JPH0140124B2 - - Google Patents

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Publication number
JPH0140124B2
JPH0140124B2 JP14975682A JP14975682A JPH0140124B2 JP H0140124 B2 JPH0140124 B2 JP H0140124B2 JP 14975682 A JP14975682 A JP 14975682A JP 14975682 A JP14975682 A JP 14975682A JP H0140124 B2 JPH0140124 B2 JP H0140124B2
Authority
JP
Japan
Prior art keywords
yarn
heat treatment
yarns
shrinkage
roller
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP14975682A
Other languages
Japanese (ja)
Other versions
JPS5943116A (en
Inventor
Michiaki Yokozawa
Takashi Katagiri
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.)
Nippon Ester Co Ltd
Original Assignee
Nippon Ester 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 Nippon Ester Co Ltd filed Critical Nippon Ester Co Ltd
Priority to JP14975682A priority Critical patent/JPS5943116A/en
Publication of JPS5943116A publication Critical patent/JPS5943116A/en
Publication of JPH0140124B2 publication Critical patent/JPH0140124B2/ja
Granted legal-status Critical Current

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  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
  • Artificial Filaments (AREA)

Description

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

本発明は、糸軸の方向に太繊度部を部分的に有
する太細糸であつて、かつ少なくとも2つの糸条
群間の熱収縮率が異なる異収縮混繊糸の製造方法
に関するものであり、その目的とするところは、
異染効果、風合改良効果にきわめて優れたポリエ
ステル系特殊糸を容易に製造できる方法を提供す
るものである。 従来から、合成繊維を天然繊維の持つすぐれた
風合に近づけるために数多くの提案がなされてい
る。 中でも、絹様の風合については布帛にした場合
の付加価値はきわめて高いので、天然の絹に近づ
けるための提案、工夫が多くなされている。一例
を挙げると、糸条の断面形状を異形にしたもの、
熱収縮率の異なる複数の糸条を混繊したもの、糸
条の中に太繊度部を部分的に発現させたものなど
の製造技術が一般的であり広く知られている。 中でも太細糸であり、かつ熱収縮率が異なる糸
条が混繊された異収縮混繊糸は、糸条群の中に部
分的に発現している太繊度部、すなわち延伸され
ていないかもしくはわずかしか延伸されていない
部分と、細繊度部、すなわち延伸されている部分
との配合度差が、染色した場合染料の吸着性能の
差となり、濃炎部が微妙に配合されたコントラス
トを呈し、また太繊度部と細繊度部の繊度差によ
り、良好なスラブ調風合が生ずる。加えて熱収縮
率が異なるために布帛にして弛緩熱処理を施すこ
とによつて糸条間に糸長差が生じ、この糸長差が
布帛表面に小さなループを形成するので、従来の
合成繊維に見られた平板感、ヌメリ感がなくな
り、ソフトで気品のある光沢、バルキー性に富ん
だすぐれた絹様の風合をかもし出す。 すなわち、太繊度部を部分的に発現させた異収
縮混繊糸は、スパンライク性能と絹様風合が混然
一体となつた複合風合をかもし出すきわめて新規
な素材糸として有用である。 本発明者らは、このような糸条を開発すべく鋭
意努力したところ、従来から公知の方法を用いた
のでは各種問題があり満足できる性能を有する糸
条を得ることができなかつた。 第1には、このように付加価値の高い糸条でも
更に市場のニーズに対応して補助的に布帛でのア
ルカリ減量処理を施すことなどが行われるが、そ
の際糸条の中に混在する未延伸糸に近い性能を有
する太繊度部分と、延伸部分との薬剤処理効果の
差が大きすぎると一方のみが減量が進み「虫く
い」状に欠落部ができる。 従つて、太繊度部が部分的に発現している異収
縮混繊糸を製造する際に供給する糸条は、通常使
用されている配向度の低い未延伸糸よりは、高速
紡糸などで一部配向の進んだ未延伸糸を用いるこ
とが必要となる。 ところが、高配向の未延伸糸を延伸すると、延
伸糸条の熱収縮率がきわめて高くなるのであり、
本発明者らの試験結果によると、太繊度部を有す
る糸条の熱収縮率は50〜60%を越えるきわめて高
い値を示すのであつて、該糸条を用いて布帛にし
た場合、布帛の寸法は初期に設計した寸法よりは
収縮して小さくなり、また風合も硬くきわめてペ
ーパーライクになつてしまう欠点を有しているの
である。 第2には、この欠点の対策として、また糸条の
熱収縮率に差をつけるために、糸条に熱処理を施
して熱収縮率を低下することが必要になるが、こ
の際、太細糸の製造後に引き続いてまたは別工程
を設けて加熱された接糸板または非接触の中空管
などを用いて熱処理を行う方法が一般的に考えら
れる。 本発明者らも、この方式を用いて熱処理を行
い、糸条の熱収縮率を下げようとしたところ、き
わめて不都合が生ずること見い出した。 すなわち、太繊度部を部分的に有した太細糸を
製造した後に熱処理領域を設けて糸条に熱処理を
施す際に、熱処理領域に設けた加熱接糸板または
接糸体に接触通過させた場合、糸条の収縮率は低
下するものの、加熱された接糸板または接糸体と
走行する糸条との摩擦張力または熱による細繊度
部の収縮張力のために糸条の中に部分的に発現さ
せた太繊度部の一部または大部分が引き伸ばされ
てしまい、太繊度部は熱処理を施す前に比較して
急激に少なくなること、また残つている部分も太
繊度部と細繊度部、すなわち延伸されている部分
との境界が不明確になり染色した場合、濃淡のコ
ントラスト効果が激減してしまうこと、更にはこ
の対応策として、加熱されている接糸板または接
糸体に接触走行している糸条の張力を低下させる
ために熱処理領域をオーバーフイードの状態にす
る方法が容易に考えられるが、この方法によつて
も太繊度部は細繊度部の熱収縮によつて発生する
張力のために上記と同様の現象が生じ、さらにオ
ーバーフイード率を上昇すると、走行糸条の張力
が低いために熱処理斑が生じ、熱収縮率にばらつ
きが発生するとともに延伸時の断糸発生率がきわ
めて高くなる。 これら熱処理温度による太繊度部が激減する挙
動は、熱処理温度にきわめて大きく影響され、処
理温度が高いほど太繊度部の減少は著しい。 すなわち、低収縮糸の方が高収縮糸に比較して
太繊度部の減少は多いことになる。 本発明者らは、以上のような問題点を解消し、
太繊度部を部分的に有する異収縮混繊糸を製造す
るためには、延伸領域において一旦形成された太
繊度部を引き伸ばすことなく熱処理を施す技術の
開発が必要であるとの結論に達し、熱処理を施す
際の熱処理部と太繊度部糸条との間に発生する摩
擦抵抗を積極的に利用することに注目して鋭意検
討を行つた。 その結果、驚くべきことに、 (1) 特殊な表面粗度を有するローラーに糸条を密
着させて加熱処理することにより、太繊度部を
引き伸ばすことなく熱収縮率を低下させること
ができること、 (2) この方法で、一度熱処理結晶化処理を行つた
糸条は、再度従来方法により加熱処理を施した
場合でも太繊度部の消滅がきわめて少ないこ
と、 という知見を得、本発明に達したものである。 すなわち本発明は、複屈折率(△n)が20×
10-3以上、60×10-3以下の高配向ポリエステル系
未延伸糸の少なくとも2つの群からなる糸条を糸
条群のいずれにも繊維軸方向に太繊度部が部分的
に発現するにように延伸し、引き続き表面粗度が
1s以下である加熱ローラーに該糸条群を捲回し、
実質的にスリツプさせることなく第1式に示す範
囲内の温度〔RT〕(℃)で第1段の熱処理を施
した後に、いずれかの糸条のみを第2式に示す範
囲内の温度〔H1〕(℃)で第2段の熱処理を行
い、次いで合糸、混繊し捲き取ることを特徴とす
る異収縮混繊糸の製造方法である。 Tg+5≦RT≦Tg+35 (1) RT+15≦H1≦RT+75 (2) 式中Tgは供給原糸のガラス転移温度(℃)で
ある。 本発明のポリエステル系供給原糸とは、延伸を
行うに際して特定の条件または装置を用いて延伸
した場合、ネツキングを生じ得るポリエステル系
の長繊維であれば任意に選ぶことができるが、中
でもエチレンテレフタレート成分を繰り返し単位
として85モル%以上含有するポリエステルを用い
ることが好ましい。 また、その際には布帛の風合や触感を改良する
アルカリ処理や加熱加工を施した場合に太繊度部
の脱落や溶解などを最少限にすること、および経
時による太繊度部の劣化を防止するなどの面から
供給原糸の複屈折率(△n)は20×10-3以上とす
ることが必要である。 一方、供給原糸の複屈折率(△n)が大きい場
合、太繊度部はアルカリなどの薬品や経時による
劣化は防止できるものの、太繊度部、すなわち延
伸がなされていないかわずかに延伸されている部
分と、細繊度部、すなわち延伸がなされている部
分の構造差がきわめて小さいものとなり、染色を
行つた場合必然的に染料の吸着性能は似たものと
なり、濃淡のコントラストが特徴の一つである本
発明の異収縮混繊糸の製造が困難になるため供給
原糸の複屈折率(△n)は60×10-3以下とすべき
である。 また、供給糸条は必ずしも同一の配向度を有す
る必要はなく、必要に応じ複屈折率の異なるも
の、繊度や断面形状が異なる糸条を供給原糸とし
て用いてもよい。 繊維軸方向に太繊度部が部分的に発現するよう
に延伸するのは、太細糸を製造できる方法であれ
ば従来公知の方法が採用でき、例えば延伸温度、
延伸倍率などを特殊な条件に設定する方法、また
は延伸領域内でドロ−レングスや張力を変動させ
て太繊度部を発現する方法などが知られている。
そして、これらの中で太繊度部が明確に発現し、
染色した際に濃色部と淡色部を明瞭に発現させ得
る方法であれば、特に方法は限定されずに採用で
きる。 式中に用いられている第1段の熱処理温度
〔RT〕は、加熱ローラーの回転時の表面温度で
あり、本発明の主旨である太繊度部が部分的に発
現している糸条群の熱収縮率をコントロールする
のに重要であり、第1段熱処理温度〔RT〕を変
えることで高収縮糸とする糸条の熱収縮率を任意
に選ぶことが可能であり、かつ低収縮糸とする糸
条に予備熱処理を施すことは、後に第2段熱処理
を施すにあたつて重要であり、延伸領域内におい
て一旦形成された太繊度部の消失、または短かく
なるのを抑制するのにきわめて高い効果を示すの
である。 すなわち、この場合低収縮糸とする糸条を加熱
ローラーにて温度〔RT〕で予備熱処理を施すこ
とにより第2段熱処理温度〔H1〕で熱処理を施
しても細繊度部の収縮による張力発生が小さく、
また張力下で熱処理を施しても太繊度部が引き伸
ばされずに太細の状態を保つたまま熱収縮率の小
さい糸条を製造することができるのである。 このため、加熱ローラーの位置は低収縮糸とす
る糸条を第2段熱処理温度〔H1〕で熱処理を施
す前に位置することが必要であつて、加熱ローラ
ーの位置が第2段熱処理温度〔H1〕で熱処理を
施した後に位置させた場合は、前記した問題点が
発生するため満足な糸条を得ることができないの
である。 第1段熱処理(加熱ローラ)温度〔RT〕は、
供給糸のガラス転移温度をTg(℃)とした時、
(Tg+5)℃〜(Tg+35)℃とする必要があり、
〔RT〕が(Tg+5)℃未満では該加熱ローラー
に糸条群を捲回した場合、糸条群の中に太繊度部
が部分的に発現している太細部の熱セツト効果が
