JPS6262183B2 - - Google Patents

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Publication number
JPS6262183B2
JPS6262183B2 JP8395180A JP8395180A JPS6262183B2 JP S6262183 B2 JPS6262183 B2 JP S6262183B2 JP 8395180 A JP8395180 A JP 8395180A JP 8395180 A JP8395180 A JP 8395180A JP S6262183 B2 JPS6262183 B2 JP S6262183B2
Authority
JP
Japan
Prior art keywords
yarn
polyester
weight loss
unstretched
yarns
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP8395180A
Other languages
Japanese (ja)
Other versions
JPS5711273A (en
Inventor
Shigetoshi Shimizu
Tatsuo Tatsuki
Yoshihiro Fujii
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP8395180A priority Critical patent/JPS5711273A/en
Publication of JPS5711273A publication Critical patent/JPS5711273A/en
Publication of JPS6262183B2 publication Critical patent/JPS6262183B2/ja
Granted legal-status Critical Current

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  • Chemical Or Physical Treatment Of Fibers (AREA)
  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
  • Decoration Of Textiles (AREA)

Description

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

本発明はポリエステル系繊維構造物の製造法に
関するものである。従来から通常の延伸法により
製造され糸条の長手方向に沿つて均一構造を有す
るポリエステル系繊維構造物は、風合を改善する
ためカセイソーダ等の強アルカリ物を用い減量加
工することが広く行なわれている。 しかしながら、同一糸条中に実質的に未延伸部
と延伸部をランダムに有するポリエステル系繊維
の生糸使い糸条Aについては、太細の不均一構造
による特殊風合と、染色した場合の濃淡霜降り模
様の発現など、特長ある素材であるにもかかわら
ず、減量加工時に極端に強力劣化を生じるため、
減量加工が必須である薄地分野に展開できないと
いう致命的な問題点があつた。 減量加工法については、一般的な方法として吊
り練りなどの浸漬法、パツドスチーミング法、コ
ールドバツチ法があり、それぞれ減量作用も異な
るが、糸条Aからなる布帛はいずれの方法を用い
ても、減量率10%程度で糸強力が1g/d以下と
なり、実用に耐えない。糸条Aからなる布帛が減
量加工により極端に強力劣化する原因は、未延伸
部と延伸部の物性差に基づく減量速度差により、
未延伸部が集中的に加水分解されることによるも
のと推定され、このような現象を回避するため
に、アルカリ処理の方法や条件を変えて対処して
もほとんど効果がないことを上述の結果が示して
いる。 劣化の原因が未延伸部の易減量性にあるので、
改善するための手段として、未延伸部の配向性や
結晶化度を高める方法が考えられるが、製糸段階
でこのような処置は、大幅な繊維物性の変化を伴
い、糸条Aの特長である濃淡色差の発現パターン
や、特殊風合を失なう結果となるので好ましいと
はいえない。 そこで本発明者はこのような問題点を解決すべ
く鋭意研究を重ね、特定のアルカリ減量速度を有
するポリエステル繊維を混ぜ合せて用いることに
より上記欠点を改善しうることを見い出し本発明
に到達した。 すなわち本発明は、同一糸条中に未延伸部と延
伸部をランダムに有するポリエステル系糸条A
と、糸条の長手方向に沿つてほぼ均一構造であ
り、該糸条Aの未延伸部とほぼ等しい複屈折を有
する未延伸ポリエステル糸条のアルカリ加水分解
速度より1.0〜5.0倍大きいアルカリ加水分解速度
を有するポリエステル系糸条Bとを含む布帛状物
に減量処理を施すことを特徴とするポリエステル
系繊維構造物の製造法に関するものである。 本発明法でいうポリエステル系繊維糸条Aと
は、ポリエチレンテレフタレートまたはエチレン
テレフタレートを主構成単位とする共重合ポリエ
ステルなどから得られるフイラメント糸であり、
同一糸条中に潜在的に易染性の未延伸部と難染性
の延伸部が交互にランダムに存在する糸条であ
る。通常は繊維軸方向に未延伸部が太く、延伸部
が細くなつており、単繊維の最も太い部分と最も
細い部分の直径の比は、特に限定されるものでは
ないが、1.2〜1.65程度であり、好ましくは1.2〜
1.5であつて、また特に限定されるものではない
が、通常、太い部分の複屈折が15×10-3〜80×
10-3、好ましくは25×10-3〜80×10-3で、細い部
分の複屈折が90×10-3〜200×10-3であるような
太細を有するものが一般に用いられる。太い部分
の長さは100mm以下が好ましく、太い部分の全体
の存在比は1:1〜1:1.5の範囲が好ましく
1:1.3が最も好ましい。 また本発明に適用される糸条Bとしては、糸条
の長手方向に沿つてアルカリ加水分解性にほとん
ど差のない均一構造を有することが第1の要件で
あり、さらに糸条Aの未延伸部とほぼ等しい複屈
折を有する未延伸ポリエステル糸条の加水分解速
度より1.0〜5.0倍速いアルカリ加水分解速度であ
ることが必要である。ただし糸条Aの未延伸部と
ほぼ等しい複屈折を有する未延伸ポリエステル糸
条とは、アルカリ加水分解速度がほとんど変化し
ない複屈折がA±10-3(ただしAは糸条Aの未延
伸部の複屈折を示す)の範囲内で同一組成の重合
体からなる糸条を基準とすることが好ましい。 また本発明におけるアルカリ加水分解速度と
は、糸条Aの平均繊度と同一の繊度構成からなる
複屈折A±10×10-3の範囲の未延伸ポリエステル
糸を、固形カセイソーダ30g/、98℃、60分間
の条件で処理した時の減量率を1.0として相対比
較するものである。 通常アルカリ加水分解速度とポリエステルの改
質度とは正の相関があるので、このような要件を
満足しうる糸条Bとして、糸条Aよりも改質度の
高いポリエステルを適用することが挙げられる。
具体的にはテレフタル酸またはそのエステル誘導
体をジカルボン酸成分とし、エチレングリコー
ル、1,4―ブタンジオールから選ばれるグリコ
ールまたはそのエステル形成性誘導体をグリコー
ル成分とするポリエステルの、ジカルボン酸成分
の一部を、たとえば5―スルホイソフタル酸のモ
ノアルカリ金属塩、イソフタル酸、ジフエニルジ
カルボン酸、ナフタレンジカルボン酸、アジピン
酸、セバシン酸、ドデカン二酸等のジカルボン酸
またはそのエステル、p―オキシ安息香酸、p―
β―オキシエトキシ安息香酸等のオキシカルボン
酸またはそのエステルで置換したものでもよく、
また脂肪族または脂環式グリコールの一部をたと
えば炭素数2〜10のアルキレングリコール、1,
4―シクロヘキサンジメタノール、1,4―ビス
(β―オキシエトキシ)ベンゼン、ビスフエノー
ルAのビスグリコールエーテル、ポリアルキレン
グリコール等の主グリコール成分以外のグリコー
ルで置きかえてもよい。 さらにペンタエリスリトール、トリメチロール
プロパン、トメリツト酸、トリメシン酸等の鎖分
岐剤やモノハイドリツクポリアルキレンオキサイ
ド、フエニル酢酸等の重合停止剤を少割合使用す
ることも可能である。また改質ポリマー以外にア
ルカリ加水分解速度の大なる素材として、極細糸
や高温熱処理糸を挙げることができる。 アルカリによるポリエステルの加水分解は、通
常、繊維表面層から順次進行するものと考えら
れ、同一素材であれば単糸繊度が小さく、表面積
の大きいものほど加水分解速度は大となる。単糸
