JPH05331758A - Production of ultrafine fiber - Google Patents

Production of ultrafine fiber

Info

Publication number
JPH05331758A
JPH05331758A JP4157293A JP15729392A JPH05331758A JP H05331758 A JPH05331758 A JP H05331758A JP 4157293 A JP4157293 A JP 4157293A JP 15729392 A JP15729392 A JP 15729392A JP H05331758 A JPH05331758 A JP H05331758A
Authority
JP
Japan
Prior art keywords
component
fiber
water
components
polyester
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
JP4157293A
Other languages
Japanese (ja)
Other versions
JP2951109B2 (en
Inventor
Sumio Nakada
純夫 中田
Toshiya Hotta
敏哉 堀田
Mikio Tashiro
幹雄 田代
Masahiko Ikeda
雅彦 池田
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.)
Teijin Ltd
Original Assignee
Teijin 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 Teijin Ltd filed Critical Teijin Ltd
Priority to JP4157293A priority Critical patent/JP2951109B2/en
Publication of JPH05331758A publication Critical patent/JPH05331758A/en
Application granted granted Critical
Publication of JP2951109B2 publication Critical patent/JP2951109B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Multicomponent Fibers (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
  • Nonwoven Fabrics (AREA)
  • Woven Fabrics (AREA)
  • Treatment Of Fiber Materials (AREA)
  • Chemical Or Physical Treatment Of Fibers (AREA)
  • Artificial Filaments (AREA)

Abstract

PURPOSE:To provide a splittable fiber capable of smoothly passing through treating processes before splitting and easily splittable to form ultrafine fibers by splitting treatment. CONSTITUTION:A component of a splittable conjugate fiber is composed of an ethylene terephthalate-type polyester and the other component contains 3-50wt.% of a polyalkylene glycol. The conjugate fiber can be split into individual components by applying a mechanical stress in the presence of water. Since a polyalkylene glycol is compounded to a component of the fiber, a strain is generated on the bonding face of the components by the absorption of water and the swelling with water to facilitate the splitting of the fiber by the application of mechanical stress.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は極細繊維の製造方法に関
する。さらに詳しくは、ポリエステル系の分割型複合繊
維を機械的に処理することによって安定に極細繊維を得
る製造方法に関する。
FIELD OF THE INVENTION The present invention relates to a method for producing ultrafine fibers. More specifically, the present invention relates to a production method for stably obtaining ultrafine fibers by mechanically treating a polyester splittable conjugate fiber.

【0002】[0002]

【従来の技術】一般に細繊度の繊維を使用した不織布、
布帛は、風合がソフト化することは周知のことであり、
かかる極細繊維を得る方法として幾多の提案がなされて
きている。最も有用な方法としては、溶解性の異なる2
種以上のポリマーにより海島型繊維を形成し、海成分を
溶解除去して極細繊維を得る方法が挙げられる。しか
し、かかる方法においては溶剤処理工程や溶剤回収工程
が必要であり、工程的に複雑となる欠点があるし、また
コスト的にも不利である。
2. Description of the Related Art Generally, non-woven fabrics using fine fibers
It is well known that the fabric has a soft texture,
Many proposals have been made as methods for obtaining such ultrafine fibers. The most useful method is 2 with different solubility.
There is a method in which sea-island fibers are formed from at least one kind of polymer, and sea components are dissolved and removed to obtain ultrafine fibers. However, in such a method, a solvent treatment step and a solvent recovery step are required, and there are drawbacks that the process becomes complicated and the cost is disadvantageous.

【0003】また別の方法としては、互いに親和性のな
いポリマー、例えばポリエステル/ポリアミド、ポリエ
ステル/ポリオレフィン、ポリアミド/ポリオレフィン
等からなる複合繊維を、パフ掛け、ニードルパンチン
グ、高圧水流処理等の機械的衝撃により分割極細繊維化
する方法が、特開昭62―133164号公報等に提案
されている。
As another method, a composite fiber composed of polymers having no affinity for each other, for example, polyester / polyamide, polyester / polyolefin, polyamide / polyolefin, etc., is subjected to mechanical shock such as puffing, needle punching, high-pressure water treatment and the like. A method of forming ultrafine fibers by the method described above is proposed in JP-A-62-133164.