充分でなく、第2段の熱処理で細繊度部が収縮し
てコントラストの明瞭な低収縮糸が満足に製造で
きないこと、および高収縮糸側の熱収縮率が高い
ために布帛にした場合寸法安定性が悪く、また硬
い風合になるため、本発明の目的にとつてふさわ
しくないものとなるのである。 また、第1段熱処理温度〔RT〕が(Tg+35)
℃を越えた場合は、糸条の熱収縮率はきわめて低
下し、低収縮率とする糸条を第2段熱処理温度
〔H1〕で熱処理を施しても高収縮糸条との熱収縮
率の差が小さいものとなり、布帛にした場合、両
糸条間の熱収縮率差が小さいためにペーパーライ
クな風合となり、目的とする絹様の風合が得られ
ないのである。 なお、ガラス転移温度〔Tg〕は差動走査熱量
計などにより測定が可能であり、例えば使用する
未延伸糸がポリエチレンテレフタレートの場合、
ガラス転移温度は約75℃であつて、この場合の第
1段熱処理温度〔RT〕は80℃以上、110℃以下
が好ましい。 また、低収縮糸とする糸条に施す第2段熱処理
温度〔H1〕は、第1段熱処理温度〔RT〕より15
〜75℃高く設定することにより、高収縮糸条と低
収縮糸条の熱収縮差にバランスがとれ、布帛にし
た場合良好な嵩高になり絹様風合を呈するのであ
つて、温度差が15℃よりも小さい場合は異収縮効
果が充分でなく、75℃よりも大きくしても収縮差
を拡大する効果が小さいだけでなく、延伸時にお
いて断糸の発生率が急激に増加するなど好ましく
ない現象が現われる。 第1段の熱処理を施す加熱ローラーの表面粗度
は、糸条時の中に発現している太繊度部を引き伸
ばさずに、すなわち、延伸領域において形成され
た太繊度部を変形することなく熱処理を施すため
にはきわめて重要な役割を有している。 表面粗度が密になるほど糸条群の中にある太繊
度部と細繊度部との染料の吸着性能差による濃淡
のコントラストを損わずに熱処理が可能であつ
て、実質的に糸条とローラー表面との間にスリツ
プを発生させないために加熱ローラーの表面粗度
は1s以下とする必要がある。糸条の繊度、艶消剤
の含有程度、糸条に付与してある油剤などの種類
によつて多少異なるが、加熱ローラーの表面粗度
は0.5s以下がさらに好ましい。 加熱ローラーの表面粗度が1sを越えると、熱処
理を施すに際し糸条を加熱ローラーに捲回した場
合、ローラー表面と糸条間にスリツプが生じ、糸
条群の中に部分的に発現させた太繊度部が引き伸
ばされる状態となり、その結果、太繊度部が消失
したり短かくなつたりして濃淡差が不明瞭なコン
トラストとなり、利用価値の低い糸条となるので
ある。 なお、ここで言う「加熱ローラーに捲回する」
とは、ローラー部とセパレートローラー部で一対
をなしたもの、あるいはローラー部を傾斜させた
ネルソンローラーなどに糸条を捲き付けることを
指しており、その際、走行系の張力を該ローラー
で同時にニツプさせる必要のある場合には、ロー
ラーと糸条間にスリツプが発生しなくなるまで捲
き付けることが必要であり、例えばセパレートロ
ーラーを併用してローラーに捲回する場合、捲回
される糸条1回のローラーへの接糸長が25cm程度
ならば2〜3回以上捲き付けるのが好ましい。 また、糸条の熱セツト効果を充分にするために
も0.05秒以上加熱接触することが好ましい。 また、低収縮糸とする糸条を熱処理温度〔H1
で第2段の熱処理を施すに際し、その加熱体は接
糸板、非接触の加熱中空管あるいは加熱ピンなど
従来公知の方法を用いることが可能であるが、第
2段熱処理前後の送り出しローラー周速度(V1
に対する集束ローラー周速度(V2)の周速度比
(V2/V1)は1.0未満にすることが本発明の効果
をさらに高めるために好ましい方法である。 以下、本発明の実施態様の一例を図面に従つて
説明する。 第1図は本発明を実施するための延撚機の具体
例を示した概略図である。 第1図に示したものは供給原糸が2つの糸条群
の場合の一例であり、供給原糸1,1′はそれぞ
れガイド2,2′を介して供給ローラー3によつ
て送り出され、供給ローラー3に対する延伸ロー
ラー5の周速度比が1.0を越える速度で回転する
延伸ローラー5により引き取られ、両ローラー間
(延伸領域)で延伸される。このとき延伸ローラ
ー5は加熱ローラーを兼ねており、糸条1,1′
は熱処理または予備熱処理が施される。 そして、供給ローラー3と延伸ローラーを兼ね
た加熱ローラー5の間には円筒型の摩擦抵抗体4
が設けられており、糸条1,1′はこの摩擦抵抗
体4に捲回されることにより太繊度部が糸条群中
に部分的に発現させられて太細糸が製造される。 従つて、延伸ローラーを兼ねた加熱ローラー5
によつて延伸され引取られた2つの糸条群からな
る太細糸は延伸ローラーを兼ねた加熱ローラー5
により熱処理または予備熱処理が施されるのであ
る。 その後延伸ローラーを兼ねた加熱ローラー5と
集束ローラー8の間であり、集束ローラー8と延
伸ローラー5の周速度比が1.0未満となつている
領域に設けられている加熱板6に、2つの糸条群
のうち、低収縮糸とする糸条のみを積極的に接触
させ、高収縮糸とする他方の糸条は分離ガイド7
によつて加熱板6から隔離させ、引き続き合糸ガ
イド9で2つの糸条を合糸し、集束ローラー8に
捲回し、合糸および混繊した後に送り出し、混繊
ガイド10を経てパーン11に捲き上げるのであ
る。 この際、延伸ローラーを兼ねた加熱ローラー5
の表面粗度は1s以下とし、糸条群中に発現してい
る太繊度部との間でスリツプを発生させないよう
にする必要がある。 第2図は本発明を構成する要点である加熱ロー
ラーの温度〔RT〕と、太繊度部が部分的に発現
している太細糸の熱収縮率の関係をポリエチレン
テレフタレートの糸条について測定した結果であ
り、加熱ローラーの温度〔RT〕が上昇するに従
つて糸条の熱収縮率が急激に低下することがわか
る。 太繊度部を部分的に有する異収縮混繊糸の特徴
である染色を行つた場合の濃淡差や太繊度部の
数、長さについては東レエンジニアリング(株)
FYL染色斑測定機や計測器工業(株)製イプネステ
スター糸斑測定器にて測定すると、官能や目視に
頼る評価よりははるかに明確な評価が可能にな
る。 また、本発明でいう熱収縮率は以下のように定
義される。すなわち、熱収縮率の異なる糸条で構
成された異収縮混繊糸をパーンから引き出し、高
収縮糸と低収縮糸に分割し、それぞれ検尺機にて
かせ取りを行い、重さW(1/3g/デニール)
の荷重下で初長l0を測定する。次に無荷重下で沸
水中に30分間浸漬を行い糸条を収縮させる。風乾
後再度重さWの荷重下で収縮後の長さl1を測定
し、熱収縮率(WS)は以下の式で算出されるも
のである。 熱収縮率(%);WS(%)=l0−l1/l0 本発明の製造方法で得られた異収縮混繊糸は後
述する実施例でその効果を述べるが、従来、太細
糸は熱処理を施すことによつて太繊度部が消失ま
たは短かくなるために製品への展開が限定されて
いたが、本発明の方法を採用することにより、ス
パンライク風合と絹様風合をそれぞれ兼ね備えた
きわめて良好な複合風合をかもし出す異収縮混繊
糸を提供できるのである。 以下、実施例をもつて本発明を説明する。 実施例 1 フエノールとテトラクロロエタンの等重量混合
溶媒を用いて20℃で測定した極限粘度〔η〕が
0.65であるポリエチレンテレフタレートを溶融
し、紡糸口金を通して紡糸時の捲取速度を変化す
ることによつて種々複屈折率(△n)が異なる糸
条を採取した。 その糸条を供給原糸として、第1図に示した装
置および延伸方法を用いて表面粗度が0.3sである
延伸ローラーを兼ねた加熱ローラーの温度
〔RT〕を100℃(Tg+25℃)にして延伸および熱
処理を行つた後、低収縮糸とする糸条のみを温度
(H1)が130℃(RT+30℃)である加熱板へ積極
的に接触せしめ、引き続き合糸および混繊して捲
取り、繊度が75デニールで、フイラメント数が48
フイラメントであり、太繊度部の複屈折率(△
n)が異なる異収縮混繊糸を得た。 引き続き、これらの異収縮混繊糸を筒編みし、
その筒編み地について70℃の水酸化ナトリウム20
%水溶液中に30分間浸漬した後風乾し、筒編み地
より糸条を解舒し、強力の低下率や太繊度部の残
存について測定および評価を行い、その評価結果
を第1表に示した。 なお、ここでいう糸条の強力低下率については
水酸化ナトリウム水溶液で処理を施し、風乾後、
筒編み地より糸条を解舒し、インストロン引張り
試験機にて強力の測定を行い、水酸化ナトリウム
水溶液で処理を施す前と比較して強力の低下率を
求めた。 また、異収縮混繊糸の中に発現している太繊度
部の残存については、前記と同様に筒編み地を水
酸化ナトリウム水溶液にて処理を施し、処理後の
筒編み地10cmを円筒状の芯に捲き付けICIピリン
グテスターにて5時間回転させた後、筒編み地を
取り出し、太繊度部の脱落の程度を目視にて評価
を行つた。
The present invention relates to a method for producing a mixed shrinkage yarn, which is a thick and thin yarn that partially has a thick portion in the direction of the yarn axis, and has different heat shrinkage rates between at least two yarn groups. , its purpose is to
The object of the present invention is to provide a method for easily producing a special polyester yarn that has extremely excellent different dyeing effects and hand-improving effects. Many proposals have been made to make synthetic fibers approach the excellent texture of natural fibers. Among these, silk-like texture has extremely high added value when made into fabric, so many proposals and innovations have been made to bring it closer to natural silk. For example, yarns with irregular cross-sectional shapes,
Manufacturing techniques such as those in which a plurality of yarns with different thermal shrinkage rates are blended, and those in which thick portions of fineness are partially expressed in the yarns are common and widely known. Among these, the mixed shrinkage yarn, which is a mixture of yarns that are thick and thin and have different heat shrinkage rates, has thick fineness parts that are partially expressed in the yarn group, that is, undrawn yarns. Alternatively, the difference in blending ratio between the slightly stretched part and the finely woven part, that is, the stretched part, causes a difference in dye adsorption performance when dyed, and the dark flame part exhibits a delicately blended contrast. Also, due to the difference in fineness between the thick and fine fineness areas, a good slab-like texture is produced. In addition, due to the different heat shrinkage