JPS61296120A - Conjugate fiber - Google Patents

Conjugate fiber

Info

Publication number
JPS61296120A
JPS61296120A JP13422185A JP13422185A JPS61296120A JP S61296120 A JPS61296120 A JP S61296120A JP 13422185 A JP13422185 A JP 13422185A JP 13422185 A JP13422185 A JP 13422185A JP S61296120 A JPS61296120 A JP S61296120A
Authority
JP
Japan
Prior art keywords
component
hot water
soluble
composite
fiber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP13422185A
Other languages
Japanese (ja)
Other versions
JPS646286B2 (en
Inventor
Nobuo Kurata
倉田 信夫
Masahiko Hayashi
政彦 林
Hiroshi Iida
汎 飯田
Naosuke Yoshida
修介 吉田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP13422185A priority Critical patent/JPS61296120A/en
Publication of JPS61296120A publication Critical patent/JPS61296120A/en
Publication of JPS646286B2 publication Critical patent/JPS646286B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To obtain a conjugate fiber capable of forming ultra-fine fiber and modified cross-section fiber easily, without using chemical reagent, etc., by the melt-forming of a polymer composition containing a specific copolymerized polyester at lest a component. CONSTITUTION:The objective conjugate fiber contains a copolymerized polyester containing 8-15mol% 5-sodium sulfoisophthalate and 5-40mol% isophthalic acid and having terephthalic acid as main acid component, as at least a component. The copolymerized polyester is insoluble in cold water and soluble in hot water, has moderate heat-resistance and stringiness even at high temperature, and can be used as a component of a conjugate fiber produced by melt spinning process.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、複合繊維に関する。さらに詳しくは、熱水可
溶型共重合ポリエステルを一成分とし、熱水除去によっ
て容易に極細繊維や特殊周形断面糸を得ることのできる
複合繊維に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to composite fibers. More specifically, the present invention relates to composite fibers that contain hot water soluble copolymerized polyester as one component and can be easily obtained into ultrafine fibers or special circumferential cross-section yarns by removing hot water.

〔従来の技術〕[Conventional technology]

従来、極細繊維を製造する方法としては、直接紡糸方法
では紡糸・延伸時の操業性や極細糸の糸質および高次加
工段階までへの取扱い易さの面で非常にむつかしく、坦
在の技術段階では困iffとされている。このため、異
種成分の複合mM(断面形状が海島型・ブレンド型・分
割性多層型など)とした後に、少なくとも一部がm紺表
面を占める一成分を溶解除去、又は膨訪分割する手段が
知られている。
Conventionally, as a method for producing ultrafine fibers, direct spinning methods are extremely difficult in terms of operability during spinning and drawing, quality of ultrafine fibers, and ease of handling up to higher processing stages, and the technology is currently limited. At this stage, it is said to be difficult. For this reason, after forming a composite mM of different components (having a cross-sectional shape of a sea-island type, a blend type, a divisible multilayer type, etc.), there is a method of dissolving and removing one component that at least partially occupies the m-dark blue surface, or dividing it by expansion. Are known.

しかしながら、前述した溶解除去又は膨潤分割するに際
し化学薬品を用いざるを)琴なかった。例えば、従来ポ
リアミドを溶解除去するためには例えば蟻酸が用いられ
、ポリエステルを溶解除去するため1こは例えば苛性ソ
ーダの熱水溶液が用いられ、ポリスチレンを溶解除去す
るためには例えばトリクロルエチレンが用いられている
However, it was necessary to use chemicals for the above-mentioned dissolution and removal or swelling and division. For example, conventionally, formic acid, for example, has been used to dissolve and remove polyamide, for example, a hot aqueous solution of caustic soda has been used to dissolve and remove polyester, and for example, trichloroethylene has been used to dissolve and remove polystyrene. There is.

これらの化学薬品の取扱いは危険性があり、溶解除去の
ための特殊な設備が必要である。このため作業者の安全
衛生面および製造]ス1−面にネックがあった。
Handling these chemicals is dangerous and requires special equipment to dissolve and remove them. This caused problems in terms of safety and health for workers and in terms of manufacturing speed.

