JPH07189058A - Multicolor-dyeing combined filament yarn and its production - Google Patents

Multicolor-dyeing combined filament yarn and its production

Info

Publication number
JPH07189058A
JPH07189058A JP34661693A JP34661693A JPH07189058A JP H07189058 A JPH07189058 A JP H07189058A JP 34661693 A JP34661693 A JP 34661693A JP 34661693 A JP34661693 A JP 34661693A JP H07189058 A JPH07189058 A JP H07189058A
Authority
JP
Japan
Prior art keywords
yarn
filament
yarns
filament yarns
multicolor
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.)
Granted
Application number
JP34661693A
Other languages
Japanese (ja)
Other versions
JP2731345B2 (en
Inventor
Terumi Shinmyo
輝美 新明
Michio Nagata
道夫 永田
Taro Murata
太郎 村田
Shoichiro Noguchi
章一郎 野口
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.)
Kanebo Ltd
Original Assignee
Kanebo Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kanebo Ltd filed Critical Kanebo Ltd
Priority to JP5346616A priority Critical patent/JP2731345B2/en
Publication of JPH07189058A publication Critical patent/JPH07189058A/en
Application granted granted Critical
Publication of JP2731345B2 publication Critical patent/JP2731345B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To obtain multicolor-dyeing combined filament yarn capable of generating fine mottle by combining plural filament yarns having different dyabilities in an extremely uniform state. CONSTITUTION:This multicolor-dyeing combined filament yarn is obtained by a running-liquid entanglement treatment of plural kinds of filament yarns made of polymers having different dyabilities. In the multicolor-dyeing combined filament yarn, the difference among plural kinds of filament yarns is <=12% in boiling-water shrinkage and <=8.0% in elongation. The filament yarns are each substantially non- twisted. The multicolor-dyeing combined filament yarn is produced by supplying each of plural kinds of polymers having different dyabilities with each other to closely placed plural spinning-drawing apparatuses, spinning plural kinds of different yarns and subsequently subjecting the obtained filament yarns to drawing and heat treatments. These treatments are performed in such a manner as to make the differences among plural kinds of the filament yarns <=12% in boiling-water shrinkage and <=8% in elongation. These filament yarns are put together without winding and then subjected to a running-liquid entanglement treatment to obtain the objective multicolor-dyeing combined filament yarn.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、染色性の異なる複数の
フィラメント糸が混繊された混繊糸に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a mixed yarn in which a plurality of filament yarns having different dyeability are mixed.

【0002】[0002]

【従来の技術】染色性の異なる複数の合成繊維フィラメ
ント糸からなる混繊糸は、これを編織した後染色を施す
と染色部分が不均一に現れ杢調の特異な外観が得られる
ため、従来より種々の提案が存在する。
2. Description of the Related Art A mixed fiber yarn composed of a plurality of synthetic fiber filament yarns having different dyeability has a conventional appearance because when dyed after weaving the dyed portion, the dyed portion appears unevenly and a peculiar appearance is obtained. There are more proposals.

【0003】例えば、特開昭59−204937号公報
には、ポリエチレンテレフタレートとカチオン染料可染
性ポリエステルとを延撚機で混繊し(延撚混繊)、前記
のような混繊糸を得ることが開示されている。また、特
開昭49−19166号公報には塩基性染料可染性ポリ
エステルと酸性染料可染性ポリエステルとを同一の紡糸
口金から紡糸して混繊し(紡糸混繊)、前記のような混
繊糸を得ることが開示されている。
For example, in JP-A-59-204937, polyethylene terephthalate and cationic dye dyeable polyester are mixed with a twisting machine (spreading twisted mixed fiber) to obtain the above-mentioned mixed yarn. It is disclosed. Further, in JP-A-49-19166, a basic dye-dyeable polyester and an acid dye-dyeable polyester are spun from the same spinneret and mixed (spinning mixed fiber). Obtaining a yarn is disclosed.