【0004】しかしながら、かかる方法により得られる
複合繊維は、ポリマー間の親和性が乏しいため、カード
工程を通過させてウェブを形成する際に成分割れが生じ
て生産性が著しく低下するといった問題がある。さら
に、一方成分として通常ポリアミド又はポリオレフィン
が用いられるがこれらは耐光/耐候性に劣り、また得ら
れる極細繊維も2種類のポリマーからなるために染色工
程が複雑になるとともに不織布等の製品の用途も限定さ
れるといった問題がある。
However, since the composite fiber obtained by such a method has a poor affinity between polymers, there is a problem that component cracking occurs when passing through the card process to form a web, resulting in a marked decrease in productivity. .. Furthermore, although polyamide or polyolefin is usually used as one component, these are inferior in light resistance / weather resistance, and the resulting ultrafine fibers are composed of two kinds of polymers, which complicates the dyeing process and also makes use of products such as nonwoven fabrics. There is a problem of being limited.

【0005】また別の方法として特公昭61―1975
6号公報には、複合繊維の一方成分にポリアルキレング
リコールを配合し、該複合繊維からなる繊維製品に高圧
水流を作用させて該ポリアルキレングリコールを含有す
る成分を破砕除去し、他方成分をフィブリル化(極細繊
維群化)させる方法が提案されている。しかしかかる方
法においては、破砕されたポリマーは最終製品の有効繊
維とはなり得ず除去されるのでコスト的に不利であり、
また破砕されたポリマーが製品から完全には除去されず
に品位を低下させるといった問題がある。
Another method is Japanese Patent Publication No. 61-1975.
No. 6 discloses that one component of a composite fiber is mixed with polyalkylene glycol, a high-pressure water stream is applied to a fiber product made of the composite fiber to crush and remove the component containing the polyalkylene glycol, and the other component is fibril. There has been proposed a method of forming (grouping ultrafine fibers). However, in such a method, the crushed polymer cannot be an effective fiber of the final product and is removed, which is disadvantageous in cost.
Further, there is a problem that the crushed polymer is not completely removed from the product and the quality is degraded.

【0006】[0006]

【発明が解決しようとする課題】本発明は、上記従来技
術の問題点に鑑みなされたもので、その目的は、カード
通過性が良好でしかも機械的応力により容易に分割する
ことができ、得られる極細繊維製品は耐光及び耐候性に
優れ且つ染色等が容易で品位も良好な、新規な極細繊維
の製造方法を提供することにある。
SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned problems of the prior art, and an object of the present invention is to obtain good card passing property and to be easily divided by mechanical stress. It is an object of the present invention to provide a novel method for producing ultrafine fibers, which has excellent light resistance and weather resistance, is easy to dye, and has good quality.

【0007】[0007]

【課題を解決するための手段】本発明者らは、上記目的
を達成するために鋭意検討した結果、複合繊維の両成分
がポリエチレンテレフタレート系ポリエステルからな
り、一方成分にポリアルキレングリコールを含有する分
割型複合繊維は、カード工程通過時は充分な接着性を有
し、一方水存在下ではその接着性が著しく低下して両成
分が容易に剥離分割できることを見い出し本発明に到達
した。
Means for Solving the Problems As a result of intensive studies to achieve the above object, the present inventors have found that both components of the composite fiber are made of polyethylene terephthalate polyester, and one component contains polyalkylene glycol. The present invention has found that the type composite fiber has sufficient adhesiveness when passing through the card process, while its adhesiveness is remarkably reduced in the presence of water so that both components can be easily separated and separated.

【0008】すなわち、本発明によれば、分割型複合繊
維の夫々の成分が主たる繰り返し単位がエチレンテレフ
タレートであるポリエステルからなり、且つ一方成分は
ポリアルキレングリコール類を3〜50重量%(ポリエ
ステルに対して)含有する分割型複合繊維に、水存在下
機械的応力を負荷させるこによって、夫々の成分に分割
することを特徴とする極細繊維の製造方法、が提供され
る。
That is, according to the present invention, each component of the splittable conjugate fiber is composed of a polyester whose main repeating unit is ethylene terephthalate, and one component is 3 to 50% by weight of polyalkylene glycol (based on the polyester). The present invention provides a method for producing an ultrafine fiber, characterized in that the contained splittable conjugate fiber is divided into respective components by applying a mechanical stress in the presence of water.