一方、特公昭58−39926号公報には20〜60m
ol%の5−スルホイソフタル酸ナトリウム塩共重合の
水溶性ポリエステルをブレンド紡糸した後延伸時に溶解
除去することが記載されている。
On the other hand, in Japanese Patent Publication No. 58-39926, 20 to 60 m
It is described that a water-soluble polyester copolymerized with 5-sulfoisophthalic acid sodium salt in an amount of 0.1 mol % is blend-spun and then dissolved and removed during stretching.

しかしイrから、これだけ多量の5−スルホイソフタル
酸プi・リウム塩を添加すると、縮重合反応時の発泡・
増粘作用で十分な重合磨のものが得られにくいため、製
糸性においても必ずしも満足できるものではなかった。
However, if such a large amount of 5-sulfoisophthalic acid salt is added, foaming during the polycondensation reaction and
Since it is difficult to obtain a product with sufficient polymer polishing due to the thickening effect, the silk-spinning property was not always satisfactory.

又、冷水でも一部溶出するために重合反応後の溶融ポリ
マ田川冷却によってカット化するために水冷が使用でき
ず特殊な装置が必要であった。
Furthermore, since some of the material is eluted even with cold water, the molten polymer is cut by Tagawa cooling after the polymerization reaction, so water cooling cannot be used and special equipment is required.

更に、水溶性ポリエステルとしては接着剤・リイジング
剤・塗料などの用途に数多くの提案(例えば特公昭47
10873号公報、57−26309@公報、60−1
334号公報など)かなされている、3ただし、これら
はいずれも溶融紡糸による繊維形成には必ずしも満足で
きるものではなかった。
Furthermore, as water-soluble polyester, there are many proposals for uses such as adhesives, rising agents, and paints (for example, Japanese Patent Publication No. 47
Publication No. 10873, 57-26309 @ Publication, 60-1
However, none of these methods were necessarily satisfactory for forming fibers by melt spinning.

更に、特公昭55−1374号公報には水溶性ポリアミ
ドが記載されている。しかしながらこの共重合ポリマは
、高温時の熱安定性やオリゴマー・七ツマ−によって製
糸゛[(1が悪いとされている。
Furthermore, Japanese Patent Publication No. 55-1374 describes water-soluble polyamides. However, this copolymer is said to be bad for yarn production due to its thermal stability at high temperatures and oligomer/seven polymer.

特に非水溶性成分がポリエステルの場合は280〜29
0’Cの紡糸温石が必要であり熱安定性および製糸安定
性に支障かあった。また溶融粘1身が高く保てず複合糸
の断面形状を保つには限界があった。溶融紡糸によって
複合糸を得るためには、高温溶融時にも適度な耐熱性・
粘度・曳糸・[Jlを保つ必要がある。特に各種の断面
形状の複合糸において、成分△と成分Bの任意の構成比
を1* J:うとずれば少なくとも成分△・Bは同レベ
ルの粘!良を保つ必要がある。両成分の粘度レベルが人
きく責;<Tると断面形状が各単糸フィラメントごとに
異な−)たり紡糸の経過により変化するなど安定性がな
くなる。さらに、該ポリマでは、熱水溶解に長時間を要
した。
Especially when the water-insoluble component is polyester, it is 280 to 29.
A spinning hot stone of 0'C was required, which caused problems in thermal stability and spinning stability. Furthermore, the melt viscosity could not be maintained high, and there was a limit to the ability to maintain the cross-sectional shape of the composite yarn. In order to obtain composite yarn by melt spinning, it is necessary to have appropriate heat resistance and
It is necessary to maintain viscosity, yarn, and Jl. In particular, in composite yarns with various cross-sectional shapes, if the composition ratio of component △ and component B is set to 1* J: At least components △ and B have the same level of viscosity! You need to keep it good. If the viscosity level of both components is too high, the cross-sectional shape will be different for each single filament, or it will change with the progress of spinning, resulting in loss of stability. Furthermore, this polymer required a long time to dissolve in hot water.