繊度と表面積の関係は略()式で表わすことが
でき、表面積と加水分解速度とは正比例の関係が
あるので、たとえば複屈折が15×10-3〜80×10-3
の範囲にある特定の未延伸ポリエステル糸条と同
一の単糸維度d1で、アルカリ分解速度が1.0〜5.0
の範囲外にある糸条Bでも、()式の関係から
おおよその適正単糸繊度d2を推定することは可能
である。 A1:d1繊度の表面積 A2:d2繊度の表面積 さらに熱履歴に関しても、同一素材で180℃、
60秒間の乾熱処理したものの加水分解速度に対し
て、220℃、60秒間の乾熱処理したものは約2倍
の速度を示すので、単糸繊度差と組合せて適宜糸
条Bに応用することができる。ここで糸条Bの構
成要件についてさらに詳述すると、糸条の長手方
向に沿つて均一構造でなければならない理由は、
強弱部が存在すると、糸条Aの弱部(未延伸部)
と糸条Bの弱部が重なり合つた場合、糸条A・糸
条Bそれぞれの平均強度よりも極端に低い強度を
示すからこれを避けるためであり、また糸条Aの
未延伸部とほぼ等しい複屈折を有する未延伸ポリ
エステル糸条の1.0〜5.0倍の範囲のアルカリ加水
分解速度でなければならないのは、次の実験例に
より説明できる。 実験例 通常のポリエチレンテレフタレートよりなり長
手方向に未延伸部と延伸部をランダムに有する
75D―24Fの糸条Aに対し、糸条Aに使用したポ
リマーにポリエチレングリコール(分子量1000)
を3〜6重量%の範囲で添加して改質した75D―
24Fの8種類の糸条B1〜B8をそれぞれ1:1の比
率でエアー混繊したのち、糸条A2本を引揃えた
水準も加えてダブルツイスターでS・Z・
2000t/mのヨリをかけて強撚糸とし、通常の方
法でジヨーゼツトに織り、シボ立て、中間セツト
後、カセイソーダ30g/、98℃の条件で減量率
が約15%になるように減量加工したもののそれぞ
れの糸強力測定結果を表1に示す。 またこれとは別に糸条Aの未延伸部の複屈折と
ほぼ等しい複屈折40±10×10-3の範囲の未延伸ポ
リエステル糸条(以下では糸条Cという)と糸条
B1〜B8のそれぞれの単独糸を筒編とし、開布、
中間セツト後、上記と同様の条件で60分間減量処
理して糸条Cに対する糸条B1〜B8の減量速度比
を求めた結果も併せて表1に示した。
The present invention relates to a method for manufacturing polyester fiber structures. Conventionally, polyester fiber structures manufactured by ordinary drawing methods and having a uniform structure along the longitudinal direction of the yarn have been widely reduced in weight using strong alkalis such as caustic soda in order to improve the texture. ing. However, yarn A using raw silk, which is a polyester fiber that has substantially random unstretched parts and stretched parts in the same yarn, has a special texture due to its thick and thin non-uniform structure, and dark and light marbling when dyed. Although it is a material with features such as the appearance of patterns, it deteriorates extremely strongly during weight reduction processing.
A fatal problem was that it could not be applied to the field of thin fabrics where weight reduction processing is essential. Regarding weight loss processing methods, there are generally dipping methods such as hanging kneading, pad steaming methods, and cold batch methods, and each method has a different weight loss effect, but the fabric made of yarn A can be processed by any of the methods. When the weight loss rate is about 10%, the yarn strength becomes less than 1 g/d, which is not suitable for practical use. The reason why the fabric made of yarn A deteriorates extremely strongly due to weight loss processing is due to the difference in weight loss rate based on the difference in physical properties between the unstretched part and the stretched part.
It is presumed that this is due to intensive hydrolysis of the unstretched area, and the above results indicate that changing the alkali treatment method or conditions to avoid this phenomenon will have little effect. shows. Since the cause of deterioration is the easy weight loss of the unstretched part,
As a means to improve this, it is possible to increase the orientation and crystallinity of the undrawn part, but such treatment at the spinning stage involves a significant change in the fiber properties, which is a characteristic of yarn A. This is not preferable because it results in the loss of the pattern of appearance of the shaded color difference and the loss of the special texture. In order to solve these problems, the inventors of the present invention have conducted intensive research and have found that the above-mentioned drawbacks can be improved by using a mixture of polyester fibers having a specific alkali weight loss rate, and have thus arrived at the present invention. That is, the present invention provides a polyester yarn A having randomly unstretched portions and stretched portions in the same yarn.