【0009】本発明で用いられる分割型複合繊維とは、
一方成分が他方成分によって多数に分割されており、該
分割された他方成分は一方成分中に埋没していない繊維
横断面形状を有するものであれば特に限定する必要はな
く、例えば特公昭39―29636号公報、特開昭50
―5650号公報等に開示されている方法により容易に
得ることができる。具体的な横断面形状としては、例え
ば図1(a)〜(e)に示すものがあげられ、なかでも
図1(a)の中空を有するものは、機械的応力が有効に
作用して分割し易くなり、また繊維内部への水浸透が良
好で分割性が一層良好となるので好ましい。
The splittable conjugate fiber used in the present invention is
One component is divided into a large number by the other component, and the divided other component is not particularly limited as long as it has a fiber cross-sectional shape which is not buried in the one component. 29636, Japanese Patent Laid-Open No. Sho 50
It can be easily obtained by the method disclosed in JP-A-5650. Specific cross-sectional shapes include, for example, those shown in FIGS. 1 (a) to 1 (e). Among them, those having a hollow in FIG. 1 (a) are divided by mechanical stress effectively acting. This is preferable because it is easy to do so, and the water penetration into the fiber is good and the splittability is further improved.

【0010】かかる分割型複合繊維を構成する両成分
は、最終的に得られる極細繊維の耐光性及び耐候性の観
点より、主たる繰り返し単位がエチレンテレフタレート
からなるポリエステルである必要があるが、両成分のポ
リエステルは同一であっても異なっていてもよい。なお
ここでいう「主たる」とは80モル%以上がエチレンテ
レフタレート単位からなることをいい、他の成分を20
モル%以下共重合されたポリエステルであってもよい。
好ましく用いられる共重合成分としては、イソフタル
酸、フタル酸、5―ナトリウムスルホイソフタル酸、ナ
フタレンジカルボン酸、4,4′―ジフェニルジカルボ
ン酸等の酸成分、トリメチレングリコール、テトラメチ
レングリコール、ジエチレングリコール、ネオペンチル
グリコール等のジオール成分等をあげることができる。
なかでもイソフタル酸、ネオペンチルグリコール等を共
重合したポリエステルを一方成分のみに用いると、複合
繊維を構成する両成分の熱水収縮率差が大きくなって、
機械的応力による分割が容易になるため好ましい。
Both components constituting such a splittable conjugate fiber must be polyesters whose main repeating unit is ethylene terephthalate from the viewpoints of light resistance and weather resistance of the ultrafine fibers to be finally obtained. The polyesters may be the same or different. The term "mainly" as used herein means that 80 mol% or more is composed of ethylene terephthalate units, and other components are 20%.
It may be a polyester copolymerized by not more than mol%.
As the copolymerization component preferably used, acid components such as isophthalic acid, phthalic acid, 5-sodium sulfoisophthalic acid, naphthalene dicarboxylic acid and 4,4'-diphenyldicarboxylic acid, trimethylene glycol, tetramethylene glycol, diethylene glycol, neo Examples thereof include diol components such as pentyl glycol.
Among them, if the polyester copolymerized with isophthalic acid, neopentyl glycol, etc. is used as only one component, the difference in hot water shrinkage between the two components constituting the composite fiber becomes large,
It is preferable because division by mechanical stress becomes easy.

【0011】次に本発明においては、上記ポリエステル
からなる複合繊維の一方成分にポリアルキレングリコー
ル類を、該成分を構成するポリエステルに対して3〜5
0重量%、好ましくは10〜50重量%含有せしめてい
ることが大切である。ポリアルキレングリコール類の配
合量が3重量%未満の場合には、複合繊維の両成分間の
接着力が増加するためと考えられ、後述する処理を施し
ても剥離分割し難くなり極細繊維が得られなくなる。一
方50重量%を越える場合には、該成分の溶融粘度の低
下が大きくなって安定に製糸できなくなるのみならず、
該成分のタフネスが低下して後述する処理を施す際に、
該成分が粉末状に破砕し易くなるので好ましくない。ま
た、耐光性も低下する。
Next, in the present invention, a polyalkylene glycol is added to one component of the above-mentioned polyester composite fiber, and 3 to 5 relative to the polyester constituting the component.
It is important to contain 0% by weight, preferably 10 to 50% by weight. When the content of the polyalkylene glycol is less than 3% by weight, it is considered that the adhesive force between the two components of the composite fiber is increased, and even if the treatment described below is applied, it becomes difficult to peel and divide to obtain ultrafine fibers. I will not be able to. On the other hand, when it exceeds 50% by weight, not only the melt viscosity of the component is greatly reduced and stable spinning cannot be performed, but also
When the toughness of the component decreases and the treatment described below is performed,
This is not preferable because the component easily breaks into powder. In addition, the light resistance is also reduced.