すなわち、熱水で容易に一成分を溶解除去して極細繊維
を得ることのできる複合、1li1Fの改善には限界が
あった。
That is, there is a limit to the improvement of 1li1F, a composite material in which ultrafine fibers can be obtained by easily dissolving and removing one component with hot water.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

本発明者らは、上記欠点のない、高温時でも適度の耐熱
性と曳糸性をもった水溶性ポリエステルを一成分とした
複合繊維について鋭意検討した結果、本発明に到達した
。特に、冷水には不溶でかつ熱水で容易に除去できる熱
水可溶型共重合ポリエステルを一成分とした複合繊維を
提供することを目的とする。
The inventors of the present invention have arrived at the present invention as a result of extensive research into composite fibers containing water-soluble polyester as one component, which do not have the above-mentioned drawbacks and have appropriate heat resistance and spinnability even at high temperatures. In particular, it is an object of the present invention to provide a composite fiber containing as one component a hot water-soluble copolyester polyester that is insoluble in cold water and easily removable in hot water.

〔問題点を解決り−るだめの手段〕[Means to solve the problem]

すなわち本発明は、少なくとも2成分からなる複合繊維
であって、該複合繊維の少なくとも1成分が8〜’15
mol%の5−プトリウムスルホイソフタル酸、および
5〜4Qmol%のイソフタル酸を含み、主たる酸成分
がテレフタル酸である共重合ポリエステルで構成されて
いることを特徴とする複合繊維である。
That is, the present invention provides a composite fiber consisting of at least two components, wherein at least one component of the composite fiber has a molecular weight of 8 to '15.
It is a composite fiber characterized in that it is composed of a copolymerized polyester containing mol % of 5-pttrium sulfoisophthalic acid and 5 to 4 Q mol % of isophthalic acid, and whose main acid component is terephthalic acid.

本発明の複合繊維とは、−成分を除去して極細繊維を得
るような極細繊維発生型複合繊維、より具体的には海島
型複合ll1iIff、混合紡糸複合11Ii維、剥離
分割型複合繊維などの多成分系複合m維や、−成分の除
去によって種々の変形断面を形成するような複合11i
Iff、また、セラ1〜俊の編織物から一成分を除去す
ることによって特殊な嵩高性と腰を= 5− 付与することの可能な複合繊維などをいう。
The conjugate fiber of the present invention refers to an ultra-fine fiber-generating conjugate fiber that obtains ultra-fine fibers by removing components, more specifically, sea-island composite ll1iIff, mixed spun composite 11Ii fiber, exfoliation split type conjugate fiber, etc. Multi-component composite m fibers and composite 11i that form various deformed cross sections by removing the -component.
Iff also refers to composite fibers that can be imparted with special bulkiness and firmness by removing one component from the knitted fabrics of Sera 1 to Shun.

本発明の複合繊維の1成分である共重合ポリエステルは
、冷水に不溶で熱水に可溶の特性をもったものである。
The copolymerized polyester, which is one component of the composite fiber of the present invention, has the property of being insoluble in cold water and soluble in hot water.

この冷水に不溶で熱水に可溶である性質は、合成繊維と
して製造上非常に有利なことである。すなわち、冷水に
も可溶であると、縮重合の反応終了後溶融ポリマーを吐
出ガツト化する際、通常用いられている水浴中での吐出
冷却が不可能となり、特別の冷J、l設備を必要とする
。例えば吐出空冷の場合、長い冷却ゾーンでかつポリマ
を送るベルトないしは1]−ルが必要となる。長い冷却
ゾーンを要することは酸化分解をも招くことになる。さ
らには複合繊維とした後の取り扱いにおいて、空気中の
水分によって変形を受()、後加工の取り扱いが困難と
なる。例えば極細繊維となっ゛たものを織物あるいは編
物・不織布などにするには、ネン糸あるいはカーデイン
グニ「稈などを経て布帛形成の機台に入るが、この間に
おける極細繊維の糸切れ・毛羽立ち・もつれなどにより
加工が困難となる。
This property of being insoluble in cold water and soluble in hot water is very advantageous in terms of manufacturing as a synthetic fiber. In other words, if it is soluble in cold water, when turning the molten polymer into a discharge tube after the completion of the polycondensation reaction, it will be impossible to cool the discharge in a water bath, which is commonly used, and special cooling equipment will be required. I need. For example, discharge air cooling requires a long cooling zone and a belt or loop for transporting the polymer. Requiring long cooling zones also leads to oxidative decomposition. Furthermore, when handling the composite fiber after it is made, it is deformed by moisture in the air, making it difficult to handle in post-processing. For example, in order to make ultra-fine fibers into woven, knitted or non-woven fabrics, they pass through cotton yarn or carding culms and enter the fabric forming machine, but during this process, the ultra-fine fibers may break, become fluffy, become tangled, etc. This makes processing difficult.

