JPH0819571B2 - Multi-component fiber suitable for producing fine fiber bundle and method for producing the same - Google Patents
Multi-component fiber suitable for producing fine fiber bundle and method for producing the sameInfo
- Publication number
- JPH0819571B2 JPH0819571B2 JP61251543A JP25154386A JPH0819571B2 JP H0819571 B2 JPH0819571 B2 JP H0819571B2 JP 61251543 A JP61251543 A JP 61251543A JP 25154386 A JP25154386 A JP 25154386A JP H0819571 B2 JPH0819571 B2 JP H0819571B2
- Authority
- JP
- Japan
- Prior art keywords
- component
- polyvinyl alcohol
- fiber
- melt
- log
- 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.)
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Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は溶融紡糸法で水処理により微細繊維束の製造
ができる多成分繊維を製造することに関する。TECHNICAL FIELD The present invention relates to the production of multi-component fibers capable of producing fine fiber bundles by water treatment by melt spinning.
従来、溶剤に対する溶解性の異なる2種または2種以
上のポリマーからなる多成分繊維の製造並びに該多成分
繊維から1成分ポリマーを除去して微細繊維束を製造す
ることは、皮革様シートの構成に利用するため多くの提
案がなされている。しかるに、従来の多成分繊維から微
細繊維を製造する方法は主として有機溶剤処理法がもつ
ぱら行われていた。Conventionally, the production of a multi-component fiber composed of two or more polymers having different solubilities in a solvent and the production of a fine fiber bundle by removing the one-component polymer from the multi-component fiber is a constitution of a leather-like sheet. Many proposals have been made for use in. However, the conventional method for producing fine fibers from multi-component fibers has been mainly performed by the organic solvent treatment method.
また、ポリビニルアルコールを一成分とし、他のポリ
マーと共通溶剤に溶解して湿式法で混合紡糸し、混合繊
維を作ることは既に特公昭42−27268号公報、特公昭41
−3759号公報その他に提案されている。Further, it is already known that the polyvinyl alcohol as one component is dissolved in a common solvent together with another polymer and mixed and spun by a wet method to prepare a mixed fiber, as described in JP-B-42-27268 and JP-B-41.
It is proposed in the Japanese Patent No. 3759 and others.
従来の多成分繊維から微細繊維束を製造する場合、微
細繊維の相が明瞭になることが前提になる。そのためは
もつぱら溶融紡糸法でチツプ混合、溶融流混合などによ
る混合または口金部あるいは紡糸頭で規制して混合相を
形成などによつて紡糸したいわゆる多成分繊維が用いら
れてきた。しかし、溶融紡糸法で得た多成分繊維から微
細繊維を作るには分散媒成分を溶剤で溶解するあるいは
分散剤で分解するなどの処理法で処理されてきた。しか
し、使用する溶剤や分解剤は有機溶剤であつたり、強ア
ルカリあるいは強酸またはそれらの塩と有機溶剤との組
み合わせであつたりして、工業的には膨大な設備を必要
とするばかりではなく、更に処理後の溶剤等の処理剤の
処理にも多大な設備が必要となる。When producing a fine fiber bundle from conventional multi-component fibers, it is premised that the fine fiber phase becomes clear. For that purpose, so-called multi-component fibers have been used which have been mixed by chip mixing, melt flow mixing, etc. by the motsu-para melt spinning method or spun by forming a mixed phase by controlling at the spinneret part or the spinning head. However, in order to form fine fibers from multi-component fibers obtained by the melt spinning method, a treatment method such as dissolving a dispersion medium component with a solvent or decomposing it with a dispersant has been used. However, the solvent or decomposing agent used is an organic solvent, or a combination of a strong alkali or a strong acid or a salt thereof and an organic solvent, which not only requires enormous facilities industrially, Furthermore, a large amount of equipment is required for treating the treating agent such as the solvent after the treatment.