【0012】なお、他方成分のポリエステルには、実質
的にポリアルキレングリコールが配合されていない方が
望ましいが、本発明の目的を阻害しない範囲内であれば
少量含有せしめてもよい。
It is desirable that the polyester of the other component is substantially not blended with polyalkylene glycol, but it may be contained in a small amount as long as it does not impair the object of the present invention.

【0013】好ましく用いられるポリアルキレングリコ
ール類としては、ポリエチレングリコール、ポリプロピ
レングリコール、ポリテトラメチレングリコール、エチ
レンオキサイド/プロピレンオキサイドブロック又はラ
ンダム共重合体等をあげることができ、これらはアルキ
ル基、アリール基、アシル基等で末端が封鎖されていて
もよく、また各種グリコール成分もしくはアミン成分並
びに酸成分を反応させたブロックポリエーテルエステル
又はブロックポリエーテルアミドであってもよい。なか
でも末端をアルキル基で封鎖したものは、耐光性が良好
となるのでより好ましい。
Polyalkylene glycols preferably used include polyethylene glycol, polypropylene glycol, polytetramethylene glycol, ethylene oxide / propylene oxide block or random copolymers, and these are alkyl groups, aryl groups, The terminal may be blocked with an acyl group or the like, and may be a block polyether ester or a block polyether amide obtained by reacting various glycol components or amine components and acid components. Among them, the one in which the end is blocked with an alkyl group is more preferable because it has good light resistance.

【0014】またこれらのポリアルキレングリコール類
は、平均分子量が5000〜600000のものを用い
ることができるが、5000〜100000、特に50
00〜50000のものが入手の面でより好ましい。5
0000以上のものは安価な方法での重合が困難となっ
てコストが高くなる。
As these polyalkylene glycols, those having an average molecular weight of 5,000 to 600,000 can be used, but 5,000 to 100,000, particularly 50.
It is more preferably from 00 to 50,000 from the viewpoint of availability. 5
If it is 0000 or more, it is difficult to carry out the polymerization by an inexpensive method and the cost becomes high.

【0015】次に上記ポリアルキレングリコール類をポ
リエステルに含有させる方法は、ポリエステルの重合時
に添加する方法、複合繊維を溶融紡糸する際にポリエス
テルチップとポリアルキレングリコール類とを混合した
後に溶融混練する方法、別々に溶融したポリエステルと
ポリアルキレングリコール類とを溶融紡糸する前に混練
する方法等任意の方法を採用することができるが、一般
にポリアルキレングリコール類は耐熱性に劣ること、溶
融紡糸の作業が容易であること等の点から、ポリエステ
ルチップとポリアキレングリコール類とを混合後溶融製
糸することが望ましい。
Next, the method of incorporating the above-mentioned polyalkylene glycols into polyester includes a method of adding during the polymerization of polyester, and a method of melt kneading after mixing polyester chips and polyalkylene glycols during melt spinning of the composite fiber. Any method such as a method in which separately melted polyester and polyalkylene glycols are kneaded before melt spinning can be adopted, but in general, polyalkylene glycols have poor heat resistance, and melt spinning work is From the standpoint of ease and the like, it is desirable that the polyester chips and the polyacetylene glycols be mixed and then melt spun.

【0016】以上に説明した本発明の分割型複合繊維
は、沸水中で20分間処理した時の各成分の熱収縮率差
が2%以上、好ましくは5%以上あることが望ましい。
かかる複合繊維は、後述する処理条件を高温にした場合
には成分間の収縮率差に基づく成分内の界面歪が生じ、
機械的応力により容易に剥離分割できるようになる。ま
た機械的応力による剥離分割が起っていない部分も、乾
燥熱処理される際に剥離分割が進行して品位の良好な極
細製品が得られる。
In the splittable conjugate fiber of the present invention described above, it is desirable that the difference in thermal shrinkage between the components when treated in boiling water for 20 minutes is 2% or more, preferably 5% or more.
Such a composite fiber causes interfacial strain in the component based on the difference in shrinkage between the components when the treatment condition described below is set to a high temperature,
It becomes easy to peel and divide due to mechanical stress. Further, even in a portion where peeling and splitting due to mechanical stress does not occur, peeling and splitting progresses during dry heat treatment, and an ultrafine product of good quality can be obtained.

