JPH0244921B2 - - Google Patents
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- JPH0244921B2 JPH0244921B2 JP60242066A JP24206685A JPH0244921B2 JP H0244921 B2 JPH0244921 B2 JP H0244921B2 JP 60242066 A JP60242066 A JP 60242066A JP 24206685 A JP24206685 A JP 24206685A JP H0244921 B2 JPH0244921 B2 JP H0244921B2
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Description
〔産業上の利用分野〕
本発明は繊維の長手方向に連続性のある層状空
洞を有する繊維およびその製造方法に関するもの
である。さらに、詳しくは吸水性が良好で、柔軟
性および保温性に富む層状空洞構造を有する繊維
およびの製造方法に関するものである。
〔従来の技術〕
合成繊維は一般に強力特性が大であり、耐摩耗
性や耐屈曲性が良好であるため、耐久性に優れて
いるが、吸水性や保温性などの機能性が劣る欠点
がある。それゆえ、これらの機能を必要とする分
野では用途が制約されているのが現状である。こ
のため、合成繊維のこのような欠点を改良する目
的で現在まで種々改良が試みられてきた。その代
表的なものは繊維自体を毛細管構造とするもので
ある。例えば、水または有機溶剤に可溶性の微粒
子を添加した繊維形成能を有する高分子重合体を
用いて中空繊維にした後、微粒子を溶出して微多
孔を持つ中空繊維にする方法がある。しかしなが
ら、この方法は微粒子を高分子重合体に添加して
混合紡糸するため、紡糸安定性の面から微粒子あ
るいはその添加量に制約があつたり、また、この
方法で得た繊維については中空部と繊維表面との
連続性が不十分であつたりして、繊維の吸水機能
も十分でないという欠点がある。
一方、近年は単糸繊度が0.1d以下の極細繊維が
容易に製造されるようになり、中空状繊維でなく
ても極細繊維束あるいは集合体の毛細管現象であ
る程度の吸水性は保てるようになつた。しかしな
がら、その反面、極細繊維は特に衣料として用い
る場合には、いま一つ吸水性が十分でなく、かつ
着色性にも劣るという致命的な欠点を有してい
る。
〔発明が解決しようとする問題点〕
本発明の目的とすることろは合成繊維の従来か
らの問題点の一つである吸水性の不足を解消する
ものであつて、また、他の目的は柔軟でかつ、繊
維内部の含気量を多くして保温性に富む構造の繊
維を提供すること、さらには、紡糸安定性の優れ
た方法による上記目的の繊維を提供することにあ
る。
〔問題点を解決するための手段〕
本発明者らは吸水性が良好でかつ、柔軟で保温
性に富む構造を有する繊維について鋭意研究を重
ねた結果、逐に本発明に到達したものである。本
発明の要旨は次のとおりである。即ち、
(1) 主として繊維の長手方向に連続性のある細長
形状の空洞1が層状に存在し、該細長形状の層
状空洞1と隣接する層状空洞1どうしの隔壁を
構成する層状部2、および該層状部2と前記層
状空洞1の外周の大部分を薄く被覆する表皮部
3とからなることを特徴とする繊維。
(2) A,B高分子重合体が相互配列した層状繊維
を製造するに際し、複数の流体流路形成用管路
構造体を直列に配置してA,Bの相互配列流を
流出させ、次いで、格子状分割ロートを通過さ
せて外周表面の大部分がA成分によつて被覆さ
れたA,B高分子相互配列体繊維を紡糸し、し
かる後、A成分に対しては非溶剤または弱溶剤
であるが、B成分に対しては溶解能のある溶剤
でB成分を除去することを特徴とする層状空洞
を有する繊維の製造方法。
(3) A,B高分子重合体が相互配列した層状繊維
を製造するに際し、複数の流体流路形成用管路
構造体を直列に配置してA,Bの相互配列流を
流出させ、次いで、A成分で該A,Bの相互配
列流の外周を被覆して、外周表面の大部分がA
成分によつて被覆されたA,B高分子相互配列
体繊維として紡糸し、しかる後、A成分に対し
ては非溶剤または弱溶剤であるが、B成分に対
しては溶解能のある溶剤でB成分を除去するこ
とを特徴とする層状空洞を有する繊維の製造方
法である。
本発明でいう層状空洞とは、繊維の横断面にお
いて、細長形状の空洞が少なくとも2つ以上存在
し、各空洞の長径は、の空洞が位置する延長上繊
維断面幅の少なくとも3分の1以上の長さであつ
て、該空洞は繊維の長手方向に連続性を有してい
るものである。
また、繊維外周表面の長手方向へ連続性のある
多数の凹凸筋とは、凹凸差が0.2μ以上で、凸部に
着目すれば、その筋は4本以上のものであり、通
常の繊維加工工程で発生する摩擦傷とは異なる。
本発明の層状空洞を有する繊維は、第1図の繊維
一部断面斜視図に示すように、細長形状の層状空
洞1と隣接する層状空洞1の隔壁を構成する層状
部2および該層状部2と層状空洞1の外周の大部
分が薄く被覆された表皮部3からなる繊維であ
る。また、本発明の層状空洞を有する繊維の外周
表面には、繊維の長手方向へ伸びる多数の凹凸筋
4を有するものも含まれている。
この凹凸筋は上記層状繊維に基づくもので、層
状部2の数をNとすると、例えば凸部に着目した
場合、筋は大凡2XN本発生している。
繊維の外周部においては、空洞に近接する部分
が主として2μ以下の極めて薄い膜状になつてい
ると共に、部分的に亀裂あるいは窪み5を形成
し、第2図の繊維横断面図に示すように、これら
の亀裂あるいは窪み5から、実質的に繊維内部の
空洞へ通じる開口構造になつている。
したがつて、繊維の長手方向へ連なる層状空洞
や、空洞と繊維外周表面との接点になつている表
面の亀裂や窪みによる開口あるいは薄膜、さらに
は多数の凹凸筋は、毛細管としての働きと合せ、
全体として吸水および吸水した水分の放水に好都
合な構造になつてる。また、本発明の繊維は内部
が層状部と空洞部から構成されているため、外部
応力に対して自由に変形し易いので柔軟である。
さらに、繊維自身が多くの空気を含むため保温性
に対しても有効な構造になつている。
上記のような層状空洞を有する繊維は、例え
ば、次のようにして得られる。
即ち、繊維形成能を有するA,B高分子重合体
を用いて、特公昭60−1048号公報に示されている
流体流路形成用管路構造体を、流体に著しい回転
を起こさせないように直列に配置した紡糸装置
で、本発明の中間体である表皮を有するA,B高
分子相互配列体繊維を紡糸し、しかる後、高分子
相互配列体の一成分を除去することによつて得ら
れる。
ここで、流体流路形成用管路構造体は直列に配
列することによつて、例えばA,B高分子重合体
を機層にも分割積層した流体積層体を得ることが
でき、流体流路形成用管路構造体をN段使用する