一方、ポリビニルアルコールを一成分とした湿式紡糸
法で得た多成分繊維は溶融紡糸法で得た多成分繊維のよ
うに分散状態が良いものではなく、不均一分散状態であ
つたり、極めて微細な分散状態であつたりして、独立性
の良好な微細繊維束が得られない。また、分散成分の独
立性を良好なものとしようとすると、分散媒成分である
ポリビニルアルコールを除去すると、残つた分散成分で
ある微細繊維束の繊維強力が極端に低下してしまい、通
常実用になる不織布を得ることは難かしい。On the other hand, the multi-component fiber obtained by the wet spinning method using polyvinyl alcohol as one component is not in a good dispersed state like the multi-component fiber obtained by the melt spinning method, and is in a non-uniform dispersed state, or is extremely fine. In the dispersed state, fine fiber bundles having good independence cannot be obtained. Further, when trying to make the independence of the dispersion component good, when the polyvinyl alcohol that is the dispersion medium component is removed, the fiber strength of the fine fiber bundle that is the remaining dispersion component extremely decreases, and it is usually used in practice. It is difficult to obtain a non-woven fabric.
本発明は、ポリビニルアルコールまたは変性ポリビニ
ルアルコールを溶融紡糸法で紡糸することができ、更に
他の溶融紡糸性ポリマーと共に溶融紡糸法で多成分繊維
が製造できる特定のポリビニルアルコールまたは変性ポ
リビニルアルコールを用いた多成分繊維を提供するにあ
る。更に、多成分繊維からポリビニルアルコールまたは
変性ポリビニルアルコールを水で溶出でき、残留ポリマ
ー成分繊維は分離性の良好な微細繊維束を形成し、かつ
通常の実用上支障を来たさない十分な強力、更にそれ以
上の強力を有する微細繊維束の繊維製品が得られるポリ
ビニルアルコールまたは変性ポリビニルアルコールを分
散媒成分とした多成分繊維を提供するにある。INDUSTRIAL APPLICABILITY The present invention uses a specific polyvinyl alcohol or modified polyvinyl alcohol capable of spinning polyvinyl alcohol or modified polyvinyl alcohol by a melt spinning method and further capable of producing a multi-component fiber by a melt spinning method together with another melt-spinning polymer. Providing multi-component fibers. Furthermore, polyvinyl alcohol or modified polyvinyl alcohol can be eluted from the multi-component fiber with water, the residual polymer component fiber forms a fine fiber bundle with good separability, and has sufficient strength that does not hinder ordinary practical use, It is another object of the present invention to provide a multi-component fiber containing polyvinyl alcohol or modified polyvinyl alcohol as a dispersion medium component, which gives a fiber product of a fine fiber bundle having a higher strength.
すなわち、本発明はケン化度が50〜98モル%であつ
て、ケン化度Xモル%と重合度Pとの関係がlog X+log
P=3.7〜4.3にあるポリビニルアルコールまたは変性ポ
リビニルアルコールを分散媒成分とし、該分散媒成分と
は溶剤に対する溶解性を異にするポリマーを分散成分と
し、これら分散媒成分と分散成分からなることを特徴と
する微細繊維束の製造に適した溶融紡糸多成分繊維であ
る。That is, in the present invention, the saponification degree is 50 to 98 mol%, and the relationship between the saponification degree X mol% and the polymerization degree P is log X + log.
A polyvinyl alcohol or a modified polyvinyl alcohol having P = 3.7 to 4.3 is used as a dispersion medium component, a polymer having a different solubility to a solvent from the dispersion medium component is used as a dispersion component, and the dispersion medium component and the dispersion component are composed. It is a melt-spun multi-component fiber suitable for producing a characteristic fine fiber bundle.
更に、本発明はケン化度が50〜98モル%であつて、ケ
ン化度Xモル%と重合度Pとの関係がlog X+log P=3.
