JP3128529B2 - Method for producing cationically dyeable spontaneously extensible polyester filament yarn, and method for producing fabric using filament yarn obtained by the method - Google Patents

Method for producing cationically dyeable spontaneously extensible polyester filament yarn, and method for producing fabric using filament yarn obtained by the method

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Publication number
JP3128529B2
JP3128529B2 JP09050086A JP5008697A JP3128529B2 JP 3128529 B2 JP3128529 B2 JP 3128529B2 JP 09050086 A JP09050086 A JP 09050086A JP 5008697 A JP5008697 A JP 5008697A JP 3128529 B2 JP3128529 B2 JP 3128529B2
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JP
Japan
Prior art keywords
filament yarn
yarn
producing
polyester filament
dyeable
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
JP09050086A
Other languages
Japanese (ja)
Other versions
JPH10251932A (en
Inventor
有紀子 佐山
秀夫 坂倉
能則 川島
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
Mitsubishi Rayon Co Ltd
Original Assignee
Mitsubishi Chemical Corp
Mitsubishi Rayon Co Ltd
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Filing date
Publication date
Application filed by Mitsubishi Chemical Corp, Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Chemical Corp
Priority to JP09050086A priority Critical patent/JP3128529B2/en
Publication of JPH10251932A publication Critical patent/JPH10251932A/en
Application granted granted Critical
Publication of JP3128529B2 publication Critical patent/JP3128529B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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、カチオン可染自発
伸長性ポリエステルフィラメント糸の製造方法、及び、
その方法で得られるフィラメント糸を用いた布帛の製造
方法に関する。
The present invention relates to a method for producing a cationically dyeable spontaneously extensible polyester filament yarn, and
The present invention relates to a method for producing a fabric using the filament yarn obtained by the method.

【0002】[0002]

【従来の技術】異収縮フィラメント混繊糸を使用した織
編物は、絹を越える風合を奏するものとして新合繊と言
われている。しかし、近年更に高級な風合、すなわちよ
り高い膨らみ感や新規な風合が求められており、フィラ
メント混繊糸を構成する高収縮成分と低収縮成分の収縮
差をより大きくすることが必要とされている。収縮差を
より大きくする方法としては、高収縮フィラメント糸の
収縮率を大きくする方法と低収縮フィラメント糸の収縮
率を小さくする方法がある。前者の方法については、共
重合成分の添加量を大きくする手段が有効であるが、ポ
リマーの結晶化速度が低下し乾燥工程でのペレット間の
融着、得られるフィラメント糸からの織編物の染色工程
での収縮による製品としての歩留まり低下等の問題点が
ある。一方、後者の方法については、収縮率をできるだ
け小さく、望ましくは自発伸長する特性を付与すること
が必要である。
2. Description of the Related Art A woven or knitted fabric using a mixed fiber of different shrinkage filaments is said to be a new synthetic fiber as having a feeling exceeding that of silk. However, in recent years, a higher-grade feel, that is, a higher swelling feeling and a new feel are required, and it is necessary to further increase the difference in shrinkage between the high shrinkage component and the low shrinkage component constituting the filament mixed yarn. Have been. As a method of increasing the shrinkage difference, there are a method of increasing the shrinkage rate of the high shrinkage filament yarn and a method of reducing the shrinkage rate of the low shrinkage filament yarn. For the former method, it is effective to increase the amount of the copolymerized component.However, the crystallization rate of the polymer is reduced, the fusion between the pellets in the drying step, and the dyeing of the woven or knitted fabric from the obtained filament yarn. There are problems such as a reduction in the yield as a product due to shrinkage in the process. On the other hand, in the latter method, it is necessary to impart the property of reducing the shrinkage as much as possible, and desirably the property of spontaneous elongation.

【0003】自発伸長する特性を付与した自発伸長性ポ
リエステルフィラメント糸と高収縮ポリエステルフィラ
メント糸の混繊糸を利用して提供される織編物の風合は
大変素晴らしく、高い膨らみ感は市場で高く評価されて
いる。かかる自発伸長性のポリエステルフィラメント糸
として、特定の複屈折率を有するポリエステル高配向未
延伸糸を特定の延伸条件で延伸し太細フィラメントとし
た後、緩和熱処理することにより、後加工工程で伸長す
る自発伸長性ポリエステルフィラメント糸が、特開平5
−1244号公報で開示されている。
[0003] The texture of a woven or knitted fabric provided by using a blended yarn of a spontaneously extensible polyester filament yarn imparted with spontaneous elongation and a high shrinkage polyester filament yarn is very excellent, and a high swelling feeling is highly appreciated in the market. Have been. As such a spontaneously extensible polyester filament yarn, a polyester highly oriented unstretched yarn having a specific birefringence is drawn under specific drawing conditions into a thick filament, and then subjected to relaxation heat treatment, so that it is stretched in a post-processing step. A spontaneously extensible polyester filament yarn is disclosed in
No. 1244.

