkage between the highly stretchable polyester filament yarn B and the spontaneously stretchable polyester filament yarn A becomes insufficient, and the woven or knitted fabric cannot be made bulky. If it exceeds 30%, the woven or knitted fabric cannot be given a soft feeling due to excessive shrinkage. On the other hand, when the difference in shrinkage rate of boiling water is less than 10%, the difference in shrinkage during dyeing and the like is insufficiently expressed, resulting in a woven or knitted fabric having poor bulkiness and softness.

【0019】高収縮性ポリエステルフィラメント糸Bと
しては、エチレンテレフタレートを主たる繰り返し単位
とするポリエステルフィラメント糸で、その製糸過程で
収縮性が付与されたポリエステルフィラメント糸でもよ
いが、イソフタル酸等の共重合成分を共重合して高収縮
性としたポリエステルフィラメント糸が好ましく用いら
れる。
The highly shrinkable polyester filament yarn B may be a polyester filament yarn containing ethylene terephthalate as a main repeating unit, and the polyester filament yarn having shrinkability during the spinning process, but a copolymerization component such as isophthalic acid. A polyester filament yarn having a high shrinkage property is preferably used by copolymerizing.

【0020】本発明の自発伸長性ポリエステルフィラメ
ント糸含有混繊糸を得るに当たっては、自発伸長性ポリ
エステルフィラメント糸と高収縮性ポリエステルフィラ
メント糸とを、それぞれ適宜の断面形状、繊度構成、構
成比率とし、引き揃え、撚り合わせ、流体噴射等の公知
の任意の混繊手段を用いて混繊する。また、本発明の自
発伸長性ポリエステルフィラメント糸含有混繊糸には、
自発伸長性ポリエステルフィラメント糸、高収縮性ポリ
エステルフィラメント糸以外に他のフィラメント糸が含
まれていてもよい。
In obtaining the mixed filament yarn containing the spontaneously extensible polyester filament yarn of the present invention, the spontaneously extensible polyester filament yarn and the highly shrinkable polyester filament yarn are made to have appropriate cross-sectional shapes, fineness constitutions and composition ratios, respectively. Mixing is performed using any known mixing means such as drawing, twisting, and fluid ejection. In addition, in the spontaneously extensible polyester filament yarn-containing mixed fiber yarn of the present invention,
In addition to the spontaneously stretchable polyester filament yarn and the high shrinkage polyester filament yarn, other filament yarns may be included.

【0021】本発明の自発伸長性ポリエステルフィラメ
ント糸含有混繊糸は、製織或いは製編されて織編物とし
た後、任意の工程、好ましくはアルカリ減量加工、染色
仕上げでのアルカリ減量、沸水処理及び160℃以上の
乾熱処理により筋状溝が繊維表面に形成された自発伸長
性ポリエステルフィラメント糸を構成するフィラメント
が混繊糸の鞘側に主に配置され、高収縮性ポリエステル
フィラメント糸を構成するフィラメントが混繊糸の芯側
に主に配置されて、織編物に嵩高性とソフトでふくらみ
感に富む風合い及びふかつき感、ヌメリ感のないドライ
感を与える。
The spontaneously extensible polyester filament yarn-containing mixed filament yarn of the present invention is woven or knitted into a woven or knitted product, and then subjected to any process, preferably alkali weight reduction processing, alkali weight reduction in dyeing finish, boiling water treatment and A filament constituting a spontaneously stretchable polyester filament yarn in which streak-like grooves are formed on the fiber surface by a dry heat treatment at 160 ° C. or more is mainly arranged on the sheath side of the mixed filament yarn, and constitutes a highly shrinkable polyester filament yarn. Is mainly arranged on the core side of the mixed fiber, and gives the woven and knitted fabric a bulky and soft texture with a full swelling feeling and a dry feeling without stickiness.

