JPH04209824A - Dyeable polyolefinic fiber and its production - Google Patents

Dyeable polyolefinic fiber and its production

Info

Publication number
JPH04209824A
JPH04209824A JP40725390A JP40725390A JPH04209824A JP H04209824 A JPH04209824 A JP H04209824A JP 40725390 A JP40725390 A JP 40725390A JP 40725390 A JP40725390 A JP 40725390A JP H04209824 A JPH04209824 A JP H04209824A
Authority
JP
Japan
Prior art keywords
polyolefin
dyeable
fiber
polymer
fibers
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP40725390A
Other languages
Japanese (ja)
Inventor
Osamu Maedo
前戸 修
Yosuke Takai
庸輔 高井
Takanori Akashi
明石 貴法
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.)
Daiwabo Create Co Ltd
Original Assignee
Daiwabo Create Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Daiwabo Create Co Ltd filed Critical Daiwabo Create Co Ltd
Priority to JP40725390A priority Critical patent/JPH04209824A/en
Publication of JPH04209824A publication Critical patent/JPH04209824A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide the subject fiber capable of being dyed with disperse dyes, etc., and having excellent water repellency and non-moisture-absorbing property by preliminarily kneading a dyeable polymer with a compatibilizing agent in a melted state, adding a polyolefin to the kneaded product in the melted state, and subsequently melt-spinning the melted mixture. CONSTITUTION:A dyeable polymer such as a polyester or polyamide is preliminarily mixed with a compatibilizing agent in a melted state, mixed with a polyolefin in the melted state, and subsequently melt-spun to provide the subject fiber comprising a polyolefinic polymer alloy containing the polyolefin as a sea component and the dyeable polymer having an average diameter of <1mum in the cross section of the fiber as an island component.

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、分散染料などの染料で
よく染色でき、撥水性、非吸湿性に優れたポリオレフィ
ン系ポリマーアロイ繊維及びその製造方法に関する。 [0002]
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a polyolefin polymer alloy fiber that can be easily dyed with dyes such as disperse dyes and has excellent water repellency and non-hygroscopicity, and a method for producing the same. [0002]

【従来の技術】ポリオレフィン系繊維は、撥水性、非吸
湿性に優れ、低比重で低熱伝導性のため軽くて暖かく、
主鎖が炭素と水素のみで構成されているため、耐酸、耐
アルカリ性などの耐薬品性に優れているなど、他の繊維
にはない種々の特長を有する。しかし、官能基を持たぬ
ため染色できず、とくに衣料用繊維の用途が制限される
ので、過去長年にわたり染色性の改善が試みられてきた
。たとえば特公昭63−51453号公報および特公平
2−42948号公報に見られる可染性成分としてエチ
レン−アミノアルキルアクリレート共重合体を練り込ん
だ可染性ポリオレフィン繊維、特開昭64−85365
号公報に見られる前記繊維にアルキルホスフェイト環系
界面活性剤を塗布して染色性を改良した繊維、および芯
成分にポリエステルあるいはポリアミドの様な可染性熱
可塑性樹脂、鞘成分にポリオレフィンを用いた硝芯型複
合繊維の芯成分を染色して可染性を付与した可染性ポノ
フォレフィン繊維がある。 [0003]
[Prior Art] Polyolefin fibers have excellent water repellency and non-hygroscopicity, and have low specific gravity and low thermal conductivity, making them lightweight and warm.
Since the main chain is composed only of carbon and hydrogen, it has various features not found in other fibers, such as excellent chemical resistance such as acid resistance and alkali resistance. However, since it does not have a functional group, it cannot be dyed, which limits its use, especially as clothing fibers, so attempts have been made over the past many years to improve its dyeability. For example, dyeable polyolefin fibers kneaded with ethylene-aminoalkyl acrylate copolymer as a dyeable component are found in Japanese Patent Publication No. 63-51453 and Japanese Patent Publication No. 2-42948; Japanese Patent Publication No. 64-85365;
The fibers shown in the above publication are coated with an alkyl phosphate cyclic surfactant to improve dyeability, and the core component is a dyeable thermoplastic resin such as polyester or polyamide, and the sheath component is a polyolefin. There is dyeable ponopholefin fiber, which is made by dyeing the core component of a glass-core composite fiber. [0003]

【発明が解決しようとする課題】しかしながら前記した
従来技術は、染色性はいまだ十分ではなく、また洗濯あ
るいは摩擦など物理的な力が繊維にかかる場合、芯鞘間
の剥離を生じやすく、剥離部分で光の散乱を生じ物理的
圧迫を受けた織編物の部分の色が薄くなり、一般に「チ
ョークマーク」と呼ぶ現象を生じるため均一に染色して
も染色品に色の濃淡を生じるという課題があった。また
エチレン−アミノアルキルアクリレート共重合体を練り
込んだ可染性ポリオレフィン繊維は、金属石ケシなどの
分散剤を使用するためこれを用いた繊維は撥水性などの
ポリオレフィンの特徴が減殺されてしまうという課題が
あった。 [00041本発明は前記従来技術の課題を解決するた
め、ポリオレフィン系繊維の特性を生かしたまま、染色
性を改善した可染性ポリオレフィン繊維及びその製造方
法を提供することを目的とする。 [0005]
[Problems to be Solved by the Invention] However, the above-mentioned conventional technology still does not have sufficient dyeability, and when physical force such as washing or friction is applied to the fiber, peeling between the core and sheath easily occurs, and the peeled part This causes light scattering and the color of parts of woven or knitted fabrics that are subjected to physical pressure becomes lighter, resulting in a phenomenon commonly referred to as ``chalk marks.'' This creates the problem of color shading in dyed products even when dyed uniformly. there were. In addition, dyeable polyolefin fibers kneaded with ethylene-aminoalkyl acrylate copolymer use dispersants such as metal soap, so fibers using this will lose the characteristics of polyolefins such as water repellency. There was an issue. [00041] In order to solve the problems of the prior art, it is an object of the present invention to provide a dyeable polyolefin fiber with improved dyeability while taking advantage of the characteristics of polyolefin fibers, and a method for producing the same. [0005]