【0004】また、一方で、優れた風合のみならず、外
観変化への期待も大きくカチオン可染性ポリエステルフ
ィラメント糸とカチオン可染性を有しないポリエステル
フィラメント糸との混繊糸により、染色性の違いを利用
したミックス調の外観を有する素材が市場で受け入れら
れている。このようなカチオン可染性ポリエステルフィ
ラメント糸についても自発伸長性を付与することが求め
られている。しかしながら、カチオン可染性ポリエステ
ルポリマ−は酸性の極性基を有するため、延伸糸の収縮
率が大きく、上記特許で制限された条件範囲では自発伸
長糸は製造できない。
[0004] On the other hand, not only excellent feeling but also high expectation of change in appearance are obtained, and the dyeing properties of the cation-dyeable polyester filament yarn and the non-cation-dyeable polyester filament yarn are improved. Materials having a mix-like appearance utilizing the difference between the two have been accepted in the market. It is required that such cationic dyeable polyester filament yarns also have spontaneous elongation. However, since the cationic dyeable polyester polymer has an acidic polar group, the stretched yarn has a large shrinkage, and a spontaneously elongated yarn cannot be produced in the condition range limited by the above patent.

【0005】かかるカチオン可染性を有する自発伸長性
ポリエステルフィラメント糸の製造方法に関しては、特
開平7−292524号公報で、特定の複屈折率を有す
る5−ナトリウムスルホイソフタル酸共重合ポリエステ
ル高配向未延伸糸を特定の延伸条件で延伸し太細フィラ
メント糸とした後、引き続き2回の緩和処理を繰り返す
ことにより自発伸長性を付与する方法が開示されてい
る。
A method for producing such a spontaneously extensible polyester filament yarn having cationic dyeability is disclosed in Japanese Unexamined Patent Publication No. Hei 7-292524, which discloses a highly oriented 5-sodium sulfoisophthalic acid copolymer polyester having a specific birefringence. A method of imparting spontaneous elongation by repeating a relaxation treatment twice after stretching a drawn yarn under specific drawing conditions to form a thick and thin filament yarn is disclosed.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、前記公
報に開示されたカチオン可染自発伸長性ポリエステルフ
ィラメント糸の製造方法では、後加工工程で伸長すると
いう自発伸長特性は満足するものの、2回の緩和処理を
施すため緩和処理中にフィラメント糸の糸張力が低下す
る傾向があり、製糸性の安定が望まれていた。そこで、
本発明の目的は、カチオン可染性を有し、かつ後工程で
自発伸長性を示すポリエステルフィラメント糸を安定に
製造する方法、及びその方法で得られたフィラメント糸
を用いた布帛の製造方法を提供することにある。
However, in the method for producing a cationically dyeable spontaneously extensible polyester filament yarn disclosed in the above-mentioned publication, spontaneous elongation characteristics of elongation in a post-processing step are satisfied, but two times of relaxation. Since the treatment is performed, the yarn tension of the filament yarn tends to decrease during the relaxation treatment, and stable yarn production has been desired. Therefore,
An object of the present invention is to provide a method for stably producing a polyester filament yarn having cationic dyeability and exhibiting spontaneous elongation in a subsequent step, and a method for producing a fabric using the filament yarn obtained by the method. To provide.

【0007】[0007]

【課題を解決するための手段】本発明の第1の要旨は、
主たる繰り返し単位がエチレンテレフタレ−トであり、
5−ナトリウムスルホイソフタ−ル酸を1.5〜3.5
モル%共重合したポリエステルからなり、複屈折率Δn
が35×10-3〜55×10-3、沸水収縮率が40%以
上である高配向未延伸糸を下記式、を満たす条件で
延伸してシック部とシン部がフィラメント間及びフィラ
メント長手方向に高度に分散した太細フィラメント糸と
し、引き続き該太細フィラメント糸を下記式、を満
たす条件で延伸し、更に下記式、を満たす条件で緩
和熱処理することを特徴とするカチオン可染自発伸長性
ポリエステルフィラメント糸の製造方法である。
A first gist of the present invention is as follows.
The main repeating unit is ethylene terephthalate,
5-sodium sulfoisophthalic acid is added to 1.5 to 3.5.
Mol% of polyester, having a birefringence Δn
Is stretched under the conditions satisfying the following formula, and a thick portion and a thin portion are formed between filaments and in the longitudinal direction of the filaments: 35 × 10 −3 to 55 × 10 −3 , and boiling water shrinkage ratio of 40% or more. Cation-dyeable spontaneous extensibility, characterized in that a highly-dispersed thick and thin filament yarn is stretched under the condition satisfying the following formula, and further subjected to relaxation heat treatment under the condition satisfying the following formula. This is a method for producing a polyester filament yarn.

【0008】 1.0<MDR×0.4≦DR1 ≦MDR×0.5 (Tg+20℃)≦HR1 ≦(Tg+50℃) 1.0<DR2 <1.1 (Tg+10℃)≦HR2 <HR1 RR1 ≧10% HP ≧(HR2 +50)℃ 1.0 <MDR × 0.4 ≦ DR 1 ≦ MDR × 0.5 (Tg + 20 ° C.) ≦ HR 1 ≦ (Tg + 50 ° C.) 1.0 <DR 2 <1.1 (Tg + 10 ° C.) ≦ HR 2 <HR 1 RR 1 ≧ 10% HP ≧ (HR 2 +50) ° C.