【0004】更に、特開昭3−279428号公報に
は、3000m/分以上の引き取り速度で溶融紡糸され
た沸水収縮率7〜12%のポリエステルフィラメント
と、沸水収縮率5%以下のポリエステルフィラメントと
を紡糸延伸後、一旦捲き取ることなく合糸し交絡処理を
施すことが開示されている。
Further, JP-A-3-279428 discloses a polyester filament having a boiling water shrinkage of 7 to 12% and a polyester filament having a boiling water shrinkage of 5% or less, which are melt-spun at a take-up speed of 3000 m / min or more. It is disclosed that after spinning and drawing, the yarns are combined and entangled without being once wound.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、前記の
如き従来技術には以下の如き問題点がある。すなはち、
紡糸混繊法は製造設備が固定されるため、多品種小ロッ
ト的な生産にはそぐわず、また各糸条の熱収縮率や伸度
等の物性を細かくコントロールすることが困難なため、
杢の微妙な調整を行うことができない。また、延撚混繊
法は混繊方法としては最も一般的で技術的にも確立され
た方法ではあるが、紡糸後に糸条を一旦パーンに捲き取
る際や延撚時にこれを解舒する際に若干の実撚が糸条に
付与されて各糸条が集束するため、十分に均一な混繊が
行えないという問題点があった。
However, the above-mentioned prior art has the following problems. Sunahachi,
Since the manufacturing equipment is fixed in the spinning mixed fiber method, it is not suitable for high-mix, small-lot production, and it is difficult to finely control the physical properties such as heat shrinkage and elongation of each yarn.
It is not possible to make fine adjustments to the heather. The twist-twisted mixed fiber method is the most general and technically established method as a mixed fiber method, but when the yarn is once wound into a pan after spinning or unwound during the twisting. However, since some actual twist is applied to the yarns and the yarns are bundled, there is a problem that the fibers cannot be mixed sufficiently uniformly.

【0006】更に、特開昭3−279428号公報に開
示された方法によれば、各糸条に実撚を付与することな
く混繊糸を得ることができるが、同公報に開示されたも
のは2種の糸条の熱収縮率差や伸度差が大きいため、得
られた混繊糸は芯鞘状の構造となって一方の糸条のみが
表面に現れ、特に染色性が著しく異なる異ポリマー糸を
混繊すると粗い杢が発生してしまうという欠点があっ
た。
Further, according to the method disclosed in Japanese Patent Laid-Open No. 3-279428, it is possible to obtain a mixed fiber yarn without imparting a real twist to each yarn. Has a large difference in heat shrinkage ratio and difference in elongation between the two types of yarns, and thus the obtained mixed fiber has a core-sheath structure, and only one yarn appears on the surface, and the dyeability is remarkably different. When mixed with different polymer yarns, there was a drawback that a coarse heat was generated.

【0007】このため、本出願人は先に提案をした特開
平1−221505号等の紡糸延伸装置を用いた異収縮
混繊糸の製造技術を鋭意研究し、該方法を改良して転用
することにより、極めて均一性に優れた混繊糸が得られ
ることを見出し、本発明に至ったのである。
[0007] Therefore, the applicant of the present invention diligently researched the manufacturing technology of the different shrinkage mixed fiber using the spin-drawing apparatus such as the previously proposed Japanese Patent Laid-Open No. 1-221505, and improved the method and diverted it. As a result, they have found that a mixed fiber having extremely excellent uniformity can be obtained, and have arrived at the present invention.

【0008】すなはち、本発明は前記の如き問題点を解
決するものであって、その目的は、染色性の異なる複数
のフィラメント糸を極めて均一に混繊することにより、
細かな杢を発生することのできる異染混繊糸を提供する
ことにある。
That is, the present invention solves the above-mentioned problems, and an object thereof is to mix a plurality of filament yarns having different dyeability very uniformly.
It is intended to provide a hetero-dyed mixed yarn capable of generating fine heather.