rates, when fabrics are made into fabrics and subjected to relaxation heat treatment, yarn length differences occur between yarns, and this yarn length difference forms small loops on the surface of the fabric, making it difficult to use with conventional synthetic fibers. The flat and slimy feel that was previously seen is gone, and a silky texture with a soft, elegant luster and bulkiness is created. In other words, the differential shrinkage mixed fiber yarn that partially exhibits the large fineness portion is useful as an extremely novel material yarn that produces a composite texture that is a mixture of spun-like performance and silk-like texture. The inventors of the present invention made earnest efforts to develop such a yarn, but found that using conventionally known methods resulted in various problems and it was not possible to obtain a yarn with satisfactory performance. First, even with these high value-added yarns, in response to market needs, supplementary alkali reduction treatment is performed on the fabric, but in this case, some If the difference in chemical treatment effect between the thick-fiber part, which has performance similar to that of undrawn yarn, and the stretched part is too large, only one part will lose weight and a "bug-like" missing part will be formed. Therefore, the yarn to be supplied when manufacturing a differentially contracted mixed fiber yarn in which the large fineness portion is partially expressed is more suitable for high-speed spinning than the normally used undrawn yarn with a low degree of orientation. It is necessary to use undrawn yarn with advanced orientation. However, when highly oriented undrawn yarn is drawn, the heat shrinkage rate of the drawn yarn becomes extremely high.
According to the test results of the present inventors, the heat shrinkage rate of yarn having a large fineness portion is extremely high, exceeding 50 to 60%. It has the disadvantage that the dimensions shrink and become smaller than the initially designed dimensions, and the texture is hard and extremely paper-like. Secondly, as a countermeasure to this drawback, and in order to differentiate the heat shrinkage rate of the yarns, it is necessary to heat treat the yarns to lower the heat shrinkage rate. A generally conceivable method is to carry out heat treatment using a heated grafting plate or a non-contact hollow tube, either subsequently or in a separate step after yarn production. The present inventors also performed heat treatment using this method in an attempt to lower the heat shrinkage rate of the yarn, but found that extremely inconveniences occurred. That is, when a heat treatment area is provided and the yarn is subjected to heat treatment after producing a thick and thin yarn partially having a thick fineness portion, the yarn is passed in contact with a heated bonding plate or a bonding body provided in the heat treatment area. In this case, the shrinkage rate of the yarn decreases, but due to the frictional tension between the heated grafting plate or grafting body and the running yarn, or the shrinkage tension of the fine-grained part due to heat, some parts of the yarn may shrink. A part or most of the thick part that has been developed during heat treatment will be stretched, and the number of thick parts will sharply decrease compared to before heat treatment, and the remaining part will also be divided into thick part and fine part. In other words, if the border with the stretched part becomes unclear and dyed, the contrast effect of light and shade will be drastically reduced. It is easy to think of a method of overfeeding the heat treatment area in order to reduce the tension of the running yarn, but even with this method, the large fineness area will be caused by heat shrinkage of the fine fineness area. The same phenomenon as above occurs due to the tension applied, and when the overfeed rate is further increased, heat treatment unevenness occurs due to the low tension of the running yarn, causing variations in heat shrinkage rate and yarn breakage during stretching. rate becomes extremely high. The behavior of drastic reduction in the thick part due to these heat treatment temperatures is extremely influenced by the heat treatment temperature, and the higher the treatment temperature, the more remarkable the reduction in the thick part is. In other words, the decrease in the thick fineness portion is greater in the low shrinkage yarn than in the high shrinkage yarn. The present inventors solved the above problems,
We came to the conclusion that in order to produce differentially shrinkable mixed fiber yarns that partially have thicker areas, it is necessary to develop a technology that heat-treats the thicker areas once formed in the drawing area without stretching them. We conducted intensive studies focusing on actively utilizing the frictional resistance generated between the heat-treated portion and the thick yarn yarn during heat treatment. As a result, we surprisingly found that (1) by heating the yarn in close contact with a roller with a special surface roughness, it was possible to reduce the heat shrinkage rate without stretching the thick part; 2) Through this method, the present invention was achieved based on the knowledge that, even if a yarn that has been heat-treated and crystallized once is heat-treated again using the conventional method, the large-fineness portion disappears very rarely. It is. That is, in the present invention, the birefringence (△n) is 20×
