JP2009144317A - Polyester multifilament fiber - Google Patents

Polyester multifilament fiber Download PDF

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JP2009144317A
JP2009144317A JP2009016487A JP2009016487A JP2009144317A JP 2009144317 A JP2009144317 A JP 2009144317A JP 2009016487 A JP2009016487 A JP 2009016487A JP 2009016487 A JP2009016487 A JP 2009016487A JP 2009144317 A JP2009144317 A JP 2009144317A
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crimp
polyester
fiber
percentage
woven
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Hideyasu Terao
秀康 寺尾
Yoshinori Kawashima
能則 川島
Hideo Sakakura
秀夫 坂倉
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Mitsubishi Rayon Co Ltd
Mitsubishi Rayon Textile Co Ltd
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Mitsubishi Rayon Co Ltd
Mitsubishi Rayon Textile Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a polyester conjugate multifilament fiber imparting stretch property and good fullness feeling of woven or knitted fabric, having good process-through property in production of a woven or knitted fabric and imparting sufficient fullness feeling and stretch property, and to provide woven or knitted fabric thereof. <P>SOLUTION: The polyester multifilament is composed of a single fiber in which two kinds of polyester polymers having different melting viscosities are bonded and simultaneously satisfies the following requirements (1), (2), and (3). (1) the percentage of crimp (CC) is ≥20 and ≤50 (%), (2) the percentage of crimp at high temperature (HC) is ≥25 and ≤60 (%), and (3) HC>CC, wherein the percentage of crimp (CC) is the percentage of crimp measured under wet heat treatment conditions for 20 min at 90°C, and the percentage of crimp at high temperture (HC) is the percentage of crimp measured under wet heat treatment conditions for 20 min at 130°C. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、織編物のストレッチ性と良好な膨らみ感を与え、織編物製造時に工程通過性が良く、深みのある色彩が得られるポリエステルマルチフィラメント繊維に関する。   The present invention relates to a polyester multifilament fiber that gives stretchability and good swelling feeling of a woven or knitted fabric, has good process-passability during the production of a woven or knitted fabric, and provides a deep color.

従来より、溶融粘度の異なる2種の熱可塑性ポリマーを同一吐出孔より吐出する複合紡糸により接合型複合繊維糸とし、熱処理によりスパイラル型クリンプを発現させ捲縮型ストレッチ糸とすることが特許文献1等で知られており、高捲縮を得るために、用いる2種の熱可塑性ポリマーの溶融粘度差を大きくすること、また高溶融粘度成分として高収縮性のポリエステルを用いることなどにより、ポリエステル系潜在捲縮性複合繊維が提案され、該繊維による織編物はストレッチ性、深みのある色彩を得ることが知られている。   Conventionally, Patent Document 1 discloses that two types of thermoplastic polymers having different melt viscosities are made into a joint type composite fiber yarn by a composite spinning that is discharged from the same discharge hole, and a spiral type crimp is expressed by heat treatment to form a crimped stretch yarn. In order to obtain a high crimp, it is possible to increase the difference in melt viscosity between the two thermoplastic polymers used, and to use a polyester having a high shrinkage as a high melt viscosity component. Latent crimped composite fibers have been proposed, and it is known that a woven or knitted fabric made of the fibers has a stretchable and deep color.

しかし、従来の潜在捲縮性複合繊維は、撚糸した後の撚止めセットの熱処理により大きな捲縮が発現しクリンプ、スナールなどが発生し、製編織工程でのガイド、筬などの糸道へ糸の引っ掛かり、擦過による糸切れなどの問題が発生しやすい。   However, the conventional latently crimped conjugate fiber produces large crimps due to heat treatment of the twisted set after twisting, and crimps, snares, etc. are generated. Problems such as thread catching and thread breakage due to abrasion are likely to occur.

特開平9−157941号公報Japanese Patent Laid-Open No. 9-157941

本発明は、かかる従来技術の欠点を解決するものであって、製編織の工程通過性に優れ、織編物としたときのストレッチ性と深みのある色彩を付与するポリエステルマルチフィラメント繊維を提供するものである。   The present invention provides a polyester multifilament fiber that solves the disadvantages of the prior art, and that is excellent in processability in knitting and weaving, and that imparts stretchability and deep color when made into a woven or knitted fabric. It is.

本発明の第1の要旨は、溶融粘度の異なる2種のポリエステルポリマーが接合した単繊維からなり、マルチフィラメント繊維として、以下の要件(1)〜(3)を同時に満足することを特徴とするポリエステルマルチフィラメント繊維にある。
(1)20≦捲縮率(CC)≦50(%)
(2)25≦高温捲縮率(HC)≦60(%)
(3)HC>CC
ただし、捲縮率(CC)は、90℃×20分間湿熱処理条件で測定された捲縮率であり、高温捲縮率(HC)は、130℃×20分間湿熱処理条件で測定された捲縮率である。
The first gist of the present invention is characterized in that it consists of a single fiber in which two types of polyester polymers having different melt viscosities are joined, and satisfies the following requirements (1) to (3) simultaneously as a multifilament fiber. Polyester multifilament fiber.
(1) 20 ≦ crimp rate (CC) ≦ 50 (%)
(2) 25 ≦ high temperature crimp rate (HC) ≦ 60 (%)
(3) HC> CC
However, the crimp ratio (CC) is a crimp ratio measured at 90 ° C. for 20 minutes under wet heat treatment conditions, and the high temperature crimp ratio (HC) is a crack measured at 130 ° C. for 20 minutes under wet heat treatment conditions. Reduction rate.