7〜4.3にあるポリビニルアルコールまたは変性ポリビニ
ルアルコールを分散媒成分とし、該分散媒成分とは溶剤
に対する溶解性を異にし、かつ溶融紡糸性を有するポリ
マーを分散成分として溶融紡糸することを特徴とする微
細繊維束の製造に適した多成分繊維の製造法である。Further, in the present invention, the saponification degree is 50 to 98 mol%, and the relationship between the saponification degree X mol% and the polymerization degree P is log X + log P = 3.
7 to 4.3 polyvinyl alcohol or modified polyvinyl alcohol as a dispersion medium component, the dispersion medium component is different in solubility in a solvent, and is melt-spun as a dispersion component polymer having melt spinnability This is a method for producing a multi-component fiber suitable for producing a fine fiber bundle.
本発明で使用する溶融紡糸可能であつて、かつ他の溶
融紡糸性ポリマーと溶融紡糸されるポリビニルアルコー
ルまたは変性ポリビニルアルコールは溶融紡糸性並びに
紡糸時の溶融粘度および多成分繊維にしてからの水溶解
性の関係から重合度およびケン化度が大きく影響し、と
りわけ多成分繊維の相を安定させるうえからも重合度と
ケン化度が特定の範囲にすることが重要であることを見
出した。すなわち、本発明で使用するポリビニルアルコ
ールまたは変性ポリビニルアルコールの重合度Pとモル
%で表わしたケン化度Xとの関係が、ケン化度50〜98モ
ル%の範囲においてlog X+log P=3.7〜4.3を満足した
ポリマーであり、この条件を満足したポリビニルアルコ
ールまたは変性ポリビニルアルコールを使用することに
よつて、溶融紡糸法で多成分繊維を安定に紡糸すること
ができ、更に、多成分繊維からポリビニルアルコールま
たは変性ポリビニルアルコールを水で溶解除去すること
ができると共に、残留ポリマー成分の微細繊維束の強力
も、繊維束として測定して1.0g/dr以上の高いものとな
る。Polyvinyl alcohol or modified polyvinyl alcohol that is melt-spinnable and melt-spun with other melt-spinnable polymers used in the present invention has melt-spinnability and melt viscosity during spinning and water-solubility after being made into multi-component fibers. It has been found that the degree of polymerization and the degree of saponification have a great influence from the relationship of sex, and that the degree of polymerization and the degree of saponification are important to stabilize the phase of the multi-component fiber. That is, the relationship between the degree of polymerization P of the polyvinyl alcohol or modified polyvinyl alcohol used in the present invention and the degree of saponification X expressed in mol% is log X + log P = 3.7 to 4.3 in the range of the saponification degree of 50 to 98 mol%. By using polyvinyl alcohol or modified polyvinyl alcohol that satisfies this condition, multicomponent fibers can be stably spun by the melt spinning method. Alternatively, the modified polyvinyl alcohol can be dissolved and removed with water, and the strength of the fine fiber bundle of the residual polymer component is as high as 1.0 g / dr or more when measured as a fiber bundle.
また、ポリビニルアルコールまたは変性ポリビニルア
ルコールのケン化度が50モル%未満では融点は低下する
が、水溶解性が低下する。一方、ケン化度が98モル%を
超えたものでは融点および溶融粘度が急激に上昇して、
たとえ重合度を低下させたポリマーでも安定な溶融紡糸
ができなくなる。従つて、log X+log Pの関係式の数値
を満足しない範囲のポリビニルアルコールまたは変性ポ
リビニルアルコールを使用すると、安定な相の形成がで
きないとか、安定な溶融紡糸ができないとか、水溶解性
が悪くなるとかの好ましくない状態になる。Further, when the saponification degree of polyvinyl alcohol or modified polyvinyl alcohol is less than 50 mol%, the melting point is lowered but the water solubility is lowered. On the other hand, if the degree of saponification exceeds 98 mol%, the melting point and melt viscosity will rise sharply,
Even if the degree of polymerization is lowered, stable melt spinning cannot be performed. Therefore, if polyvinyl alcohol or modified polyvinyl alcohol in a range not satisfying the relational expression of log X + log P is used, a stable phase cannot be formed, stable melt spinning cannot be performed, or water solubility is deteriorated. It becomes an unfavorable state.