【0009】[0009]

【課題を解決するための手段】本発明は、染色性の異な
るポリマーからなる複数のフィラメント糸が流体交絡処
理されてなるマルチフィラメント糸において、該複数種
のフィラメント糸の沸水収縮率の差が12%以下、伸度
の差が8.0%以下であり、更に各フィラメント糸は実
質的に無撚であることを特徴とする異染混繊糸であり、
かかる異染混繊糸は、隣接する紡糸延伸装置に、互いに
染色性の異なるポリマーを供給して複数のフィラメント
糸を紡糸し、該複数のフィラメント糸の沸水収縮率の差
が12%以下、伸度の差が8.0%以下となるように延
伸、熱処理した後、一旦捲き取ることなく合糸し、次い
で流体交絡処理を施すことにより得られる。
DISCLOSURE OF THE INVENTION The present invention is a multifilament yarn obtained by subjecting a plurality of filament yarns made of polymers having different dyeing properties to a fluid entanglement treatment, wherein the difference in boiling water shrinkage between the plurality of types of filament yarns is 12. % Or less, the difference in elongation is 8.0% or less, and each filament yarn is a substantially non-twisted yarn.
Such hetero-dyed mixed fiber yarns are produced by supplying polymers having different dyeability to adjacent spinning and drawing devices to spin a plurality of filament yarns, and the difference in boiling water shrinkage of the plurality of filament yarns is 12% or less, It is obtained by stretching and heat-treating so that the difference in degree becomes 8.0% or less, then once tying without winding, and then performing fluid entanglement treatment.

【0010】本発明のフィラメント糸としては、繊維形
成性のポリマーであるポリエステル,ポリアミド,ポリ
オレフィン等を用いることができ、ポリエステルとして
は、ポリエチレンテレフタレート,ポリブチレンテレフ
タレート,ポリエチレンオキシベンゾエート,ポリジメ
チルシキロヘキサンテレフタレート,ポリピバロラクト
ン等のホモポリエステルや、これらのポリエステル成分
に第二酸成分として、イソフタル酸,スルホイソフタル
酸を共重合させたものや、第二アルコール成分としてポ
リピレングリコール,ポリエチレングリコールを共重合
させたもの等を用いることができる。
As the filament yarn of the present invention, a fiber-forming polymer such as polyester, polyamide, or polyolefin can be used. As the polyester, polyethylene terephthalate, polybutylene terephthalate, polyethyleneoxybenzoate, polydimethylcyclohexane can be used. Homopolyesters such as terephthalate and polypivalolactone, those obtained by copolymerizing these polyester components with isophthalic acid and sulfoisophthalic acid as secondary acid components, and polypyrene glycol and polyethylene glycol as secondary alcohol components. A polymerized product can be used.

【0011】また、ポリアミドとしては、ナイロン6,
ナイロン66,ナイロン610,ナイロン11,ナイロ
ン12,ビス(パラアミノシクロヘキシル)メタンとド
デカン二酸との縮合体や、これらのポリアミド形成成分
間で共重合させたものや、他のジカルボン酸やジアミン
を共重合させたもの等を用いることができ、ポリオレフ
ィンとしては、ポリエチレン,ポリプロピレン等のホモ
ポリオレフィンや、少量の第2成分を含むものを用いる
ことができる。
As the polyamide, nylon 6,
Nylon 66, Nylon 610, Nylon 11, Nylon 12, Condensates of bis (paraaminocyclohexyl) methane and dodecanedioic acid, those copolymerized between these polyamide forming components, and other dicarboxylic acids and diamines. A polymerized product or the like can be used, and as the polyolefin, a homopolyolefin such as polyethylene or polypropylene, or a product containing a small amount of the second component can be used.