本発明の第2の要旨は、前記主要な構成における溶融粘度の異なる2種のポリエステルポリマーのうち高粘度成分が、第三成分を5〜15モル%共重合させた共重合ポリエチレンテレフタレートである請求項1記載のポリエステルマルトフィラメント繊維本発明のポリエステルマルチフィラメント繊維を含み、織物収縮率(LC)が20〜40%であることを特徴とする織編物にある。   The second gist of the present invention is a copolymerized polyethylene terephthalate obtained by copolymerizing a high-viscosity component of 5 to 15 mol% of the third component among the two types of polyester polymers having different melt viscosities in the main constitution. The polyester maltofilament fiber according to Item 1 is a woven or knitted fabric characterized by including the polyester multifilament fiber of the present invention and having a fabric shrinkage (LC) of 20 to 40%.

本発明は、織編物製造時に工程通過性がよく、深みのある色彩が得られ、十分な膨らみ感とストレッチ性を付与するポリエステル複合マルチフィラメント繊維及びその織編物が得られる。   The present invention provides a polyester composite multifilament fiber and a woven or knitted fabric that have good process passability during the production of a woven or knitted fabric, provide a deep color, and impart sufficient swelling and stretchability.

以下、本発明の好適な実施の形態について具体的に説明する。   Hereinafter, preferred embodiments of the present invention will be specifically described.

本発明のポリエステル複合マルチフィラメント繊維は、布帛とした際にストレッチ性を発現させるために、溶融粘度の異なる2種のポリエステルポリマーを接合した単繊維からなるマルチフィラメント繊維であることが必要である。   The polyester composite multifilament fiber of the present invention needs to be a multifilament fiber composed of single fibers obtained by joining two kinds of polyester polymers having different melt viscosities in order to develop stretchability when used as a fabric.

該単繊維を構成するポリエステルポリマーとしては、繊維としたときに良好なストレッチ性を得るために溶融粘度の異なる組合せであれば、同一ポリマーで低粘度と高粘度の組合せでも良い。粘度の異なるの一方の成分であるポリエステル(A)は高粘度で高収縮成分として作用し、他方の成分であるポリエステル(B)は低粘度で低収縮成分として作用する。   The polyester polymer constituting the single fiber may be a combination of a low viscosity and a high viscosity with the same polymer as long as it has a combination of different melt viscosities in order to obtain good stretchability when formed into fibers. Polyester (A), which is one component having a different viscosity, has a high viscosity and acts as a high shrinkage component, and polyester (B), which is the other component, acts as a low viscosity and low shrinkage component.

また捲縮発現の点から、溶融粘度の異なる2種のポリエステルポリマーのうち高粘度成分が、第三成分を5〜15モル%共重合させた共重合ポリエチレンテレフタレートが好ましい。   From the viewpoint of crimping, a copolymerized polyethylene terephthalate in which a high viscosity component is copolymerized in an amount of 5 to 15 mol% among two polyester polymers having different melt viscosities is preferable.

第三成分が5モル%未満では捲縮発現力が十分得られにくく、15モル%を超えると融点低下が著しく複合紡糸自体が困難になるだけでなく、捲縮発現力も不十分となりやすい。   If the third component is less than 5 mol%, it is difficult to obtain sufficient crimping power, and if it exceeds 15 mol%, the melting point is remarkably lowered and not only composite spinning itself becomes difficult, but also crimping power tends to be insufficient.

第三成分としては、テレフタル酸成分以外の芳香族ジカルボン酸、脂肪族ジカルボン酸等の酸成分、エチレングリコール成分以外の脂肪族ジオール、脂環式ジオール、芳香族ジオール等のジオール成分が挙げられ、具体的には、イソフタル酸、アジピン酸、セバシン酸、1,4−ブタンジオール、シクロヘキサンジオール、ビスフェノールAエチレンオキシド付加物、スルホイソフタル酸金属塩、2,2−ビス[4−(2−ヒドロキシエトキシ)フェニル]プロパン等が挙げられ、特にイソフタル酸、アジピン酸、スルホイソフタル酸金属塩、2,2−ビス[4−(2−ヒドロキシエトキシ)フェニル]プロパンが好ましいものとして挙げられる。これらの第三成分は単独或いは2種以上の組み合わせであってもよい。   Examples of the third component include aromatic dicarboxylic acids other than terephthalic acid components, acid components such as aliphatic dicarboxylic acids, aliphatic diols other than ethylene glycol components, alicyclic diols, diol components such as aromatic diols, Specifically, isophthalic acid, adipic acid, sebacic acid, 1,4-butanediol, cyclohexanediol, bisphenol A ethylene oxide adduct, sulfoisophthalic acid metal salt, 2,2-bis [4- (2-hydroxyethoxy) Phenyl] propane and the like, and isophthalic acid, adipic acid, sulfoisophthalic acid metal salt, and 2,2-bis [4- (2-hydroxyethoxy) phenyl] propane are particularly preferable. These third components may be used alone or in combination of two or more.