本発明で使用するポリビニルアルコールはケン化度50
〜98モル%、重合度400以下のポリマーであり、また、
変性ポリビニルアルコールは酢酸アリルを共重合、末端
パラフイン変性等の共重合あるいは末端変性の水溶性変
性ポリビニルアルコールでケン化度50〜98モル%、重合
度400以下のポリマーである。The polyvinyl alcohol used in the present invention has a saponification degree of 50.
~ 98 mol%, a polymer having a degree of polymerization of 400 or less,
The modified polyvinyl alcohol is a polymer having a saponification degree of 50 to 98 mol% and a polymerization degree of 400 or less, which is a water-soluble modified polyvinyl alcohol copolymerized with allyl acetate, modified by terminal paraffin modification, or modified by terminal modification.
また、本発明の多成分繊維を構成する他の溶融紡糸性
ポリマーとしては、溶融時にポリビニルアルコールまた
は変性ポリビニルアルコールと反応しないあるいは反応
性が小さい熱可塑性ポリマーであり、例えば、ポリエチ
レン、ポリプロピレン、ポリブチレン等のポリオレフイ
ンまたは共重合ポリオレフイン。ナイロン−610、ナイ
ロン−11、ナイロン−12、ナイロン−6−66、ナイロン
−6等のポリアミド。ポリブチレンテレフタレート、ポ
リエチレンテレフタレートまたは共重合ポリエチレンテ
レフタレート等のポリエステル、ポリウレタンエラスト
マー、ポリエステルエラストマー、ポリアミドエラスト
マーなどから選ばれた1種類または2種類以上のポリマ
ーであり、好ましくは融点270℃以下の熱可塑性ポリマ
ーである。The other melt-spinnable polymer that constitutes the multi-component fiber of the present invention is a thermoplastic polymer that does not react with polyvinyl alcohol or modified polyvinyl alcohol during melting or has low reactivity, such as polyethylene, polypropylene and polybutylene. Polyolefin or copolymerized polyolefin. Polyamides such as nylon-610, nylon-11, nylon-12, nylon-6-66, nylon-6. One or more polymers selected from polyesters such as polybutylene terephthalate, polyethylene terephthalate or copolymerized polyethylene terephthalate, polyurethane elastomers, polyester elastomers, polyamide elastomers, etc., preferably thermoplastic polymers having a melting point of 270 ° C. or less. is there.
そして、ポリビニルアルコールまたは変性ポリビニル
アルコールと熱可塑性ポリマーとの溶融紡糸法は両ポリ
マーを同一溶融系で溶融混合して紡糸する方法。別々の
溶融系で溶融し、紡糸頭で両ポリマーの混合流を形成し
て紡糸する方法。口金部で分散成分と分散成分を規制し
て紡糸する方法のいずれの方法でも紡糸できるが、両ポ
リマーが熱時に反応性を有する場合には後者の紡糸法が
好ましい。また、多成分繊維の分散成分数(微細繊維
数)を多くしようとする場合には前者の紡糸法が好まし
い。そして、溶融紡糸においてポリビニルアルコールま
たは変性ポリビニルアルコールを分散媒成分とするため
には、関係log X+log P=3.7〜4.3の範囲において選ば
れたポリビニルアルコールまたは変性ポリビニルアルコ
ールであつて、組み合わせるポリマーの溶融粘度より低
い溶融粘度のポリマーを使用することが好ましい。The melt spinning method of polyvinyl alcohol or modified polyvinyl alcohol and a thermoplastic polymer is a method in which both polymers are melt mixed in the same melting system and spun. A method of spinning by melting in separate melting systems and forming a mixed flow of both polymers at the spinning head. Spinning can be carried out by any method of spinning with the disperse component and the dispersive component being regulated by the spinneret, but the latter spinning method is preferred when both polymers have reactivity when heated. The former spinning method is preferable when the number of dispersed components (the number of fine fibers) of the multi-component fiber is to be increased. In order to use polyvinyl alcohol or modified polyvinyl alcohol as a dispersion medium component in melt spinning, the polyvinyl alcohol or modified polyvinyl alcohol selected in the range of the relation log X + log P = 3.7 to 4.3, and the melt viscosity of the polymer to be combined. It is preferred to use lower melt viscosity polymers.