and an alkaline hydrolysis rate that is 1.0 to 5.0 times higher than the alkaline hydrolysis rate of an undrawn polyester yarn that has a substantially uniform structure along the longitudinal direction of the yarn and has a birefringence that is approximately equal to that of the undrawn portion of the yarn A. The present invention relates to a method for producing a polyester fiber structure, which is characterized by subjecting a fabric-like article containing a polyester yarn B having a high velocity to a weight reduction treatment. The polyester fiber yarn A as used in the method of the present invention is a filament yarn obtained from polyethylene terephthalate or a copolyester having ethylene terephthalate as a main constituent unit,
This is a yarn in which unstretched areas that are potentially easily dyed and stretched areas that are difficult to dye exist alternately and randomly in the same yarn. Usually, the unstretched part is thick in the fiber axis direction, and the stretched part is thin.The ratio of the diameters of the thickest part and the thinnest part of a single fiber is not particularly limited, but is approximately 1.2 to 1.65. Yes, preferably 1.2~
1.5, and although it is not particularly limited, the birefringence of the thick part is usually 15×10 -3 to 80×
10 -3 , preferably 25 x 10 -3 to 80 x 10 -3 , and a thin part having a birefringence of 90 x 10 -3 to 200 x 10 -3 is generally used. The length of the thick portion is preferably 100 mm or less, and the overall abundance ratio of the thick portion is preferably in the range of 1:1 to 1:1.5, and most preferably 1:1.3. The first requirement for the yarn B applied to the present invention is that it has a uniform structure with almost no difference in alkali hydrolyzability along the longitudinal direction of the yarn, and in addition, the unstretched yarn A It is necessary that the alkaline hydrolysis rate is 1.0 to 5.0 times faster than the hydrolysis rate of an undrawn polyester yarn having a birefringence approximately equal to 100%. However, an undrawn polyester yarn having a birefringence almost equal to that of the undrawn part of yarn A means that the birefringence of which the alkali hydrolysis rate hardly changes is A±10 -3 (where A is the undrawn part of yarn A). It is preferable to use yarns made of polymers having the same composition within the range of 100% birefringence). In addition, the alkaline hydrolysis rate in the present invention refers to undrawn polyester yarn having the same fineness structure as the average fineness of yarn A and having a birefringence A±10×10 -3 at 30 g of solid caustic soda at 98°C. The relative comparison is made assuming that the weight loss rate when treated for 60 minutes is 1.0. Since there is usually a positive correlation between the alkaline hydrolysis rate and the degree of modification of polyester, it is recommended to use polyester with a higher degree of modification than yarn A as yarn B that can satisfy these requirements. It will be done.
Specifically, a part of the dicarboxylic acid component of a polyester containing terephthalic acid or its ester derivative as the dicarboxylic acid component and a glycol selected from ethylene glycol and 1,4-butanediol or its ester-forming derivative as the glycol component. , for example, monoalkali metal salts of 5-sulfoisophthalic acid, dicarboxylic acids such as isophthalic acid, diphenyldicarboxylic acid, naphthalene dicarboxylic acid, adipic acid, sebacic acid, dodecanedioic acid, or their esters, p-oxybenzoic acid, p-
It may be substituted with oxycarboxylic acid such as β-oxyethoxybenzoic acid or its ester,
In addition, some of the aliphatic or alicyclic glycols may be replaced with alkylene glycols having 2 to 10 carbon atoms, 1,