さらに本発明の溶融粘度の異なる2種のポリエステルポリマーの接合は、複合繊維としたときに良好なストレッチ性が発現する接合であればいかなる接合でも良い。好ましくはサイドバイサイド型または偏芯芯鞘型などが用いられ、より好ましくはサイドバイサイド型が高度なストレッチ性を得るために用いられる。   Furthermore, the joining of the two polyester polymers having different melt viscosities according to the present invention may be any joining as long as the joint fiber exhibits good stretchability. The side-by-side type or the eccentric core-sheath type is preferably used, and the side-by-side type is more preferably used for obtaining a high stretch property.

また本発明では、マルチフィラメント繊維として捲縮率(CC)が20〜50%、且つ高温捲縮率(HC)が25〜60%であることが必要である。   Moreover, in this invention, it is required as a multifilament fiber that a crimp rate (CC) is 20 to 50%, and a high temperature crimp rate (HC) is 25 to 60%.

捲縮率(CC)は撚糸後の撚り止めセットの際に発生する捲縮に影響し、CCの下限は20%以上、好ましくは30%以上、上限は50%以下、好ましくは45%以下が良い。20%未満であると製編織の工程通過性は良いが、布帛にした際のストレッチ性が劣る。50%を超えると、撚糸後の撚り止めセットで発現する捲縮が、製編織工程の糸切れの原因となり、また、織編物とした際の形態も安定しない。   The crimp ratio (CC) affects the crimp generated during the twisting set after twisting. The lower limit of CC is 20% or more, preferably 30% or more, and the upper limit is 50% or less, preferably 45% or less. good. If it is less than 20%, the processability of knitting and weaving is good, but the stretchability when made into a fabric is inferior. If it exceeds 50%, the crimps appearing in the twisted set after twisting will cause yarn breakage in the knitting and weaving process, and the form of the knitted or knitted fabric will not be stable.

さらに高温捲縮率(HC)は、染色工程での熱処理により発現する捲縮率を示し、HCの下限は25%以上、好ましくは30%以上、上限は60%以下、好ましくは50%以下が良い。HCが25%未満であると織編物としたときのストレッチ性が劣り、60%を超えると染色工程で捲縮が発現する際に、著しい凹凸となり、織編物の形態が安定しない。   Further, the high temperature crimp ratio (HC) indicates the crimp ratio developed by heat treatment in the dyeing process, and the lower limit of HC is 25% or more, preferably 30% or more, and the upper limit is 60% or less, preferably 50% or less. good. If the HC is less than 25%, the stretchability when the woven or knitted fabric is made is inferior, and if it exceeds 60%, when the crimp is developed in the dyeing process, the unevenness becomes remarkable and the form of the woven or knitted fabric is not stable.

また本発明では、HC>CCであることが必要である。HCがCCより大きいことにより、撚糸後の撚り止めセットで熱処理した後の、製編織後の染色工程の熱処理でも捲縮が生じ、織編物となった際のストレッチ性に優れたものとなる。
さらに本発明のマルチフィラメント繊維は、伸度(DE)の下限が好ましくは20%以上、より好ましくは30%以上、上限は70%以下、より好ましくは60%以下が望ましい。伸度が70%を超えると、織編物としたときに十分な捲縮が発現しにくく、満足すべきストレッチ性能が得られにくい。また20%未満では、製編織の工程にて伸度不十分なため糸切れが発生しやすく工程通過性不良となりやすい。
In the present invention, it is necessary that HC> CC. When HC is larger than CC, crimping occurs even in the heat treatment in the dyeing process after weaving and weaving after heat treatment with a twisting set after twisting, and the stretch properties are excellent when it becomes a woven or knitted fabric.
Furthermore, the lower limit of the degree of elongation (DE) of the multifilament fiber of the present invention is preferably 20% or more, more preferably 30% or more, and the upper limit is 70% or less, more preferably 60% or less. When the elongation exceeds 70%, sufficient crimping is less likely to occur when a woven or knitted fabric is obtained, and it is difficult to obtain satisfactory stretch performance. If it is less than 20%, the elongation is insufficient in the process of weaving and weaving, so yarn breakage is likely to occur, and process passability is likely to be poor.

次に本発明のポリエステルマルチフィラメント繊維を得る製造方法を具体的に説明する。   Next, the production method for obtaining the polyester multifilament fiber of the present invention will be specifically described.