【0017】本発明においては、上述した複合繊維に、
水存在下機械的応力を作用させることが大切である。水
が実質的に存在しない場合には、機械的応力を負荷させ
ても成分間の剥離分割は進行し難く、充分な分割を達成
するためには極めて大きな応力を負荷させなければなら
ず得られる製品の品位が低下するので好ましくない。水
の温度は高温であるほど、応力による剥離分割が容易に
なるのでより好ましい。
In the present invention, the above-mentioned composite fiber is
It is important to apply mechanical stress in the presence of water. When water is not substantially present, exfoliation and splitting between components is difficult to proceed even when mechanical stress is applied, and extremely large stress must be applied to achieve sufficient splitting. This is not preferable because the quality of the product is degraded. The higher the temperature of water is, the easier the separation by peeling due to stress is, which is more preferable.

【0018】水を存在させる方法は特に限定されず、機
械的応力を負荷させる前の段階、例えば水に浸漬して極
細繊維にあらかじめ水を吸着させてもよく、あるいは応
力を負荷させる際に同時に水を付与してもよい。具体的
には、例えば短繊維からのカード法、クロスラッパー
法、ランダムウエバー法又は長繊維フィラメントからの
スパンボンド法等の不織布形成法により作成した不織布
を水に浸漬した後にニードルパンチングする方法、上記
不織布を水に浸漬することなく高圧水流でウォーターニ
ードリングする方法、さらには、布帛となした後に染色
・パフ掛けする方法等を例示することができる。
The method of allowing water to be present is not particularly limited, and water may be adsorbed to the ultrafine fibers in advance before mechanical stress is applied, for example, by immersing in water, or at the same time when stress is applied. Water may be added. Specifically, for example, a card method from short fibers, a cross wrapper method, a random weber method or a method of needle punching after immersing a nonwoven fabric prepared by a nonwoven fabric forming method such as a spun bond method from long fiber filaments in water, Examples of the method include a method of water-needing a non-woven fabric with a high-pressure water stream without immersing it in water, and a method of dyeing and puffing after forming a fabric.

【0019】なお、本発明に用いられる複合繊維は得ら
れる極細繊維の繊度が0.8デニール以下となる範囲内
で0.5〜20デニールとするのが望ましく、また機械
的応力を負荷して剥離分割させる以前の段階、特に製糸
の段階では、できるだけ水分を付与しないことが望まし
く、水中に浸漬する必要がある場合には時間を可及的に
短くするとともに早く乾燥することが望ましい。
The composite fiber used in the present invention preferably has a fineness of the obtained ultrafine fiber of 0.5 to 20 denier within a range of 0.8 denier or less, and is subjected to mechanical stress. In the stage before the separation and division, especially in the stage of the yarn making, it is desirable that moisture is not applied as much as possible, and when it is necessary to immerse in water, it is desirable to shorten the time as much as possible and dry it quickly.

【0020】[0020]

【発明の作用効果】本発明が対象とする分割型複合繊維
は、一方成分に3〜50重量%のポリアルキレングリコ
ール類が配合されたポリエチレンテレフタレート系ポリ
エステルを用いているので、水処理することによつ吸水
膨潤し、他方成分のポリアルキレングリコール類が実質
的に配合されていないポリエチレンテレフタレート系ポ
リエステルとの接合面に歪が発生し、その結果機械的応
力の負荷により界面が容易に剥離されて、複合繊維の夫
々の成分が極細繊維となるのである。このことは、図2
に添付した分割剥離後の繊維形態写真からも裏付けられ
ている。
The splittable conjugate fiber which is the object of the present invention uses polyethylene terephthalate polyester in which one component contains 3 to 50% by weight of polyalkylene glycol. Due to water absorption and swelling, distortion occurs on the joint surface with the polyethylene terephthalate-based polyester in which the other component polyalkylene glycol is not substantially blended, and as a result, the interface is easily peeled off due to the load of mechanical stress. Each component of the composite fiber becomes an ultrafine fiber. This is shown in FIG.
It is also supported by the photograph of the fiber morphology after the split peeling attached to.

【0021】かかる本発明により得られる極細繊維は、
従来とは異なって全成分がポリエチレンテレフタレート
系ポリエステルよりなるので、染色が容易、耐光性及び
耐候性に優れ、且つ耐熱性も良好であるといった特徴を
有する。しかも本発明にかかる複合繊維は、カード工
程、不織布製造工程等の如き実質的に水が付着していな
い工程では、機械的応力が負荷されてもほとんど成分割
れが発生せず工程通過性が良好であるといった特徴をも
有し、その工業的価値は極めて高い。
The ultrafine fibers obtained by the present invention are:
Since all the components are made of polyethylene terephthalate polyester unlike the conventional ones, they are characterized by easy dyeing, excellent light resistance and weather resistance, and good heat resistance. Moreover, the composite fiber according to the present invention has a good process-passing property even in the process where substantially no water is adhered, such as a card process and a non-woven fabric manufacturing process, in which component cracking hardly occurs even when mechanical stress is applied. It also has the characteristic that it has an extremely high industrial value.