【課題を解決するための手段】前記目的を達成するため
、本発明の可染性ポリオレフィン繊維は、ポリオレフィ
ンを海成分とする繊維であって、前記繊維断面における
平均直径が1μm未満の可染性ポリマを島成分として含
むポリオレフィン系ポリマーアロイからなることを特徴
とする。 [0006]前記構成においては、可染性ポリマの存在
量が5〜55重量%であることが好ましい。 [0007]また前記構成においては、可染性ポリマが
ポリアミド及び/またはポリエステル、及びこれらの共
重合体から選ばれる少なくとも一種のポリマであること
が好ましい。 [0008]さらに本発明の可染性ポリオレフィン繊維
の製造方法は、ポリオレフィンを海成分とし、繊維断面
における直径が1μm未満の可染性ポリマを島成分とし
て含むポリオレフィン系ポリマーアロイ繊維を製造する
方法であって、可染性ポリマと相溶化剤を溶融状態であ
らかじめ混練し、次いでポリオレフィン系ポリマを溶融
状態で混合し、しかる後溶融紡糸することを特徴とする
。 [00091
[Means for Solving the Problems] In order to achieve the above object, the dyeable polyolefin fiber of the present invention is a fiber containing polyolefin as a sea component, and has a dyeable polyolefin fiber having an average diameter of less than 1 μm in the fiber cross section. It is characterized by being made of a polyolefin polymer alloy containing a polymer as an island component. [0006] In the above configuration, it is preferable that the amount of the dyeable polymer present is 5 to 55% by weight. [0007] Furthermore, in the above configuration, it is preferable that the dyeable polymer is at least one type of polymer selected from polyamide and/or polyester, and copolymers thereof. [0008] Furthermore, the method for producing dyeable polyolefin fibers of the present invention is a method for producing polyolefin-based polymer alloy fibers containing polyolefin as a sea component and dyeable polymers having a diameter of less than 1 μm in the fiber cross section as an island component. It is characterized in that the dyeable polymer and the compatibilizer are kneaded in advance in a molten state, then the polyolefin polymer is mixed in a molten state, and then melt-spun. [00091