本発明のポリエステルマルチフィラメント繊維は、下記の式(a)を満足するポリエステル(A)とポリエステル(B)とを、2500m/分以下の引取速度で紡糸した接合型複合繊維の未延伸糸を、下記の式(b)〜(f)を満足する条件下で加熱ローラー延伸することで得られる。
[η]A−[η]B>0.145 (a)
1.000≦DR1 (b)
MDR×0.65≦DR2≦MDR×0.73 (c)
DR1<DR2 (d)
Tg≦TDR1≦Tc−30 (e)
Tg+20≦TDR2≦Tc (f)
(但し、式中、[η]A、[η]B、はそれぞれポリエステル(A)、(B)の固有粘度、MDRは延伸温度85℃における未延伸糸の最大延伸倍率を表す。DR1は1段目延伸倍率、DR2は2段目延伸倍率、TDR1は1段目延伸におけるローラー温度、TDR2は2段目延伸におけるローラー温度)、Tg(℃)は未延伸糸のガラス転移温度、Tc(℃)は未延伸糸の結晶化温度を示す。なお、複合繊維の未延伸糸の結晶化温度、ガラス転移温度がそれぞれ2点測定される場合は、低い方の温度を結晶化温度、高い方の温度をガラス転移温度とする)
The polyester multifilament fiber of the present invention is an unstretched yarn of a joint type composite fiber obtained by spinning polyester (A) and polyester (B) satisfying the following formula (a) at a take-up speed of 2500 m / min or less. It can be obtained by drawing with a heated roller under conditions that satisfy the following formulas (b) to (f).
[Η] A− [η] B> 0.145 (a)
1.000 ≦ DR1 (b)
MDR × 0.65 ≦ DR2 ≦ MDR × 0.73 (c)
DR1 <DR2 (d)
Tg ≦ TDR1 ≦ Tc-30 (e)
Tg + 20 ≦ TDR2 ≦ Tc (f)
(In the formula, [η] A and [η] B are the intrinsic viscosities of polyesters (A) and (B), respectively, and MDR is the maximum draw ratio of the undrawn yarn at a draw temperature of 85 ° C. DR1 is 1. Stage draw ratio, DR2 is the second stage draw ratio, TDR1 is the roller temperature in the first stage drawing, TDR2 is the roller temperature in the second stage drawing), Tg (° C.) is the glass transition temperature of the undrawn yarn, Tc (° C. ) Indicates the crystallization temperature of the undrawn yarn. In addition, when the crystallization temperature and the glass transition temperature of the undrawn yarn of the composite fiber are each measured at two points, the lower temperature is the crystallization temperature and the higher temperature is the glass transition temperature)

ポリエステル(A)とポリエステル(B)の固有粘度の差は0.145より大きいことが好ましい。固有粘度の差が0.145以下の場合、ポリエステル(A)とポリエステル(B)の収縮差が小さく、捲縮の発現が不足しストレッチ性能が得られない。   The difference in intrinsic viscosity between polyester (A) and polyester (B) is preferably greater than 0.145. When the difference in intrinsic viscosity is 0.145 or less, the difference in shrinkage between the polyester (A) and the polyester (B) is small, the expression of crimp is insufficient, and the stretch performance cannot be obtained.

また、複合紡糸に際してのポリエステル(A)/ポリエステル(B)の接合比(重量比)Wは、複合繊維の形態下で捲縮発現力を与えるうえで4/6<W<6/4が好ましい。接合比が上記範囲外では製糸性が低下しやすく、複合繊維の形態下での捲縮発現力も不足しやすい。   In addition, the joining ratio (weight ratio) W of polyester (A) / polyester (B) during composite spinning is preferably 4/6 <W <6/4 in order to give a crimp expression in the form of the composite fiber. . If the joining ratio is out of the above range, the spinning property is likely to be lowered, and the crimping ability in the form of the composite fiber is likely to be insufficient.

さらに未延伸糸の延伸は、前記式(b)〜(f)を満足する条件で、加熱ローラーで2段延伸することが必要である。熱ピンによる延伸では延伸点が熱ピン上に固定され、捲縮率(CC)が高くなり、製編織の際に工程通過性が不良となり、捲縮率(CC)が高温捲縮率(HC)以上となる。   Furthermore, the unstretched yarn needs to be stretched in two stages with a heating roller under the conditions satisfying the formulas (b) to (f). In drawing with a hot pin, the drawing point is fixed on the hot pin, the crimp rate (CC) becomes high, the process passability becomes poor during weaving and weaving, and the crimp rate (CC) becomes high temperature crimp rate (HC). ) Or more.

また、DR1が1.000未満では、延伸機台上で糸が弛み製糸できず、DR2がMDR×0.65未満であると、十分に延伸されないことによるネッキングが生じ染色時に太細斑による濃色部、淡色部が発生する。MDR×0.73を超えると捲縮率(CC)が高くなり、製編織の工程で糸切れが発生し工程不安定になる。   Further, if DR1 is less than 1.000, the yarn is loosened and cannot be produced on the stretching machine table, and if DR2 is less than MDR × 0.65, necking occurs due to insufficient stretching, resulting in thickening due to thick spots during dyeing. A color portion and a light color portion are generated. When MDR × 0.73 is exceeded, the crimp ratio (CC) increases, and yarn breakage occurs in the weaving and weaving process, which makes the process unstable.

さらにDR1<DR2が好ましい。DR1がDR2を超える場合、1段目延伸ローラー上で予熱された繊維が冷延伸されるため、繊維に太細斑が発現することがある。   Further, DR1 <DR2 is preferable. When DR1 exceeds DR2, the fiber preheated on the first-stage stretching roller is cold-drawn, so that thick spots may appear on the fiber.