本発明の多成分繊維はポリビニルアルコールまたは変
性ポリビニルアルコールが分散媒成分(海成分、鞘成分
を包括して称する)となり、他のポリマーが多数の分散
成分(島成分、芯成分を包括して称する)となつた繊維
である。そして、多成分繊維からポリビニルアルコール
または変性ポリビニルアルコールを水で溶解除去すると
残留ポリマー成分繊維は微細繊維束となる。ポリビニル
アルコールまたは変性ポリビニルアルコールを水で溶解
するには通常の水または温水で処理することでもよい
が、溶解除去を工業的に有利に進めるためには界面活性
剤を添加して表面張力を50dyne/cm以下、好ましくは40d
yne/cm以下に調整した水であらかじめ処理することが好
ましい。In the multi-component fiber of the present invention, polyvinyl alcohol or modified polyvinyl alcohol serves as a dispersion medium component (collectively includes sea component and sheath component), and other polymers collectively include a large number of dispersion components (island component and core component). ) Is a fiber that has been. When the polyvinyl alcohol or modified polyvinyl alcohol is dissolved and removed from the multi-component fiber with water, the residual polymer component fiber becomes a fine fiber bundle. In order to dissolve polyvinyl alcohol or modified polyvinyl alcohol in water, it may be treated with normal water or warm water, but in order to industrially proceed with dissolution removal, a surfactant is added to adjust the surface tension to 50 dyne / cm or less, preferably 40d
Pretreatment with water adjusted to yne / cm or less is preferable.
本発明の多成分繊維は織布、編布、不織布、絡合処理
された不織布などの繊維シート、あるいは繊維シートに
は弾性ポリマーを含有せしめて得た繊維質シートとした
後、ポリビニルアルコールまたは変性ポリビニルアルコ
ールを溶解除去することによつて微細繊維束からなる繊
維シートあるいは繊維質シートが得られ、嵩高性の製
品、柔軟な製品が得られる。更に短繊維にして紙の製造
に使用すると地合いの良好な紙が得られる。また、フロ
ツク加工用パイル、皮革様シートの製造用繊維、フイル
ター用繊維等多岐にわたる用途がある。The multi-component fiber of the present invention is a woven fabric, knitted fabric, non-woven fabric, entangled non-woven fabric or other fibrous sheet, or a fibrous sheet obtained by containing an elastic polymer in the fibrous sheet, and then polyvinyl alcohol or modified By dissolving and removing polyvinyl alcohol, a fiber sheet or a fibrous sheet composed of fine fiber bundles can be obtained, and a bulky product and a flexible product can be obtained. When it is further made into short fibers and used in the production of paper, a paper having a good texture can be obtained. It also has a wide variety of uses such as piles for flocking, fibers for manufacturing leather-like sheets, and fibers for filters.
以下、本発明の実施態様を実施例で具体的に説明す
る。なお、実施例中部および%はことわりのない限り重
量に関するものである。Hereinafter, embodiments of the present invention will be specifically described with reference to examples. In the examples, "parts" and "%" relate to weight unless otherwise specified.