【0009】ここで、DR1 :第1段延伸域での延伸倍
率 MDR:予熱温度85〜90℃で測定した最大延伸倍率 HR1 :第1段延伸域の引取ロ−ラ−の表面温度(℃) Tg :ガラス転移温度(℃) DR2 :第2段延伸域での延伸倍率 HR2 :第2段延伸域の引取ロ−ラ−の表面温度(℃) RR1 :第2段延伸後の第1段緩和処理域での緩和率
(%) HP :第1段緩和処理域の緩和温度(℃)
Here, DR 1 : a draw ratio in the first-stage drawing region MDR: a maximum drawing ratio measured at a preheating temperature of 85 to 90 ° C. HR 1 : a surface temperature of a take-off roller in the first-stage drawing region ( ° C.) Tg: glass transition temperature (℃) DR 2: draw ratio HR 2 in the second stage drawing zone: take-off of the second-stage stretching zone b - La - surface temperature (℃ of) RR 1: after the second step stretching In the first-stage relaxation treatment area (%) HP: Relaxation temperature in the first-stage relaxation treatment area (° C)

【0010】また、本発明の第2の要旨は、上述の方法
で得られたカチオン可染自発伸長性ポリエステルフィラ
メント糸と高収縮糸を混繊した後、布帛を形成し、アル
カリ減量加工、分散染料及びカチオン染料による染色を
行い、乾熱処理を施すことを特徴とするカチオン可染自
発伸長性ポリエステルフィラメント糸を用いた布帛の製
造方法である。
[0010] The second gist of the present invention is to blend a cationically dyeable spontaneously extensible polyester filament yarn obtained by the above-mentioned method and a high shrinkage yarn, to form a fabric, and to carry out alkali weight reduction processing and dispersion. This is a method for producing a fabric using a cationically dyeable spontaneously extensible polyester filament yarn, wherein the cloth is dyed with a dye and a cationic dye and subjected to a dry heat treatment.

【0011】[0011]

【発明の実施の形態】本発明のポリエステルフィラメン
ト糸におけるポリエステルは、カチオン染料に対し可染
性を示し主たる繰り返し単位がエチレンテレフタレ−ト
であるポリエステルであることが必要であり、カチオン
染料に可染性を示すポリエステルとしては、酸性の極性
基を有する共重合成分として、5−ナトリウムスルホイ
ソフタール酸が共重合されたポリエチレンテレフタレ−
トであることが好ましい。本発明のポリエステルフィラ
メント糸がかかるカチオン染料可染性を示すことが、高
収縮フィラメント糸との混繊において、染色特性の差異
により外観及び色彩上の多様性を奏する。
BEST MODE FOR CARRYING OUT THE INVENTION The polyester in the polyester filament yarn of the present invention needs to be a polyester which is dyeable to a cationic dye and whose main repeating unit is ethylene terephthalate. Examples of the polyester exhibiting dyeability include polyethylene terephthalate copolymerized with 5-sodium sulfoisophthalic acid as a copolymer component having an acidic polar group.
Is preferred. The fact that the polyester filament yarn of the present invention exhibits such cationic dye dyeability provides a variety of appearances and colors due to the difference in dyeing characteristics when mixed with a high shrinkage filament yarn.

【0012】本発明のポリエステルフィラメント糸は、
沸水処理時の伸長率が0〜5%、すなわち収縮率でいえ
ば−5〜0%であり、沸水処理後130℃以上での乾熱
処理時の伸長率が1〜4%。収縮率でいえば−4〜−1
%であり。湿熱及び乾熱においての自発伸長性を有す
る。沸水処理時の伸長率が0%未満では、収縮を生じ、
5%を越えると、染色工程等の湿熱下で織編物の形態変
化を招く。また乾熱処理時の伸長率が1%未満では、高
収縮フィラメント糸との収縮差による風合向上効果が少
なく、4%を越えると、加工工程での通過性を不安定に
する。
[0012] The polyester filament yarn of the present invention comprises:
The elongation at the time of the boiling water treatment is 0 to 5%, that is, -5 to 0% in terms of shrinkage, and the elongation at the time of the dry heat treatment at 130 ° C. or more after the boiling water treatment is 1 to 4%. -4 to -1 in terms of shrinkage
%. It has spontaneous elongation on wet heat and dry heat. If the elongation rate during the boiling water treatment is less than 0%, shrinkage occurs,
If it exceeds 5%, the woven or knitted fabric undergoes morphological change under wet heat such as a dyeing step. If the elongation percentage during the dry heat treatment is less than 1%, the effect of improving the feeling due to the difference in shrinkage from the high shrinkage filament yarn is small, and if it exceeds 4%, the permeability in the processing step becomes unstable.

【0013】また、本発明のポリエステルフィラメント
糸は、シック部とシン部をフィラメント間及びフィラメ
ント長手方向に分散して有する。かかるシック部とシン
部の存在が本発明のポリエステルフィラメント糸の前記
自発伸長性を助長し、かつ高度に分散していることによ
り伸長斑を小さくする。
Further, the polyester filament yarn of the present invention has a thick part and a thin part dispersed between filaments and in the longitudinal direction of the filament. The presence of such a thick part and a thin part promotes the spontaneous elongation of the polyester filament yarn of the present invention, and reduces the unevenness due to the high degree of dispersion.