A yarn consisting of at least two groups of highly oriented polyester undrawn yarns of 10 -3 or more and 60 × 10 -3 or less is formed so that a large fineness portion is partially expressed in the fiber axis direction in each of the yarn groups. The surface roughness continues to increase.
Winding the yarn group around a heated roller for 1 s or less,
After performing the first heat treatment at a temperature [RT] (°C) within the range shown in the first equation without causing any slippage, only one of the yarns is heated at a temperature [RT] (°C) within the range shown in the second equation. H 1 ] (° C.), followed by doubling, mixing, and winding. Tg+5≦RT≦Tg+35 (1) RT+15≦H 1 ≦RT+75 (2) In the formula, Tg is the glass transition temperature (° C.) of the supplied yarn. The polyester feed raw yarn of the present invention can be arbitrarily selected as long as it is a polyester long fiber that can cause netting when stretched using specific conditions or equipment, but among them, ethylene terephthalate It is preferable to use a polyester containing 85 mol% or more of the component as a repeating unit. In addition, when performing alkali treatment or heat processing to improve the texture and feel of the fabric, it is necessary to minimize the shedding or dissolution of the thicker part, and to prevent the thicker part from deteriorating over time. In view of this, it is necessary that the birefringence index (Δn) of the supplied yarn be 20×10 −3 or more. On the other hand, when the birefringence index (△n) of the supplied raw yarn is large, the thick part can be prevented from deterioration due to chemicals such as alkali and over time, but the thick part, that is, the part that has not been stretched or has been slightly The structural difference between the part where the material is drawn and the part where the fineness is drawn is extremely small, and when dyeing is carried out, the adsorption performance of the dye will inevitably be similar, and one of the characteristics is the contrast of light and shade. The birefringence index (Δn) of the supplied raw yarn should be 60×10 −3 or less because it becomes difficult to manufacture the differentially shrinkable mixed fiber yarn of the present invention. Furthermore, the supplied yarns do not necessarily have to have the same degree of orientation, and yarns with different birefringences, finenesses, and cross-sectional shapes may be used as the supplied raw yarns, if necessary. For drawing so that a thick part is partially expressed in the fiber axis direction, any conventionally known method can be used as long as it is a method that can produce thick and thin yarns, for example, by adjusting the drawing temperature,
A method is known in which the stretching ratio is set to special conditions, or a method in which the draw length or tension is varied within the stretching region to create a thick fineness section.
Among these, the thick part is clearly expressed,
Any method can be used without particular limitation as long as it can clearly produce dark and light colored areas when dyed. The first stage heat treatment temperature [RT] used in the formula is the surface temperature of the heating roller during rotation, and is the temperature of the yarn group in which the large fineness portion, which is the gist of the present invention, is partially expressed. It is important to control the heat shrinkage rate, and by changing the first stage heat treatment temperature [RT], it is possible to arbitrarily select the heat shrinkage rate of the yarn to be made into a high shrinkage yarn, and it is also possible to select the heat shrinkage rate of the yarn to be made into a high shrinkage yarn. It is important to perform preliminary heat treatment on the yarn to be subjected to the second heat treatment later, and to suppress the disappearance or shortening of the thick part once formed in the drawing area. It shows extremely high effectiveness. In other words, in this case, by preheating the yarn to be a low-shrinkage yarn using a heating roller at temperature [RT], even if heat treatment is performed at the second heat treatment temperature [H 1 ], tension will not be generated due to shrinkage in the fine-grained portion. is small,
Moreover, even if heat treatment is performed under tension, a yarn with a low heat shrinkage rate can be produced while maintaining a thick and thin state without stretching the thick portion. For this reason, the heating roller must be positioned before the yarn to be made into a low shrinkage yarn is heat treated at the second heat treatment temperature [H 1 ], and the heating roller must be positioned at the second heat treatment temperature [H 1 ]. If the yarn is placed after being heat-treated with [H 1 ], the above-mentioned problems occur and a satisfactory yarn cannot be obtained. The first stage heat treatment (heating roller) temperature [RT] is
When the glass transition temperature of the supplied yarn is Tg (℃),
(Tg+5)℃~(Tg+35)℃,
If [RT] is less than (Tg + 5)°C, when the yarn group is wound around the heated roller, the heat setting effect of the thick part where the thick fineness part is partially expressed in the yarn group will not be sufficient. , the fineness part shrinks in the second heat treatment, making it impossible to produce a low-shrinkage yarn with clear contrast, and the high-shrinkage yarn side has a high heat shrinkage rate, resulting in poor dimensional stability when made into a fabric. Moreover, since it has a hard texture, it is not suitable for the purpose of the present invention. In addition, the first stage heat treatment temperature [RT] is (Tg + 35)