と、A,B高分子重合体からなる層が2XN乗層
できる。流体流路形成用管路構造体はこのように
流体を順次交互に層状に配列する機能を持つたも
のである。
第3図は本発明の中間体である表皮を有する高
分子相互配列体繊維の憶断面図で、A成分6とB
成分7が交互に層状に配列し、その外周がA成分
によつて薄く皮状(表皮部)8に囲まれたもので
ある。
ここに用いるA成分6は実用繊維として有効な
高分子重合体、B成分7は溶剤に対する溶解性が
A成分と異なり、中間体である表皮を有する高分
子相互配列体繊維を得るための捕完的役割を果す
高分子重合体であり、後工程で除去されるもので
ある。
第3図のような表皮を有する高分子相互配列体
繊維は、次のような紡糸パツク内に特殊装置を設
けることによつて得ることができる。
その一つは、紡糸パツク内の流体流路形成用管
路構造体群から流出したA,B相互配列流の層状
流を、交叉して流体を切断するような格子状のセ
パレータの設置であり、他の一つは、第4図の紡
糸パツク概略断面図に示すように、流体流路形成
用管路構造体群からA,B成分の相互配列流9が
押し出されて口金吐出孔10に至るまでの間で、
A,B成分の相互配列流9の外周を被覆するよう
に、別の高分子配列流の被覆用吐出口11からA
成分を押し出す方法である。
前者の方法、即ち、流体流路形成用管路構造体
群下流におけるセパレータは、多孔口金に通じる
蛸足分岐管の上部に、尖つたみねを有する格子状
分割ロートを配置することによつて達成される。
この蛸足分岐によるA,B相互配列流の吐出方法
は、配列流の層に平行して分割される分だけ、
A,Bからなる層の数は減少するが、経済性や生
産性の面から好ましく、また、本発明に係る繊維
外周表面の凹凸筋を付与する面からも好ましい方
法である。
さらに、この方法におけるA,B高分子重合体
の選択は、紡糸温度における溶融粘度がA>Bの
関係またはA,B成分の重量比がA>Bの関係に
あることが特に好ましい。このような関係は、繊
維の外周表面がA成分によつて被覆されたA,B
高分子相互配列体繊維の得易い条件である。
一方、後者の第4図の高分子配列流の被覆用吐
出口11からA,B相互配列流の外周被覆用のA
成分の押し出し量は、重量比で、層状のA,B成
分相互配列流100部に対し、3及至30部であり、
好ましくは7及至20部である。押し出し量が多過
ぎれば、肉厚の皮となつてB成分の除去が困難と
なるばかりでなく、層状空洞と繊維表面の連続性
が弱くなつて好ましくない。また、逆に少な過ぎ
れば、皮の形成ができなくなつて本発明の繊維が
得られないので、適宜その押し出し量は調節する
必要がある。
A,B成分相互配列体、所謂A,Bの交互層状
部分のA成分とB成分の比率は、重量比で85:15
乃至25:75の範囲をとり得るが、紡糸安定性、B
成分除去後の層状空洞の形成性から、A,Bは
70:30乃至40:60が好ましい範囲である。
上記層状部分のA,B成分の比率から、本発明
に係る層状空洞の繊維横断面に占める面積は、層
状部分のB成分の占める面積にほぼ等しくなるは
ずであるが、種々加工工程における圧力などで押
し潰されるため、通常は5乃至50%である。
本発明に用にるA成分の高分子重合体は、ポリ
エチレンテレフタレート(以下PETという)お
よびその共重合体、ポリブチレンテレフタレート
(以下PBTという)、ナイロン6、ナイロン66、
ポリエチレン、ポリプロピレンなどの高分子重合
体であり、その一種または2種以上が用いられ
る。
B成分の高分子重合体は、ポリスチレン(以下
PSTという)、2−エチルヘキシルアクリレート
共重合PST、5−ソデイウムスルホイソフタレ
ート共重合PET、ナイロン6、ナイロン66、
ポリビニールアルコールなどの高分子重合体であ
り、その一種または2種以上が用いられる。
A成分およびB成分は繊維形成能を有すれば、
上記に限定されるものではないが、A成分として
はPET、PBT、ナイロン6、ナイロン66が実
用性能面から好ましく、中でも、PETは層状空
洞の形成性からとくに好ましい高分子重合体であ
る。また、B成分としては、PST、2−エチル
ヘキシルアクリレート共重合PST、5−ソデイ
ウムスルホイソフタレート共重合PETが加工性
の面から特に好ましい高分子重合体である。
表皮を有するA,B高分子相互配列体繊維から
B成分の除去は、従来公知の方法で乾熱延伸、湿
熱延伸あるいは液浴延伸を行なつた後、長繊維や
短繊維のまま、あるいは用途に応じて加工される
編物、織物、不織布、紐などの繊維構造物のいず
れでも行なうことができる。取扱いおよび効率の
面からは、繊維構造物の状態で除去するのが特に
好ましい。この場合、繊維構造物は本発明以外の
他の繊維を混入したものでもよいことはいうまで
もない。
B成分の除去剤はA成分の繊維としての性能に
影響を及ぼさない範囲で適宜選択する必要がある
が、例えば、B成分がPSTおよびその共重合体
であるときは、トリクロロエチレン、パークロル
エチレン、四塩化炭素などの塩素系有機化合物の
溶剤が一般に用いられ、5−ソデイウムスルホイ
ソフタレート共重合PETであるときは、アルカ
リ溶液による処理、所謂、アルカリ減量加工が行
なわれる。
また、B成分を除去する装置は、処理糸の形態
によつて異なるが、マングル、バイブロワツシヤ
ー、染色機など用いることができ、適宜選択して
行なえばよい。
かくして、B成分を除去して得られた繊維は、
第1図および第2図のように、繊維横断面図にお
いて、層状空洞が形成され、あるいは、また、繊
維外周面には繊維の長手方向へ連続性のある凹凸
筋を伴つて、吸水性、柔軟性、保温性に好適な構
造になる。
上記B成分を除去したものが糸条状態のままで
あるときは、用途に応じて繊維構造物である編
物、織物、不織布などの布帛および紐などに加工
し、必要に応じて染色、その他仕上げ加工を施し
て、吸水性をはじめとする機能性に優れた繊維構
造物を提供することができる。
なお、本発明の層状空洞を有する繊維は、延
伸、編織物、不織布、紐などの加工および起毛、
染色その他仕上げ加工時の物理的な外力あるいは
紡糸時の合流などに原因して、部分的に層状空洞
が押し潰され易いが、繊維の主体が本発明の繊維
であれば、その有効性には影響がほとんどない。
〔実施例〕次に実施例をあげて本発明を具体的に
説明するが、これらに限定されるものではない。
実施例 1
直列に配置した6個の流体流路形成用管路構造
体と、その下部に6×3に分割する格子状分割ロ
ートおよび分岐管、それに18ホールの口金を備え
た紡糸パツクを用い、該流体流路形成用管路構造
体の上部から、紡糸温度285℃における溶融粘度
が3000ポイズのPETと同じく450ポイズの2−エ
チルヘキシルアクリレート共重合PSTを、それ
ぞれ重量比で50:50の割合で送り込み、高分子相
互配列体繊維を紡糸した。次いで、85℃の乾熱延
伸を行ない、単糸繊度3dの延伸糸を得た。
続いて、この延伸糸を綛状にし、トリクロロエ