【0022】[0022]

【実施例】以下実施例にて本発明をさらに詳しく説明す
る。なお、沸水収縮率差は下記の方法にしたがって測定
した。 沸水収縮率差 複合短繊維からなる目付20g/m2 のウェッブを沸水
中に20分間浸漬処理した後、直径0.1mmの孔が
0.6mmピッチで1列に並んだ噴射ノズルから圧力1
20kg/cm2 で柱状水流を噴きあて、剥離した繊維
の繊維長分布から収縮率差を求めた。
The present invention will be described in more detail with reference to the following examples. The difference in shrinkage rate of boiling water was measured according to the following method. Difference in shrinkage rate of boiling water After immersing a web made of composite short fibers and having a basis weight of 20 g / m 2 in boiling water for 20 minutes, pressure 1 was applied from a jet nozzle in which holes with a diameter of 0.1 mm were arranged in a row at a pitch of 0.6 mm.
A columnar water stream was sprayed at 20 kg / cm 2 , and the shrinkage ratio difference was obtained from the fiber length distribution of the separated fibers.

【0023】[0023]

【実施例1】分割型複合繊維の一方成分Aとしてポリエ
チレンテレフタレート(固有粘度0.63)とポリエチ
レングリコール(分子量20000)とを重量比100
/11.1の割合で混合したもの、他方成分Bとしてポ
リエチレンテレフタレート(固有粘度0.63)を用
い,夫々を真空吸引可能なルーダーで溶融し、重量比1
/1で図1(a)に示す横断面形状を有する複合繊維に
紡糸し、1000m/分の速度で引き取って未延伸糸を
得た。
Example 1 Polyethylene terephthalate (intrinsic viscosity 0.63) and polyethylene glycol (molecular weight 20000) were used as one component A of the splittable conjugate fiber in a weight ratio of 100.
/ 11. 1 mixed with polyethylene terephthalate (intrinsic viscosity 0.63) as the other component B, each of which was melted in a vacuum suction ruder to give a weight ratio of 1
An undrawn yarn was obtained by spinning a composite fiber having a cross-sectional shape shown in FIG. 1 (a) at a speed of 1/1 and taking it up at a speed of 1000 m / min.

【0024】この未延伸糸を引き揃えて延伸温度80℃
で3.0倍に延伸し、油剤を付与した後捲縮を付与し、
次いで90℃20分間弛緩熱処理して単糸繊度2デニー
ル、繊維長51mmの短繊維を得た。
The undrawn yarns are drawn together and drawn at a drawing temperature of 80 ° C.
Stretching to 3.0 times with, and applying crimp after applying oil agent,
Then, relaxation heat treatment was performed at 90 ° C. for 20 minutes to obtain short fibers having a single yarn fineness of 2 denier and a fiber length of 51 mm.

【0025】得られた短繊維を紡績、織工程を通した
後、130℃下で染色し引き続いてパフ処理を施した。
その結果、上記の工程通過性は良好で、得られた布帛を
顕微鏡で観察すると、約98%の繊維(極細繊維形成成
分)が剥離分割させており、布帛の風合は極めて良好で
あった。
The short fibers obtained were passed through a spinning and weaving process, dyed at 130 ° C. and subsequently subjected to puffing.
As a result, the above-mentioned process passability was good, and when the obtained cloth was observed with a microscope, about 98% of the fibers (ultrafine fiber-forming components) were separated and separated, and the texture of the cloth was extremely good. ..

【0026】[0026]

【比較例1】一方成分Aとして、ナイロン6(固有粘度
1.34)を用いる以外は実施例1と同様に行なったと
ころ、紡績工程、織工程で成分割れが発生し、安定に布
帛を得ることが困難であった。
Comparative Example 1 On the other hand, the same procedure as in Example 1 was carried out except that nylon 6 (intrinsic viscosity 1.34) was used as the component A. As a result, component cracking occurred in the spinning and weaving processes, and a stable fabric was obtained. Was difficult.