−〇 − このため、本発明は8〜15mol%の5−ナトリウム
スルホイソフタル酸と5〜40mol%のイソフタル酸
の共重合ポリエステルを用いているので、冷水に不溶で
熱水には可溶とイ^す、かつ溶融紡糸における複合mM
の一成分と成し1qることができる。
-〇- Therefore, since the present invention uses a copolymerized polyester of 8 to 15 mol% of 5-sodium sulfoisophthalic acid and 5 to 40 mol% of isophthalic acid, it is insoluble in cold water but soluble in hot water. ^su, and composite mM in melt spinning
It can be made with one component of 1q.

つまり、本発明の複合mmtの一成分である共重合ポリ
エステルは、共重合成分に5−ナトリウムスルホインフ
タル酸とイソフタル酸を共用した点に特徴がある。
That is, the copolymerized polyester which is one component of the composite mmt of the present invention is characterized in that 5-sodium sulfoiphthalic acid and isophthalic acid are used as copolymerized components.

共重合成分の5−ナトリウムスルホイソフタル酸は8〜
15m0I%、好ましくは10〜12.5mol%がよ
い。8mol%未満では1目いとする熱水可溶のものが
得られない。また、15mol′Xを越えると熱水可溶
であっても冷水で一部溶出され、実際取扱い上好ましく
ない。さらに、5−す1〜リウムスルホイソフタル酸と
共に5〜7!lOmol%のイソフタル酸の共重合を必
要とする。イソフタル酸が5mol%未満では熱水溶解
04にフレーク状の不溶物が残存する。また、イソフタ
ル酸が40mol%を越えると縮重合反応速度が遅くな
ったり、1qられるポリマの軟化点が100’C以下と
なり溶融紡糸前の乾燥が十分に行なえなくなったり、高
温時の溶融粘度が高いものがjqられなくなるなど、実
用上の弊害がでてくる。
The copolymerization component 5-sodium sulfoisophthalic acid is 8-
15 mol%, preferably 10 to 12.5 mol%. If the amount is less than 8 mol %, a hot water-soluble product cannot be obtained. Moreover, if the amount exceeds 15 mol'X, even if it is soluble in hot water, it will be partially eluted with cold water, which is not preferable in terms of handling. Furthermore, 5-7! Requires copolymerization of 10 mol% isophthalic acid. If the isophthalic acid content is less than 5 mol %, flaky insoluble matter remains in the hot water solution 04. In addition, if isophthalic acid exceeds 40 mol%, the condensation polymerization reaction rate will be slow, the softening point of the 1q polymer will be 100'C or lower, making it difficult to dry sufficiently before melt spinning, and the melt viscosity at high temperatures will be high. There are practical problems, such as not being able to jq things.

前述の如く、ポリエステルの水溶化には5−スルホイソ
フタル酸の共重合が不可欠ではあるが、イソフタル酸の
補助効果なしでは達し1蝉ない。イソフタル酸の代わり
番こそれ以外の成分、例えば脂環族ジカルボン酸あるい
は脂肪族ジカルボン酸あるいは親水性のポリオール成分
などを用いると、冷水でも膨潤変形したり高温での耐熱
性が悪くなり、本発明の目的とするものが得がたい。
As mentioned above, copolymerization of 5-sulfoisophthalic acid is essential for making polyester water-soluble, but this cannot be achieved without the auxiliary effect of isophthalic acid. If other components are used in place of isophthalic acid, such as alicyclic dicarboxylic acids, aliphatic dicarboxylic acids, or hydrophilic polyol components, they may swell and deform even in cold water or have poor heat resistance at high temperatures. It's hard to get what you're aiming for.

なお、熱水可溶型共重合ポリエステルは、溶解して透明
液となるものおよび乳化微分散状態となるものでもよい
。いずれにしても、何ら助剤を用いることなく熱水で異
物残存物を残さなければ良いのである。
The hot water-soluble copolyester may be one that dissolves into a transparent liquid or one that becomes an emulsified finely dispersed state. In any case, it is sufficient to use hot water without using any auxiliary agents and leaving no foreign matter residues behind.