チレンを用いて室温で浸漬、マングルによる絞液
を繰り返し行なつて、2−エチルヘキシルアクリ
レート共重合PSTを十分溶解除去した。
処理して得られた繊維について繊維の長手方向
の数箇所について走査型電顕で観察したところ、
外周表面には表皮が形成されていた。また、繊維
横断面には細長形状の空洞が2乃至10個形成さ
れ、層状空洞になつていた。
さらに、上記繊維の外周面には、繊維の長手方
向に連続性のある凹凸差0.2乃至1.5μの多数の凹
凸筋が形成されていると共に、部分的に層状空洞
に通じる亀裂あるいは窪みのある開口が認められ
た。
実施例 2
直列に配置した6個の流体流路形成用管路構造
体の下流に格子状分割ロートを設けらないで、代
つて、第4図の如き1ホールの口金吐出孔を設
け、流体流路形成用管路構造体から流出した高分
子相互配列流の外周を被覆するように、円形のス
リツト吐出口を設けた紡糸パックを用いた。該流
体流路形成用管路構造体の上部から、紡糸温度
285℃における溶融粘度が3000ポイズのPETと同
450ポイズの2−エチルヘキシルアクリレート共
重合PSTを、また、高分子相互配列流の被覆用
吐出口からは、同3000ポイズのPETを、それぞ
れ重量比で50:50:15の割合で送り込み、高分子
相互配列体繊維を紡糸した。
次いで、85℃で乾熱延伸を行ない、単糸繊度
3.1dの延伸糸を得た。
続いで、この延伸糸を綛状にし、トリクロロエ
チレンを用いて室温で浸漬、マングルによる絞液
を繰り返し行なつて、2−エチルヘキシルアクリ
レート共重合PSTを十分溶解除去した。
このように処理した繊維について、走査型電顕
で観察したところ、実施例1と同様に、層状繊維
の外周は薄く表皮状に結合され、繊維の横断面に
は層状空洞が形成されていた。また、この繊維の
外周表面には、実施例1のものより、全体にやや
浅い感じであるが、繊維の長手方向に連続性のあ
る多数の凹凸筋と部分的に層状空洞に通じる亀裂
あるいは窪みが形成されていた。
比較例 1
直列に配置した6個の流体流路形成用管路構造
体の下流に格子状分割ロートを設けないで、実施
例1のPETと2−エチルヘキシルアクリレート
共重合PSTを、それぞれ重量比で50:50の割合
で流体流路形成用管路構造体から流出させ、その
まま、1ホール口金により紡糸し、以下実施例1
と同様に加工した繊維は、層状空洞が形成されな
かつた。
実施例 3
実施例1で紡糸した未延伸糸について、80℃の
液溶でトウ延伸を行ない、捲縮を施した後、カツ
ト長51mm、単糸繊度3.2d、捲縮数13山/インチの
原綿を作成した。次いで、カード、クロスラツパ
ーの工程を経てウエツプを作成し、2000本/cm2の
ニールドパンチを行なつて目付重量510g/m2の
高分子相互配列体繊維からなる不織布にした。
続いて、この不織布を85℃の熱水で収縮処理し
て乾燥した後、トリクロロエチレンを用いて、浸
漬、マングルによる絞液を繰り返し行なつて、不
織布構成繊維中の2−エチルヘキシルアクリレー
ト共重合PSTを十分除去した。
このように処理した不織布の断面について走査
型電顕で観察したところ、繊維は部分的に変形が
認められたものの、繊維断面および外周表面は、
ほぼ実施例1と同様の構造であつた。
次に、この不織布を幅2cm、長さ15cmにカツト
して、水を入れたビーカーに不織布の一端を5cm
浸漬し、他の端をビーカー外に垂下させ、垂れ下
がつた不織布から2分間に滴下する水の重量を測
定した。
この結果を同様にニードルパンチして調整した
他のPET繊維の比較例2および3の結果と共に
第1表に示した。
第1表の結果から明らかなように、本発明の繊
維を用いた不織布は、比較例に対するものより極
めて良好な吸水性を示した。
なお、不織布の風合についても、本発明繊維の
不織布は、繊度が同程度の比較例2の不織布に比
べて手ざわりが良く、柔軟な風合であつた。
[Industrial Application Field] The present invention relates to a fiber having continuous layered cavities in the longitudinal direction of the fiber and a method for producing the same. More specifically, the present invention relates to a fiber having a layered cavity structure with good water absorption, flexibility and heat retention, and a method for producing the same. [Conventional technology] Synthetic fibers generally have high strength properties and good abrasion resistance and bending resistance, so they are excellent in durability, but they have the disadvantage of poor functionality such as water absorption and heat retention. be. Therefore, the current situation is that applications are restricted in fields that require these functions. For this reason, various improvements have been attempted up to now in order to overcome these drawbacks of synthetic fibers. A typical example is one in which the fiber itself has a capillary structure. For example, there is a method in which hollow fibers are made using a high molecular weight polymer having fiber-forming ability to which fine particles soluble in water or an organic solvent are added, and then the fine particles are eluted to make hollow fibers with fine pores. However, this method involves adding fine particles to a high molecular weight polymer