【0012】また、染色性の異なるフィラメント糸の組
み合わせとしては、ポリエステルとポリアミドのように
異なった種類のものを組み合わせても良いが、后加工や
染色処理の容易性から同種のポリマーの共重合体で、染
色性が大きく異なる組み合わせを選ぶことが好ましく、
例えば、ポリエチレンテレフタレートとカチオン可染性
ポリエステルとの組み合わせ等を挙げることができる。
さて、本発明の混繊糸に特徴的なことは、第1に染色性
の異なるポリマーからなる複数のフィラメント糸の物性
が近似している点であり、第2に各フィラメント糸が実
撚によって集束し群を形成することがない状態で混繊さ
れている点にある。
Further, as a combination of filament yarns having different dyeability, different types such as polyester and polyamide may be combined, but a copolymer of the same type of polymer is preferable because of easy post-processing and dyeing treatment. Therefore, it is preferable to select a combination whose dyeing properties are significantly different,
For example, a combination of polyethylene terephthalate and a cationic dyeable polyester can be used.
What is characteristic of the mixed yarn of the present invention is that firstly, the physical properties of a plurality of filament yarns composed of polymers having different dyeability are similar to each other, and secondly, each filament yarn is formed by actual twisting. The point is that the fibers are mixed without being bundled and forming a group.

【0013】先ず、各フィラメント糸の物性について説
明する。本発明の混繊糸は、各フィラメント糸の熱収縮
率が極めて近似しており、所謂異収縮混繊糸とは異なる
ものである。例えば、カチオン可染性ポリエステルのよ
うな共重合ポリエステルの場合、ポリエチレンテレフタ
レートと同様の延伸条件や熱履歴、例えばポリエチレン
テレフタレートの場合沸水収縮率が6.0〜8.0%の
範囲となるような条件で製造を行うと、ポリエチレンテ
レフタレートとは1.5%以上の沸水収縮率差を生じて
しまう。本発明では、両糸の条件を夫々設定すること等
によって、沸水収縮率の差を1.2%以下、好ましくは
0.8%以下とする。また、本発明の混繊糸の沸水収縮
率は5〜10%とすることが好ましい。
First, the physical properties of each filament yarn will be described. In the mixed fiber of the present invention, the heat shrinkage rates of the respective filament yarns are very similar, and are different from so-called different shrinkage mixed fiber. For example, in the case of a copolyester such as a cationic dyeable polyester, the same stretching conditions and heat history as those of polyethylene terephthalate, for example, in the case of polyethylene terephthalate, the boiling water shrinkage is in the range of 6.0 to 8.0%. If the production is carried out under the conditions, a boiling water shrinkage ratio difference of 1.5% or more will occur with polyethylene terephthalate. In the present invention, the difference in boiling water shrinkage is set to 1.2% or less, preferably 0.8% or less by setting the conditions of both yarns, respectively. Further, the boiling water shrinkage of the mixed yarn of the present invention is preferably 5 to 10%.

【0014】更に、本発明の混繊糸は各フィラメント糸
の伸度の差も8.0%以下、好ましくは4.0%以下と
なっており、製品となった際、糸長差によって芯鞘形状
等の一方の糸条だけが表面に現れる構造を呈することの
ないものである。また、各フィラメント糸の総繊度は2
0〜200デニール程度で、各フィラメント糸間の繊度
差は混繊糸の総繊度の1/3以下であることが好まし
い。
Further, in the mixed fiber of the present invention, the difference in the elongation of each filament yarn is 8.0% or less, preferably 4.0% or less. It does not have a structure in which only one yarn such as a sheath shape appears on the surface. The total fineness of each filament yarn is 2
About 0 to 200 denier, the difference in fineness between the filament yarns is preferably 1/3 or less of the total fineness of the mixed yarns.

【0015】次に、各フィラメント糸の集束性について
説明する。本発明の混繊糸は、各フィラメント糸が実質
的に集束することなく混繊されているものである。これ
は、具体的には各フィラメント糸が実質的に実撚を有し
ないことを意味する。実撚が付与されると、各フィラメ
ント糸は長手方向に沿って連続的に集束せしめられ、こ
のような糸条同志に交絡処理を施してももはや十分に均
一な混繊を行うことはできない。また、かかる実撚の撚
数としては、延伸装置においてパーンを捲き取る際のス
ピンドルの回転により付与されるものや、該パーンを解
舒する際に付与される解舒撚り等の5T/M程度以上の
ものを指す。
Next, the converging property of each filament yarn will be described. The mixed fiber of the present invention is one in which each filament yarn is mixed without being substantially bundled. This specifically means that each filament yarn has substantially no real twist. When the real twist is applied, the filament yarns are continuously bundled along the longitudinal direction, and even if the filament yarns are entangled, it is no longer possible to sufficiently uniformly mix them. Further, the number of twists of the actual twist is about 5 T / M such as that imparted by rotation of the spindle when winding up the pan in the stretching device, or untwisted twist imparted when unwinding the pan. Refers to the above.

