JPH02182957A - Polyester nonwoven fabric - Google Patents
Polyester nonwoven fabricInfo
- Publication number
- JPH02182957A JPH02182957A JP64000802A JP80289A JPH02182957A JP H02182957 A JPH02182957 A JP H02182957A JP 64000802 A JP64000802 A JP 64000802A JP 80289 A JP80289 A JP 80289A JP H02182957 A JPH02182957 A JP H02182957A
- Authority
- JP
- Japan
- Prior art keywords
- intrinsic viscosity
- polyethylene terephthalate
- crimp
- heat
- polymer
- 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.)
- Pending
Links
Landscapes
- Multicomponent Fibers (AREA)
- Nonwoven Fabrics (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はスポーツ衣料、素材、寝具等の用途に好適な柔
軟で伸縮性に優れたポリエステル系不織布に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a polyester nonwoven fabric that is flexible and has excellent elasticity and is suitable for use in sports clothing, materials, bedding, and the like.
〔従来技術及び発明が解決しようとする課題〕従来から
多種の素材により不織布が製造されており、短繊維を熱
接着性繊維と混合してウェブとなし、加熱処理により接
着して不織布を形成する方法も会知である。[Prior art and problems to be solved by the invention] Nonwoven fabrics have been manufactured from various materials in the past, and short fibers are mixed with heat-adhesive fibers to form a web, which is then bonded by heat treatment to form a nonwoven fabric. The method is also known to Kaichi.
特にスポーツ衣料、素材用としては伸縮性の優れた不織
布に対する要望が高まっておシ、これらに適合する不織
布の開発が進められている。In particular, there is an increasing demand for nonwoven fabrics with excellent elasticity for use in sports clothing and materials, and efforts are being made to develop nonwoven fabrics that meet these demands.
伸縮性に優れた不織布の製法としては、捲縮発現性の高
A短繊維を使用するのが好ましく、かかる短繊維の製造
法としては収縮率の異なる2種類のポリマーをサイドバ
イサイド型に貼り合わせるのが一般的な製造法である。As a method for manufacturing a nonwoven fabric with excellent elasticity, it is preferable to use high A short fibers that exhibit crimp properties, and a method for manufacturing such short fibers is to bond two types of polymers with different shrinkage rates side-by-side. is a common manufacturing method.
収縮率の異なるポリマーとしては通常固有粘度の異なる
ポリマーを使用する、つまシ2種のポリマーが同一組成
から成る場合には分子量に差をつけて結晶化速度の差に
よシ収縮率をコントロールし、捲縮を発現させるもので
ある。これは分子量が低い場合には結晶化速度が速いた
め熱処理時の収縮率が低く、分子量が高い場合忙は結晶
化速度が遅いため熱処理時の収縮率が高くなるという現
象を応用したものである。As polymers with different shrinkage rates, polymers with different intrinsic viscosities are usually used.When two types of polymers have the same composition, the shrinkage rates are controlled by making a difference in molecular weight and using the difference in crystallization rate. , which causes crimping. This is an application of the phenomenon that when the molecular weight is low, the crystallization rate is fast, so the shrinkage rate during heat treatment is low, and when the molecular weight is high, the crystallization rate is slow, so the shrinkage rate during heat treatment is high. .
よって高い捲縮を得ようとした場合尤は2つのポリマー
の固有粘度の差をできるだけ大きくすることが望ましb
が、固有粘度差の増大にともなり紡糸ノズル出口でニー
リングを生じ易くなるため自ずと取り得る固有粘度差が
限定されてしまb繊維の捲縮発現の大きさも限界が生じ
る。Therefore, when trying to obtain high crimp, it is desirable to make the difference in intrinsic viscosity between the two polymers as large as possible.
However, as the difference in intrinsic viscosity increases, knealing becomes more likely to occur at the exit of the spinning nozzle, which naturally limits the difference in intrinsic viscosity that can be obtained, and also limits the degree of crimp development in the fibers.
かかる問題点の改良法として固有粘度差を増大させても
溶融粘度差を増大させな込方法、つまり高固有粘度ポリ
マーの溶融粘度を下げる方法として添加剤を加える方法
が種々提案されてbるが、実用性能を充分忙満足する効
果的表方法は未だ見つかってかない。Various methods have been proposed to improve this problem, including increasing the intrinsic viscosity difference but increasing the melt viscosity difference, that is, adding additives to lower the melt viscosity of high intrinsic viscosity polymers. However, an effective table method that satisfies practical performance has not yet been found.