【0022】[0022]

【実施例】以下、本発明を実施例により具体的に説明す
る。なお、実施例中の各特性値は、下記の方法により測
定した。
The present invention will be described below in more detail with reference to examples. In addition, each characteristic value in an Example was measured by the following method.

【0023】〈沸水収縮率(SHW)〉1デニール当た
り1/30gの張力下で糸長1mの10回巻きカセを準
備し、1デニール当たり1/30×20gの荷重を負荷
して初期カセ長(L0)を測定する。そのカセを無荷重
状態で沸騰水中に30分間浸漬した後、1デニール当た
り2/3gの荷重を負荷してカセ長(L1)を測定し、
次式より沸水収縮率を算出する。 SHW(%)=〔(L0−L1)/L0〕×100
<Boiling Water Shrinkage (SHW)> A 10-turn winding cassette having a yarn length of 1 m is prepared under a tension of 1/30 g per 1 denier, and a load of 1/30 × 20 g per 1 denier is applied to the initial cassette length. (L 0 ) is measured. After immersing the skein in boiling water for 30 minutes in an unloaded state, a skein length (L 1 ) is measured by applying a load of 2/3 g per 1 denier,
The shrinkage rate of boiling water is calculated from the following formula. SHW (%) = [(L 0 −L 1 ) / L 0 ] × 100

【0024】〈乾熱収縮率(SHD)〉沸水収縮率測定
後、カセを雰囲気温度160℃下で無荷重状態で10分
間放置した後、カセ長(L2)を測定し、次式より沸水
収縮率を算出する。 SHD(%)=〔(L0−L2)/L0〕×100
<Dry Heat Shrinkage (SHD)> After measuring the boiling water shrinkage, the cassette was allowed to stand for 10 minutes under an unloaded condition at an ambient temperature of 160 ° C., and then the cassette length (L 2 ) was measured. Calculate the shrinkage. SHD (%) = [(L 0 −L 2 ) / L 0 ] × 100

【0025】(実施例1)ポリエチレンテレフタレート
生成時のエステル化反応終了後に炭素数15のアルキル
スルホン酸ナトリウム1重量%を加えた極限粘度0.7
1のポリマーを、紡糸温度285℃、紡糸速度2900
m/分で溶融紡糸し、複屈折率Δnが0.046の12
0デニール/36フィラメントの高配向ポリエステル未
延伸フィラメント糸を得た。この高配向ポリエステル未
延伸フィラメント糸を、三菱重工業(株)製仮撚機LS
−6を用い、糸速度100m/分、ヒーター温度120
℃、延伸倍率1.10で、0.09g/dの張力下にヒ
ーターに接触させて熱処理する延伸加工を施した。
Example 1 After the completion of the esterification reaction at the time of producing polyethylene terephthalate, 1% by weight of sodium alkylsulfonate having 15 carbon atoms was added to give an intrinsic viscosity of 0.7.
Polymer No. 1 with spinning temperature 285 ° C., spinning speed 2900
12 with a birefringence Δn of 0.046 after melt spinning at m / min
Highly oriented polyester unstretched filament yarn of 0 denier / 36 filament was obtained. This highly oriented polyester unstretched filament yarn is manufactured by Mitsubishi Heavy Industries, Ltd. false twisting machine LS
-6, yarn speed 100 m / min, heater temperature 120
Stretching was carried out at a temperature of 0 ° C. and a draw ratio of 1.10 by contacting a heater with a tension of 0.09 g / d for heat treatment.