【0014】本発明のカチオン可染自発伸長性ポリエス
テルフィラメント糸の製造方法について説明すると、本
発明におけるポリエステルとして、固有粘度[η]が
0.45〜0.65の範囲にあり、主たる繰り返し単位
がエチレンテレフタレ−トであり、5−ナトリウムスル
ホイソフタール酸を1.5〜3.5モル%共重合したポ
リエステルを用いる。5−ナトリウムスルホイソフター
ル酸の共重合量が1.5モル%未満では、カチオン染料
による良好な染色性が得られず、3.5モル%を越える
と、溶融粘度が大きくなりすぎ曳糸性が不良となる。
The method for producing the cationically dyeable spontaneously extensible polyester filament yarn of the present invention will be described. As the polyester of the present invention, the intrinsic viscosity [η] is in the range of 0.45 to 0.65, and the main repeating unit is Ethylene terephthalate, a polyester obtained by copolymerizing 1.5-3.5 mol% of 5-sodium sulfoisophthalic acid is used. If the copolymerization amount of 5-sodium sulfoisophthalic acid is less than 1.5 mol%, good dyeability with a cationic dye cannot be obtained, and if it exceeds 3.5 mol%, the melt viscosity becomes too large and the spinnability becomes too large. Becomes defective.

【0015】本発明においては、5−ナトリウムスルホ
イソフタール酸共重合ポリエステルが公知の溶融紡糸法
により紡糸され未延伸糸とされるが、未延伸糸として、
複屈折率△nが35×10-3〜55×10-3、好ましく
は40×10-3〜50×10-3の高配向未延伸糸を用い
る。更に高配向未延伸糸の沸水収縮率を40%以上、好
ましくは45%以上とする必要がある。未延伸糸の複屈
折率△nが35×10-3未満では、得られるフィラメン
ト糸の沸水処理での収縮が大きくなり、55×10-3
越えると、乾熱処理時の伸長はあるものの、沸水処理で
の伸長がなく、また、高配向化に伴い発生する収縮斑が
著しくなり染色斑が生ずる。また、高配向未延伸糸の沸
水収縮率が40%以下であると、緩和処理時に糸条の安
定走行に必要な糸張力が十分確保できず、糸揺れが起こ
り安定に緩和処理ができなくなる。溶融紡糸された未延
伸糸の繊維断面形状は、円形断面であってもまた異型断
面であってもよい。
In the present invention, the 5-sodium sulfoisophthalic acid copolymerized polyester is spun by a known melt spinning method to obtain an undrawn yarn.
A highly oriented undrawn yarn having a birefringence Δn of 35 × 10 −3 to 55 × 10 −3 , preferably 40 × 10 −3 to 50 × 10 −3 is used. Further, the boiling water shrinkage of the highly oriented undrawn yarn needs to be 40% or more, preferably 45% or more. When the birefringence index Δn of the undrawn yarn is less than 35 × 10 −3 , the shrinkage of the obtained filament yarn in the boiling water treatment becomes large, and when it exceeds 55 × 10 −3 , there is elongation during dry heat treatment, There is no elongation in the boiling water treatment, and shrinkage spots generated due to high orientation are remarkable, and stain spots are generated. On the other hand, if the boiling water shrinkage of the highly oriented undrawn yarn is 40% or less, the yarn tension required for stable running of the yarn during the relaxation treatment cannot be sufficiently secured, and the yarn will sway and the relaxation treatment cannot be performed stably. The fiber cross-sectional shape of the melt-spun undrawn yarn may be a circular cross section or an irregular cross section.

【0016】かかる高配向未延伸糸を、第1段の延伸域
で、室温の給糸ロ−ラ−と(Tg+20℃)〜(Tg+
50℃)の表面温度に加熱された引取ロ−ラ−から構成
される1対のロ−ラ−間で延伸倍率が1.0を越え、か
つ予熱温度85〜90℃で測定した最大延伸倍率(MD
R)の40〜50%に設定した延伸倍率で延伸する。こ
の延伸において、延伸が引取ロ−ラ−上で延伸点が微小
に変動する不均一延伸となり、シック部とシン部がフィ
ラメント間及びフィラメント長手方向に高度に分散した
太細フィラメント糸が得られる。
The highly oriented unstretched yarn is supplied to a yarn feed roller at room temperature (Tg + 20 ° C.) to (Tg +
50 ° C.) The maximum draw ratio measured at a preheating temperature of 85 to 90 ° C. between a pair of rollers composed of a take-up roller heated to a surface temperature of 50 ° C. (MD
The film is stretched at a stretch ratio set to 40 to 50% of R). In this drawing, the drawing becomes uneven drawing in which the drawing point slightly fluctuates on the take-off roller, and a thick and thin filament yarn in which the thick portion and the thin portion are highly dispersed between the filaments and in the longitudinal direction of the filament is obtained.

【0017】この太細フィラメント糸を、引き続き、第
2段延伸域で(Tg+10℃)以上かつ第1段延伸域の
引取ロ−ラ−の表面温度を越えない表面温度に加熱され
た引取ロ−ラ−により、1.0〜1.1倍の延伸倍率で
延伸する。次いで、更にこの延伸されたフィラメント糸
を、第1段緩和処理域で、(第2段延伸域の引取ロ−ラ
−の表面温度+50℃)以上の緩和温度で、10%以
上、好ましくは15%以上の緩和率に緩和処理する。
The thick and thin filament yarn is continuously heated to a surface temperature of (Tg + 10 ° C.) or more in the second-stage drawing area and not higher than the surface temperature of the take-up roller in the first-stage drawing area. The film is stretched at a draw ratio of 1.0 to 1.1 times by a liner. Next, the stretched filament yarn is further subjected to a relaxation temperature of (the surface temperature of the take-up roller in the second-stage drawing zone + 50 ° C.) or more in the first-stage relaxation treatment area, at least 10%, preferably 15% or more. % Relaxation processing.