【0016】以下、本発明の混繊糸を製造する方法につ
いて説明する。本発明方法で用いる紡糸延伸装置は、所
謂スピンドロー(紡糸直接延伸)装置と呼ばれるもの
で、例えば特開平1−221505号公報等に記載され
たものを用いることができる。
The method for producing the mixed yarn of the present invention will be described below. The spinning / drawing apparatus used in the method of the present invention is a so-called spin draw (spin direct drawing) apparatus, and for example, those described in JP-A-1-221505 can be used.

【0017】図1はかかる紡糸延伸装置の概略を示す説
明図である。同図に示す如く、通常の紡糸延伸装置では
複数の紡糸系列(錘)が併設されており、本発明方法で
はかかる2錘を1組として用いる。同図の場合、Sは紡
糸部、Dは延伸部を示し、ペレット貯蔵槽1a,1bに
貯蔵された各フィラメント糸の原料ポリマーは、溶融押
出機2a,2bにより溶融されてギヤポンプ3a,3b
により紡糸口金4a,4bより夫々溶融紡糸され、冷却
装置5a,5bによって冷却個化される。
FIG. 1 is an explanatory view showing the outline of such a spinning and drawing apparatus. As shown in the figure, in a normal spinning and drawing apparatus, a plurality of spinning series (weights) are provided side by side, and in the method of the present invention, two such weights are used as one set. In the figure, S is a spinning section, D is a drawing section, and the raw material polymer of each filament yarn stored in the pellet storage tanks 1a and 1b is melted by the melt extruders 2a and 2b to be gear pumps 3a and 3b.
Are melt-spun from the spinnerets 4a and 4b, respectively, and are individually cooled by the cooling devices 5a and 5b.

【0018】次いで、紡糸冷却された糸条は、第1ゴデ
ットローラ6a,6bに引き取られ、第2ゴデットロー
ラ7a,7bとの間で所定の延伸が施される。延伸され
た2つの糸条は右部紡糸系列の第2ゴデットローラ7a
上で合糸され流体交絡ノズル8によって混繊交絡処理さ
れた後、パッケージ9に巻き取られる。
Next, the spun-cooled yarn is taken up by the first godet rollers 6a, 6b and subjected to a predetermined drawing with the second godet rollers 7a, 7b. The two drawn yarns are the second godet roller 7a of the right spinning system.
After the above yarns are combined and mixed and entangled by the fluid entanglement nozzle 8, they are wound into a package 9.

【0019】本発明方法では、前記ペレット貯蔵槽1
a,1bに染色性の異なる原料ポリマーチップ例えば、
右部紡糸系列のペレット貯蔵槽1aにポリエチレンテレ
フタレートチップを、左部紡糸系列のペレット貯蔵槽1
bにカチオン可染性ポリエステルチップを夫々投入す
る。
In the method of the present invention, the pellet storage tank 1 is used.
Raw material polymer chips with different dyeability to a and 1b, for example,
A polyethylene terephthalate chip is placed in the pellet storage tank 1a of the right spinning system, and a pellet storage tank 1 of the left spinning system 1a.
Cationic dyeable polyester chips are put into b.