【0026】得られた延伸糸は、沸水収縮率(SHW)
が3.8%、乾熱収縮率(SHD)が0%で、160℃
での乾熱処理によりSHD−SHWが−3.8%の収
縮、即ち3.8%伸長し、自発伸長性を示した。得られ
たこの自発伸長性糸を用い製編して編地とし、減量率2
0%に沸騰下でアルカリ減量加工し、さらに130℃で
染色仕上げ加工した。得られた編地の繊維表面を走査型
電子顕微鏡で観察したところ、繊維軸方向に幅0.1〜
3μm、長さ5μm以上の筋状溝が隣接間隔5μm以下
に繊維表面に形成されていることが確認され、編地は、
ドライ感を有するものであった。
The drawn yarn thus obtained has a boiling water shrinkage (SHW).
Is 3.8%, dry heat shrinkage (SHD) is 0%, 160 ° C
SHD-SHW contracted by -3.8%, that is, expanded by 3.8% by the dry heat treatment at 1, indicating spontaneous elongation. The obtained spontaneously extensible yarn is knitted into a knitted fabric, and the weight loss rate is 2
Alkali weight loss processing was performed under boiling to 0%, and dyeing finishing processing was further performed at 130 ° C. When the fiber surface of the obtained knitted fabric was observed by a scanning electron microscope, the width of the fiber was 0.1 to 0.1 in the fiber axis direction.
It was confirmed that streak grooves with a length of 3 μm and a length of 5 μm or more were formed on the fiber surface at intervals of 5 μm or less, and the knitted fabric was
It had a dry feeling.

【0027】(実施例2〜7、比較例1〜6)表1に示
すアルキルスルホン酸ナトリウム量及び複屈折率Δnの
120デニール/36フィラメントの高配向ポリエステ
ル未延伸フィラメント糸を用い、実施例1におけると同
様にして表1に示す条件で延伸加工を施した。得られた
延伸フィラメント糸の沸水収縮率、収縮率差、編地での
アルカリ減量加工、染色仕上げ加工後の風合いの測定、
評価結果を表1に示す。
(Examples 2 to 7 and Comparative Examples 1 to 6) Using highly oriented polyester unstretched filament yarn of 120 denier / 36 filaments having the amount of sodium alkylsulfonate and birefringence Δn shown in Table 1, Example 1 was used. Stretching was performed under the conditions shown in Table 1 in the same manner as in. Boiling water shrinkage of the obtained drawn filament yarn, shrinkage difference, alkali weight reduction processing in knitted fabric, measurement of texture after dyeing and finishing,
Table 1 shows the evaluation results.

【0028】[0028]

【表1】 [Table 1]

【0029】(実施例8)実施例1で得た自発伸長性糸
Aと沸水収縮率18%の75デニール/18フィラメン
トの高収縮性ポリエステル糸Bとを、(株)愛機製作所
製AT−501機を用いて、それぞれオーバーフィード
率8%、4%とし、糸速度200m/分、エア圧4kg
/cm2でタスランノズル(ヘバライン社製T−31
1)にてエア噴射により混繊した。得られた混繊糸を用
い、製織して織物とし、沸騰下でアルカリ減量加工、1
30℃で染色仕上げ加工し、さらに180℃で乾熱セッ
トした。得られた織物は、嵩高性とソフトでふくらみ感
に富み、かつドライ感ドライ感を有するものであった。
(Example 8) A self-expanding yarn A obtained in Example 1 and a highly shrinkable polyester yarn B of 75 denier / 18 filaments having a boiling water shrinkage of 18% were manufactured by AT-Aki Co., Ltd. Using 501 machines, the overfeed rate was 8% and 4% respectively, the yarn speed was 200 m / min, and the air pressure was 4 kg.
/ Cm 2 Taslan nozzle (T-31 manufactured by Hebaline Co., Ltd.
In 1), the fibers were mixed by air injection. Using the obtained mixed-fiber yarn, weaving into a woven fabric, alkali reduction processing under boiling, 1
It was dyed and finished at 30 ° C., and further dried and heat set at 180 ° C. The obtained woven fabric was bulky, soft, rich in swelling, and dry and dry.