It may be replaced with a glycol other than the main glycol component, such as 4-cyclohexanedimethanol, 1,4-bis(β-oxyethoxy)benzene, bisglycol ether of bisphenol A, or polyalkylene glycol. Furthermore, it is also possible to use a small proportion of a chain branching agent such as pentaerythritol, trimethylolpropane, tomelitic acid, trimesic acid, etc., or a polymerization terminator such as monohydric polyalkylene oxide, phenylacetic acid, etc. In addition to modified polymers, examples of materials with a high alkaline hydrolysis rate include ultrafine threads and high-temperature heat-treated threads. It is thought that hydrolysis of polyester by alkali normally proceeds sequentially from the fiber surface layer, and if the same material is used, the smaller the single fiber fineness and the larger the surface area, the faster the hydrolysis rate. The relationship between single fiber fineness and surface area can be roughly expressed by the formula (), and since there is a direct proportional relationship between surface area and hydrolysis rate, for example, if the birefringence is 15 × 10 -3 to 80 × 10 -3
With the same filament fiber index d 1 as a specific undrawn polyester yarn in the range of 1.0 to 5.0, the alkaline decomposition rate is
Even for yarn B that is outside the range of , it is possible to roughly estimate the appropriate single yarn fineness d 2 from the relationship in equation ( ). A 1 : Surface area of d 1 fineness A 2 : Surface area of d 2 fineness Furthermore, regarding the thermal history, the same material can be heated to 180℃,
Compared to the hydrolysis rate of the one treated with dry heat for 60 seconds, the hydrolysis rate of the one treated with dry heat at 220℃ for 60 seconds is about twice, so it can be applied to Yarn B as appropriate in combination with the difference in single yarn fineness. can. To explain in more detail the structural requirements of the yarn B, the reason why the yarn must have a uniform structure along the longitudinal direction is as follows.
If a strong/weak part exists, the weak part (undrawn part) of yarn A
This is to avoid the fact that if the weak parts of yarn A and yarn B overlap, the strength will be extremely lower than the average strength of each of yarn A and yarn B, and this is to avoid this. The need for an alkaline hydrolysis rate in the range of 1.0 to 5.0 times that of an undrawn polyester yarn with equal birefringence can be illustrated by the following experimental example. Experimental example: Made of ordinary polyethylene terephthalate, with random unstretched parts and stretched parts in the longitudinal direction.
For yarn A of 75D-24F, the polymer used for yarn A is polyethylene glycol (molecular weight 1000).
75D modified by adding 3 to 6% by weight of
After air-mixing 8 types of 24F yarns B 1 to B 8 at a ratio of 1:1, a level of two yarns A pulled together was added, and a double twister was used to create S, Z, and
After twisting at 2000t/m to make a hard-twisted yarn, weaving it into a jersey using the usual method, raising the grain, and intermediate setting, the yarn was weight-reduced to 30g of caustic soda at a temperature of 98°C so that the weight loss rate was approximately 15%. Table 1 shows the results of measuring each yarn strength. In addition, there are also undrawn polyester yarns (hereinafter referred to as yarn C) with a birefringence of 40±10×10 -3 that is approximately equal to the birefringence of the undrawn portion of yarn A.
Each individual yarn of B 1 to B 8 is knitted into a tube, and the fabric is opened and
After the intermediate setting, the yarns were subjected to weight loss treatment for 60 minutes under the same conditions as above, and the weight loss rate ratios of yarns B 1 to B 8 to yarn C were determined, and the results are also shown in Table 1.