本発明の複合繊維は前記熱水可溶型ポリエステルと非水
溶性成分で構成される。非水溶性成分としては、繊維形
成性を有し、水に不溶のポリマーであれば、特に限定さ
れることなく使用可能である。例えばナイロン4・ナイ
ロン6・ノーイロン7・ナイロン1トナイロン12・ナ
イロン66などのポリアミド類、ポリエチレンテレフタ
レー1〜・ポリブチレンテレフタレートなどのポリエス
テル類、ポリエチレン・ポリプロピレンなどのポリオレ
フィン類およびこれらの共重合物・変性体などが好適に
用いられる。
The composite fiber of the present invention is composed of the hot water-soluble polyester and a water-insoluble component. As the water-insoluble component, any polymer can be used without particular limitation as long as it has fiber-forming properties and is insoluble in water. For example, polyamides such as nylon 4, nylon 6, norylon 7, nylon 1, nylon 12, and nylon 66, polyesters such as polyethylene terephthalate 1 to polybutylene terephthalate, polyolefins such as polyethylene and polypropylene, and copolymers of these. Modified products and the like are preferably used.

また、この非水溶・[(1成分は何ら一成分に限らない
。二成分以上でも何らかまわない。いずれにしても、熱
水可溶型共重合ポリエステルが、少なくとも繊維表面の
一部を占める断面形態をもった複合繊維でおれば良いわ
けである。
In addition, this water-insoluble [(1 component is not limited to one component at all. It does not matter if there are two or more components. In any case, the hot water-soluble copolymerized polyester It is sufficient if it is a composite fiber with a certain shape.

すなわち、例えば、海鳥型複合繊維の海成分に熱水可溶
型共重合ポリエステルを使用した場合は熱水除去によっ
て極細繊維を極めて容易に得ることができる。また、熱
水可溶型共重合ポリエステルの配置を種々考慮した複合
繊維の場合は、配置に対応した形状の変形断面糸を1q
ることもできる。
That is, for example, when a hot water soluble copolymerized polyester is used as the sea component of a seabird composite fiber, ultrafine fibers can be obtained extremely easily by removing hot water. In addition, in the case of composite fibers in which various arrangements of hot water-soluble copolymerized polyester are considered, 1q of deformed cross-section yarn with a shape corresponding to the arrangement
You can also

−9〜 ざらに複合1jIf[の編織物をセラ1〜した後熱水可
溶型共重合ポリエステルを適宜除去して、独特′1.【
嵩と腰を有するシルクライクな風合を付与することもで
きる。これらは、本発明の複合繊維の利用形態の一例を
示したに過ぎずこれらに限定されるものではない。
-9 ~ After subjecting the knitted fabric of Zaraani Composite 1jIf to Cera 1 ~, the hot water soluble copolyester was appropriately removed to obtain a unique '1. [
It is also possible to impart a silk-like texture with bulk and waist. These are merely examples of the usage of the composite fiber of the present invention, and the present invention is not limited thereto.

〔実施例〕〔Example〕

以下に実施例にJ:って本発明をざらに詳細に説明する
。実施例中の部は重量部を意味する。また評価は次の方
法に従った。
The present invention will be explained in detail in the following Examples. Parts in the examples mean parts by weight. The evaluation was conducted in accordance with the following method.

■ 冷水中の変化:30’Cの水にチップ(約3m…φ
X5mm長)を20時間浸漬した後、チップの表面状況
・チップ形状・重量の変化をみた。
■ Changes in cold water: Chips (approximately 3 m...φ
After immersing a chip (x5 mm length) for 20 hours, changes in the surface condition, chip shape, and weight of the chip were observed.

■ 熱水溶解性:95°Cの熱水1000にチップ(約
3mmφX5mm艮)1Qを投入、マグネッ1〜スター
ラで攪拌しつつ溶解をみた。
(2) Solubility in hot water: 1Q of chips (approximately 3 mm φ x 5 mm) were placed in 95°C hot water 1000°C, and dissolution was observed while stirring with a magnet 1 to a stirrer.

■ 耐熱性:チップを120’08時間真空乾燥した後
メルトインデクサ−で、285°Cで溶融貯留時間10
分おJ:び30分における粘度と曳糸性をみた。
■ Heat resistance: After vacuum drying the chip for 120'08 hours, melt it in a melt indexer at 285°C for 10 hours.
The viscosity and stringiness at 30 minutes and 30 minutes were examined.