【作用]前記した本発明の構成によれば、ポリオレフィ
ンを海成分とする繊維であり、また繊維断面における(
すなわち繊維断面方向から見て)平均直径が1μm未満
の可染性ポリマを島成分として含むポリマーアロイであ
るから、ポリオレフィン系繊維の特性を生かしたまま、
染色性を改善した可染性ポリオレフィン繊維とすること
ができる。 [00103前記、可染性ポリマの存在量が5〜55重
量%であるという本発明の好ましい構成によれば、ポリ
オレフィン系繊維の特性を生かしたまま染色性を改善で
きるという点においてさらに優れたものとすることがで
きる。 [0011]また前記、可染性ポリマがポリアミド及び
/またはポリエステル、及びこれらの共重合体から選ば
れる少なくとも一種のポリマであるという本発明の好ま
しい構成によれば、通常の染色条件を用いて分散染料な
どで染色できる。 [0012]さらに前記した本発明方法によれば、可染
性ポリマと相溶化剤を溶融状態であらかじめ混練し、次
いでポリオレフィン系ポリマを溶融状態で混合し、しか
る後溶融紡糸するので、ポリオレフィン系繊維中に可染
性ポリマを微分散させることができる。 [0013] 【実施例】以下実施例を用いて本発明をさらに具体的に
説明する。なお本発明は以下の実施例によって限定され
るものではない。 [0014]本発明者らは、疎水性のポリオレフィンを
海成分とし、可染成分のポリアミドまたはポリエステル
を島成分とするポリマーアロイを用い、空気中に押し出
す溶融紡糸法によって繊維を形成すると、繊維表面がほ
とんど海成分のポリオレフィンで占められることを見い
出だした。このようにして得た繊維は、撥水性などポリ
オレフィン繊維の特徴が失われず、かつ分散染料を用い
て高圧染色すると良好に深色染色でき、島成分の繊維断
面における直径が1μm未満のポリマーアロイは、防糸
性および延伸性が通常のポリオレフィン繊維に劣らない
ことを見い出し本発明に至った。 [0015]本発明の島成分として用いる可染性ポリマ
は、薬の細長いカプセルに類似した形となっており、繊
維断面における直径が1μm未満であること、すなわち
1個の島成分の容積がおおむね10μm3未満であるこ
とが好ましく、平均値として1μm以下であっても3μ
mを越える島成分が存在すると繊維成形性が劣るため好
ましくない。用いる島成分には、熱可塑性のナイロン6
、ナイロン66、ナイロン12などのポリアミド類およ
びポリエチレンテレフタレート、ポリブチレンテレフタ
レートなどのポリエステル類のホモポリマー、共重合体
、およびこれらの変性体が都合良く、この他にポリカー
ボネートなど可染性の熱可塑性樹脂を用いることができ
る。前記において、たとえばポリエチレンテレフタレー
トを用いたときは分散染料可染性繊維とすることができ
る。またたとえばポリエチレンテレフタレートに2゜4
〜10モル%の5−ナトリウムスルホイソフタル酸成分
ユニットを共玉合すれば、塩基性可染タイプの繊維とす
ることができ、とくに2.4〜4.0モル%程度の共重
合体であれば加圧可染型、5〜10モル%程度の共重合
体であれば常圧可染型とすることができる。 [0016]前記可染性ポリマは、融点が100〜28
0℃の範囲のものがポリマーアロイの加工上好ましい。 融点が280℃を超えると繊維成形温度を300℃以上
としなければならず、この場合ポリオレフィン中の安定
剤の熱劣化が大きくなる。また融点が100℃以下では
、繊維成形加工が困難で好ましくない。 [00171本発明において使用する海成分のポリオレ
フィンは、たとえばポリプロピレン、ポリエチレン、ポ
リブテン−1、ポリメチルテンなどの融点が100℃以
上のαポリオレフィンのホモポリマー、コーポリマーお
よびその変形体が都合よく、繊維成形上ポリプロピレン
がとくに好ましい。 [0018]また島成分を微分散させる都合上相溶化剤
を用いる。相溶化剤としては、たとえばエチレン−アク
リル酸またはその誘導体の共重合体を用いる。より具体
的には下記のものがある。 (1)アクリル酸メチルが15〜35wt%のエチレン
−メチルアクリレート共重合体(EMA)。 (2)アクリル酸エチルが15〜35wt%のエチレン
−エチルアクリレート共重合体(EMA)。 (3)アクリル酸5〜15wt%、アクリル酸メチルが
5〜15wt%で、エチレンが85〜65wt%のエチ
レン−アクリル酸−アクリル酸メチルの三元共重合体。 (4)メタアクリル酸が10〜20wt%のエチレン−
メタアクリル酸共重合体(EMAA)のカルボン酸のう
ち15〜50モル%が亜鉛もしくはアルカリ金属塩とな
っているアイオノマー。 (5)メタアクリル酸とアクリル酸が合計で10〜20
wt%のエチレン−メタアクリル酸−アクリル酸共重合
体のアイオノマー。 [0019]そのほか、共押し出し多層フィルムの接着
層に用いている°°アトマー°゛(三片石油化学社製)
、゛モディック°° (三菱油化社製)なども使用でき
る。なお、アクリル酸系もしくはメタクリル酸系のエチ
レン共重合体においては、側鎖のカルボン酸がエステル
またはアイオノマータイプの塩の状態である方が耐熱性
の点で好ましい。 [00201なお、海成分と島成分の比は染色性の点で
少なくとも島成分を5wt%以上、好ましくは10〜4
0wt%添加するのがよく、55wt%を超えると海鳥
成分の逆転が生じやすく好ましくない。 [00211本発明に用いる可染性ポリオレフィン繊維
の紡糸温度(T’C)は海成分のポリオレフィンの融点
をTs℃、島成分の融点を11℃とするとTs+10≦
T〈360が可能で、Ts <T+ の組み合わせのポ
リマーアロイを用いTI +5≦T≦320の範囲を採
ることがさらに好ましい。紡糸温度が360℃を超える
と海成分のポリオレフィンの分解が生じ好ましくなく、
ポリオレフィン中の各種安定剤の耐熱性を考慮すると3
20℃以下がより好ましい。用いるポリマーアロイの溶
融粘度は、紡糸温度を測定温度とするJISK7210
 (加重2169 g)に準じて測定したメルトフロー
レート(MFR;g/10分)で10≦MF R<30
0が都合よく、2〜0.5デニールの細繊度では30〜
100g/10分、30〜15デニールの太繊度では1
0〜30g/10分が特に好ましく、さらに太繊度では
10g/10分前後が好ましい。MFR>300では、
流動性過多で繊維成形が失われるため紡糸温度を低くし
繊維成形するのが好ましい。 [002233本発明紡績糸は一般に0. 5〜4デニ
ルの上記繊維を用いて通常のポリプロピレン繊維と全く
同様にして得られ、通常のポリプロピレン繊維と紡績性
は変わらない。また本発明の紡績糸は通常のポリプロピ
レン紡績糸と変わらない織編機への適用性を持っている
ため織編物にする上で問題はない。染色した場合本発明
の繊維が20%未満であると染むらが目立ち好ましくな
い。本発明に用いる繊維がマルチフィラメントの形であ
っても同様である。 [00231本発明のポリオレフィン系ポリマーアロイ
からなるポリオレフィン繊維は、繊維中に微細に分散し
ている島成分が、分散染料を用いた高圧染色法によって
容易に染色され、かつ繊維表面が海成分のポリオレフィ
ンによって占められているため良好な撥水性を示し、摩
擦堅牢度等の繊維物性も良好である。また、島成分が繊
維断面において1μm未満という微細径のため、従来の
鞘芯複合繊維の芯径に比らべ格段に細く、物理的外因に
よる海島成分間の剥離が生じにくいため(たとえばフィ
ブリル化など)、本発明の可染性ポリオレフィン繊維を
紡績糸、その織編物およびマルチフィラメントの織編物
としても、チョークマークを生ぜず、均一な深染品を提
供することができる。 [0024]以下具体的実験例を説明する。 [0025]実施例1〜7、比較例1〜2数平均分子量
18000、融点220℃のナイロン−6を100重量
部と、エチレンアクリル酸エステル共重合体系相溶化剤
10重量部を280℃二軸押出機で混練後、ナイロン−
6が30wt%、20wt%、10wt%、0wt%に
なるように230℃のMFRが8g/10分、融点16
2℃のポリプロピレンパウダー(直径1.5mm、長さ
4〜5mm)を添加しながら再度二軸押出機で混合し、
ポリマーアロイとした。このポリマーアロイを、紡糸口
金孔数400の紡糸口金を用い、吐出量125g/分、
紡糸温度285℃で溶融紡糸して、4.5デニール(d
)および43dの未延伸糸とし、95℃熱水中で3.5
倍に延伸し、スタッファボックスで機械捲縮を付与した
後、120℃のネットコンベアー式乾燥機で乾燥し51
mmに切断し1.5dおよび15dのステープルとした
。得られたステープルの繊維断面をギ酸で抽出して走査
型電子顕微鏡を用い高径を測定した。 (0026]また、得られたステープルをパラレル型ロ
ーラーカードフラットカードでウェブとした後、ニード
ルパンチングマシーンで60g/m2、のフェルトとな
して、カヤロンポリエステルBR−3(染料)1g/リ
ットル、テキサトンTH3−100(分散剤)0.3g
/リットル、および硫酸アンモニウム(緩衝剤)200
g/リットルと酢酸3.3ml/リットルのpH調整液
10m1/リツトルからなる染液中に浸漬し130℃で
30分高圧染色し、ソーダ灰2g/リットルおよびハイ
ドロサルファ482g/リットルを含む80℃浴中で5
分間処理した後、水洗乾燥して染色したニット地または
紡績糸を得、JISZ8721標準色票で評価した。 [0027]また上記の染色したフェルトの撥水性をフ
ェルト上30cmの位置から蒸留水を滴下し、フェルト
表面に水球として残存する(○印とする)か否か(×印
とする)で判定した。結果を表1に示す。なお表1にお
いて、可紡性は12dの未延伸糸が引き取れない場合を
×としく但しその場合は手で未延伸糸を引き取り断面を
観察)、それぞれの未延伸糸が引き取れた場合を○とし
た。また染色性と撥水性はフェルトで評価した。 [0028] 実施例8 実施例3の繊維から作られたフェルトを実施例3と同様
にしてスミカロンS−2RL、S−3RF、5E−3G
L、5−BDFおよび5−BGを用いて染色した。この
結果、実施例3と同様の深色に染色できた。 [0029]実施例9 [η]0.63(ただし[η]は稀薄溶液粘度であり、
平均分子量を示す一つの尺度である。)、融点260℃
のポリエチレンテレフタレート20wt%を島成分と、
実施例1のポリプロピレンを海成分として、実施例1と
同様にポリマーアロイを製造した。このポリマーアロイ
を紡糸口金孔数100の紡糸口金を用い、吐出量125
g/分、紡糸温度290℃で溶融紡糸して43dの未延
伸糸とし、95℃熱水中で2.8倍に延伸して、実施例
1と同様にして19dのステープルとした。 [00301得られた繊維を実施例1と同様に染色した
ところ、実施例1と同様の深色に染色できた。 [00311実施例10〜13 比較例3〜4数平均分
子量18000、融点220℃のナイロン6を100重
鳳部とエチレンアクリル酸エステル共重合体系相溶化剤
10重量部を温度280℃で二軸押出機を用いて混線後
、ナイロン−6が30wt%、20wt%、10wt%
、0wt%になる様に、230℃MFRが8g/10分
、融点162℃のポリプロピレンパウダーを添加しなが
ら再度二軸押出機で混合し、ポリマーアロイとした。こ
のポリマーアロイを紡糸口金孔数400の紡糸口金を用
い吐出量125g/分、紡糸温度285℃で溶融紡糸し
て4.5dおよび12dの未延伸糸とし、95℃熱水中
で3.5倍に延伸し、スタッファボックスで機械捲縮を
付与した後、120℃のネットコンベアー式乾燥機で乾
燥し51mmに切断し、太さ1.5dおよtl、4dの
ステープルとした。得られたステープルの繊維断面をギ
酸で抽出して走査型電子顕微鏡を用い高径を測定した。 [0032]また。得られたステープルをフラットカー
ドでジノとし、紡績して約23番手および5番手の紡績
糸とした。この23番手紡績糸を50×18ゲージ/i
nのシンカー丸編機で天竺編して60g/m2のニット
地とした。このニット地もしくは5番手を脱脂した後、
染色性をカヤロンポリエステルBR−31g/リットル
、テキサトンTH3−1000,3g/リットルおよび
硫酸アンモニウム200 g/リットルと酢酸3.3m
I/リットルのpH調整液10m1/リツトルからなる
染液中に浸漬し、温度130℃30分高圧染色し、ソー
ダ灰2g/リットルおよびハイドロサルファ182g/
リットルを含む80℃浴中で5分間処理した後水洗乾燥
して染色したニット地または紡績糸を得、JISZ87
21標準色票で評価した。 [0033]また上記の染色したニット地の撥水性をニ
ット地上30cmの位置から蒸留水を滴下し、ニット地
表面に水球として残存する(○印とする)か否か(×印
とする)で判定した。結果を表2に示す。 [0034]なお可紡性は、12dの未延伸糸力司1き
取れない場合を×但しその場合は手で未延伸糸を引き取
り断面を観察した。またそれぞれの未延伸糸が引き取れ
た場合を○とする。 [0035] 実施例14 実施例10の繊維から作られたニット地を実施例10と
同様にしてスミカロンS−2RL、S−3RF、5E3
GL、5−BDFおよび5−BGを用いて染色したが実
施例10と同様の深色に染色できた。 [0036]比較例5 実施例10の繊維と比較例4の繊維を混綿して実施例1
0と同様にして約23番手の紡績糸とし、60g/m2
のニット地とし、染色して染めむらを観察したところ、
実施例10の混綿率が15%では染めむらを明確に生じ
た。 [0037]実施例15 実施例12と同様にして600 d/400本のマルチ
フィラメントを作成し、小型の手動式織機で縦15本/
in、横9本/ i nの平織物を作成して、同様に染
色した所10RP5/12の染色品を得た。 [00381以上説明したように、本実施例によれば、
従来達し得なかったポリオレフィン繊維の染色が可能と
なり、カラフルで永久撥水性の繊維素材を安価に供給で
きる。この繊維は紡績糸、フィラメント糸、不織布、カ
ーペットなど様々な分野に応用することができる。また
他の繊維と混綿、混紡、混繊、混編織、交織することも
任意にでき、その混合割合も任意に選択できる。また、
衣料用途のみならず、インチリヤ分野や産業分野など広
い分野に展開することができる。 [0039]
[Function] According to the configuration of the present invention described above, the fiber has polyolefin as a sea component, and the fiber cross section has (
In other words, since it is a polymer alloy containing a dyeable polymer with an average diameter of less than 1 μm (as seen from the fiber cross-sectional direction) as an island component, it maintains the properties of polyolefin fibers.