【0027】[0027]

【比較例2】一方成分Aとして、ポリエチレングリコー
ルの配合量が2重量%のものを用いる以外は実施例1と
同様に行なった。その結果、紡績及び製織工程の通過性
は良好であるものの、極細繊維への分割がほとんど進行
せず、得られた布帛の風合は硬いものであった。
Comparative Example 2 On the other hand, the same procedure as in Example 1 was carried out except that as the component A, a polyethylene glycol compounding amount of 2% by weight was used. As a result, although the passability in the spinning and weaving processes was good, the division into ultrafine fibers hardly proceeded, and the obtained fabric had a hard texture.

【0028】[0028]

【実施例2】他方成分Bとしてイソフタル酸成分を10
モル%(全酸成分に対して)共重合した固有粘度0.6
4のポリエチレンテレフタレート糸ポリエステルを用い
る以外は実施例1と同様にして複合繊維を得た。
Example 2 On the other hand, as the component B, 10 parts of an isophthalic acid component were used.
Mol% (based on all acid components) Copolymerized intrinsic viscosity 0.6
A composite fiber was obtained in the same manner as in Example 1 except that the polyethylene terephthalate yarn polyester of 4 was used.

【0029】得られた短繊維を、ローラーカード(60
m/分)に通して目付20g/m2のウェッブとなし、
次いで直径0.1mmの孔が0.6mmピッチで1列に
配列した噴射ノズル群から圧力120kg/cm2 で柱
状水流を噴き当てる処理を3回繰り返して絡合させた
後、160℃で20分間熱風乾燥した。
The obtained staple fibers were put into a roller card (60
m / min) to make a web with a basis weight of 20 g / m 2 .
Then, a process of spraying a columnar water stream at a pressure of 120 kg / cm 2 from a group of jet nozzles in which holes having a diameter of 0.1 mm are arranged in a row at a pitch of 0.6 mm is repeated three times to entangle, and then at 160 ° C. for 20 minutes. It was dried with hot air.

【0030】得られたシートを顕微鏡で観察したとこ
ろ、約95%の繊維が剥離分割されていた。
When the obtained sheet was observed with a microscope, about 95% of the fibers were separated and separated.

【0031】なお、複合繊維の両成分の沸水収縮率差
は、A成分の方の繊維長が50.6mm、B成分の方が
48mmで5.1%であった。
The difference in boiling water shrinkage between the two components of the composite fiber was 5.1% when the fiber length of the A component was 50.6 mm and that of the B component was 48 mm.

【0032】[0032]

【比較例3】一方成分Aとして固有粘度が0.63のポ
リエチレンテレフタレート単独を用いる以外は実施例2
と同様に行なった。その結果、カード通過性は良好なる
も、極細繊維への分割がほとんど認められず、得られた
シートの風合は劣ったものであった。
Comparative Example 3 Example 2 except that polyethylene terephthalate having an intrinsic viscosity of 0.63 alone is used as the component A
It carried out similarly to. As a result, although the card passing property was good, almost no division into ultrafine fibers was observed, and the obtained sheet had a poor texture.

【0033】[0033]

【実施例3】成分Aとしてポリエチレングリコールの配
合量を5重量%のものを用いる以外は実施例2と同様に
行なった。得られたシートを顕微鏡で観察したところ約
90%の繊維が、剥離分割されていた。
Example 3 The same procedure as in Example 2 was carried out except that polyethylene glycol was used as the component A in an amount of 5% by weight. When the obtained sheet was observed with a microscope, about 90% of the fibers were separated and separated.

【0034】なお複合繊維の両成分の沸水収縮率差はA
成分の方の繊維長が50.8mmB成分の方が48mm
で5.5%であった。
The difference in shrinkage of boiling water between the two components of the composite fiber is A
Fiber length of component is 50.8mm B component is 48mm
Was 5.5%.

【0035】[0035]

【実施例4】成分Aとしてポリエチレングリコールの配
合量を45重量%のものを用いる以外は実施例2と同様
に行なった。得られたシートを顕微鏡で観察したところ
約97%の繊維が、剥離分割されていた。
Example 4 Example 4 was repeated except that polyethylene glycol was used as the component A in an amount of 45% by weight. When the obtained sheet was observed with a microscope, about 97% of the fibers were separated and separated.

【0036】なお複合繊維の両成分の沸水収縮率差はA
成分の繊維長が50.9mm B成分の方が48mmで
5.7%であった。
The difference in shrinkage rate of boiling water between the two components of the composite fiber is A
The fiber length of the component was 50.9 mm, and that of the B component was 48 mm, which was 5.7%.