実施例1 テレフタル1l(TPA>のメチルエステルであるテレ
フタル酸ジメチル(DM丁)99.7部、イソフタル酸
(TPA)のメチルエステルであるインフタル酸ジメヂ
ル(DMI)25.7部、■チレングリコール93.3
部、酢酸カルシウム0゜135部をフラス]に仕込み1
30〜230’Cで副生メタノールを留出しながらエス
テル交換反応をさせた。次いで、5−ナトリウムスルホ
イソフタルI(SI)のメチルエステルである5−すj
〜リウムスルホイソフタル酸ジメチル(DMS I >
26.1部、三酸化アンチモン0.03部、リン酸0.
0075部、酢酸リチュウム0.3部を連添230〜2
50’Cで1時間の反応後、250〜275°C減圧下
(1m1TltlcI以下)で3時間の縮重合を行なっ
た。重合後常温水浴中にポリマを吐出しガツト化チップ
を得た。かくして得たポリマのIV (o、c、p溶液
での固有粘度)は0.92、軟化点は130℃であった
。このチップを特性評価したところ表1に示すように、
冷水でのチップ変化もなく、かつ熱水可溶であった。更
に耐熱性も良好であった。
Example 1 1 liter of terephthalate (TPA), 99.7 parts of dimethyl terephthalate (DM Ding), a methyl ester of isophthalic acid (TPA), 25.7 parts of dimethyl inphthalate (DMI), a methyl ester of isophthalic acid (TPA), ■93 ethylene glycol .3
1 part, 0°135 parts of calcium acetate into a flask]
The transesterification reaction was carried out at 30 to 230'C while distilling off the by-product methanol. Next, 5-suj, the methyl ester of 5-sodium sulfoisophthal I (SI)
~Dimethyl sulfoisophthalate (DMS I)
26.1 parts, antimony trioxide 0.03 parts, phosphoric acid 0.
0075 parts, 230~2 parts of lithium acetate 0.3 parts
After reaction at 50'C for 1 hour, condensation polymerization was carried out at 250-275°C under reduced pressure (1 ml TltlcI or less) for 3 hours. After polymerization, the polymer was discharged into a water bath at room temperature to obtain gutted chips. The thus obtained polymer had an IV (intrinsic viscosity in o, c, p solutions) of 0.92 and a softening point of 130°C. The characteristics of this chip were evaluated and as shown in Table 1,
There was no chip change in cold water, and it was soluble in hot water. Furthermore, the heat resistance was also good.

実施例2、比較例1〜6 TPA、TPA、Srの量を変更しあるいはTPAの代
りにアジピンM(△A)、又はポリエチレングリコール
(PEG)を用いて、実施例1と同様にして表1に示す
各種組成の共重合ポリマを1qだ。それらの結果は表1
に示1とおりであった。
Example 2, Comparative Examples 1 to 6 Table 1 was carried out in the same manner as in Example 1 by changing the amounts of TPA, TPA, and Sr, or using adipine M (ΔA) or polyethylene glycol (PEG) instead of TPA. 1 q of copolymer polymers with various compositions shown in . The results are shown in Table 1
It was as shown in 1.

実施例3 実施例1で14だチップを100’C1011,1間真
空乾燥したものと、ホモポリエチレンテレフタレー1〜
(P「T)チップ(IVo、70)を150’C60)
間真空乾燥したものを、別々にスクリュー押出機で溶融
(285°C)しギヤポンプで16島18グループの海
島型紡糸「)金に送り、複合紡糸した。実施例1のポリ
マは海成分として、その吐出量は5.2g/分、P「I
−は島成分としてぞの田用吊は20.8(J/分として
口金孔から紡出・空冷して、変成Aレフイン類でオイリ
ングした後1000m/分で巻取った。1qられた未延
伸糸を90°Cの熱ロールおよび120’Cの熱板を通
過させて3.2倍に延伸し、75デニール18フイラメ
ントの延伸糸を得た。紡糸・延伸中の糸切れIJ1殆ど
なかった。
Example 3 The chip No. 14 in Example 1 was vacuum-dried for 100'C1011,1, and homopolyethylene terephthalate 1~
(P'T) Chip (IVo, 70) 150'C60)
The dried materials were separately melted (at 285°C) in a screw extruder and sent to a sea-island type spinning machine with 16 islands and 18 groups using a gear pump for composite spinning.The polymer of Example 1 was used as a sea component. The discharge amount is 5.2g/min, P"I
- is an island component, and the unstretched material was spun at 20.8 (J/min) from the die hole, air-cooled, oiled with modified A reflex, and then wound at 1000 m/min. The yarn was passed through a hot roll at 90°C and a hot plate at 120'C and drawn 3.2 times to obtain a drawn yarn of 75 denier and 18 filaments.There was almost no yarn breakage IJ1 during spinning and drawing.