【表】【table】

【表】 表1でわかるように糸条Cに対する減量速度比
が1.91まで(糸条B1〜糸条B5)は速度比が高くな
るにつれ糸強力が上り、2.72以上(糸条B6〜糸条
B8)では逆にこれより低下する傾向がある。した
がつて最適速度比は1.91〜2.72の間にあるものと
考えられるが、ポリエステル商品として実用に耐
えうる最低強力を経験上2.5g/d以上とする
と、糸条Cのアルカリ加水分解速度に対して速度
比1.0〜5.0までは採用しうる範囲である。糸条A
の未延伸部と延伸部を区分してサンプリングする
ことが困難なので、それぞれの明確な減量速度は
測定できないが、表1の結果から、糸条Cに対し
て5倍以上の減量速度比の糸条Bでは糸条Aの未
延伸部よりも糸条B自体の減量が進みすぎること
になり、強力が維持しにくくなるものと推定され
る。 上記実験例において、糸条Aの細繊度である
50D―24Fの糸条A′と糸条Bの細繊度である50D
―24Fの糸条B′を8本用いて、種々の混合比率で
エアー混繊したのち、以下上記実験例の通りの処
理を施した。 結果を次の表2に示す。
[Table] As can be seen from Table 1, when the weight loss speed ratio to yarn C is up to 1.91 (yarn B 1 to yarn B 5 ), the yarn strength increases as the speed ratio increases ; yarn
B8 ), on the other hand, tends to be lower than this. Therefore, the optimum speed ratio is considered to be between 1.91 and 2.72, but based on experience, if the minimum strength that can withstand practical use as a polyester product is 2.5 g/d or more, Therefore, a speed ratio of 1.0 to 5.0 is an acceptable range. Yarn A
Because it is difficult to separate and sample the unstretched and stretched parts, it is not possible to clearly measure the weight loss rate for each, but from the results in Table 1, it is clear that yarns with a weight loss rate ratio of 5 times or more compared to yarn C It is presumed that in the yarn B, the yarn B itself loses weight more than the undrawn portion of the yarn A, making it difficult to maintain strength. In the above experimental example, the fineness of yarn A is
50D - 50D which is the fineness of yarn A' and yarn B of 24F
Eight -24F yarns B' were air mixed at various mixing ratios, and then treated as in the above experimental example. The results are shown in Table 2 below.