【0018】本発明における第1段延伸と第2段延伸及
び第1段緩和処理により、得られる太細フィラメント糸
は、構造歪みが緩和され、沸水処理時の収縮率が0〜−
5%(マイナス値は伸長を表す)であり、沸水処理後1
30℃以上での乾熱処理時の伸長率が1〜4%である、
非可逆的な伸長を示す自発伸長性能を有する。本発明の
延伸及び緩和処理の条件の範囲を外れると、自発伸長性
が得られなかったり、得られてもシック部とシン部の分
散が悪く、染色斑を生じ、またフィラメント間及びフィ
ラメント長手方向に伸長斑を生ずる。
In the present invention, the thick filament yarn obtained by the first-stage drawing, the second-stage drawing, and the first-stage relaxation treatment has a reduced structural distortion, and has a shrinkage of 0 to −− during the boiling water treatment.
5% (a negative value indicates elongation), and 1% after boiling water treatment.
Elongation at the time of dry heat treatment at 30 ° C. or more is 1 to 4%,
It has spontaneous elongation performance showing irreversible elongation. If the conditions of the stretching and relaxation treatment of the present invention are out of the range, spontaneous elongation may not be obtained, or even if it is obtained, the dispersion of the thick part and the thin part may be poor, causing staining spots, and between filaments and in the filament longitudinal direction. Plaques on the skin.

【0019】前記条件の中で、特に第2段延伸倍率を
1.0〜1.1の範囲に設定すること、第1段延伸域の
引取ロ−ラ−の温度を第2段延伸域の引取ロ−ラ−の温
度以上に設定することが、製糸安定性を確保しつつ自発
伸長糸を得る上で大変重要である。
Among the above conditions, in particular, the second-stage stretching ratio is set in the range of 1.0 to 1.1, and the temperature of the take-up roller in the first-stage stretching region is set in the second-stage stretching region. It is very important to set the temperature to a temperature equal to or higher than the temperature of the take-off roller, in order to obtain spontaneously-extended yarns while ensuring yarn-making stability.

【0020】第2延伸倍率を1.0以上に設定すること
により、処理時のフィラメント糸の張力が著しく低下す
るのを防ぎ、糸切れ等の問題を解決し、安定に製造する
ことができるようになる。また、1.1以上に設定する
と第1段延伸域で形成されたフィラメント長手方向に高
度に分散したシック部とシン部の太細差が減少し、自発
伸長性の低下を招くため第2延伸倍率は、1.0〜1.
1の範囲に設定する必要がある。
By setting the second draw ratio to 1.0 or more, it is possible to prevent the tension of the filament yarn during processing from being remarkably reduced, solve problems such as yarn breakage, and stably manufacture the yarn. become. On the other hand, when the ratio is set to 1.1 or more, the thickness difference between the thick portion and the thin portion which are highly dispersed in the longitudinal direction of the filament formed in the first stretching region is reduced, and the spontaneous elongation is reduced. Magnification is 1.0-1.
Must be set in the range of 1.

【0021】第1段延伸域の引取ロ−ラ−の温度を第2
段延伸域の引取ロ−ラ−の温度以上に設定することが重
要である。このように設定すると第2段延伸域の引取ロ
−ラ−は、1.0以上の延伸倍率でありながら、実質上
フィラメント糸を熱緩和する効果を持ち、良好な自発伸
長性をフィラメント糸に付与することができるのであ
る。
The temperature of the take-off roller in the first-stage stretching zone is adjusted to the second
It is important to set the temperature at or above the take-up roller in the step stretching area. With this setting, the take-up roller in the second-stage drawing region has an effect of substantially relaxing the filament yarn while having a draw ratio of 1.0 or more, and provides a good spontaneous elongation to the filament yarn. It can be granted.

【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、沸水収縮率、乾熱収縮率は、次の方法により
測定した。また、Tgは示差走査熱量測定機(セイコ−
電子工業社製DSC220)にて測定した。
The present invention will be described below in more detail with reference to examples. The boiling water shrinkage and dry heat shrinkage were measured by the following methods. Tg is measured by a differential scanning calorimeter (Seiko-
It was measured by DSC220 manufactured by Electronic Industries Co., Ltd.

【0023】沸水収縮率(BWS):1デニ−ルあたり
1/30gの張力下で試長1mの10回巻のカセを準備
し、1デニ−ルあたり2/3g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分浸漬した後、再び荷重をかけて測定カセ長
(L1 )を測定し、次式より算出する。 沸水収縮率(%)=(L0−L1)/L0×100
Boiling water shrinkage (BWS): A 10-turn scab having a test length of 1 m was prepared under a tension of 1/30 g per denier, and a load of 2/3 g per denier was initially applied. The mosquito length (L 0 ) is measured. The hull is immersed in boiling water for 30 minutes with no load, and then a load is applied again to measure the hull length (L 1 ), which is calculated by the following equation. Boiling water shrinkage (%) = (L 0 −L 1 ) / L 0 × 100

【0024】乾熱収縮率(HAS):180℃での乾熱
収縮率は、沸水収縮率を測定した後のカセサンプルを雰
囲気温度180℃で無荷重状態で10分間放置した後、
測定カセ長(L2 )を測定し、次式より算出する。 乾熱収縮率(%)=(L0−L2)/L0×100
Dry Heat Shrinkage (HAS): The dry heat shrinkage at 180 ° C. was determined by leaving the cassette sample after measuring the boiling water shrinkage at 180 ° C. in an atmosphere temperature of 180 ° C. with no load for 10 minutes.
The measuring length (L 2 ) is measured and calculated by the following equation. Dry heat shrinkage (%) = (L 0 −L 2 ) / L 0 × 100