If the temperature exceeds ℃, the heat shrinkage rate of the yarn will be extremely low, and even if the yarn with a low shrinkage rate is heat-treated at the second heat treatment temperature [H 1 ], the heat shrinkage rate will be lower than that of the high-shrinkage yarn. The difference is small, and when made into a fabric, the difference in heat shrinkage rate between the two yarns is small, resulting in a paper-like texture, and the desired silk-like texture cannot be obtained. The glass transition temperature [Tg] can be measured using a differential scanning calorimeter, etc. For example, when the undrawn yarn used is polyethylene terephthalate,
The glass transition temperature is about 75°C, and the first stage heat treatment temperature [RT] in this case is preferably 80°C or higher and 110°C or lower. In addition, the second stage heat treatment temperature [H 1 ] applied to the yarn to be made into a low shrinkage yarn is 15% lower than the first stage heat treatment temperature [RT].
By setting the temperature higher by ~75℃, the difference in heat shrinkage between high-shrinkage yarn and low-shrinkage yarn is balanced, and when made into fabric, it has good bulk and a silky texture, and the temperature difference is 15℃. If it is lower than 75°C, the differential shrinkage effect will not be sufficient, and if it is higher than 75°C, not only will the effect of increasing the shrinkage difference be small, but the incidence of yarn breakage will increase rapidly during stretching, which is undesirable. A phenomenon appears. The surface roughness of the heating roller that performs the first-stage heat treatment is determined by heat treatment without stretching the thick-fineness portions that appear in the yarn, that is, without deforming the thick-fineness portions formed in the drawing region. It has an extremely important role in carrying out this. The denser the surface roughness, the more heat treatment is possible without impairing the contrast in shading due to the difference in dye adsorption performance between the thick and fine fineness parts of the yarn group, and it is possible to The surface roughness of the heating roller must be 1s or less to prevent slips from occurring between the heating roller and the roller surface. The surface roughness of the heating roller is more preferably 0.5 s or less, although it varies somewhat depending on the fineness of the yarn, the degree of content of the matting agent, the type of oil agent applied to the yarn, etc. If the surface roughness of the heating roller exceeds 1s, slips may occur between the roller surface and the yarn when the yarn is wound around the heating roller during heat treatment, and slips may occur partially within the yarn group. The thicker part becomes stretched, and as a result, the thicker part disappears or becomes shorter, resulting in an unclear contrast between light and shade, resulting in a yarn with low utility value. Note that "winding on a heating roller" is used here.
refers to winding the yarn around a pair of rollers and separate rollers, or a Nelson roller with an inclined roller.In this case, the tension of the running system is simultaneously applied to the rollers. If it is necessary to nip, it is necessary to wind the yarn until no slip occurs between the roller and the yarn. For example, when winding the yarn around the roller using a separate roller, the yarn 1 If the length of the yarn to be tied to the roller is about 25 cm, it is preferable to wind the yarn 2 to 3 times or more. Further, in order to obtain a sufficient thermal setting effect of the yarn, it is preferable to carry out heating contact for 0.05 seconds or more. In addition, the heat treatment temperature [H 1 ] of the yarn to be made into a low shrinkage yarn
When performing the second stage heat treatment, the heating body can be a conventionally known method such as a bonding plate, a non-contact heating hollow tube, or a heating pin. Circumferential speed (V 1 )
In order to further enhance the effects of the present invention, it is preferable to set the peripheral speed ratio (V 2 / V 1 ) of the focusing roller peripheral speed (V 2 ) to less than 1.0. An example of an embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic diagram showing a specific example of a twisting machine for carrying out the present invention. What is shown in FIG. 1 is an example in which the supply yarns are two yarn groups, and the supply yarns 1 and 1' are sent out by a supply roller 3 via guides 2 and 2', respectively. It is taken up by the stretching roller 5 which rotates at a speed where the peripheral speed ratio of the stretching roller 5 to the supply roller 3 exceeds 1.0, and is stretched between both rollers (stretching area). At this time, the stretching roller 5 also serves as a heating roller, and
is subjected to heat treatment or preheat treatment. A cylindrical friction resistor 4 is disposed between the supply roller 3 and the heating roller 5 which also serves as a stretching roller.
The yarns 1 and 1' are wound around this frictional resistor 4, so that thick fineness portions are partially expressed in the yarn group, and thick and fine yarns are manufactured. Therefore, the heating roller 5 which also serves as a stretching roller
The thick and thin yarn consisting of the two yarn groups drawn and taken by the heating roller 5 which also serves as a drawing roller