【表】【table】

【表】 表2からわかるように、本発明の糸条Aと糸条
Bとの混用は通常の混紡糸、混繊糸の場合と同じ
く25/75〜75/25という混合比率の範囲で適用でき
る。 前記実験例に用いた織物は吊り練りによる減量
加工(実験例)のほか、パツドスチーム法、コー
ルドバツチ法でもテストした吊り練り法と同様の
結果を示すので、本発明法では特に減量加工法を
限定する必要はない。また糸条Aと糸条Bを含む
とは、糸条Aと糸条Bまたは必要に応じ他の糸条
(繊維)から布帛が形成されていることを云い、
たとえば糸条Aと糸条B、さらに必要に応じこれ
以外の糸条を、引揃え、混繊、合撚あるいは交絡
などの方法で混ぜ合せ布帛状とする場合があげら
れるがこれに限定されるものではない。 本発明法による糸条Aと糸条Bの混繊・交撚な
どの混合効果は糸条Bの混合により糸条Aの易減
量部の易減量性が緩和され耐減量加工性が向上す
るばかりでなく、糸条Aとは異質の糸条が混入さ
れるので、濃淡差や風合の面でより幅広い表現を
可能ならしめる。以下に実施例によりさらに本発
明を詳しく説明するが、これにより本発明が制限
されるものではない。 実施例 ポリエチレンテレフタレートを主構成単位とす
るポリエステル糸であり、長手方向に未延伸部と
延伸部が不規則に存在する75D―18Fの糸条A
と、ポリエチレンテレフタレートを主構成単位と
するポリエステルに、エチレン5―ソジユームス
ルフオイソフタレートを3.8重量%を加えて紡糸
延伸した75D―36Fの糸条Bを2本引揃えた糸条
(本発明法)と糸条Aを2本引揃えた糸条(比較
法)をそれぞれイタリー式撚糸機により2400T/
Mの撚糸(S・Zヨリ)を行なつたのち80℃、45
分間のスチーム処理でヨリ止めセツトした。この
糸を通常の手法で製織し、梨地ジヨーゼツトの生
機を各5疋得た。さらにこの各5疋の生機を通常
の条件でシボ立て、中間セツトを行なつて各1疋
ずつ吊り練り減量すべく、あんどん巻きに準備
し、固形カセイソーダ20g/、98℃の液槽でそ
れぞれ、約5%、10%、15%、20%、25%の減量
率になるように減量処理を施した。引続き湯水
洗、解反、結反、乾燥工程を経たのち、糸条A2
本引揃え織物(比較品)は、 Dianix Navy Blue ER―FS(三菱化成社製分
散染料) 0.1%o.w.f Dianix Yellow AC―E(三菱化成社製分散染
料) 0.5%o.w.f I.P.キヤリヤ―N―20(一方社製ポリエステル
用膨潤剤) 3.0%o.w.f の浴組成で液流染色機(サーキユラータイプ)に
より115℃、60分間染色した。また糸条Aと糸条
Bを引揃えた織物(本発明品)は、前記の浴組成
にEstrol Red N―GSL(住友化学社製カチオン
染料)と、オスピンKB―30F(東海製油社製分
散剤)を1%o.w.fを加えた浴組成で糸条A2本引
揃え織物同様、サーキユラー染色機で115℃、60
分間の染色を実施した。さらに比較品、本発明品
とも同一条件で仕上加工を行ない製品としたの
ち、それぞれの分解糸をテンシロン型引張試験機
により糸強力測定した結果を表3に示す。 比較品5水準、本発明品5水準とも異色効果の
発現した織物に仕上つたが、比較品のそれは、濃
淡効果だけであるのに対し、本発明品は3色の異
色となり、よりあざやかな異色を示した。 また表3の結果からわかるように比較品の糸強
力は減量率約5%でも2.5g/d以下になるのに
対し、本発明品はおどろくことに減量率が何と25
%減量でも2.5g/dをクリアーした実用に耐え
る製品となつた。なお使用した糸条Bのアルカリ
分解速度を測定した結果は1.5であつた。
[Table] As can be seen from Table 2, the mixture of yarn A and yarn B of the present invention can be applied within the mixing ratio range of 25/75 to 75/25, as in the case of ordinary blended yarns and mixed yarns. can. The fabric used in the above experimental example was tested by the pad steam method and the cold batch method in addition to the weight loss processing by hanging kneading (experimental example), and the results were similar to those of the hanging kneading method. Therefore, the method of the present invention specifically limits the weight loss processing method. There's no need. In addition, "containing yarn A and yarn B" means that the fabric is formed from yarn A and yarn B or other yarns (fibers) as necessary.
For example, yarn A and yarn B, and other yarns as necessary, may be mixed together to form a fabric by methods such as pulling, blending, twisting, or interlacing, but the examples are limited thereto. It's not a thing. The mixing effect of yarn A and yarn B, such as blending and intertwisting, according to the method of the present invention, is that the mixing of yarn B alleviates the easy weight loss property of the easy weight loss part of yarn A, and improves the resistance to weight loss processability. Instead, a yarn different from yarn A is mixed in, making it possible to create a wider range of expressions in terms of shading and texture. The present invention will be explained in more detail with reference to Examples below, but the present invention is not limited thereto. Example Yarn A of 75D-18F is a polyester yarn whose main constituent unit is polyethylene terephthalate, and has unstretched parts and stretched parts irregularly in the longitudinal direction.