【0025】(実施例1)固有粘度[η]が0.53の
5−ナトリウムスルホイソフタ−ル酸を2.25モル%
共重合したポリエチレンテレフタレートを、孔径0.2
mm、孔数48の紡糸口金を用い、紡糸温度290℃で
溶融紡糸し、3000m/分で巻き取って120d/4
8fの未延紳糸を得た。得られた未延紳糸のMDRは
2.45、Δnが40.8×10-3、Tgが80℃であ
った。この未延紳糸を下記の延伸条件で延伸、緩和熱処
理してポリエステルフィラメント糸を得た。
Example 1 5.25 mol% of 5-sodium sulfoisophthalic acid having an intrinsic viscosity [η] of 0.53
The copolymerized polyethylene terephthalate was added with a pore size of 0.2
melt spinning at a spinning temperature of 290 ° C. using a spinneret having a hole diameter of 48 mm and a winding speed of 3,000 m / min and 120 d / 4.
8f unrolled men's yarn was obtained. The MDR of the obtained unrolled gentle yarn was 2.45, Δn was 40.8 × 10 −3 , and Tg was 80 ° C. This unrolled gentle yarn was stretched and relaxed under the following stretching conditions to obtain a polyester filament yarn.

【0026】 第1延伸倍率(DR1 )=MDR×0.47 第2延伸倍率(DR2 )=1.01 第1緩和率(RR1 )=15% 第1延伸域の引取ロ−ラ−温度(HR1 )=110℃ 第2延伸域の引取ロ−ラ−温度(HR2 )=100℃ 第1緩和処理温度(HP)=190℃First stretch ratio (DR 1 ) = MDR × 0.47 Second stretch ratio (DR 2 ) = 1.01 First relaxation ratio (RR 1 ) = 15% Take-up roller in first stretch region Temperature (HR 1 ) = 110 ° C. Take-up roller temperature (HR 2 ) in second stretching zone = 100 ° C. First relaxation treatment temperature (HP) = 190 ° C.

【0027】得られたフィラメント糸の収縮特性を表1
に示したが、このフィラメント糸は、沸水処理での収縮
率(BWS)及び180℃乾熱処理での収縮率(HA
S)がマイナス値であり自発伸長性を有するものであっ
た。得られた常圧カチオン可染性自発伸長性太細繊維と
イソフタル酸を8.0モル%共重合したポリエチレンテ
レフタレートを使用して製造した75d/18fの高収
縮糸とをエア−混繊し、195d/66fの混繊糸を製
造、平織織物を作成し、常法により減量加工、分散染料
及びカチオン染料による染色後、175℃で1分の乾熱
処理を実施した。得られた織物は嵩高性に優れ、膨らみ
感のあるソフトな風合いを有していた。更に、異種の染
料によるミックス調を呈する織物であった。
Table 1 shows the shrinkage characteristics of the obtained filament yarn.
As shown in the figure, this filament yarn has a shrinkage ratio (BWS) in a boiling water treatment and a shrinkage ratio (HA) in a 180 ° C. dry heat treatment.
S) was a negative value and had spontaneous elongation. Air-blending the obtained normal pressure cationic dyeable spontaneously extensible fine fiber and a 75d / 18f high shrinkage yarn produced using polyethylene terephthalate obtained by copolymerizing 8.0% by mole of isophthalic acid, A mixed fiber yarn of 195d / 66f was produced, a plain woven fabric was prepared, weight-reduced by a conventional method, dyed with a disperse dye and a cationic dye, and then subjected to a dry heat treatment at 175 ° C for 1 minute. The obtained woven fabric was excellent in bulkiness and had a swelling soft texture. Furthermore, it was a woven fabric exhibiting a mixed tone by different kinds of dyes.

【0028】(実施例2〜5、比較例1〜5)実施例1
における未延紳糸の複屈折率Δn、延伸条件、緩和条件
を表1に示したように変更した以外は、実施例1と同様
にしてポリエステルフィラメント糸を得た。得られたフ
ィラメント糸の収縮特性を表1に示した。
(Examples 2 to 5, Comparative Examples 1 to 5) Example 1
A polyester filament yarn was obtained in the same manner as in Example 1 except that the birefringence Δn, stretching conditions, and relaxation conditions of the unrolled men's yarn were changed as shown in Table 1. Table 1 shows the shrinkage characteristics of the obtained filament yarn.