Heat treatment or pre-heat treatment is performed. Thereafter, the two yarns are placed on a heating plate 6 provided in an area between the heating roller 5, which also serves as a stretching roller, and the focusing roller 8, and where the circumferential speed ratio of the focusing roller 8 and the drawing roller 5 is less than 1.0. Among the yarn groups, only the yarns to be low shrinkage yarns are brought into active contact, and the other yarns to be high shrinkage yarns are brought into contact with the separation guide 7.
The two yarns are then separated from the heating plate 6 by a doubling guide 9, wound around a converging roller 8, and sent out after being doubled and mixed, and passed through a mixing guide 10 to a pirn 11. It is rolled up. At this time, a heating roller 5 which also serves as a stretching roller
The surface roughness of the yarn must be 1s or less to prevent slips from occurring between the yarns and the thicker yarns. Figure 2 shows the relationship between the temperature [RT] of the heating roller, which is a key component of the present invention, and the thermal shrinkage rate of a thick and thin yarn in which a thick part is partially expressed, measured for a polyethylene terephthalate yarn. The results show that as the temperature [RT] of the heating roller increases, the thermal shrinkage rate of the yarn rapidly decreases. Toray Engineering Co., Ltd. has information about the difference in shading when dyeing, the number and length of thick areas, which are characteristic of differential shrinkage mixed fiber yarns that partially have thick areas.
Measuring with the FYL dye spot measuring device or the Ipnes Tester yarn spot measuring device manufactured by Keizai Kogyo Co., Ltd. enables a much clearer evaluation than evaluations that rely on sensory or visual inspection. Moreover, the thermal shrinkage rate in the present invention is defined as follows. That is, a mixed shrinkage yarn composed of yarns with different heat shrinkage rates is pulled out from the pirn, divided into high shrinkage yarn and low shrinkage yarn, each skeined with a measuring machine, and the weight W (1 /3g/denier)
Measure the initial length l 0 under the load of . Next, the yarn is immersed in boiling water for 30 minutes under no load to shrink the yarn. After air drying, the length l 1 after shrinkage was measured again under a load of weight W, and the heat shrinkage rate (WS) was calculated by the following formula. Thermal shrinkage rate (%); WS (%) = l 0 − l 1 /l 0 The effects of the differentially shrinkable mixed fiber yarn obtained by the manufacturing method of the present invention will be described in the examples described later, but conventionally When yarn is heat-treated, its thick part disappears or becomes short, so its application to products has been limited, but by adopting the method of the present invention, it has been possible to create spun-like textures and silk-like textures. This makes it possible to provide a differential shrinkage mixed fiber yarn that exhibits an extremely good composite texture that has both of the following. The present invention will be explained below with reference to Examples. Example 1 The intrinsic viscosity [η] measured at 20°C using a mixed solvent of equal weights of phenol and tetrachloroethane was
By melting polyethylene terephthalate having a molecular weight of 0.65 and changing the take-up speed during spinning through a spinneret, yarns having various birefringence indexes (Δn) were collected. Using the yarn as a feed raw yarn, the temperature [RT] of the heating roller, which also serves as a drawing roller and has a surface roughness of 0.3 s, is set to 100℃ (Tg + 25℃) using the apparatus and drawing method shown in Figure 1. After stretching and heat treatment, only the yarn to be made into a low-shrinkage yarn is actively brought into contact with a heating plate at a temperature (H 1 ) of 130°C (RT + 30°C), followed by piling, mixing, and winding. The fineness is 75 denier and the number of filaments is 48.
It is a filament, and the birefringence of the thick part (△
Different shrinkage mixed fiber yarns with different n) were obtained. Subsequently, these differential shrinkage mixed fiber yarns are knitted into tubes,
About the tube knitted fabric Sodium hydroxide 20 at 70℃
% aqueous solution for 30 minutes, air-dried, unraveled the yarn from the tubular knitted fabric, and measured and evaluated the rate of decrease in tenacity and the remaining large fineness portion. The evaluation results are shown in Table 1. In addition, regarding the strength reduction rate of the yarn mentioned here, it was treated with a sodium hydroxide aqueous solution, and after air drying,
The threads were unwound from the tubular knitted fabric, and the strength was measured using an Instron tensile tester to determine the rate of decrease in strength compared to before treatment with an aqueous sodium hydroxide solution. In addition, regarding the remaining large fineness portions that appear in the differentially shrinkable mixed fiber yarns, the tubular knitted fabric was treated with an aqueous sodium hydroxide solution in the same manner as above, and 10 cm of the tubular knitted fabric after the treatment was shaped into a cylindrical shape. After wrapping it around a core and rotating it for 5 hours using an ICI pilling tester, the tubular knitted fabric was taken out and the degree of shedding of the thicker part was visually evaluated.