実施例1 温度60℃の減圧乾燥機中で24時間乾燥した重合度110
(log P=2.04)、ケン化度67モル%=(log X=1.83)
のポリビニルアルコール(log X+log P=3.87)50部と
メルトインデツク(以下MIとする)10のポリプロピレン
50部とをペレツト状で十分混合し、直径25mmのスクリユ
ーエクストルーダー紡糸機を用い、紡糸機のスクリユー
後部以後紡糸口金までの温度を230℃に調整し、ノズル
孔径0.3mm、孔数48ホールの口金を用いて溶融紡糸し、
吐出した糸条は口金直下に設けられた冷却風帯によつて
急冷して捲き取つた。吐出量30g/分、捲き取り速度450m
/分で紡糸し、単糸繊度約12デニールの多成分繊維を得
た。この多成分繊維の放流糸の断面を顕微鏡写真に撮影
して分散相の状態を観察した結果、明確な海島構造の形
状を示しており、断面の島数は平均1200個であつた。Example 1 Polymerization degree 110 after drying in a vacuum dryer at a temperature of 60 ° C. for 24 hours
(Log P = 2.04), saponification degree 67 mol% = (log X = 1.83)
Polyvinyl alcohol (log X + log P = 3.87) 50 parts and melt index (hereinafter MI) polypropylene 10 parts
Mix well with 50 parts in pellet form, use a screw extruder spinning machine with a diameter of 25 mm, adjust the temperature from the rear part of the spinning machine to the spinneret to 230 ° C, nozzle hole diameter 0.3 mm, number of holes 48 holes Melt spinning using the spinneret of
The discharged yarn was rapidly cooled and wound up by a cooling wind zone provided directly below the spinneret. Discharge rate 30g / min, winding speed 450m
The fiber was spun at a spinning rate of / min to obtain a multi-component fiber having a single yarn fineness of about 12 denier. As a result of observing the state of the dispersed phase by photographing the cross section of the discharge yarn of this multi-component fiber with a micrograph, the shape of a clear sea-island structure was shown, and the average number of islands in the cross section was 1200.
捲き取つた多成分繊維は温度25℃、湿度80%に調整し
た室内に24時間放置して調湿した後、80℃の空気浴帯で
2.5倍に延伸した。この延伸フイラメントをオレイン酸
ソーダ0.2%添加した常温の水(表面強力28dyne/cmに1
分間浸漬し、次いで30℃の水に30分間浸漬して乾燥した
結果、多成分繊維の減量率は49.3%であつて、ポリビニ
ルアルコールはほとんど溶解除去され、残つたポリプロ
ピレンは分散性の良好な微細繊維束が得られた。この微
細繊維束の強度は2.5g/drであつた。The wound multi-component fiber is left in a room adjusted to a temperature of 25 ° C and a humidity of 80% for 24 hours to control the humidity, and then in an air bath zone at 80 ° C.
It was stretched 2.5 times. This drawn filament was added with 0.2% of sodium oleate at room temperature water (surface strength of 28 dyne / cm
As a result of soaking for 30 minutes and then soaking in water at 30 ° C for 30 minutes and drying, the weight loss rate of the multi-component fiber was 49.3%, polyvinyl alcohol was almost dissolved and removed, and the remaining polypropylene was fine with good dispersibility. A fiber bundle was obtained. The strength of this fine fiber bundle was 2.5 g / dr.