TDR1はTg≦TDR1≦Tc−30とすることで、未延伸糸を1段目延伸ローラー上で予熱し、後の2段目延伸で十分に延伸することが可能となる。   By setting Tg1 to Tg ≦ TDR1 ≦ Tc−30, the undrawn yarn can be preheated on the first-stage drawing roller and sufficiently drawn in the subsequent second-stage drawing.

TDR2がTg+20℃未満では、得られる繊維の配向度が低く強度不十分となり、Tcを超えると捲縮率が高くなるため製編織の際に工程通過性不良となる。   If the TDR2 is less than Tg + 20 ° C., the degree of orientation of the resulting fiber is low and the strength is insufficient, and if it exceeds Tc, the crimping rate increases, resulting in poor processability during knitting.

また本発明のポリエステルマルチフィラメント繊維の製造方法により得られる織編物は、本発明のポリエステルマルチフィラメント繊維に撚りを施した糸条を用いて布帛とし、引き続き、熱セットを施すことによって、織物収縮率(LC)が20〜40%となることが必要である。LCが20%未満であると十分なストレッチ性を得ることができない。40%を超えると織編物とした際の形態が安定しない。   Further, the woven or knitted fabric obtained by the method for producing a polyester multifilament fiber of the present invention is made into a fabric using a yarn obtained by twisting the polyester multifilament fiber of the present invention, and subsequently subjected to heat setting, thereby shrinking the fabric. (LC) needs to be 20 to 40%. If the LC is less than 20%, sufficient stretch properties cannot be obtained. If it exceeds 40%, the form of the knitted or knitted fabric is not stable.

なお、本発明の織編物は、例えば、本発明のポリエステルマルチフィラメント繊維を単独及び/または混繊した後、公知の方法により織編物とし、染色処理することによって得ることができる。   The woven or knitted fabric of the present invention can be obtained, for example, by singly and / or blending the polyester multifilament fibers of the present invention, and then making a woven or knitted fabric by a known method and dyeing it.

以下、本発明を実施例により具体的に説明する。なお、実施例における特性値の評価は次の方法によって拠った。   Hereinafter, the present invention will be specifically described by way of examples. In addition, evaluation of the characteristic value in an Example depended on the following method.

(捲縮率CC)
サンプル原糸を枠周1mで巻き数10回の綛を作成し、綛が乱れないように2ヶ所を束ねてくくり、8の字状にして2つ折に重ねて輪にすることを2回繰り返し、ガーゼに包み水浴に浸したときに浮かないように金網箱に入れ、90℃に調整した恒温槽に20分間浸漬する。恒温槽から金網箱を取り出し、水を切り綛が乱れない様にろ紙の上に並べる。20時間以上放置し、自然乾燥した後に捲縮を引き伸ばさない様に注意しながら、余分な絡まりをほぐす。
(Crimping rate CC)
Create a cocoon of sample yarn with a winding of 10 turns with a frame circumference of 1 m, wrap two places so that the cocoon does not get disturbed, repeat the process twice, making it into a figure of 8 and folding it into two. Then, wrap in gauze, put in a wire mesh box so that it will not float when immersed in a water bath, and immerse in a thermostat adjusted to 90 ° C. for 20 minutes. Remove the wire mesh box from the thermostatic chamber, drain the water, and place it on the filter paper so that the sputum is not disturbed. Leave it for 20 hours or more and let it dry naturally and loosen any excess entanglement, taking care not to stretch the crimp.

表示デシテックス(1.1dtex)当り49/25000cN×20の初荷重を掛け1分後の長さ(L0)を測る。初荷重を除重後に表示デシテックス当りの49/500cN×20の測定荷重を掛けて1分後の長さ(L1)を測り、除重後2分間放置して再び初荷重を掛けて1分後の長さ(L2)を測る。捲縮率CCは下記式により算出する。
捲縮率CC(%)=(L1−L2)/L1×100
Apply an initial load of 49/25000 cN × 20 per display decitex (1.1 dtex) and measure the length (L0) after 1 minute. After weighing the initial load, apply a measurement load of 49/500 cN × 20 per display decitex, measure the length (L1) after 1 minute, leave it for 2 minutes after dewetting, and then reapply the initial load and 1 minute later Measure the length (L2). The crimp rate CC is calculated by the following formula.
Crimp rate CC (%) = (L1-L2) / L1 × 100

(高温捲縮率(HC))
サンプル原糸を枠周1mで巻き数10回の綛を作成し、綛が乱れないように2ヶ所を束ねてくくり、8の字状にして2つ折に重ねて輪にすることを2回繰り返す。水温40℃に調整したポットに該綛を投入し、昇温速度4℃/分で70℃まで昇温後、昇温速度2℃/分で130℃まで昇温する。130℃で20分キープした後、降温速度4℃/分で60℃にした後、該綛を取り出し、水を切り綛が乱れない様にろ紙の上に並べる。
(High temperature crimp rate (HC))
Create a cocoon with a sample circumference of 1m and wrapping 10 times with a frame circumference of 1m, wrap two places so that the cocoon is not disturbed, and repeat the process of making a circle by folding it into a figure of 8 and folding it twice. . The soot is put into a pot adjusted to a water temperature of 40 ° C., heated to 70 ° C. at a heating rate of 4 ° C./min, and then heated to 130 ° C. at a heating rate of 2 ° C./min. After keeping at 130 ° C. for 20 minutes, the temperature is lowered to 60 ° C. at a temperature lowering rate of 4 ° C./minute, and then the water is taken out and drained and placed on a filter paper so as not to disturb the water.