【0030】(実施例9〜12、比較例7〜10)表2
に示すような実施例1と同様にして得た沸水収縮率の自
発伸長性糸Aと各沸水収縮率の高収縮性糸Bとを用い、
実施例8におけると同様にして混繊した。得られた混繊
糸を用い、製織して織物とし、沸騰下でアルカリ減量加
工、130℃で染色仕上げ加工し、さらに180℃で乾
熱セットした。得られた織物の評価結果を表2に示す。
(Examples 9 to 12, Comparative Examples 7 to 10) Table 2
As shown in Example 1, using a spontaneously elongating yarn A having a boiling water shrinkage and a highly shrinkable yarn B having a respective boiling water shrinkage,
The fibers were mixed in the same manner as in Example 8. Using the obtained mixed fiber, it was woven into a woven fabric, which was subjected to alkali weight reduction processing in boiling, dyeing finishing processing at 130 ° C., and further dry-heat set at 180 ° C. Table 2 shows the evaluation results of the obtained woven fabric.

【0031】[0031]

【表2】 [Table 2]

【0032】[0032]

【発明の効果】本発明の自発伸長性ポリエステルフィラ
メント糸は、自発伸長性とアルカリ減量加工の際に筋状
溝を繊維表面に形成するものであり、また、この自発伸
長性ポリエステルフィラメント糸と高収縮性ポリエステ
ルフィラメント糸を組み合わせてなる混繊糸は、織編物
に嵩高性とソフトでふくらみ感に富む風合い及びふかつ
き感、ヌメリ感のないドライ感を与えるものである。
EFFECTS OF THE INVENTION The spontaneously stretchable polyester filament yarn of the present invention forms a linear groove on the surface of the fiber during spontaneous stretching and alkali weight reduction processing. A mixed fiber yarn formed by combining shrinkable polyester filament yarns gives a woven or knitted fabric a bulky and soft texture that is full of swelling, a feeling of stuffiness, and a dry feeling without sliminess.

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

【図1】本発明の自発伸長性ポリエステルフィラメント
糸の製造工程図である。
FIG. 1 is a process drawing of a spontaneously extensible polyester filament yarn of the present invention.

【符号の説明】[Explanation of symbols]

1 高配向未延伸フィラメント糸 2 フィードローラー 3 ヒーター 4 デリベリローラー 5 ワインダー 1 Highly oriented unstretched filament yarn 2 Feed roller 3 Heater 4 Delivery roller 5 Winder

フロントページの続き (72)発明者 高田 靖夫 愛知県名古屋市東区砂田橋四丁目1番60号 三菱レイヨン株式会社商品開発研究所内Front Page Continuation (72) Inventor Yasuo Takada 4-60 Sunadabashi, Higashi-ku, Nagoya, Aichi Prefecture Mitsubishi Rayon Co., Ltd. Product Development Laboratory