【0020】そして、紡糸糸条を第1ゴデットローラ6
a,6bにより引き取るとともに、第2ゴデットローラ
7a,7bとの間で延伸がなされるが、かかる条件は例
えば、ポリエチレンテレフタレートとカチオン可染性ポ
リエステルの場合、ポリエチレンテレフタレートの系列
は第1ゴデットローラ6aの速度を、1000〜140
0m/min程度、表面温度を80〜100℃程度、第
2ゴデットローラ6bの速度を、3000〜4500m
/min程度、表面温度を135〜155℃程度とする
ことが好ましく、かかる条件によれば沸水収縮率が7%
前後の延伸糸を得ることができる。また、カチオン可染
性ポリエステルの系列は第1ゴデットローラ6aの速度
を、1200〜1800m/min程度、表面温度を8
0〜100℃程度、第2ゴデットローラ6bの速度を、
3000〜4500m/min程度、表面温度を120
〜140℃程度とすることにより、前記ポリエチレンテ
レフタレート糸と同程度の熱収縮率、伸度を有した糸条
を得ることができる。さらに、流体交絡処理は、糸条の
走行速度を3700m/min程度とした場合、2.0
〜5.0kg/cm3 程度の圧力にて15〜60個/m
の交絡数(フック法)となるように行うことが好まし
い。
Then, the spun yarn is attached to the first godet roller 6
a and 6b, and stretching is performed between the second godet rollers 7a and 7b. For example, in the case of polyethylene terephthalate and cationic dyeable polyester, the polyethylene terephthalate series is the speed of the first godet roller 6a. 1000-140
0 m / min, the surface temperature is 80 to 100 ° C., the speed of the second godet roller 6 b is 3000 to 4500 m.
/ Min, the surface temperature is preferably about 135 to 155 ° C., and under these conditions, the boiling water shrinkage is 7%.
Front and back drawn yarns can be obtained. Further, the cationic dyeable polyester series has a speed of the first godet roller 6a of about 1200 to 1800 m / min and a surface temperature of 8 mm.
0 ~ 100 ℃, the speed of the second godet roller 6b,
3000-4500 m / min, surface temperature 120
By setting the temperature to about 140 ° C., it is possible to obtain a yarn having the same heat shrinkage and elongation as the polyethylene terephthalate yarn. Further, the fluid entanglement treatment is 2.0 when the traveling speed of the yarn is about 3700 m / min.
15 to 60 pieces / m at a pressure of about 5.0 kg / cm 3
It is preferable to carry out so that the number of entanglements (hook method) becomes.

【0021】以上の如く得られた混繊糸は、これを必要
に応じて追撚したり、他の糸条と交撚したりして用い、
一方のフィラメント糸のみを染色したり、夫々のフィラ
メント糸を異色に染めたりすることによって、杢調の外
観を得ることができる。
The mixed filament yarn obtained as described above is used by further twisting it as necessary or by twisting it with other yarns,
A heathered appearance can be obtained by dyeing only one filament yarn or dyeing each filament yarn in a different color.

【0022】[0022]

【実施例】【Example】

(実施例1)固有粘度(η)0.635のポリエチレン
テレフタレートチップと、ポリエチレンテレフタレート
にスルホイソフタル酸を2.5モル%共重合したカチオ
ン可染性ポリエステルチップを用意し、図1に示す紡糸
延伸装置のチップ貯蔵槽に投入し、以下の条件で150
d/48fの異染混繊糸を得た。
(Example 1) A polyethylene terephthalate chip having an intrinsic viscosity (η) of 0.635 and a cationic dyeable polyester chip obtained by copolymerizing polyethylene terephthalate with 2.5 mol% of sulfoisophthalic acid were prepared, and the spinning drawing shown in Fig. 1 was performed. Put it in the chip storage tank of the device and
A dyed mixed yarn of d / 48f was obtained.

【0023】〔ポリエチレンテレフタレート〕 繊度 75d/24f 溶融温度 287℃ 第1ゴデットローラ 表面速度 1150m/min 表面温度 90℃ 第2ゴデットローラ 表面速度 3750m/min 表面温度 130℃[Polyethylene terephthalate] Fineness 75d / 24f Melting temperature 287 ° C. First godet roller surface speed 1150 m / min Surface temperature 90 ° C. Second godet roller surface speed 3750 m / min Surface temperature 130 ° C.