and performing mixed spinning, so there are restrictions on the fine particles or the amount of the added amount from the viewpoint of spinning stability. There are disadvantages in that the continuity with the fiber surface is insufficient and the water absorption function of the fiber is also insufficient. On the other hand, in recent years, ultrafine fibers with a single filament fineness of 0.1d or less have become easily produced, and even if they are not hollow fibers, they can maintain a certain degree of water absorption through the capillary action of ultrafine fiber bundles or aggregates. Ta. However, on the other hand, ultrafine fibers have fatal drawbacks, especially when used for clothing, in that they do not have sufficient water absorption and are poor in colorability. [Problems to be Solved by the Invention] The purpose of the present invention is to solve one of the conventional problems of synthetic fibers, which is the lack of water absorption. The object of the present invention is to provide a fiber having a structure that is flexible and has a high heat retention property by increasing the air content inside the fiber, and furthermore to provide the above-mentioned fiber by a method with excellent spinning stability. [Means for Solving the Problems] The present inventors have conducted extensive research on fibers that have good water absorption, flexibility, and a structure with excellent heat retention properties, and as a result, they have gradually arrived at the present invention. . The gist of the present invention is as follows. That is, (1) layered portions 2 in which elongated cavities 1 that are continuous mainly in the longitudinal direction of the fibers exist in a layered manner, and constitute partition walls between the elongated layered cavities 1 and adjacent layered cavities 1; A fiber characterized by comprising the layered portion 2 and a skin portion 3 that thinly covers most of the outer periphery of the layered cavity 1. (2) When manufacturing a layered fiber in which A and B polymers are mutually arranged, a plurality of fluid channel forming pipe structures are arranged in series to allow the mutually arranged flows of A and B to flow out, and then , the A and B polymer mutually arranged fibers are passed through a lattice-shaped dividing funnel, most of the outer peripheral surface of which is covered with the A component, and then spun, and then a non-solvent or a weak solvent is used for the A component. However, a method for producing fibers having layered cavities, characterized in that component B is removed using a solvent capable of dissolving component B. (3) When manufacturing a layered fiber in which A and B polymers are mutually arranged, a plurality of fluid channel forming conduit structures are arranged in series to allow the mutually arranged flows of A and B to flow out, and then , A component covers the outer periphery of the mutually arranged flow of A and B, so that most of the outer periphery surface is A.