A yarn (a yarn made by aligning two 75D-36F yarns B made by adding 3.8% by weight of ethylene 5-sodium sulfoisophthalate to a polyester whose main constituent unit is polyethylene terephthalate) is spun and drawn. Inventive method) and two yarns A (comparative method) were each twisted at 2400T/2 by an Italian twisting machine.
After twisting M yarn (S/Z twist), 80℃, 45
It was set with steam treatment for 1 minute to prevent it from twisting. This yarn was woven in a conventional manner to obtain 5 pieces each of pear-skinned jersey gray fabrics. Furthermore, each of these 5 squares of greige was embossed under normal conditions, an intermediate setting was performed, and each 1 square was prepared into andon rolls to reduce the weight. Weight loss treatment was performed to achieve a weight loss rate of approximately 5%, 10%, 15%, 20%, and 25%. After successively washing with hot water, unraveling, tying, and drying, yarn A2
The fabrics in this collection (comparison products) are: Dianix Navy Blue ER-FS (disperse dye manufactured by Mitsubishi Kasei) 0.1% owf Dianix Yellow AC-E (dispersed dye manufactured by Mitsubishi Kasei) 0.5% owf IP carrier N-20 ( Dyeing was carried out at 115°C for 60 minutes using a jet dyeing machine (circular type) with a bath composition of 3.0% owf (swelling agent for polyester manufactured by Ichiba Co., Ltd.). In addition, the fabric (product of the present invention) in which yarn A and yarn B are aligned is prepared by adding Estrol Red N-GSL (cationic dye manufactured by Sumitomo Chemical Co., Ltd.) and Ospin KB-30F (dispersion dye manufactured by Tokai Oil Co., Ltd.) to the bath composition described above. Similar to fabrics with 2 yarns A drawn in a bath composition with 1% OWF added, dyeing was carried out using a circular dyeing machine at 115℃ and 60℃.
Staining was performed for minutes. Furthermore, both the comparison product and the product of the present invention were finished under the same conditions to produce products, and the yarn strength of each decomposed yarn was measured using a Tensilon type tensile tester. Table 3 shows the results. Both the 5-level comparative product and the 5-level inventive product produced fabrics with a unique color effect, but while the comparative product only had a shading effect, the inventive product had 3 unique colors, with a more vivid unique color. showed that. Furthermore, as can be seen from the results in Table 3, the thread tenacity of the comparative product is less than 2.5 g/d even with a weight loss rate of about 5%, whereas the yarn strength of the product of the present invention surprisingly has a weight loss rate of 25 g/d.
Even with a % weight loss of 2.5 g/d, the product has become a product that can withstand practical use. The alkali decomposition rate of the yarn B used was measured and the result was 1.5.