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 下記(1)及び(2)の要件を満足する
収縮率を有し、かつアルカリ減量の際に繊維軸方向に幅
0.1〜3μm、長さ5μm以上の筋状溝が隣接間隔5
μm以下に繊維表面に形成されることを特徴とする自発
伸長性ポリエステルフィラメント糸。 (1) SHD−SHW≦0% (2) SHW≦8% (但し、SHWは沸水収縮率(%)、SHDは沸水処理
後の160℃での乾熱収縮率(%)を示す)
1. A linear groove having a shrinkage ratio satisfying the following requirements (1) and (2) and having a width of 0.1 to 3 μm and a length of 5 μm or more in the fiber axis direction during alkali weight reduction. Adjacent spacing 5
A spontaneously stretchable polyester filament yarn, which is formed on the surface of the fiber to have a thickness of less than μm. (1) SHD-SHW ≤ 0% (2) SHW ≤ 8% (where SHW indicates boiling water shrinkage (%), SHD indicates dry heat shrinkage (%) at 160 ° C after boiling water treatment)
【請求項2】 エチレンテレフタレートを主たる繰り返
し単位とし、一般式R−SO3M(Rは炭素数3〜30
のアルキル基、炭素数7〜40のアリール基、Mはアル
カリ金属)で表される有機スルホン酸金属塩を0.1〜
10重量%含有する複屈折率Δnが0.03〜0.08
の高配向ポリエステル未延伸フィラメント糸を、ヒータ
ーにてガラス転移温度〜130℃の温度で0.02〜
0.12g/dの張力下で接触熱処理することを特徴と
する自発伸長性ポリエステルフィラメント糸の製造方
法。
2. Ethylene terephthalate as a main repeating unit, R-SO 3 M (R is a carbon number of 3 to 30)
Is an alkyl group, an aryl group having 7 to 40 carbon atoms, and M is an alkali metal).
Birefringence Δn containing 10% by weight is 0.03 to 0.08
The highly oriented polyester unstretched filament yarn of 0.02 to 0.02 at a temperature of glass transition temperature to 130 ° C. with a heater.
A method for producing a spontaneously extensible polyester filament yarn, which comprises subjecting the material to contact heat treatment under a tension of 0.12 g / d.
【請求項3】 請求項1記載の自発伸長性ポリエステル
フィラメント糸Aと、下記(3)及び(4)の要件を満
足する収縮率を有する高収縮性ポリエステルフィラメン
ト糸Bとを含み、自発伸長性ポリエステルフィラメント
糸Aと高収縮性ポリエステルフィラメント糸Bとが混繊
されたことを特徴とする自発伸長性ポリエステルフィラ
メント糸含有混繊糸。 (3) 10%≦SHW(B)≦30% (4) SHW(B)−SHW(A)≧10% (但し、SHW(A)は自発伸長性ポリエステルフィラ
メント糸Aの沸水収縮率(%)、SHW(B)は高収縮
性ポリエステルフィラメント糸Bの沸水収縮率(%)を
示す)
3. A spontaneously stretchable polyester filament yarn A according to claim 1, and a highly shrinkable polyester filament yarn B having a shrinkage ratio satisfying the following requirements (3) and (4). A spontaneously extensible polyester filament yarn-containing mixed filament yarn, wherein the polyester filament yarn A and the highly shrinkable polyester filament yarn B are mixed. (3) 10% ≤ SHW (B) ≤ 30% (4) SHW (B) -SHW (A) ≥ 10% (where SHW (A) is the boiling water shrinkage rate (%) of the spontaneously extensible polyester filament yarn A). , SHW (B) indicates the boiling water shrinkage rate (%) of the highly shrinkable polyester filament yarn B).
JP10645096A 1996-04-04 1996-04-04 Spontaneously extensible polyester filament yarn, method for producing the same, and blended yarn containing spontaneously extensible polyester filament yarn Pending JPH09273043A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10645096A JPH09273043A (en) 1996-04-04 1996-04-04 Spontaneously extensible polyester filament yarn, method for producing the same, and blended yarn containing spontaneously extensible polyester filament yarn

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10645096A JPH09273043A (en) 1996-04-04 1996-04-04 Spontaneously extensible polyester filament yarn, method for producing the same, and blended yarn containing spontaneously extensible polyester filament yarn

Publications (1)

Publication Number Publication Date
JPH09273043A true JPH09273043A (en) 1997-10-21

Family

ID=14433952

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10645096A Pending JPH09273043A (en) 1996-04-04 1996-04-04 Spontaneously extensible polyester filament yarn, method for producing the same, and blended yarn containing spontaneously extensible polyester filament yarn

Country Status (1)

Country Link
JP (1) JPH09273043A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100814249B1 (en) * 2004-12-31 2008-03-17 주식회사 효성 Concentrated spontaneous elongated processed yarn and its manufacturing method
KR101003216B1 (en) * 2005-09-16 2010-12-21 주식회사 효성 Spontaneous Elongated Yarn with Trilobite Pioy and Its Manufacturing Method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100814249B1 (en) * 2004-12-31 2008-03-17 주식회사 효성 Concentrated spontaneous elongated processed yarn and its manufacturing method
KR101003216B1 (en) * 2005-09-16 2010-12-21 주식회사 효성 Spontaneous Elongated Yarn with Trilobite Pioy and Its Manufacturing Method

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