The A and B polymers are spun as fibers coated with the A and B polymers, and are then spun in a non-solvent or weak solvent for the A component but a solvent capable of dissolving the B component. This is a method for producing fibers having layered cavities, characterized by removing component B. In the present invention, the term "layered cavity" means that at least two elongated cavities exist in the cross section of the fiber, and the major axis of each cavity is at least one-third or more of the fiber cross-sectional width in the extension where the cavity is located. The length of the fiber is such that the cavity has continuity in the longitudinal direction of the fiber. In addition, a large number of concave and convex streaks that are continuous in the longitudinal direction on the outer peripheral surface of the fiber means that the difference in concavity and convexity is 0.2 μ or more, and if you focus on the convex part, there are four or more streaks, which is the result of normal fiber processing. This is different from friction scratches that occur during the process.
The fiber having layered cavities of the present invention, as shown in the partially cross-sectional perspective view of the fiber in FIG. Most of the outer periphery of the layered cavity 1 is made up of a thin skin part 3. Further, the outer circumferential surface of the fiber having layered cavities of the present invention includes a fiber having a large number of concavo-convex lines 4 extending in the longitudinal direction of the fiber. These uneven streaks are based on the above-mentioned layered fibers, and if the number of layered parts 2 is N, for example, when focusing on a convex part, approximately 2XN streaks are generated. At the outer periphery of the fiber, the part close to the cavity is mainly in the form of an extremely thin film of 2μ or less, and cracks or depressions 5 are formed in some parts, as shown in the cross-sectional view of the fiber in FIG. , these cracks or depressions 5 have an open structure that leads substantially to the cavity inside the fiber. Therefore, the layered cavities that extend in the longitudinal direction of the fibers, the openings or thin films caused by cracks and depressions on the surface that are the contact points between the cavities and the outer circumferential surface of the fibers, and the large number of uneven streaks act as capillaries. ,
The structure as a whole is convenient for absorbing water and releasing absorbed water. Further, since the fiber of the present invention is composed of a layered portion and a hollow portion inside, it is flexible because it easily deforms freely in response to external stress.
Furthermore, since the fiber itself contains a large amount of air, it has an effective structure for heat retention. The fiber having layered cavities as described above can be obtained, for example, as follows. That is, the pipe structure for forming a fluid flow path shown in Japanese Patent Publication No. 1048/1988 is made by using A and B polymers having fiber-forming ability, so as not to cause significant rotation of the fluid. The fibers obtained by spinning the fibers of the A and B polymeric mutual arrays having a skin, which are the intermediates of the present invention, in spinning devices arranged in series, and then removing one component of the polymeric mutual arrays. It will be done. By arranging the fluid channel forming pipe structures in series, it is possible to obtain, for example, a fluid laminate in which the polymers A and B are laminated separately in the machine layer. When N stages of forming conduit structures are used, 2×N layers of A and B polymers can be formed. The fluid channel forming pipe structure has the function of sequentially and alternately arranging fluid in layers in this way. FIG. 3 is a cross-sectional view of a polymer mutual array fiber having a skin, which is an intermediate of the present invention, and shows A component 6 and B component 6.
Components 7 are arranged alternately in layers, and the outer periphery is surrounded by a thin skin (epidermis) 8 of component A. The A component 6 used here is a polymer effective as a practical fiber, and the B component 7 has a solubility in a solvent different from that of the A component, and is used as an intermediate to obtain a polymer interlayer array fiber with a skin. It is a high molecular weight polymer that plays a critical role and is removed in a subsequent process. Polymer interlayer fibers having a skin as shown in FIG. 3 can be obtained by providing special equipment in the spinning pack as follows. One of these is the installation of a lattice-shaped separator that crosses and cuts the laminar flow of A and B mutually arranged flows flowing out from a group of pipe structures for forming fluid flow paths in the spinning pack. , and the other, as shown in the schematic cross-sectional view of the spinning pack in FIG. Until then,
A from the coating discharge port 11 of another polymer array flow so as to cover the outer periphery of the mutually array flow 9 of the A and B components.
This is a method of extruding ingredients. The former method, i.e., the separator downstream of the group of conduit structures for forming fluid flow paths, is achieved by arranging a lattice-like dividing funnel with sharp corners at the top of the octopus branch pipe leading to the porous mouthpiece. be done.
The method of discharging the A and B mutually aligned flows using this octopus branch is as follows:
Although the number of layers consisting of A and B is reduced, this method is preferable from the viewpoint of economy and productivity, and is also preferable from the viewpoint of imparting unevenness to the outer peripheral surface of the fiber according to the present invention. Furthermore, it is particularly preferable that the A and B polymers are selected in this method so that the melt viscosity at the spinning temperature is in the relationship A>B or the weight ratio of the A and B components is in the relationship A>B. This relationship is based on A and B where the outer peripheral surface of the fiber is covered with the A component.