【表】【table】

【表】【table】

Claims (1)

【特許請求の範囲】[Claims] 1 同一糸条中に未延伸部と延伸部をランダムに
有するポリエステル系糸条Aと、糸条の長手方向
に沿つてほぼ均一構造であり、該糸条Aの未延伸
部とほぼ等しい複屈折を有する未延伸ポリエステ
ル糸条のアルカリ加水分解速度より1.0〜5.0倍大
きいアルカリ加水分解速度を有するポリエステル
系糸条Bとを含む布帛状物をアルカリにより減量
処理することを特徴とするポリエステル系繊維構
造物の製造方法。
1 A polyester yarn A having unstretched parts and stretched parts randomly in the same yarn, and a nearly uniform structure along the longitudinal direction of the yarn, and a birefringence that is almost equal to the unstretched part of the yarn A. A polyester fiber structure characterized in that a fabric-like material comprising a polyester yarn B having an alkali hydrolysis rate 1.0 to 5.0 times higher than the alkali hydrolysis rate of an undrawn polyester yarn having the above is subjected to a weight reduction treatment with an alkali. How things are manufactured.
JP8395180A 1980-06-23 1980-06-23 Production of polyester fiber structure Granted JPS5711273A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8395180A JPS5711273A (en) 1980-06-23 1980-06-23 Production of polyester fiber structure

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8395180A JPS5711273A (en) 1980-06-23 1980-06-23 Production of polyester fiber structure

Publications (2)

Publication Number Publication Date
JPS5711273A JPS5711273A (en) 1982-01-20
JPS6262183B2 true JPS6262183B2 (en) 1987-12-25

Family

ID=13816886

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8395180A Granted JPS5711273A (en) 1980-06-23 1980-06-23 Production of polyester fiber structure

Country Status (1)

Country Link
JP (1) JPS5711273A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2695543B2 (en) * 1991-06-18 1997-12-24 株式会社クラレ Polyester special mixed yarn
JP2538735B2 (en) * 1992-02-10 1996-10-02 帝人株式会社 Method for manufacturing wool-like fabric
DE4415905C2 (en) * 1994-05-06 1996-08-22 Thyssen Industrie Process and plant for the preparation of heterogeneous mixtures resulting from comminution processes

Also Published As

Publication number Publication date
JPS5711273A (en) 1982-01-20

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