【0029】[0029]

【表1】 [Table 1]

【0030】[0030]

【発明の効果】本発明の製造方法により、カチオン染料
可染性で、かつ沸水等の湿熱下及び130℃以上の乾熱
下では収縮せず可逆的に伸長する自発伸長性ポリエステ
ルフィラメント糸を安定に製造することができる。得ら
れたカチオン可染自発伸長性ポリエステルフィラメント
糸は、高収縮ポリエステルフィラメント糸と組み合わせ
て混繊糸とするならば、嵩高性に優れ、ソフトで膨らみ
感に富む風合の織編物ができるだけでなく、分散染料と
カチオン染料との組合せにより染料の鮮明色の差に基づ
く深みのあるミックス調の織編物を得ることができ衣料
分野での織編物素材として極めて好適なるものである。
According to the production method of the present invention, a spontaneously extensible polyester filament yarn capable of dyeing a cationic dye and reversibly extending without shrinking under the moist heat of boiling water or the dry heat of 130 ° C. or more is stabilized. Can be manufactured. If the resulting cationic dyeable spontaneously extensible polyester filament yarn is mixed with a high shrinkage polyester filament yarn to form a mixed fiber yarn, not only can the woven and knitted fabric with excellent bulkiness, softness and swelling feel be obtained, The combination of a disperse dye and a cationic dye makes it possible to obtain a deep-mixed woven or knitted fabric based on the difference in the vivid colors of the dyes, which is extremely suitable as a woven or knitted fabric material in the field of clothing.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI D03D 15/04 D03D 15/04 A (58)調査した分野(Int.Cl.7,DB名) D02J 1/22 D01F 6/84 305 D03D 15/00 D03D 15/04 ──────────────────────────────────────────────────続 き Continuation of the front page (51) Int.Cl. 7 identification code FI D03D 15/04 D03D 15/04 A (58) Investigated field (Int.Cl. 7 , DB name) D02J 1/22 D01F 6 / 84 305 D03D 15/00 D03D 15/04