A dyeable polyolefin fiber with improved dyeability can be obtained. [00103 According to the above-mentioned preferred configuration of the present invention in which the amount of the dyeable polymer is 5 to 55% by weight, the present invention is even more excellent in that the dyeability can be improved while taking advantage of the properties of the polyolefin fiber. It can be done. [0011] Furthermore, according to the preferred configuration of the present invention in which the dyeable polymer is at least one kind of polymer selected from polyamide and/or polyester, and a copolymer thereof, the dyeable polymer can be dispersed using ordinary dyeing conditions. It can be dyed with dyes. [0012] Furthermore, according to the method of the present invention described above, the dyeable polymer and the compatibilizer are kneaded in advance in a molten state, and then the polyolefin polymer is mixed in a molten state, and then melt-spun, so that polyolefin fibers A dyeable polymer can be finely dispersed therein. [0013] [0013] The present invention will be explained in more detail below using Examples. Note that the present invention is not limited to the following examples. [0014] The present inventors used a polymer alloy containing hydrophobic polyolefin as a sea component and dyeable polyamide or polyester as an island component, and formed fibers by a melt spinning method extruded into the air. It was found that most of the polyolefins are made up of sea-based polyolefins. The fibers obtained in this way do not lose the characteristics of polyolefin fibers such as water repellency, and can be dyed well in deep colors when high-pressure dyed using disperse dyes. The present inventors have discovered that the anti-thread properties and stretchability are comparable to those of ordinary polyolefin fibers, leading to the present invention. [0015] The dyeable polymer used as the island component of the present invention has a shape similar to an elongated capsule of medicine, and the diameter in the fiber cross section is less than 1 μm, that is, the volume of one island component is approximately It is preferably less than 10 μm3, and even if the average value is 1 μm or less, it is 3 μm.
The presence of island components exceeding m is not preferable because the fiber formability is poor. The island component used is thermoplastic nylon 6.
Conveniently, homopolymers and copolymers of polyamides such as , nylon 66 and nylon 12, and polyesters such as polyethylene terephthalate and polybutylene terephthalate, and modified products thereof, as well as dyeable thermoplastic resins such as polycarbonate. can be used. In the above, for example, when polyethylene terephthalate is used, the fiber can be dyed with a disperse dye. For example, polyethylene terephthalate has 2°4
If ~10 mol% of 5-sodium sulfoisophthalic acid component units are copolymerized, a basic dyeable type fiber can be obtained, especially if it is a copolymer of about 2.4 to 4.0 mol%. For example, a pressure dyeable type can be used, and a pressure dyeable type can be used if the copolymer is about 5 to 10 mol%. [0016] The dyeable polymer has a melting point of 100 to 28
A temperature in the range of 0°C is preferable for processing the polymer alloy. If the melting point exceeds 280°C, the fiber forming temperature must be 300°C or higher, and in this case, thermal deterioration of the stabilizer in the polyolefin increases. Furthermore, if the melting point is 100° C. or less, it is difficult to process the fibers, which is not preferable. [00171 The sea-component polyolefin used in the present invention is conveniently a homopolymer, a copolymer, or a modified product thereof of an α-polyolefin having a melting point of 100°C or higher, such as polypropylene, polyethylene, polybutene-1, or polymethylthene, and is suitable for fiber molding. Particularly preferred is polypropylene. [0018] Also, a compatibilizer is used for convenience of finely dispersing the island components. As the compatibilizing agent, for example, a copolymer of ethylene-acrylic acid or a derivative thereof is used. More specifically, there are the following. (1) Ethylene-methyl acrylate copolymer (EMA) containing 15 to 35 wt% of methyl acrylate. (2) Ethylene-ethyl acrylate copolymer (EMA) containing 15 to 35 wt% of ethyl acrylate. (3) An ethylene-acrylic acid-methyl acrylate terpolymer containing 5 to 15 wt% of acrylic acid, 5 to 15 wt% of methyl acrylate, and 85 to 65 wt% of ethylene. (4) Ethylene containing 10 to 20 wt% methacrylic acid
An ionomer in which 15 to 50 mol% of the carboxylic acid of methacrylic acid copolymer (EMAA) is zinc or alkali metal salt. (5) Methacrylic acid and acrylic acid total 10-20
wt% ethylene-methacrylic acid-acrylic acid copolymer ionomer. [0019] In addition, °°Atomer°゛ (manufactured by Mikata Petrochemical Co., Ltd.) used in the adhesive layer of coextruded multilayer film
, Modic °° (manufactured by Mitsubishi Yuka Co., Ltd.) can also be used. In addition, in the acrylic acid-based or methacrylic acid-based ethylene copolymer, it is preferable that the carboxylic acid in the side chain is in the form of an ester or an ionomer type salt from the viewpoint of heat resistance. [00201 Note that the ratio of the sea component to the island component is at least 5 wt% or more, preferably 10 to 4 wt% of the island component in terms of dyeability.
It is preferable to add 0 wt%, and if it exceeds 55 wt%, the seabird component tends to be reversed, which is not preferable. [00211 The spinning temperature (T'C) of the dyeable polyolefin fiber used in the present invention is Ts+10≦, assuming that the melting point of the sea component polyolefin is Ts°C and the melting point of the island component is 11°C.
T<360 is possible, and it is more preferable to use a polymer alloy with a combination of Ts<T+ and adopt a range of TI +5≦T≦320. If the spinning temperature exceeds 360°C, the polyolefin of the sea component will decompose, which is undesirable.
Considering the heat resistance of various stabilizers in polyolefin, 3
More preferably, the temperature is 20°C or lower. The melt viscosity of the polymer alloy used is determined according to JISK7210, where the spinning temperature is the measurement temperature.
Melt flow rate (MFR; g/10 min) measured according to (weighted 2169 g) 10≦MF R<30
0 is convenient, and 30 to 30 for fineness of 2 to 0.5 denier.
100g/10 minutes, 1 for thick fineness of 30-15 denier
Particularly preferred is 0 to 30 g/10 minutes, and more preferably around 10 g/10 minutes for large fineness. For MFR>300,
Since fiber formation is lost due to excessive fluidity, it is preferable to lower the spinning temperature to form fibers. [002233 The spun yarn of the present invention generally has a 0. It is obtained in exactly the same manner as ordinary polypropylene fibers using the above-mentioned 5-4 denyl fibers, and the spinnability is the same as that of ordinary polypropylene fibers. Furthermore, since the spun yarn of the present invention has the same applicability to weaving and knitting machines as ordinary polypropylene spun yarn, there is no problem in making it into woven or knitted fabrics. When dyed, if the content of the fiber of the present invention is less than 20%, uneven dyeing will be noticeable, which is not preferable. The same applies even if the fiber used in the present invention is in the form of a multifilament. [00231 The polyolefin fiber made of the polyolefin polymer alloy of the present invention is such that the island component finely dispersed in the fiber can be easily dyed by a high-pressure dyeing method using a disperse dye, and the fiber surface has a sea component polyolefin. Since it is dominated by , it exhibits good water repellency and also has good fiber properties such as fastness to friction. In addition, because the island component has a fine diameter of less than 1 μm in the fiber cross section, it is much thinner than the core diameter of conventional sheath-core composite fibers, and peeling between the sea-island components due to external physical factors is less likely to occur (for example, due to fibrillation). etc.), even when the dyeable polyolefin fiber of the present invention is used as a spun yarn, a woven or knitted fabric thereof, or a multifilament woven or knitted fabric, it is possible to provide a uniformly deep-dyed product without producing chalk marks. [0024] Specific experimental examples will be explained below. [0025] Examples 1 to 7, Comparative Examples 1 to 2 100 parts by weight of nylon-6 with a number average molecular weight of 18,000 and a melting point of 220°C and 10 parts by weight of an ethylene acrylic ester copolymer compatibilizer were heated at 280°C biaxially. After kneading with an extruder, nylon