【0024】〔カチオン可染性ポリエステル〕 繊度 75d/24f 溶融温度 287℃ 第1ゴデットローラ 表面速度 1500m/min 表面温度 87℃ 第2ゴデットローラ 表面速度 3750m/min 表面温度 146℃ 交絡処理 30個/m 各フィラメント糸の物性値を表1に示す。[Cationic dyeable polyester] Fineness 75d / 24f Melting temperature 287 ° C First godet roller surface speed 1500m / min Surface temperature 87 ° C Second godet roller surface speed 3750m / min Surface temperature 146 ° C Entanglement treatment 30 pieces / m Each filament The physical properties of the yarn are shown in Table 1.

【0025】[0025]

【表1】 [Table 1]

【0026】次いで、かかる混繊糸に300T/Mの追
撚を施した後、これを経緯糸に用いて平織物を製織し、
カチオン染料により灰色に染色したところ、均一で微細
な杢の見られる外観となった。
Next, after 300 T / M additional twisting is applied to the mixed yarn, the plain weave is woven using this as the warp and weft,
When it was dyed gray with a cationic dye, it had an appearance of uniform and fine heather.

【0027】[0027]

【発明の効果】本発明によれば、従来の異染混繊糸では
得られなかった細かな杢調の外観を有した繊維製品を得
ることができる。また、本発明方法は、かかる異染混繊
糸を極めて効率良く製造することが可能であって、その
有用性は明らかである。
EFFECTS OF THE INVENTION According to the present invention, it is possible to obtain a fiber product having a fine heathered appearance which cannot be obtained by the conventional hetero-dyed mixed yarn. Further, the method of the present invention can produce such a heterochromatic dyed yarn extremely efficiently, and its usefulness is clear.

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

【図1】本発明方法で用いる紡糸延伸装置の概略を示す
説明図である。
FIG. 1 is an explanatory view showing an outline of a spinning / drawing apparatus used in the method of the present invention.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 染色性の異なるポリマーからなる複数の
フィラメント糸が流体交絡処理されてなるマルチフィラ
メント糸において、該複数種のフィラメント糸の沸水収
縮率の差が1.2%以下、伸度の差が8.0%以下であ
り、更に各フィラメント糸は実質的に無撚であることを
特徴とする異染混繊糸。
1. A multifilament yarn obtained by subjecting a plurality of filament yarns made of polymers having different dyeing properties to a fluid entanglement treatment, wherein the difference in boiling water shrinkage between the plurality of filament yarns is 1.2% or less, and the elongation The heterochromatic dyed yarn, wherein the difference is 8.0% or less, and each filament yarn is substantially untwisted.
【請求項2】 隣接する紡糸延伸装置に、互いに染色性
の異なるポリマーを供給して複数のフィラメント糸を紡
糸し、該複数のフィラメント糸の沸水収縮率の差が1.
2%以下、伸度の差が8.0%以下となるように延伸、
熱処理した後、一旦捲き取ることなく合糸し、次いで流
体交絡処理を施すことを特徴とする異染混繊糸の製造方
法。
2. A plurality of filament yarns are spun by supplying polymers having different dyeability to adjacent spinning and drawing devices, and the difference in boiling water shrinkage ratio between the plurality of filament yarns is 1.
2% or less, stretched so that the difference in elongation is 8.0% or less,
A method for producing a hetero-dyed mixed fiber, which comprises heat-treating, then winding the yarn without winding it, and then subjecting it to a fluid entanglement treatment.
JP5346616A 1993-12-22 1993-12-22 Cross-dyed mixed yarn and method for producing the same Expired - Fee Related JP2731345B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5346616A JP2731345B2 (en) 1993-12-22 1993-12-22 Cross-dyed mixed yarn and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5346616A JP2731345B2 (en) 1993-12-22 1993-12-22 Cross-dyed mixed yarn and method for producing the same

Publications (2)

Publication Number Publication Date
JPH07189058A true JPH07189058A (en) 1995-07-25
JP2731345B2 JP2731345B2 (en) 1998-03-25

Family

ID=18384646

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5346616A Expired - Fee Related JP2731345B2 (en) 1993-12-22 1993-12-22 Cross-dyed mixed yarn and method for producing the same

Country Status (1)