実施例2 温度60℃の減圧乾燥機中で24時間乾燥した重合度220
(log P=2.34)、ケン化度71モル%(log X=1.85)の
ポリビニルアルコール(融点240℃、log X+log P=4.1
9)と、温度250℃、荷重325gで測定した溶融流動指数が
20のナイロン−6を2台のエクストルーダーに別々に供
給して溶融し、口金を1本の多成分繊維が芯成分15本で
ある多芯芯鞘型多成分繊維用口金で、ノズル孔径0.8m
m、孔数10ホールの口金を用い、芯成分にナイロン−6
を、鞘成分にポリビニルアルコールをそれぞれギヤーポ
ンプで計量し、ナイロン−6が24g/分、ポリビニルアル
コールが8g/分で供給して溶融紡糸し、捲き取り速度150
0m/分で紡糸し、単糸繊度約19デニールの多成分繊維を
得た。Example 2 Polymerization degree 220 dried in a vacuum dryer at a temperature of 60 ° C. for 24 hours
(Log P = 2.34), saponification degree 71 mol% (log X = 1.85), polyvinyl alcohol (melting point 240 ° C., log X + log P = 4.1
9) and the melt flow index measured at a temperature of 250 ° C and a load of 325g
Twenty nylon-6 are separately supplied to two extruders and melted, and the die is a multi-core sheath-type multi-component fiber die with one multi-component fiber having 15 core components and a nozzle hole diameter of 0.8. m
Nylon-6 is used as the core component by using a mouthpiece with m and 10 holes.
Polyvinyl alcohol was measured as a sheath component with a gear pump, nylon-6 was supplied at 24 g / min, and polyvinyl alcohol was supplied at 8 g / min, melt-spun, and a winding speed of 150
Spinning was performed at 0 m / min to obtain a multi-component fiber having a single yarn fineness of about 19 denier.
この多成分繊維は調湿度、85℃の空気浴帯で3倍に延
伸し、熱固定して6.1デニールの延伸した多成分繊維を
得た。この繊維で織布を作り、染色時の精練湯通し工程
でポリビニルアルコールを除去して細繊維束化し、次い
で金属錯塩染料で染色して得た布帛は絹様の風合いを有
するものとなつた。This multi-component fiber was stretched 3 times in an air bath at 85 ° C. with humidity control and heat-set to obtain a stretched multi-component fiber of 6.1 denier. A woven fabric was made from this fiber, polyvinyl alcohol was removed in the scouring and hot-watering process at the time of dyeing to form fine fiber bundles, and then the fabric obtained by dyeing with a metal complex salt dye had a silky texture.
実施例3 温度60℃の減圧乾燥機中で24時間乾燥した重合度110
(log P=2.04)、ケン化度96モル%(log X=1.98)の
酢酸アリル共重合ポリビニルアルコールを実施例2のポ
リビニルアルコールに替えて用い、実施例2と同様に紡
糸した結果、良好な紡糸性を有し、捲き取り速度1600m/
分で捲き取つても安定した相の多成分繊維が得られた。Example 3 Polymerization degree 110 after drying in a vacuum dryer at a temperature of 60 ° C. for 24 hours
(Log P = 2.04), saponification degree 96 mol% (log X = 1.98) allyl acetate copolymerized polyvinyl alcohol was used in place of the polyvinyl alcohol of Example 2, and spinning was carried out in the same manner as in Example 2. As a result, good results were obtained. It has spinnability and a winding speed of 1600m /
A multi-component fiber having a stable phase was obtained even when wound in minutes.
比較のために、温度60℃の減圧乾燥機中で24時間乾燥
した重合度220(log P=2.34)、ケン化度98モル%(lo
g X=1.99)の酢酸アリル共重合ポリビニルアルコール
を実施例3の共重合ポリビニルアルコールに替えて同様
に紡糸した結果、ゲル状物が発生して断糸を生じ、長時
間連続紡糸ができなかつた。更に芯成分にもバラツキが
見られた。For comparison, the polymer was dried for 24 hours in a vacuum dryer at a temperature of 60 ° C for a degree of polymerization of 220 (log P = 2.34) and a degree of saponification of 98 mol% (lo).
(g X = 1.99) Allyl acetate copolymerized polyvinyl alcohol was replaced with the copolymerized polyvinyl alcohol of Example 3 and the same spinning was performed. As a result, a gel-like substance was generated to cause yarn breakage, and continuous spinning was not possible for a long time. . Furthermore, variations were found in the core component.