20時間以上放置し、自然乾燥した後に捲縮を引き伸ばさない様に注意しながら、余分な絡まりをほぐす。表示デシテックス(1.1dtex)当り49/25000cN×20の初荷重を掛け1分後の長さ(H0)を測る。初荷重を除重後に表示デシテックス当りの49/500cN×20の測定荷重を掛けて1分後の長さ(H1)を測り、除重後2分間放置して再び初荷重を掛けて1分後の長さ(H2)を測る。高温捲縮率(HC)は下記式により算出する。
高温捲縮率HC(%)=(H1−H2)/H1×100
Leave it for 20 hours or more and let it dry naturally and loosen any excess entanglement, taking care not to stretch the crimp. Apply an initial load of 49/25000 cN × 20 per display decitex (1.1 dtex) and measure the length (H0) after 1 minute. After weighing the initial load, apply a measurement load of 49/500 cN × 20 per display decitex, measure the length (H1) after 1 minute, leave it for 2 minutes after dewetting, and then reapply the initial load and 1 minute later Measure the length (H2). The high temperature crimp ratio (HC) is calculated by the following formula.
High temperature crimp rate HC (%) = (H1-H2) / H1 × 100

(伸度(DE))
島津製作所(株)製オートグラフシステムSD−100−Cを用い、サンプル長20cm、引張速度20m/分の条件で測定した。
(Elongation (DE))
Using an autograph system SD-100-C manufactured by Shimadzu Corporation, measurement was performed under the conditions of a sample length of 20 cm and a tensile speed of 20 m / min.

(織物収縮率(LC))
サンプル原糸を撚係数K=100(T=K×√DTは1m当りの撚数、Dはサンプル原糸の繊度)の条件で撚糸を施し、温度70℃、湿度90%RHの条件下で40分間セットした糸を緯糸として、該サンプル糸の繊度(D)から打ち込み本数(本/cm)=311.1/√Dで算出される打ち込み本数で、縦糸密度39.6本/cmに設定された56dtex18フィラメントの原糸を経糸として製織した後、織物緯糸方向に長さ1mの間隔で印を付け(M0)緯糸に平行に10cm幅のサンプル布を切り出し、130度℃×30分間、熱水処理する。熱水処理したサンプル布を風乾後、片端を固定して垂直に垂らし、下方の他端に0.45g/dtexの荷重をかけ、先に付けた印の間隔(M1)を測定し、織物収縮率(LC)=(M0−M1)/M0×100で算出した。
(Textile shrinkage (LC))
The sample yarn is twisted under the conditions of a twist coefficient K = 100 (T = K × √DT is the number of twists per meter, D is the fineness of the sample yarn), and the temperature is 70 ° C. and the humidity is 90% RH. Using the yarn set for 40 minutes as the weft, the number of driven yarns (number / cm) = 311.1 / √D from the fineness (D) of the sample yarn, and the warp yarn density was set to 39.6 yarns / cm After weaving the original 56 dtex 18 filament yarn as warp, the fabric is marked at intervals of 1 m in the weft direction (M0), and a 10 cm wide sample cloth is cut out parallel to the weft, and heated at 130 ° C. for 30 minutes. Treat with water. After air-drying the sample fabric treated with hot water, one end is fixed and hung vertically, a load of 0.45 g / dtex is applied to the other end below, and the distance (M1) between the first marks is measured to shrink the fabric. Calculated as ratio (LC) = (M0−M1) / M0 × 100.

(固有粘度[η])
ポリマーをフェノールとテトラクロロエタンの1:1の混合溶媒に溶解し、ウベローデ粘度計を用いて25℃で測定した。
(Intrinsic viscosity [η])
The polymer was dissolved in a 1: 1 mixed solvent of phenol and tetrachloroethane and measured at 25 ° C. using an Ubbelohde viscometer.

(織物風合)
サンプル原糸による織物を作成し、サンプル織物の引っ張り弾性を触感による官能テストにより次の基準で評価した。
○:伸長、反発弾性が共に非常に良好
△:伸長、反発弾性が共に良好
×:伸長、反発弾性が共に不十分
(Textile texture)
A woven fabric made of sample yarn was prepared, and the tensile elasticity of the sample woven fabric was evaluated according to the following criteria by a sensory test using tactile sensation.
○: Both elongation and impact resilience are very good. Δ: Both elongation and impact resilience are good. ×: Both elongation and impact resilience are insufficient.