Claims (13)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 主たる繰り返し単位がエチレンテレフタ
レ−トであり、5−ナトリウムスルホイソフタ−ル酸を
1.5〜3.5モル%共重合したポリエステルからな
り、複屈折率Δnが35×10-3〜55×10-3、沸水
収縮率が40%以上である高配向未延伸糸を下記式、
を満たす条件で延伸してシック部とシン部がフィラメ
ント間及びフィラメント長手方向に高度に分散した太細
フィラメント糸とし、引き続き該太細フィラメント糸を
下記式、を満たす条件で延伸し、更に下記式、
を満たす条件で緩和熱処理することを特徴とするカチオ
ン可染自発伸長性ポリエステルフィラメント糸の製造方
法。 1.0<MDR×0.4≦DR1 ≦MDR×0.5
(Tg+20℃)≦HR1 ≦(Tg+50℃)
1.0<DR2 <1.1
(Tg+10℃)≦HR2 <HR1
RR1 ≧10%
HP ≧(HR2 +50)℃
ここで、DR1 :第1段延伸域での延伸倍率 MDR:予熱温度85〜90℃で測定した最大延伸倍率 HR1 :第1段延伸域の引取ロ−ラ−の表面温度(℃) Tg :ガラス転移温度(℃) DR2 :第2段延伸域での延伸倍率 HR2 :第2段延伸域の引取ロ−ラ−の表面温度(℃) RR1 :第2段延伸後の第1段緩和処理域での緩和率
(%) HP :第1段緩和処理域の緩和温度(℃)
1. A main repeating unit is ethylene terephthalate, which is a polyester obtained by copolymerizing 1.5 to 3.5 mol% of 5-sodium sulfoisophthalic acid, and has a birefringence Δn of 35 ×. 10 −3 to 55 × 10 −3 , a highly oriented undrawn yarn having a boiling water shrinkage of 40% or more is represented by the following formula:
The filament is drawn under the condition that the thick part and the thin part are highly dispersed between the filaments and in the longitudinal direction of the filament, and the thin filament yarn is stretched under the condition that the following formula is satisfied. ,
A method for producing a cationically dyeable spontaneously extensible polyester filament yarn, characterized by performing a relaxation heat treatment under conditions satisfying the following conditions. 1.0 <MDR × 0.4 ≦ DR 1 ≦ MDR × 0.5
(Tg + 20 ° C) ≦ HR 1 ≦ (Tg + 50 ° C)
1.0 <DR 2 <1.1
(Tg + 10 ° C.) ≦ HR 2 <HR 1
RR 1 ≧ 10%
HP ≧ (HR 2 +50) ° C.
Here, DR 1 : stretching ratio in the first-stage stretching region MDR: maximum stretching ratio measured at a preheating temperature of 85 to 90 ° C. HR 1 : surface temperature of the take-off roller in the first-stage stretching region (° C.) Tg : Glass transition temperature (° C.) DR 2 : Stretching ratio in second-stage stretching region HR 2 : Surface temperature of take-up roller in second-stage stretching region (° C.) RR 1 : First after second-stage stretching Relaxation rate (%) in the first stage relaxation treatment area HP: Relaxation temperature (° C) in the first stage relaxation treatment area
【請求項2】 DR1が1.0〜1.3である請求項1
記載のカチオン可染自発伸長性ポリエステルフィラメン
ト糸の製造方法。
2. The method according to claim 1, wherein DR 1 is 1.0 to 1.3.
A method for producing the cationically dyeable spontaneously extensible polyester filament yarn described above.
【請求項3】 HR1が100〜130℃である請求項
1又は請求項2記載のカチオン可染自発伸長性ポリエス
テルフィラメント糸の製造方法。
3. The method for producing a cationically dyeable spontaneously extensible polyester filament yarn according to claim 1, wherein HR 1 is 100 to 130 ° C.
【請求項4】 HR2が90〜100℃である請求項1
〜3のいずれか1項に記載のカチオン可染自発伸長性ポ
リエステルフィラメント糸の製造方法。
4. The method according to claim 1, wherein HR 2 is 90 to 100 ° C.
The method for producing a cationically dyeable spontaneously extensible polyester filament yarn according to any one of Items 1 to 3.
【請求項5】第2段延伸後の第1段緩和処理域での緩和
率(RR1)が15%以上である請求項1〜4のいずれ
か1項に記載のカチオン可染自発伸長性ポリエステルフ
ィラメント糸の製造方法。
5. The cationically dyeable spontaneous extensibility according to claim 1, wherein the relaxation rate (RR 1 ) in the first-stage relaxation treatment area after the second-stage stretching is 15% or more. A method for producing a polyester filament yarn.
【請求項6】 用いるポリエステルの固有粘度[η]が
0.45〜0.65である請求項1〜5のいずれか1項
に記載のカチオン可染自発伸長性ポリエステルフィラメ
ント糸の製造方法。
6. The method for producing a cationically dyeable spontaneously extensible polyester filament yarn according to claim 1, wherein the polyester used has an intrinsic viscosity [η] of 0.45 to 0.65.
【請求項7】 得られるカチオン可染自発伸長性ポリエ
ステルフィラメント糸の沸水処理時の伸長率が0〜5%
である請求項1〜6のいずれか1項に記載のカチオン可
染自発伸長性ポリエステルフィラメント糸の製造方法。
7. The obtained cationically dyeable spontaneously extensible polyester filament yarn has an elongation of 0 to 5% during a boiling water treatment.
The method for producing a cationically dyeable spontaneously extensible polyester filament yarn according to any one of claims 1 to 6.
【請求項8】 得られるカチオン可染自発伸長性ポリエ
ステルフィラメント糸の沸水処理後、130℃以上での
乾熱処理時の伸長率が1〜4%である請求項1〜7のい
ずれか1項に記載のカチオン可染自発伸長性ポリエステ
ルフィラメント糸の製造方法。
8. The method according to claim 1, wherein the obtained cationically dyeable spontaneously extensible polyester filament yarn has an elongation ratio of 1 to 4% when subjected to a dry heat treatment at 130 ° C. or more after boiling water treatment. A method for producing the cationically dyeable spontaneously extensible polyester filament yarn described above.
【請求項9】 請求項1〜8記載の方法で得られたカチ
オン可染自発伸長性ポリエステルフィラメント糸と高収
縮糸を混繊した後、布帛を形成し、アルカリ減量加工、
染色を行い、乾熱処理を施すことを特徴とするカチオン
可染自発伸長性ポリエステルフィラメント糸を用いた布
帛の製造方法。
9. A click obtained by the method according to claim 1.
On dyeable spontaneous stretchable polyester filament yarn and high yield
After blending the condensed yarn, a fabric is formed, alkali weight reduction processing,
Cation characterized by being dyed and subjected to dry heat treatment
Cloth using dyeable spontaneously extensible polyester filament yarn
Fabric production method.
【請求項10】 混繊する高収縮糸が、主たる繰り返し10. The high shrinkage yarn to be mixed is mainly repeated.
単位がエチレンテレフタレ−トであり、イソフタル酸をThe unit is ethylene terephthalate, and isophthalic acid
5〜10モル%共重合した改質ポリエステルである請求5 to 10 mol% of a modified polyester copolymerized
項9記載のカチオン可染自発伸長性ポリエステルフィラItem 10. A cationically dyeable spontaneously extensible polyester filler according to item 9.
メント糸を用いた布帛の製造方法。A method for producing a fabric using a ment yarn.
【請求項11】 混繊する高収縮糸が、主たる繰り返し11. The high shrinkage yarn to be mixed is mainly repeated.
単位がエチレンテレフタレ−トであり、イソフタル酸をThe unit is ethylene terephthalate, and isophthalic acid
8モル%共重合した改質ポリエステルである請求項1011. A modified polyester copolymerized by 8 mol%.
記載のカチオン可染自発伸長性ポリエステルフィラメンThe cationically dyeable spontaneously extensible polyester filament described
ト糸を用いた布帛の製造方法。A method for producing a fabric using a yarn.
【請求項12】 布帛が織物である請求項9〜11のい12. The method according to claim 9, wherein the fabric is a woven fabric.
ずれか1項に記載のカチオン可染自発伸長性ポリエステThe cationically dyeable spontaneously extensible polyester according to any one of claims 1 to 4.
ルフィラメント糸を用いた布帛の製造方法。A method for producing a fabric using a filament yarn.
【請求項13】 分散染料及びカチオン染料による染色13. Dyeing with a disperse dye and a cationic dye
を行う請求項9〜12のいずれか1項に記載のカチオンThe cation according to any one of claims 9 to 12, wherein the cation is performed.
可染自発伸長性ポリエステルフィラメント糸をDyeable spontaneous stretchable polyester filament yarn 用いた布Cloth used
帛の製造方法。Fabric production method.
JP09050086A 1997-03-05 1997-03-05 Method for producing cationically dyeable spontaneously extensible polyester filament yarn, and method for producing fabric using filament yarn obtained by the method Expired - Lifetime JP3128529B2 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014136902A (en) * 2013-01-17 2014-07-28 Nippon Steel & Sumikin Engineering Co Ltd Anti-corrosive structure and construction method of the same

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008231625A (en) * 2007-03-22 2008-10-02 Teijin Fibers Ltd Cation-dyeable polyester moire fancy yarn

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014136902A (en) * 2013-01-17 2014-07-28 Nippon Steel & Sumikin Engineering Co Ltd Anti-corrosive structure and construction method of the same

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