MFR at 230°C is 8 g/10 min, melting point 16 so that 6 is 30 wt%, 20 wt%, 10 wt%, 0 wt%.
While adding polypropylene powder (diameter 1.5 mm, length 4-5 mm) at 2°C, mix again using a twin screw extruder.
Made of polymer alloy. This polymer alloy was processed using a spinneret with 400 spinneret holes at a discharge rate of 125 g/min.
Melt-spun at a spinning temperature of 285°C to obtain a 4.5 denier (d
) and 43 d of undrawn yarn, and 3.5
Stretched to double size, mechanically crimped using a stuffer box, and then dried using a net conveyor dryer at 120°C.
It was cut into 1.5 d and 15 d staples. The fiber cross section of the obtained staple was extracted with formic acid, and the diameter was measured using a scanning electron microscope. (0026) Also, the obtained staple was made into a web using a parallel roller card flat card, and then made into a felt of 60 g/m2 using a needle punching machine. TH3-100 (dispersant) 0.3g
/liter, and ammonium sulfate (buffer) 200
g/liter and acetic acid 3.3 ml/liter pH adjusting solution 10 ml/liter and high-pressure dyeing at 130°C for 30 minutes. 5 inside
After being treated for minutes, the dyed knitted fabric or spun yarn was washed and dried with water and evaluated using the JIS Z8721 standard color chart. [0027] Furthermore, the water repellency of the dyed felt was determined by dropping distilled water from a position 30 cm above the felt and whether it remained as a water sphere on the felt surface (marked with an ○) or not (marked with an x). . The results are shown in Table 1. In Table 1, the spinnability is indicated as × if the undrawn yarn of 12d cannot be pulled off (in that case, the undrawn yarn is pulled off by hand and the cross section is observed), and when each undrawn yarn is pulled off as ○. did. Furthermore, dyeability and water repellency were evaluated using felt. [0028] Example 8 The felt made from the fibers of Example 3 was made in the same manner as in Example 3 to produce Sumikalon S-2RL, S-3RF, and 5E-3G.
stained using L, 5-BDF and 5-BG. As a result, it was possible to dye the product in the same deep color as in Example 3. [0029] Example 9 [η] 0.63 (where [η] is the dilute solution viscosity,
It is a measure of average molecular weight. ), melting point 260℃
20wt% of polyethylene terephthalate as an island component,
A polymer alloy was produced in the same manner as in Example 1 using the polypropylene of Example 1 as the sea component. This polymer alloy was processed using a spinneret with 100 spinneret holes and a discharge rate of 125
g/min at a spinning temperature of 290° C. to obtain a 43 d undrawn yarn, which was drawn 2.8 times in hot water at 95° C. to obtain a 19 d staple in the same manner as in Example 1. [00301 When the obtained fiber was dyed in the same manner as in Example 1, it was dyed in the same deep color as in Example 1. [00311 Examples 10 to 13 Comparative Examples 3 to 4 Nylon 6 with a number average molecular weight of 18,000 and a melting point of 220°C was twin-screw extruded with 100 parts by weight of an ethylene acrylate copolymer compatibilizer at a temperature of 280°C. After mixing using a machine, nylon-6 is 30wt%, 20wt%, 10wt%
While adding polypropylene powder having a MFR of 230° C. of 8 g/10 minutes and a melting point of 162° C., the mixture was mixed again using a twin-screw extruder so as to have a concentration of 0 wt % to obtain a polymer alloy. This polymer alloy was melt-spun using a spinneret with 400 holes at a flow rate of 125 g/min at a spinning temperature of 285°C to obtain undrawn yarns of 4.5 d and 12 d, which were 3.5 times larger in hot water at 95° C. After being mechanically crimped in a stuffer box, it was dried in a net conveyor dryer at 120° C. and cut into 51 mm to obtain staples with thicknesses of 1.5 d, tl, and 4 d. The fiber cross section of the obtained staple was extracted with formic acid, and the diameter was measured using a scanning electron microscope. [0032] Again. The resulting staples were flat carded and spun into approximately 23 count and 5 count yarns. This 23rd spun yarn is 50×18 gauge/i
It was knitted into a cotton jersey fabric with a weight of 60 g/m2 using a sinker circular knitting machine. After degreasing this knit fabric or No. 5 fabric,
Dyeability was determined using Kayalon Polyester BR-31g/liter, Texaton TH3-1000, 3g/liter, ammonium sulfate 200g/liter and acetic acid 3.3m.
It was immersed in a dye solution consisting of 10 ml/liter of a pH adjustment solution of 1/liter, and subjected to high pressure dyeing at a temperature of 130°C for 30 minutes, followed by 2 g/liter of soda ash and 182 g/liter of hydrosulfur.
After treatment for 5 minutes in an 80°C bath containing a
Evaluation was made using 21 standard color charts. [0033] Also, the water repellency of the dyed knit fabric was determined by dropping distilled water from a position 30 cm above the knit fabric surface and whether it remained as a water ball on the knit fabric surface (marked with an ○) or not (marked with an x). I judged it. The results are shown in Table 2. [0034] The spinnability was determined when the undrawn yarn strength of 12d could not be removed. However, in that case, the undrawn yarn was pulled off by hand and the cross section was observed. In addition, the case where each undrawn yarn is taken off is marked as ○. [0035] Example 14 The knit fabric made from the fiber of Example 10 was made in the same manner as in Example 10 to produce Sumikaron S-2RL, S-3RF, and 5E3.
When stained using GL, 5-BDF and 5-BG, the same deep color as in Example 10 could be obtained. [0036] Comparative Example 5 Example 1 was prepared by blending the fibers of Example 10 and Comparative Example 4.
In the same manner as 0, a spun yarn of approximately 23rd count was made, and the amount was 60g/m2.
When we dyed the knitted fabric and observed the uneven dyeing,
When the cotton blend ratio of Example 10 was 15%, uneven dyeing clearly occurred. [0037] Example 15 600 d/400 multifilaments were made in the same manner as in Example 12, and 15 vertical filaments/400 pieces were made using a small manual loom.
A plain woven fabric of 9 widths/in was prepared and dyed in the same manner to obtain a dyed product of 10RP5/12. [00381 As explained above, according to this embodiment,
It is now possible to dye polyolefin fibers, which was previously impossible, and to supply colorful, permanently water-repellent fiber materials at low cost. This fiber can be applied to various fields such as spun yarn, filament yarn, nonwoven fabric, and carpet. It can also be mixed, blended, mixed, mixed, knitted, or interwoven with other fibers, and the mixing ratio can also be selected arbitrarily. Also,
It can be used not only for clothing, but also for a wide range of fields, such as indoor and industrial fields. [0039]