These conditions make it easy to obtain fibers with mutually arranged polymers. On the other hand, from the coating discharge port 11 of the polymer array flow shown in the latter FIG.
The extrusion amount of the components is 3 to 30 parts by weight per 100 parts of the laminar A and B component mutually arranged flow,
Preferably it is 7 to 20 parts. If the amount of extrusion is too large, not only will the skin become thick and it will be difficult to remove component B, but also the continuity between the layered cavities and the fiber surface will be weakened, which is not preferable. On the other hand, if the amount is too small, the fiber of the present invention cannot be obtained due to the inability to form a skin, so it is necessary to adjust the amount of extrusion as appropriate. The ratio of the A component and the B component of the A and B component mutual array, so-called A and B alternating layered portion is 85:15 by weight.
It can range from 25:75 to 25:75, but spinning stability,
From the formation of layered cavities after component removal, A and B are
A preferred range is 70:30 to 40:60. From the ratio of the A and B components in the layered portion, the area occupied by the layered cavity in the cross section of the fiber according to the present invention should be approximately equal to the area occupied by the B component in the layered portion. Usually it is 5 to 50%. The polymers of component A used in the present invention include polyethylene terephthalate (hereinafter referred to as PET) and its copolymer, polybutylene terephthalate (hereinafter referred to as PBT), nylon 6, nylon 66,
It is a high molecular weight polymer such as polyethylene or polypropylene, and one or more types thereof are used. The polymer of component B is polystyrene (hereinafter referred to as
PST), 2-ethylhexyl acrylate copolymer PST, 5-sodium sulfoisophthalate copolymer PET, nylon 6, nylon 66,
It is a high molecular weight polymer such as polyvinyl alcohol, and one or more types thereof are used. If component A and component B have fiber-forming ability,
Although not limited to the above, PET, PBT, nylon 6, and nylon 66 are preferable as component A from the viewpoint of practical performance, and among them, PET is a particularly preferable polymer because of its ability to form layered cavities. Further, as component B, PST, 2-ethylhexyl acrylate copolymer PST, and 5-sodium sulfoisophthalate copolymer PET are particularly preferred polymers from the viewpoint of processability. The B component can be removed from the A and B polymer mutual array fibers having a skin by performing dry heat stretching, wet heat stretching, or liquid bath stretching using a conventionally known method. Any fibrous structures such as knitted fabrics, woven fabrics, nonwoven fabrics, and strings can be used. From the viewpoint of handling and efficiency, it is particularly preferable to remove the fiber structure. In this case, it goes without saying that the fiber structure may contain fibers other than those of the present invention. The removing agent for component B must be selected appropriately within a range that does not affect the performance of component A as a fiber. For example, when component B is PST and its copolymer, trichlorethylene, perchlorethylene, Solvents of chlorinated organic compounds such as carbon tetrachloride are generally used, and in the case of 5-sodium sulfoisophthalate copolymerized PET, treatment with an alkaline solution, so-called alkali reduction processing, is performed. Further, although the device for removing component B varies depending on the form of the treated yarn, a mangle, a vibrowasher, a dyeing machine, etc. can be used, and the device may be selected as appropriate. Thus, the fiber obtained by removing component B is
As shown in FIGS. 1 and 2, layered cavities are formed in the cross-sectional view of the fibers, or the outer circumferential surface of the fibers has uneven streaks that are continuous in the longitudinal direction of the fibers. The structure is suitable for flexibility and heat retention. If the product from which the above B component has been removed remains in a yarn state, it can be processed into fiber structures such as knitted fabrics, woven fabrics, non-woven fabrics, and strings depending on the purpose, and dyed or otherwise finished as necessary. By processing, it is possible to provide a fiber structure with excellent functionality including water absorption. In addition, the fibers having layered cavities of the present invention can be stretched, knitted fabrics, nonwoven fabrics, processed into strings, etc., raised,
The layered cavities are likely to be partially crushed due to physical external forces during dyeing and other finishing processes or merging during spinning, but if the fibers are mainly the fibers of the present invention, their effectiveness is limited. There is almost no impact. [Examples] Next, the present invention will be specifically explained with reference to Examples, but the present invention is not limited to these. Example 1 A spinning pack was used, which was equipped with 6 pipe structures for forming fluid flow channels arranged in series, a lattice-like dividing funnel and branch pipes divided into 6 x 3 at the bottom, and an 18-hole spinneret. , PET with a melt viscosity of 3000 poise at a spinning temperature of 285°C and 2-ethylhexyl acrylate copolymer PST with a melt viscosity of 450 poise at a weight ratio of 50:50 from the upper part of the fluid channel forming pipe structure. The fibers of the polymer mutual array were spun. Next, dry heat drawing was performed at 85°C to obtain a drawn yarn with a single yarn fineness of 3d. Subsequently, this drawn yarn was made into a skein shape, and the 2-ethylhexyl acrylate copolymer PST was sufficiently dissolved and removed by repeatedly immersing the yarn in trichlorethylene at room temperature and squeezing it with a mangle. When the treated fibers were observed at several locations in the longitudinal direction of the fibers using a scanning electron microscope,