(実施例1)
イソフタル酸(IPA)8モル%をポリエチレンテレフタレートに共重合した固有粘度0.647の共重合ポリエチレンテレフタレートをポリマー(A)、固有粘度0.484のポリエチレンテレフタレートをポリマー(B)とし、紡糸温度を290℃とし、紡糸吐出孔の上流で2種のポリマー流を面対称に合流させ、接合比(重量比)5/5で、孔径0.6mm、長さ1.5mmの細孔の吐出孔を24個有する複合紡糸口金より紡出した。この紡出糸条を冷却、オイリング後、2100m/分の引取速度で巻き取り、228dtex/24フィラメントのの未延伸糸を得た。Tgは70℃。Tcは145℃であった。
Example 1
Polyethylene terephthalate having an intrinsic viscosity of 0.647 obtained by copolymerizing 8 mol% of isophthalic acid (IPA) with polyethylene terephthalate is polymer (A), polyethylene terephthalate having an intrinsic viscosity of 0.484 is polymer (B), and the spinning temperature is 290. The temperature was set to 0 ° C., and two types of polymer streams were joined in plane symmetry upstream of the spinning discharge holes, and 24 discharge holes having a pore diameter of 0.6 mm and a length of 1.5 mm at a joining ratio (weight ratio) of 5/5 were obtained. Spinning was performed from a composite spinneret. The spun yarn was cooled and oiled, and then wound up at a take-up speed of 2100 m / min to obtain an undrawn yarn of 228 dtex / 24 filament. Tg is 70 ° C. Tc was 145 ° C.

該未延伸糸を表1に示す条件で延伸して109dtex/24フィラメントのポリエステルマルチフィラメント繊維を得た。   The undrawn yarn was drawn under the conditions shown in Table 1 to obtain a polyester multifilament fiber of 109 dtex / 24 filament.

該延伸糸を加撚糸条にした後に、70℃にて湿熱セットし、経糸及び緯糸に使用して、表1に示す条件の生機密度でポプリンを製織した。この生機を小野森鉄工所製の液流染色機にて、ソーダ灰1g/l、界面活性剤0.5g/lを併用した溶液を用いて、120℃、20分間、リラックス精練を行い乾燥した。次いで、市金工業株式会社製のピンテンターにて、織物の経及び緯方向に張力をかけずに、乾熱180℃,30秒にてヒートセットを行なった。   After the drawn yarn was twisted, it was wet-heat set at 70 ° C., used for warp and weft, and woven poplin at the green density of the conditions shown in Table 1. This raw machine was dried with a liquid dyeing machine manufactured by Onomori Iron Works using a solution containing 1 g / l soda ash and 0.5 g / l surfactant in combination at 120 ° C. for 20 minutes. . Next, heat setting was performed with a pin tenter manufactured by Ichikin Kogyo Co., Ltd. without applying tension in the warp and weft directions of the fabric at a dry heat of 180 ° C. for 30 seconds.

次いで、液流染色機を用いアルカリ減量処理を施して、20質量%減量した。この後、小野森鉄工所製の液流染色機にて分散染料DianixBlackBG−FS200を15o.w.f%、染色温度130℃、時間30分にて染色した後、織物のL値を測定した。   Next, an alkali weight loss treatment was performed using a liquid dyeing machine to reduce the weight by 20% by mass. Thereafter, the disperse dye DianixBlackBG-FS200 was added to the liquid dyeing machine manufactured by Onomori Iron Works, 15o. w. After dyeing at f%, dyeing temperature 130 ° C., time 30 minutes, the L value of the fabric was measured.

表1に得られたポリエステルマルチフィラメント繊維及び織物の評価結果を示した。   Table 1 shows the evaluation results of the polyester multifilament fibers and fabrics obtained.

(実施例2)
実施例1と同様のポリマーを用い、同様の紡糸条件で、吐出孔を12個有する複合紡糸口金で、115dtex/12フィラメントの未延伸糸を得た。
(Example 2)
An undrawn yarn of 115 dtex / 12 filaments was obtained with a composite spinneret having 12 discharge holes using the same polymer as in Example 1 and under the same spinning conditions.

該未延伸糸を、表1に示す条件で延伸して55dtex/12フィラメントのポリエステルマルチフィラメント繊維を得た。また該繊維を用いて実施例1と同様に織物を得た。   The undrawn yarn was drawn under the conditions shown in Table 1 to obtain a polyester multifilament fiber of 55 dtex / 12 filament. In addition, a woven fabric was obtained in the same manner as in Example 1 using the fiber.

表1に得られたポリエステルマルチフィラメント繊維及び織物の評価結果を示した。   Table 1 shows the evaluation results of the polyester multifilament fibers and fabrics obtained.

(実施例3)
実施例2と同様のポリマーを用い、同様の紡糸条件で、吐出孔を12個有する複合紡糸口金で、62dtex/12フィラメントの未延伸糸を得た。
(Example 3)
An undrawn yarn of 62 dtex / 12 filaments was obtained with a composite spinneret having 12 discharge holes using the same polymer as in Example 2 and under the same spinning conditions.

得られた未延伸糸を、表1に示す条件で延伸して33dtex/12フィラメントのポリエステルマルチフィラメント繊維を得た。また該繊維を用いて実施例1と同様に織物を得た。   The obtained undrawn yarn was drawn under the conditions shown in Table 1 to obtain a 33 dtex / 12 filament polyester multifilament fiber. In addition, a woven fabric was obtained in the same manner as in Example 1 using the fiber.