【発明の効果】以上説明した通り、本発明によれば、ボ
ッオレフィンを海成分とする繊維であり、また繊維断面
における(すなわち繊維断面方向から見て)平均直径が
1μm未満の可染性ポリマを島成分として含むポリマー
アロイであるから、ポリオレフィン系繊維の特性を生か
したまま、染色性を改善した可染性ポリオレフィン繊維
とすることができる。 [00401また、可染性ポリマの存在量が5〜55玉
量%であるという本発明の好ましい構成によれば、ポリ
オレフィン系繊維の特性を生かしたまま染色性を改善で
きるという点においてさらに優れたものとすることがで
きる。 [00411また、可染性ポリマがポリアミド及び/ま
たはポリエステル、及びこれらの共重合体から選ばれる
少なくとも一種のポリマであるという本発明の好ましい
構成によれば、通常の染色条件を用いて分散染料などで
染色できる。 [00421さらに本発明方法によれば、可染性ポリマ
と相溶化剤を溶融状態であらかじめ混練し、次いでポリ
オレフィン系ポリマを溶融状態で混合し、しかる後溶融
紡糸するので、ポリオレフィン系繊維中に可染性ポリマ
を微分散させることができる。
Effects of the Invention As explained above, according to the present invention, a dyeable polymer which is a fiber containing Boolefin as a sea component and has an average diameter of less than 1 μm in the fiber cross section (that is, viewed from the direction of the fiber cross section) Since it is a polymer alloy containing as an island component, it is possible to make a dyeable polyolefin fiber with improved dyeability while taking advantage of the properties of polyolefin fiber. [00401 Furthermore, according to a preferred configuration of the present invention in which the amount of the dyeable polymer is 5 to 55% by weight, an even better result is achieved in that the dyeability can be improved while taking advantage of the properties of polyolefin fibers. can be taken as a thing. [00411 Furthermore, according to a preferred configuration of the present invention in which the dyeable polymer is at least one kind of polymer selected from polyamide and/or polyester, and copolymers thereof, disperse dyes etc. can be dyed using normal dyeing conditions. Can be dyed with [00421] Furthermore, according to the method of the present invention, the dyeable polymer and the compatibilizer are kneaded in advance in a molten state, and then the polyolefin polymer is mixed in a molten state, and then melt-spun, so that the dyeable polymer and the compatibilizer are mixed in a molten state, and then melt-spun. The dyeable polymer can be finely dispersed.