An epidermis was formed on the outer peripheral surface. In addition, 2 to 10 elongated cavities were formed in the cross section of the fiber, forming layered cavities. Furthermore, on the outer peripheral surface of the fiber, a large number of continuous unevenness lines with a difference of 0.2 to 1.5μ are formed in the longitudinal direction of the fiber, and there are also cracks or depressions that partially communicate with the layered cavity. was recognized. Example 2 Instead of providing a lattice-shaped split funnel downstream of the six fluid channel forming pipe structures arranged in series, a one-hole mouthpiece discharge hole as shown in FIG. A spinning pack provided with a circular slit outlet was used so as to cover the outer periphery of the mutually arranged polymer flow flowing out from the flow path forming pipe structure. From the upper part of the fluid flow path forming pipe structure, the spinning temperature is
Same as PET with melt viscosity of 3000 poise at 285℃
450 poise 2-ethylhexyl acrylate copolymerized PST and 3000 poise PET from the coating outlet of the polymer mutually aligned flow are fed in a weight ratio of 50:50:15, respectively. The reciprocal array fibers were spun. Next, dry heat stretching was carried out at 85℃, and the single yarn fineness was
A drawn yarn of 3.1 d was obtained. Subsequently, this drawn yarn was made into a skein, and the 2-ethylhexyl acrylate copolymer PST was sufficiently dissolved and removed by repeatedly immersing the yarn in trichlorethylene at room temperature and squeezing it with a mangle. When the fibers treated in this manner were observed using a scanning electron microscope, it was found that, as in Example 1, the outer periphery of the layered fibers was bonded in a thin skin-like manner, and layered cavities were formed in the cross section of the fibers. Furthermore, although the outer peripheral surface of this fiber is slightly shallower overall than that of Example 1, there are many continuous uneven lines in the longitudinal direction of the fiber, and cracks or depressions that partially lead to layered cavities. was formed. Comparative Example 1 PET and 2-ethylhexyl acrylate copolymer PST of Example 1 were mixed in weight ratio without providing a lattice-like dividing funnel downstream of the six fluid channel forming pipe structures arranged in series. The fluid flowed out from the conduit structure for forming a fluid flow path at a ratio of 50:50, and was then spun using a one-hole spinneret, as described in Example 1 below.
In the fibers processed in the same manner as above, no layered cavities were formed. Example 3 The undrawn yarn spun in Example 1 was tow-stretched in a solution at 80°C and crimped, resulting in a yarn with a cut length of 51 mm, a single yarn fineness of 3.2 d, and a number of crimps of 13 threads/inch. Created raw cotton. Next, a web was prepared through a carding and cross-wrapping process, and 2000 pieces/cm 2 of needle punching was performed to obtain a non-woven fabric made of polymer interlayer array fibers with a basis weight of 510 g/m 2 . Next, this nonwoven fabric was shrink-treated with hot water at 85°C and dried, and then repeatedly soaked in trichlorethylene and squeezed with a mangle to remove the 2-ethylhexyl acrylate copolymerized PST in the fibers constituting the nonwoven fabric. Sufficiently removed. When the cross section of the nonwoven fabric treated in this way was observed using a scanning electron microscope, it was found that the fibers were partially deformed, but the fiber cross section and outer peripheral surface were
The structure was almost the same as that of Example 1. Next, cut this non-woven fabric to 2 cm wide and 15 cm long, and place one end of the non-woven fabric 5 cm long into a beaker filled with water.
The other end of the nonwoven fabric was immersed in the beaker, and the other end was allowed to hang outside the beaker, and the weight of water dripping in 2 minutes from the hanging nonwoven fabric was measured. These results are shown in Table 1 together with the results of Comparative Examples 2 and 3 of other PET fibers prepared by needle punching in the same manner. As is clear from the results in Table 1, the nonwoven fabric using the fibers of the present invention exhibited significantly better water absorption than that of the comparative example. Regarding the texture of the nonwoven fabric, the nonwoven fabric made of the fibers of the present invention had a good feel and a soft texture compared to the nonwoven fabric of Comparative Example 2, which had a similar fineness.
本発明の繊維は上述したように、繊維の特殊な
横断面構造と、付随した特殊な表面構造を有する
ため、吸水性、柔軟性、保温性などが要求される
衣料用分野には、特に、高機能性素材として活用
できる。
一方、吸水性などに有効な毛細管を有する繊維
の製造方法においても、本発明にかかわる流体流
路形成用管路構造体によるものは、紡糸性が極め
て安定であり、上記機能を有する層状空洞を極め
て効果的に提供できる。
As mentioned above, the fibers of the present invention have a special cross-sectional structure and an associated special surface structure, so they are particularly suitable for the field of clothing, which requires water absorption, flexibility, heat retention, etc. It can be used as a highly functional material. On the other hand, in the manufacturing method of fibers having capillary tubes which are effective for water absorption, etc., the method using the conduit structure for forming a fluid flow path according to the present invention has extremely stable spinnability and has layered cavities having the above functions. can be provided extremely effectively.