Country Link
JP (1) JP2731345B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003074769A1 (en) * 2002-03-01 2003-09-12 Invista Technologies S.À.R.L. Methods for manufacture of mixed polyamide yarns
GB2372512B (en) * 2001-02-27 2004-10-27 Du Pont Methods for the manufacture of mixed polyamide yarns
JP2013537264A (en) * 2010-09-17 2013-09-30 コーロン インダストリーズ インク Mixed fiber and method for producing the same

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03279428A (en) * 1990-03-26 1991-12-10 Teijin Ltd Combined polyester filament yarn
JPH04352835A (en) * 1991-05-23 1992-12-07 Kuraray Co Ltd Specific combined filament yarn of polyester

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03279428A (en) * 1990-03-26 1991-12-10 Teijin Ltd Combined polyester filament yarn
JPH04352835A (en) * 1991-05-23 1992-12-07 Kuraray Co Ltd Specific combined filament yarn of polyester

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2372512B (en) * 2001-02-27 2004-10-27 Du Pont Methods for the manufacture of mixed polyamide yarns
WO2003074769A1 (en) * 2002-03-01 2003-09-12 Invista Technologies S.À.R.L. Methods for manufacture of mixed polyamide yarns
US7585440B2 (en) 2002-03-01 2009-09-08 Invista North America S.A R. L. Methods for the manufacture of mixed polyamide yarns
JP2013537264A (en) * 2010-09-17 2013-09-30 コーロン インダストリーズ インク Mixed fiber and method for producing the same
JP2016006248A (en) * 2010-09-17 2016-01-14 コーロン インダストリーズ インク Mixed fiber and method for producing the same

Also Published As

Publication number Publication date
JP2731345B2 (en) 1998-03-25

Similar Documents

Publication Publication Date Title
EP3011086B1 (en) Process for the preparation of a fiber, a fiber and a yarn made from such a fiber
EP0207489A2 (en) Highly-shrinkable polyester fiber, process for preparation thereof, blended polyester yarn and process for preparation thereof
JP3269874B2 (en) Method for producing modified cross-section composite fiber and spinneret
JP2760990B2 (en) Manufacturing method of different shrinkage mixed fiber
JP2731345B2 (en) Cross-dyed mixed yarn and method for producing the same
US4359557A (en) Process for producing low pilling textile fiber and product of the process
CA1242557A (en) Process and apparatus for cospinning synthetic filament yarns consisting of two component yarns spun from identical or different polymers
US6503622B1 (en) Texturized, combined polyester multifilament yarn and process for producing same
JP3020838B2 (en) Manufacturing method of hetero-dyed mixed yarn
JPH07243144A (en) Method for producing polyester combined filament yarn
JPS6163768A (en) Production of cloth having silk spun like feeling
JP3103023B2 (en) Method for producing composite sewing thread
JPH0335412B2 (en)
JPH0959838A (en) Spun yarn
JP2591715B2 (en) Method for producing different shrinkage blended polyester yarn
KR102219084B1 (en) Interlace composite yarn with high strength and elongation and method for producing the same
JP2609009B2 (en) Method for producing polyester ultrafine fiber
JP2009138284A (en) Interlaced textured yarn
JPS6245326B2 (en)
JPH1136138A (en) Production of combined polyester filament yarn having different shrinkage
JP3418265B2 (en) Method for producing cation-mix-like fine fiber
JP3346575B2 (en) Manufacturing method of high filament count fine filament polyester yarn
JPH0735606B2 (en) Method for manufacturing polyester thermal shrinkage difference mixed yarn
JPH0327140A (en) Mixed yarn having different fineness and shrinkage
JP3469076B2 (en) Slab-like polyester mixed fiber yarn having different shades and shades and method for producing the same

Legal Events

Date Code Title Description
S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313113

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20081219

Year of fee payment: 11

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091219

Year of fee payment: 12

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091219

Year of fee payment: 12

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101219

Year of fee payment: 13

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101219

Year of fee payment: 13

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111219

Year of fee payment: 14

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121219

Year of fee payment: 15

LAPS Cancellation because of no payment of annual fees