【表】 実施例 2 実施例1で採取した未延伸糸の中から、紡速が
3000m/分であり、複屈折率(△n)が38.9×
10-3である未延伸糸を供給原糸とし、実施例1と
同方法の装置を用いて延伸ローラーを兼ねた加熱
ローラーの温度〔RT〕および低収縮糸とする糸
条を再熱処理を施す温度〔H1〕を種々変更し、
繊度が75デニールでフイラメント数が48本である
異収縮混繊糸を得た。これらの異収縮混繊糸を経
糸および緯糸として用い、ニツサンジエツト1000
(商品名)にて羽二重の組織で製織を行い、得ら
れた布帛を精練、プレセツト、アルカリ処理、染
色を施し、その織物について10人のパネラーによ
つてぬくもり感、スパンライク性、光沢、コント
ラストなどを評価し、その総合評価結果を第2表
に示した。
[Table] Example 2 Among the undrawn yarns collected in Example 1, the spinning speed was
3000m/min, and the birefringence (△n) is 38.9×
Using the undrawn yarn of 10-3 as the supplied raw yarn, use the same method as in Example 1 to set the temperature of the heating roller that also serves as a drawing roller [RT], and reheat the yarn to be made into a low shrinkage yarn. By variously changing the temperature [H 1 ],
A mixed shrinkage yarn with a fineness of 75 denier and a number of filaments of 48 was obtained. Using these different shrinkage blend yarns as the warp and weft yarns, Nitsu Sanjetsu 1000
(Product name), the resulting fabric is scoured, preset, alkali treated, and dyed, and 10 panelists evaluate the fabric for its warmth, spun-like properties, and luster. , contrast, etc. were evaluated, and the overall evaluation results are shown in Table 2.