【手続補正書] 【提出日】平成3年8月21日[Procedural amendment] [Submission date] August 21, 1991

【手続補正1】[Procedural amendment 1]

【補正対象書類色】明細書[Document color to be corrected] Specification

【補正対象項目名] 0014 【補正方法】変更[Correction target item name] 0014 [Correction method] Change

【補正内容】[Correction details]

[0014]本発明者らは、疎水性のポリオレフィンを
海成分とし、可染成分のポリアミドまたはポリエステル
を島成分とするポリマーアロイを用い、空気中に押し出
す溶融紡糸法によって繊維を形成すると、繊維表面がほ
とんど海成分のポリオレフィンで占められることを見い
出した。このようにして得た繊維は、撥水性などポリオ
レフィン繊維の特徴が失われず、かつ分散染料を用いて
高圧染色すると良好に深色染色でき、また、島成分の繊
維断面における直径が1μm未満のポリマーアロイは、
紡糸性および延伸性が通常のポリオレフィン繊維に劣ら
ないことを見い出し本発明に至った。
[0014] The present inventors used a polymer alloy containing hydrophobic polyolefin as a sea component and dyeable polyamide or polyester as an island component, and formed fibers by a melt spinning method extruded into the air. It was found that most of the polyolefins are made up of sea-based polyolefins. The fibers obtained in this way do not lose the characteristics of polyolefin fibers such as water repellency, can be dyed well in deep colors when high-pressure dyed using disperse dyes, and are made of polymers with a diameter of less than 1 μm in the fiber cross section of the island component. Alloy is
It was discovered that the spinnability and drawability of this fiber are comparable to those of ordinary polyolefin fibers, leading to the present invention.

【手続補正2】[Procedural amendment 2]

【補正対象書類色】明細書[Document color to be corrected] Specification

【補正対象項目名] 0032 【補正方法】変更[Correction target item name] 0032 [Correction method] Change

【補正内容】[Correction details]

[0032]また、得られたステープルをフラットカー
ドでジノとし、紡績して約23番手および5番手の紡績
糸とした。この23番手紡績糸を50×18ゲージ/i
nのシンカー丸編機で天竺績して60g/m2のニット
地とした。このニット地もしくは5番手を脱脂した後、
染色性をカヤロンポリエステルBR−3Ig/リットル
、テキサトンTH8−1000,3g/リットルおよび
硫酸アンモニウム200 g/リットルと酢酸3.3m
l/リットルのpH調整液10m1/リツトルからなる
染液中に浸漬し、温度130℃、30分高圧染色し、ソ
ーダ灰2g/リットルおよびハイドロサルラフ152g
/リットルを含む80℃洛中で5分間処理した後水洗乾
燥して染色したニット地または紡績糸を得、JISZ8
721標準色票で評価した。
[0032] The resulting staples were also flat carded and spun into approximately 23 count and 5 count spun yarns. This 23rd spun yarn is 50×18 gauge/i
A knit fabric of 60 g/m2 was knitted using a sinker circular knitting machine. After degreasing this knit fabric or No. 5 fabric,
The dyeability was determined using Kayalon Polyester BR-3Ig/liter, Texaton TH8-1000, 3g/liter, ammonium sulfate 200g/liter, and acetic acid 3.3m.
It was immersed in a dye solution consisting of 10 ml/liter of a pH adjusting solution and dyed under high pressure for 30 minutes at a temperature of 130°C, followed by 2 g/liter of soda ash and 152 g of hydrosaraf.
/liter for 5 minutes at 80°C, washed with water and dried to obtain dyed knit fabric or spun yarn, JISZ8
Evaluation was made using the 721 standard color chart.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】ポリオレフィンを海成分とする繊維であっ
て、前記繊維断面における平均直径が1μm未満の可染
性ポリマを島成分として含むポリオレフィン系ポリマー
アロイからなることを特徴とする可染性ポリオレフィン
繊維。
1. A dyeable polyolefin fiber comprising a polyolefin as a sea component, comprising a polyolefin polymer alloy containing a dyeable polymer having an average diameter of less than 1 μm in the cross section of the fiber as an island component. fiber.
【請求項2】可染性ポリマの存在量が5〜55重量%で
ある請求項1記載の可染性ポリオレフィン繊維。
2. The dyeable polyolefin fiber according to claim 1, wherein the amount of the dyeable polymer present is 5 to 55% by weight.
【請求項3】可染性ポリマがポリアミド及び/またはポ
リエステル、及びこれらの共重合体から選ばれる少なく
とも一種のポリマである請求項1記載の可染性ポリオレ
フィン繊維。
3. The dyeable polyolefin fiber according to claim 1, wherein the dyeable polymer is at least one polymer selected from polyamides, polyesters, and copolymers thereof.
【請求項4】ポリオレフィンを海成分とし、繊維断面に
おける直径が1μm未満の可染性ポリマを島成分として
含むポリオレフィン系ポリマーアロイ繊維を製造する方
法であって、可染性ポリマと相溶化剤を溶融状態であら
かじめ混練し、次いでポリオレフィンを溶融状態で混合
し、しかる後溶融紡糸することを特徴とする可染性ポリ
オレフィン繊維の製造方法。
4. A method for producing a polyolefin polymer alloy fiber containing a polyolefin as a sea component and a dyeable polymer having a diameter of less than 1 μm in the cross section of the fiber as an island component, the method comprising: 1. A method for producing dyeable polyolefin fibers, characterized in that the fibers are kneaded in advance in a molten state, then polyolefin is mixed in a molten state, and then melt-spun.
JP40725390A 1990-12-07 1990-12-07 Dyeable polyolefinic fiber and its production Pending JPH04209824A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP40725390A JPH04209824A (en) 1990-12-07 1990-12-07 Dyeable polyolefinic fiber and its production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP40725390A JPH04209824A (en) 1990-12-07 1990-12-07 Dyeable polyolefinic fiber and its production