表1に得られたポリエステルマルチフィラメント繊維及び織物の評価結果を示した。   Table 1 shows the evaluation results of the polyester multifilament fibers and fabrics obtained.

(比較例1)
実施例1において得られた未延伸糸を1対の熱ピンを介して、第1摩擦抵抗ピンを80℃、第2摩擦抵抗ピンを150℃で延伸倍率2.11倍(MDR×0.71)で延伸して109dtex/24フィラメントのポリエステルマルチフィラメント繊維を得て、該繊維を用いて実施例1と同様に織物を得た。
(Comparative Example 1)
The unstretched yarn obtained in Example 1 was passed through a pair of heat pins, the first frictional resistance pin was 80 ° C., the second frictional resistance pin was 150 ° C. and the draw ratio was 2.11 times (MDR × 0.71). ) To obtain a polyester multifilament fiber of 109 dtex / 24 filament, and using this fiber, a woven fabric was obtained in the same manner as in Example 1.

表1に得られたポリエステルマルチフィラメント繊維及び織物の評価結果を示した。製織の際に毛羽、糸切れが発生し工程通過性が劣るものであった。   Table 1 shows the evaluation results of the polyester multifilament fibers and fabrics obtained. Fluff and thread breakage occurred during weaving, and the process passability was poor.

(比較例2)
実施例2において得られた未延伸糸を1対の熱ピンを介して、第1摩擦抵抗ピンを80℃、第2摩擦抵抗ピンを150℃で延伸倍率2.11倍(MDR×0.71)で延伸して55dtex/12フィラメントのポリエステルマルチフィラメント繊維を得て、該繊維を用いて実施例1と同様に織物を得た。
(Comparative Example 2)
The unstretched yarn obtained in Example 2 was passed through a pair of heat pins, the first frictional resistance pin was 80 ° C., the second frictional resistance pin was 150 ° C. and the draw ratio was 2.11 times (MDR × 0.71). ) To obtain a polyester multifilament fiber of 55 dtex / 12 filament, and using this fiber, a woven fabric was obtained in the same manner as in Example 1.

表1に得られたポリエステルマルチフィラメント繊維及び織物の評価結果を示した。製織の際に毛羽、糸切れが発生し工程通過性が劣るものであった。   Table 1 shows the evaluation results of the polyester multifilament fibers and fabrics obtained. Fluff and thread breakage occurred during weaving, and the process passability was poor.

(比較例3)
実施例3において得られた未延伸糸を、表1に示す条件で延伸して33dtex/12フィラメントのポリエステル複合マルチフィラメント繊維を繊維を得て、該繊維を用いて実施例1と同様に織物を得た。
(Comparative Example 3)
The undrawn yarn obtained in Example 3 was drawn under the conditions shown in Table 1 to obtain a 33 dtex / 12 filament polyester composite multifilament fiber, and the fabric was used in the same manner as in Example 1 using the fiber. Obtained.

表1に得られたポリエステルマルチフィラメント繊維及び織物の評価結果を示した。製織の際に毛羽、糸切れが発生し工程通過性が劣るものであった。   Table 1 shows the evaluation results of the polyester multifilament fibers and fabrics obtained. Fluff and thread breakage occurred during weaving, and the process passability was poor.

Figure 2009144317
Figure 2009144317

Claims (2)

溶融粘度の異なる2種のポリエステルポリマーが接合した単繊維からなり、マルチフィラメント繊維として、以下の要件(1)〜(3)を同時に満足することを特徴とするポリエステルマルチフィラメント繊維。
(1)20≦捲縮率(CC)≦50(%)、
(2)25≦高温捲縮率(HC)≦60(%)、
(3)HC>CC
ただし、捲縮率(CC)は、90℃×20分間湿熱処理条件で測定された捲縮率であり、高温捲縮率(HC)は、130℃×20分間湿熱処理条件で測定された捲縮率である。
A polyester multifilament fiber comprising a single fiber in which two kinds of polyester polymers having different melt viscosities are joined, and satisfying the following requirements (1) to (3) simultaneously as a multifilament fiber.
(1) 20 ≦ crimp rate (CC) ≦ 50 (%),
(2) 25 ≦ high temperature crimp rate (HC) ≦ 60 (%),
(3) HC> CC
However, the crimp ratio (CC) is a crimp ratio measured at 90 ° C. for 20 minutes under wet heat treatment conditions, and the high temperature crimp ratio (HC) is a crack measured at 130 ° C. for 20 minutes under wet heat treatment conditions. Reduction rate.
溶融粘度の異なる2種のポリエステルポリマーのうち高粘度成分が、第三成分を5〜15モル%共重合させた共重合ポリエチレンテレフタレートである請求項1記載のポリエステルマルトフィラメント繊維。   The polyester maltofilament fiber according to claim 1, wherein the high viscosity component of two polyester polymers having different melt viscosities is a copolymerized polyethylene terephthalate obtained by copolymerizing 5 to 15 mol% of the third component.
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Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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