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

【図1】(a)〜(e)は本発明で用いられる分割型複
合繊維の一例を示す横断面形状である。
1A to 1E are cross-sectional shapes showing an example of a splittable conjugate fiber used in the present invention.

【図2】実施例2で得られた複合繊維の、極細繊維への
分割を示す2000倍の走査型電子顕微鏡写真である。
FIG. 2 is a scanning electron micrograph (× 2000) showing the division of the conjugate fiber obtained in Example 2 into ultrafine fibers.

【符号の説明】[Explanation of symbols]

1 分割型複合繊維の一方成分 2 分割型複合繊維の他方成分 3 中空部 1 component of splittable conjugate fiber 2 other component of splittable conjugate fiber 3 hollow part

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 D01F 8/14 D 7199−3B D03D 15/00 F 7199−3B D04H 1/46 A 7199−3B D06C 11/00 Z D06M 11/05 11/84 (72)発明者 池田 雅彦 愛媛県松山市北吉田町77番地 帝人株式会 社松山事業所内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Internal reference number FI Technical display location D01F 8/14 D 7199-3B D03D 15/00 F 7199-3B D04H 1/46 A 7199-3B D06C 11/00 Z D06M 11/05 11/84 (72) Inventor Masahiko Ikeda 77 Kitayoshidacho, Matsuyama City, Ehime Prefecture Teijin Limited Matsuyama Office

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 分割型複合繊維の夫々の成分が主たる繰
り返し単位がエチレンテレフタレートであるポリエステ
ルからなり、且つ一方成分はポリアルキレングリコール
類を3〜50重量%(ポリエステルに対して)含有する
分割型複合繊維に、水存在下機械的応力を負荷させるこ
によって、夫々の成分に分割することを特徴とする極細
繊維の製造方法。
1. A split-type composite fiber in which each component of the split-type conjugate fiber comprises a polyester whose main repeating unit is ethylene terephthalate, and one component of which contains 3 to 50% by weight (based on polyester) of a polyalkylene glycol. A method for producing an ultrafine fiber, characterized in that the composite fiber is divided into respective components by applying a mechanical stress in the presence of water.
【請求項2】 分割型複合繊維を構成する両成分の沸水
収縮率が2%以上異なる請求項1記載の極細繊維の製造
方法。
2. The method for producing ultrafine fibers according to claim 1, wherein the boiling water shrinkage ratios of both components constituting the splittable conjugate fiber differ by 2% or more.
JP4157293A 1992-05-26 1992-05-26 Production method of ultrafine fiber Expired - Fee Related JP2951109B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4157293A JP2951109B2 (en) 1992-05-26 1992-05-26 Production method of ultrafine fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4157293A JP2951109B2 (en) 1992-05-26 1992-05-26 Production method of ultrafine fiber

Publications (2)

Publication Number Publication Date
JPH05331758A true JPH05331758A (en) 1993-12-14
JP2951109B2 JP2951109B2 (en) 1999-09-20

Family

ID=15646497

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4157293A Expired - Fee Related JP2951109B2 (en) 1992-05-26 1992-05-26 Production method of ultrafine fiber

Country Status (1)

Country Link
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006183158A (en) * 2004-12-27 2006-07-13 Unitika Ltd Method for producing filament nonwoven fabric
JP2006322085A (en) * 2005-05-17 2006-11-30 Toray Ind Inc Splittable conjugate fiber
CN102517884A (en) * 2011-12-27 2012-06-27 厦门保视丽无尘科技有限公司 Method for manufacturing completely split superfine fiber cleaning cloth

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58197369A (en) * 1982-05-13 1983-11-17 東レ株式会社 Fibrilation of sheet constituting fiber

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58197369A (en) * 1982-05-13 1983-11-17 東レ株式会社 Fibrilation of sheet constituting fiber

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006183158A (en) * 2004-12-27 2006-07-13 Unitika Ltd Method for producing filament nonwoven fabric
JP2006322085A (en) * 2005-05-17 2006-11-30 Toray Ind Inc Splittable conjugate fiber
JP4736531B2 (en) * 2005-05-17 2011-07-27 東レ株式会社 Split fiber type composite fiber
CN102517884A (en) * 2011-12-27 2012-06-27 厦门保视丽无尘科技有限公司 Method for manufacturing completely split superfine fiber cleaning cloth

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