次いで、この延伸糸を用いて筒編地を試作し清水に10
分浸漬した後乾燥した。浸漬前の重化は7.40(編地
約1m長)のものが、浸漬処理後5.9Qとなり、タッ
チも非常に柔かくしなやかなものとなった。更に延伸糸
の断面は18ノイラメンI〜のものが288フイラメン
1〜の極細繊維に分割されていた。
Next, a tube-knitted fabric was prototyped using this drawn yarn and placed in Shimizu for 10 minutes.
After soaking for a minute, it was dried. The weight before dipping was 7.40 (knitted fabric approximately 1 m long), but after dipping treatment it became 5.9Q, and the touch was also very soft and supple. Further, the cross section of the drawn yarn was divided into ultrafine fibers of 18 filamen I and 288 filaments 1 and more.

実施例4 11iIftの断面形状が3葉形であって、実施例1の
ポリマか、3葉の111点から繊維内部方向に先細りの
くさび状となって配置される紡糸[]金を用いて実施例
3にtl(じた製糸を行イ賞い、75デニール・36フ
イラメン]・の複合繊維を1qだ。
Example 4 The cross-sectional shape of 11iIft is trilobal, and it was carried out using either the polymer of Example 1 or the spun [ ] gold which was arranged in a wedge shape tapering toward the inside of the fiber from the 111 points of the trilobal. In Example 3, 1 q of tl (75 denier, 36 filament) composite fiber is used.

次いで゛、実施例3に準じて筒編地を形成し、続いて潮
水10分浸漬処理を行4【つたところ、熱水可溶Qll
共車台ポリTステルが除去されて、3葉の拍点に繊維内
部り向に先細りのくさび状の凹みが形成されてシルクラ
イク’j 優9rt(な光沢と風合をもつ−bのか19
られた。
Next, a tubular knitted fabric was formed according to Example 3, and then immersed in salt water for 10 minutes.
The co-car chassis poly T stell was removed, and wedge-shaped indentations were formed at the points of the three leaves that tapered in the direction of the inside of the fibers, giving it a Silk-Like 'J Yu 9rt (-B or 19 with a gloss and texture).
It was done.

〔発明の効果〕〔Effect of the invention〕

本発明の複合繊維は2以上の成分中、少なくとも一成分
が冷水不溶でかつ熱水可溶なため、従来の如く化学薬品
1.−1とを用いること4【り、例えば極細繊維や変形
断面糸を容易に1qることができる。
Since at least one of the two or more components of the composite fiber of the present invention is insoluble in cold water and soluble in hot water, chemical agents 1. By using -1 and 4, for example, ultrafine fibers or yarn with a deformed cross section can be easily reduced to 1q.

このため、特殊4■安全防護設備などを必要としないの
で、作業環境が著しく改善される。
Therefore, special 4■ safety protection equipment is not required, so the working environment is significantly improved.

また、本発明の複合mlffを用いた編織物を一1?ッ
ト後、熱水可溶成分を除去すると、独特な嵩と腰を口す
るシルクライクな風合の加工製品を得ることができる。
In addition, a knitted fabric using the composite mlff of the present invention is also available. After cutting, the hot water soluble components are removed to obtain a processed product with a unique bulk and silk-like texture.