【表】【table】

【表】 実施例 3 実施例2と同様の未延伸糸を供給原糸とし、実
施例1と同方法の装置を用いて延伸ローラーを兼
ね合わせた加熱ローラーの表面温度〔RT〕を
100℃(Tg+25℃)にし、低収縮糸とする糸条に
再度熱処理を施す加熱板の温度〔H1〕を130℃
(RT+30℃)にして、延伸ローラーを兼ねた加
熱ローラーの表面粗度を種々変更し、繊度が75デ
ニールでフイラメント数が48本である異収縮混繊
糸を得た。 この異収縮混繊糸を実施例2と同様に製織およ
び染色を行つて得られた織物について10人のパネ
ラーによつて濃淡のコントラストに着目して評価
を行い、その評価結果を第3表に示した。
[Table] Example 3 The same undrawn yarn as in Example 2 was used as the supplied raw yarn, and the surface temperature [RT] of the heating roller that also served as a drawing roller was determined using the same method as in Example 1.
The temperature of the heating plate [H 1 ] to 100℃ (Tg + 25℃) and heat treatment on the yarn to be made into low shrinkage yarn is 130℃.
(RT+30°C), and variously changed the surface roughness of the heating roller that also served as a drawing roller, to obtain a differentially shrinkable mixed fiber yarn with a fineness of 75 denier and a number of filaments of 48. The fabrics obtained by weaving and dyeing this differentially shrinkable mixed fiber yarn in the same manner as in Example 2 were evaluated by 10 panelists, focusing on the contrast of shading, and the evaluation results are shown in Table 3. Indicated.

【表】【table】 【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の太繊度部を含む異収縮混繊糸
を製造するための装置の一例である延撚機の概略
図、第2図は加熱ローラーの表面温度〔RT〕値
と太繊度部を含む糸条の熱収縮率との関係を示す
グラフである。 1,1′:供給原糸、2,2′:ガイド、3:供
給ローラー、4:摩擦抵抗体、5:延伸ローラー
を兼ねた加熱ローラー、6:加熱板、7:分離ガ
イド、8:集束ローラー、9:合糸ガイド、1
0:混繊ガイド、11:パーン。
Fig. 1 is a schematic diagram of a drawing and twisting machine which is an example of a device for producing a differentially shrinkable mixed fiber yarn containing a large fineness portion according to the present invention, and Fig. 2 shows the surface temperature [RT] value of the heating roller and the large fineness. FIG. 1, 1': Supply yarn, 2, 2': Guide, 3: Supply roller, 4: Frictional resistor, 5: Heating roller that also serves as a stretching roller, 6: Heating plate, 7: Separation guide, 8: Convergence Roller, 9: Doubling guide, 1
0: Mixed fiber guide, 11: Pern.

Claims (1)

【特許請求の範囲】 1 複屈折率(△n)が20×10-3以上、60×10-3
以下の高配向ポリエステル系未延伸糸の少なくと
も2つの群からなる糸条を糸条群のいずれにも繊
維軸方向に太繊度部が部分的に発現するように延
伸し、引き続き表面粗度が1s以下である加熱ロー
ラーに該糸条群を捲回し、実質的にスリツプさせ
ることなく第(1)式に示す範囲内の温度〔RT〕
(℃)で第1段の熱処理を施した後に、いずれか
の糸条のみを第(2)式に示した温度〔H1〕(℃)で
第2段の熱処理を行い、次いで合糸混繊し捲き取
ることを特徴とする異収縮混繊糸の製造方法。 Tg+5≦RT≦Tg+35 (1) RT+15≦H1≦RT+75 (2) 式中Tgは、供給原糸のガラス転移温度である。
[Claims] 1. Birefringence (△n) is 20×10 -3 or more, 60×10 -3
A yarn consisting of at least two groups of the following highly oriented polyester undrawn yarns is drawn so that a large fineness part is partially expressed in the fiber axis direction in each yarn group, and then the surface roughness is reduced to 1s. The yarn group is wound around a heating roller as follows, and the temperature [RT] is within the range shown in equation (1) without substantially slipping.
After performing the first heat treatment at (°C), one of the yarns is subjected to the second heat treatment at the temperature [H 1 ] (°C) shown in equation (2), and then the yarn is mixed. A method for producing a differentially shrinkable mixed yarn characterized by spinning and winding. Tg+5≦RT≦Tg+35 (1) RT+15≦H 1 ≦RT+75 (2) In the formula, Tg is the glass transition temperature of the supplied yarn.
JP14975682A 1982-08-28 1982-08-28 Manufacture of combined filament yarn having different shrinkage Granted JPS5943116A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14975682A JPS5943116A (en) 1982-08-28 1982-08-28 Manufacture of combined filament yarn having different shrinkage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14975682A JPS5943116A (en) 1982-08-28 1982-08-28 Manufacture of combined filament yarn having different shrinkage

Publications (2)

Publication Number Publication Date
JPS5943116A JPS5943116A (en) 1984-03-10
JPH0140124B2 true JPH0140124B2 (en) 1989-08-25

Family

ID=15482058

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14975682A Granted JPS5943116A (en) 1982-08-28 1982-08-28 Manufacture of combined filament yarn having different shrinkage

Country Status (1)

Country Link
JP (1) JPS5943116A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6285046A (en) * 1985-10-08 1987-04-18 帝人株式会社 Low silk like polyester knitted fabric
JPS62110934A (en) * 1985-11-05 1987-05-22 日本エステル株式会社 Different finness blended special irregular yarn

Also Published As

Publication number Publication date
JPS5943116A (en) 1984-03-10

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