Publications (1)

Publication Number Publication Date
JPH04209824A true JPH04209824A (en) 1992-07-31

Family

ID=18516871

Family Applications (1)

Application Number Title Priority Date Filing Date
JP40725390A Pending JPH04209824A (en) 1990-12-07 1990-12-07 Dyeable polyolefinic fiber and its production

Country Status (1)

Country Link
JP (1) JPH04209824A (en)

Cited By (12)

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US5869183A (en) * 1994-08-24 1999-02-09 Toyo Boseki Kabushiki Kaisha Polymer blend fibers having phase separation structure and method for producing the same
WO2005123996A1 (en) * 2004-06-22 2005-12-29 Toray Industries, Inc. Polyester fiber excelling in weight lightness
JP2008538391A (en) * 2005-03-22 2008-10-23 アクアダイ・ファイバーズ インコーポレイテッド Dyed polyolefin yarn and fiber fabric using the yarn
JP2009084737A (en) * 2007-09-28 2009-04-23 Daiwabo Co Ltd Polycarbonate split type conjugate fiber, fiber aggregate and nonwoven fabric using the same
JPWO2013141033A1 (en) * 2012-03-23 2015-08-03 東レ株式会社 Polymethylpentene composite fiber or polymethylpentene porous fiber and fiber structure comprising the same
JP2015148027A (en) * 2014-02-07 2015-08-20 東レ株式会社 Dyeable polyolefin fiber and method of producing the same
KR20180121477A (en) 2016-03-11 2018-11-07 도레이 카부시키가이샤 The flame-resistant polyolefin fiber and the fiber structure made of the same
KR20190038759A (en) 2016-08-18 2019-04-09 도레이 카부시키가이샤 Smokable construction made of flame-resistant polyolefin fiber
WO2019142718A1 (en) 2018-01-18 2019-07-25 東レ株式会社 Dyeable polyolefin fiber and fibrous structure comprising same
JP2019127679A (en) * 2018-01-22 2019-08-01 東レ株式会社 Dyeable polyolefin core sheath type composite fiber and fiber structure made thereof
JP2020020061A (en) * 2018-08-01 2020-02-06 東レ株式会社 Knitted fabric
CN113638071A (en) * 2021-08-19 2021-11-12 江苏尚科聚合新材料有限公司 Preparation method of polyolefin composite fiber

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6039412A (en) * 1983-08-11 1985-03-01 Kuraray Co Ltd Mixed yarn for forming nonwoven fabric

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6039412A (en) * 1983-08-11 1985-03-01 Kuraray Co Ltd Mixed yarn for forming nonwoven fabric

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5869183A (en) * 1994-08-24 1999-02-09 Toyo Boseki Kabushiki Kaisha Polymer blend fibers having phase separation structure and method for producing the same
US6245268B1 (en) 1994-08-24 2001-06-12 Toyo Boseki Kabushiki Kaisha Method for producing polymer blend fibers having phase separation structure
WO2005123996A1 (en) * 2004-06-22 2005-12-29 Toray Industries, Inc. Polyester fiber excelling in weight lightness
JP2008538391A (en) * 2005-03-22 2008-10-23 アクアダイ・ファイバーズ インコーポレイテッド Dyed polyolefin yarn and fiber fabric using the yarn
JP2009084737A (en) * 2007-09-28 2009-04-23 Daiwabo Co Ltd Polycarbonate split type conjugate fiber, fiber aggregate and nonwoven fabric using the same
JPWO2013141033A1 (en) * 2012-03-23 2015-08-03 東レ株式会社 Polymethylpentene composite fiber or polymethylpentene porous fiber and fiber structure comprising the same
JP2015148027A (en) * 2014-02-07 2015-08-20 東レ株式会社 Dyeable polyolefin fiber and method of producing the same
KR20180121477A (en) 2016-03-11 2018-11-07 도레이 카부시키가이샤 The flame-resistant polyolefin fiber and the fiber structure made of the same
US10793976B2 (en) 2016-03-11 2020-10-06 Toray Industries, Inc. Dyeable polyolefin fiber and fibrous structure comprising same
KR20190038759A (en) 2016-08-18 2019-04-09 도레이 카부시키가이샤 Smokable construction made of flame-resistant polyolefin fiber
US11359310B2 (en) 2016-08-18 2022-06-14 Toray Industries, Inc. False twist yarn comprising dyeable polyolefin fibers
WO2019142718A1 (en) 2018-01-18 2019-07-25 東レ株式会社 Dyeable polyolefin fiber and fibrous structure comprising same
JP2019127679A (en) * 2018-01-22 2019-08-01 東レ株式会社 Dyeable polyolefin core sheath type composite fiber and fiber structure made thereof
JP2020020061A (en) * 2018-08-01 2020-02-06 東レ株式会社 Knitted fabric
CN113638071A (en) * 2021-08-19 2021-11-12 江苏尚科聚合新材料有限公司 Preparation method of polyolefin composite fiber

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