第1図は本発明の繊維の一部断面をあらわす斜
視図、第2図は第1図のX−X′線の断面図、第
3図は本発明の中間体である表皮を有する高分子
相互配列体繊維の断面図、第4図は高分子相互配
列体繊維の紡糸パツクの概略断面図である。
1:層状空洞、2:層状部、3,8:表皮部、
4:凹凸筋、5:亀裂あるいは窪み、6:A成
分、7:B成分、9:高分子相互配列流、10:
口金吐出孔、11:高分子配列流の被覆用吐出
口。
Fig. 1 is a perspective view showing a partial cross section of the fiber of the present invention, Fig. 2 is a sectional view taken along line X-X' in Fig. 1, and Fig. 3 is a polymer having a skin, which is an intermediate of the present invention. Cross-sectional view of inter-arrayed fibers. FIG. 4 is a schematic cross-sectional view of a spun pack of polymeric inter-arrayed fibers. 1: layered cavity, 2: layered part, 3, 8: epidermal part,
4: Uneven lines, 5: Cracks or depressions, 6: A component, 7: B component, 9: Polymer mutual alignment flow, 10:
Mouth discharge hole, 11: discharge port for coating of polymer array flow.
Claims (1)
形状の空洞1が層状に存在し、該細長形状の層状
空洞1と隣接する層状空洞1どうしの隔壁を構成
する層状部2、および該層状部2と前記層状空洞
1の外周の大部分を薄く被覆する表皮部3とから
なることを特徴とする繊維。 2 繊維の外周表面が、繊維の長手方向に連続性
のある多数の凹凸筋を有する特許請求の範囲第1
項記載の層状空洞を有する繊維。 3 A,B高分子重合体が相互配列した層状繊維
を製造するに際し、複数の流体流路形成用管路構
造体を直列に配置してA,Bの相互配列流を流出
させ、次いで、格子状分割ロートを通過させて外
周表面の大部分がA成分によつて被覆されたA,
B高分子相互配列体繊維を紡糸し、しかる後、A
成分に対しては非溶剤または弱溶剤であるが、B
成分に対しては溶解能のある溶剤でB成分を除去
することを特徴とする層状空洞を有する繊維の製
造方法。 4 妨糸温度におけるA,B高分子重合体の溶融
粘度が、A>Bの関係を有する特許請求の範囲第
3項記載の層状空洞を有する繊維の製造方法。 5 A,B高分子重合体が相互配列した層状繊維
を製造するに際し、複数の流体流路形成用管路構
造体を直列に配置してA,Bの相互配列流を流出
させ、次いで、A成分で該A,Bの相互配列流の
外周を被覆して、外周表面の大部分がA成分によ
つて被覆されたA,B高分子相互配列体繊維を紡
糸し、しかる後、A成分に対しては非溶剤または
弱溶剤であるが、B成分に対しては溶解能のある
溶剤でB成分を除去することを特徴とする層状空
洞を有する繊維の製造方法。[Scope of Claims] 1 A layered portion 2 in which elongated cavities 1 that are continuous mainly in the longitudinal direction of the fibers exist in a layered manner, and constitute partition walls between the elongated layered cavities 1 and adjacent layered cavities 1. , and a skin part 3 that thinly covers most of the outer periphery of the layered cavity 1 and the layered part 2. 2. Claim 1, in which the outer peripheral surface of the fiber has a large number of concave and convex lines that are continuous in the longitudinal direction of the fiber.
A fiber having layered cavities as described in Section 1. 3. When producing a layered fiber in which the polymers A and B are mutually arranged, a plurality of fluid channel forming conduit structures are arranged in series to allow the mutually arranged flows of A and B to flow out, and then a lattice is formed. A, in which most of the outer peripheral surface is coated with the A component by passing through a shaped dividing funnel;
B The polymer interlayer array fibers are spun, and then A
Although it is a non-solvent or weak solvent for the component, B
A method for producing fibers having layered cavities, characterized in that component B is removed using a solvent capable of dissolving the components. 4. The method for producing a fiber having layered cavities according to claim 3, wherein the melt viscosities of the polymers A and B at the filament temperature satisfy the relationship A>B. 5. When producing a layered fiber in which the polymers A and B are mutually arranged, a plurality of fluid channel forming pipe structures are arranged in series to allow the mutually arranged flow of A and B to flow out, and then The outer periphery of the mutually arranged stream of A and B is coated with the component, and the A and B polymer mutually arranged fibers with most of the outer circumferential surface covered with the A component are spun, and then the A component is A method for producing fibers having layered cavities, characterized in that the B component is removed using a non-solvent or weak solvent for the B component, but a solvent capable of dissolving the B component.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24206685A JPS62104909A (en) | 1985-10-29 | 1985-10-29 | Yarn having lamellar void and production thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24206685A JPS62104909A (en) | 1985-10-29 | 1985-10-29 | Yarn having lamellar void and production thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62104909A JPS62104909A (en) | 1987-05-15 |
| JPH0244921B2 true JPH0244921B2 (en) | 1990-10-05 |
Family
ID=17083770
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24206685A Granted JPS62104909A (en) | 1985-10-29 | 1985-10-29 | Yarn having lamellar void and production thereof |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62104909A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH046619U (en) * | 1990-05-08 | 1992-01-22 |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6414311A (en) * | 1987-07-08 | 1989-01-18 | Toray Industries | Modified cross-section yarn and production thereof |
| JPH0229472U (en) * | 1988-08-10 | 1990-02-26 |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS56112535A (en) * | 1980-02-04 | 1981-09-04 | Kuraray Co | Knitted fabric with excellent water absorbability |
-
1985
- 1985-10-29 JP JP24206685A patent/JPS62104909A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH046619U (en) * | 1990-05-08 | 1992-01-22 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62104909A (en) | 1987-05-15 |
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