本発明は水処理で容易に微細繊維束が得られるポリビ
ニルアルコールまたは変性ポリビニルアルコールを分散
媒成分とし、他の溶融紡糸性ポリマーを分散成分とした
多成分繊維を溶融紡糸法で安定に紡糸することができ、
更に、分繊性の良好な微細繊維束が得られる多成分繊維
である。INDUSTRIAL APPLICABILITY The present invention is capable of stably spinning a multi-component fiber using a polyvinyl alcohol or a modified polyvinyl alcohol as a dispersion medium component and another melt-spinning polymer as a dispersion component, which can easily obtain a fine fiber bundle by water treatment, by a melt spinning method. Can
Further, it is a multi-component fiber that can obtain a fine fiber bundle with good splitting property.
Claims (2)
度Xモル%と重合度Pとの関係がlog X+log P=3.7〜
4.3であるポリビニルアルコールまたは変性ポリビニル
アルコールを分散媒成分とし、該分散媒成分とは溶剤に
対する溶解性を異にするポリマーを分散成分とし、これ
ら分散媒成分と分散成分とからなることを特徴とする、
微細繊維束の製造に適した溶融紡糸多成分繊維。1. The saponification degree is 50-98 mol%, and the relationship between the saponification degree X mol% and the polymerization degree P is log X + log P = 3.7-
4.3 is a polyvinyl alcohol or modified polyvinyl alcohol as a dispersion medium component, the dispersion medium component is a polymer having a different solubility in a solvent as a dispersion component, characterized by comprising these dispersion medium component and the dispersion component ,
A melt-spun multi-component fiber suitable for the production of fine fiber bundles.
度Xモル%と重合度Pとの関係がlog X+log P=3.7〜
4.3であるポリビニルアルコールまたは変性ポリビニル
アルコールを分散媒成分とし、該分散媒成分とは溶剤に
対する溶解性を異にし、かつ溶融紡糸性を有するポリマ
ーを分散成分として溶融紡糸することを特徴とする微細
繊維束の製造に適した多成分繊維の製造方法。2. The saponification degree is 50 to 98 mol%, and the relationship between the saponification degree X mol% and the polymerization degree P is log X + log P = 3.7 to
A fine fiber characterized in that polyvinyl alcohol or modified polyvinyl alcohol of 4.3 is used as a dispersion medium component, and the dispersion medium component has a different solubility in a solvent and is melt-spun with a polymer having melt spinnability as a dispersion component. A method for producing a multi-component fiber suitable for producing a bundle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61251543A JPH0819571B2 (en) | 1986-10-21 | 1986-10-21 | Multi-component fiber suitable for producing fine fiber bundle and method for producing the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61251543A JPH0819571B2 (en) | 1986-10-21 | 1986-10-21 | Multi-component fiber suitable for producing fine fiber bundle and method for producing the same |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63105112A JPS63105112A (en) | 1988-05-10 |
| JPH0819571B2 true JPH0819571B2 (en) | 1996-02-28 |
Family
ID=17224387
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61251543A Expired - Fee Related JPH0819571B2 (en) | 1986-10-21 | 1986-10-21 | Multi-component fiber suitable for producing fine fiber bundle and method for producing the same |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0819571B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04174719A (en) * | 1990-10-29 | 1992-06-22 | Kuraray Co Ltd | Conjugate yarn |
| US5733603A (en) * | 1996-06-05 | 1998-03-31 | Kimberly-Clark Corporation | Surface modification of hydrophobic polymer substrate |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5857316B2 (en) * | 1975-03-14 | 1983-12-19 | ユニチカ株式会社 | Polyvinyl alcohol film |
| JPS5417053A (en) * | 1977-07-08 | 1979-02-08 | Toshiba Corp | Analog input device |
-
1986
- 1986-10-21 JP JP61251543A patent/JPH0819571B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63105112A (en) | 1988-05-10 |
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