Claims (1)

【特許請求の範囲】[Claims] 少なくとも2成分からなる複合繊維であって、該複合繊
維の少なくとも1成分が8〜15mol%の5−ナトリ
ウムスルホイソフタル酸、および5〜40mol%のイ
ソフタル酸を含み、主たる酸成分がテレフタル酸である
共重合ポリエステルで構成されていることを特徴とする
複合繊維。
A composite fiber consisting of at least two components, wherein at least one component of the composite fiber contains 8 to 15 mol% of 5-sodium sulfoisophthalic acid and 5 to 40 mol% of isophthalic acid, and the main acid component is terephthalic acid. Composite fiber characterized by being composed of copolymerized polyester.
JP13422185A 1985-06-21 1985-06-21 Conjugate fiber Granted JPS61296120A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13422185A JPS61296120A (en) 1985-06-21 1985-06-21 Conjugate fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13422185A JPS61296120A (en) 1985-06-21 1985-06-21 Conjugate fiber

Publications (2)

Publication Number Publication Date
JPS61296120A true JPS61296120A (en) 1986-12-26
JPS646286B2 JPS646286B2 (en) 1989-02-02

Family

ID=15123248

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13422185A Granted JPS61296120A (en) 1985-06-21 1985-06-21 Conjugate fiber

Country Status (1)

Country Link
JP (1) JPS61296120A (en)

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JP2010216052A (en) * 2009-03-19 2010-09-30 Kuraray Co Ltd Sea-island type conjugate fiber and ultrafine melt-anisotropic aromatic polyester fiber obtained from the sea-island type conjugate fiber
US8691130B2 (en) 2003-06-19 2014-04-08 Eastman Chemical Company Process of making water-dispersible multicomponent fibers from sulfopolyesters
US8840757B2 (en) 2012-01-31 2014-09-23 Eastman Chemical Company Processes to produce short cut microfibers
US9273417B2 (en) 2010-10-21 2016-03-01 Eastman Chemical Company Wet-Laid process to produce a bound nonwoven article
US9303357B2 (en) 2013-04-19 2016-04-05 Eastman Chemical Company Paper and nonwoven articles comprising synthetic microfiber binders
US9598802B2 (en) 2013-12-17 2017-03-21 Eastman Chemical Company Ultrafiltration process for producing a sulfopolyester concentrate
US9605126B2 (en) 2013-12-17 2017-03-28 Eastman Chemical Company Ultrafiltration process for the recovery of concentrated sulfopolyester dispersion
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0178557U (en) * 1987-11-17 1989-05-26

Cited By (14)

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Publication number Priority date Publication date Assignee Title
US8691130B2 (en) 2003-06-19 2014-04-08 Eastman Chemical Company Process of making water-dispersible multicomponent fibers from sulfopolyesters
JP2010216052A (en) * 2009-03-19 2010-09-30 Kuraray Co Ltd Sea-island type conjugate fiber and ultrafine melt-anisotropic aromatic polyester fiber obtained from the sea-island type conjugate fiber
US9273417B2 (en) 2010-10-21 2016-03-01 Eastman Chemical Company Wet-Laid process to produce a bound nonwoven article
US8906200B2 (en) 2012-01-31 2014-12-09 Eastman Chemical Company Processes to produce short cut microfibers
US8871052B2 (en) 2012-01-31 2014-10-28 Eastman Chemical Company Processes to produce short cut microfibers
US8882963B2 (en) 2012-01-31 2014-11-11 Eastman Chemical Company Processes to produce short cut microfibers
US8840758B2 (en) 2012-01-31 2014-09-23 Eastman Chemical Company Processes to produce short cut microfibers
US9175440B2 (en) 2012-01-31 2015-11-03 Eastman Chemical Company Processes to produce short-cut microfibers
US8840757B2 (en) 2012-01-31 2014-09-23 Eastman Chemical Company Processes to produce short cut microfibers
US9303357B2 (en) 2013-04-19 2016-04-05 Eastman Chemical Company Paper and nonwoven articles comprising synthetic microfiber binders
US9617685B2 (en) 2013-04-19 2017-04-11 Eastman Chemical Company Process for making paper and nonwoven articles comprising synthetic microfiber binders
US9598802B2 (en) 2013-12-17 2017-03-21 Eastman Chemical Company Ultrafiltration process for producing a sulfopolyester concentrate
US9605126B2 (en) 2013-12-17 2017-03-28 Eastman Chemical Company Ultrafiltration process for the recovery of concentrated sulfopolyester dispersion
JP2018184674A (en) * 2017-04-24 2018-11-22 Kbセーレン株式会社 Conjugated fiber, fabric, method for producing fiber structure, and clothing

Also Published As

Publication number Publication date
JPS646286B2 (en) 1989-02-02

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