本発明は固有粘度差を溶融紡糸が可能な範囲にとどめて
も、尚且つ充分な捲縮性能を有するポリエステル複合繊
維を用いることにより、柔軟で伸縮性に優れた不織布を
提供するものである。The present invention provides a nonwoven fabric that is flexible and has excellent elasticity by using polyester composite fibers that have sufficient crimp performance while keeping the difference in intrinsic viscosity within a range that allows melt spinning.
本発明は、固有粘度差がα15〜IIL25の範囲にあ
る2種のポリエチレンテレフタレート系ポリマーがサイ
ドバイサイド型に接合された複合繊維であって、高固有
粘度側のポリマーがイソフタル酸を6〜12モルチ共重
合したポリエチレンテレフタレート系ポリマーからなり
、且つ両ポリマー間の結晶化開始温度が40℃以上異な
る複合短繊維と、ポリエチレンテレフタレート系低融点
ポリマーからなる熱接着性短繊維とが60:40〜90
:100割合で混合され、熱接着及び捲縮発現処理され
ているポリエステル系不織布である。The present invention is a composite fiber in which two types of polyethylene terephthalate polymers having an intrinsic viscosity difference in the range of α15 to IIL25 are joined in a side-by-side manner, and the polymer on the higher intrinsic viscosity side absorbs isophthalic acid by 6 to 12 molt. Composite short fibers made of a polymerized polyethylene terephthalate-based polymer and in which the crystallization initiation temperatures between the two polymers differ by 40°C or more, and heat-adhesive short fibers made of a polyethylene terephthalate-based low melting point polymer are mixed in a ratio of 60:40 to 90.
: Polyester nonwoven fabric that has been mixed at a ratio of 100 and subjected to thermal adhesion and crimp development treatment.
本発明を更に詳細に説明すると、本発明で使用する複合
短繊維は、先ずサイドバイサイド型に接合される2種の
ポリマー間の固有粘度差がl115〜α25の範囲にな
ければならない。すなわち、前述のように2種のポリマ
ーの固有粘度差は大きいほど捲縮発現に有利であるが、
固有粘度差が(L25を越えると紡糸時にノズル出口に
おりてニードリングが生じ、紡糸安定性が著しく悪くな
り、又[115未満では捲縮の発現性が著しく低下する
。しかしながら、同一組成のポリエチレンテレフタレー
トを用すた場合は、固有粘度差を(L15〜a、25の
範囲内忙留めても捲縮発現の程度はあまり高くならない
。To explain the present invention in more detail, in the composite short fibers used in the present invention, the difference in intrinsic viscosity between two types of polymers joined side-by-side must be in the range of l115 to α25. In other words, as mentioned above, the larger the difference in intrinsic viscosity between the two types of polymers, the more advantageous it is to developing crimp.
If the intrinsic viscosity difference exceeds L25, needling occurs at the nozzle outlet during spinning, resulting in significantly poor spinning stability; When terephthalate is used, even if the intrinsic viscosity difference is kept within the range of (L15 to a, 25), the degree of crimp development does not become very high.
そこで本発明におhては固有粘度を015〜α25の範
囲にとどめ、且つ両ポリマー間の結晶化開始温度差を大
きくすることにより、不織布の熱処理に於て結晶化温度
の低b1つまり結晶化速度の速bポリマーを結晶化させ
て収JII率を小さい範囲にとどめ、結晶化温度の高b
ポリマーを実質的に非晶状態とすることにより高い収縮
率を発現させ、その収縮率差にょシ極めて大きな捲縮を
得ることを可能ならしめたものである。ところが同一組
成のポリマーを使用し、固有粘度を変更しただけでは固
有粘度差115〜(L25の範囲では結晶化開始温度差
が40℃以上には成り得ない。Therefore, in the present invention, by keeping the intrinsic viscosity within the range of 015 to α25 and increasing the difference in crystallization initiation temperature between both polymers, the crystallization temperature is low b1, that is, crystallization A high rate of crystallization of the polymer to keep the JII yield within a small range, and a high crystallization temperature of the polymer
By making the polymer substantially amorphous, it exhibits a high shrinkage rate, and the difference in shrinkage rate makes it possible to obtain extremely large crimp. However, if polymers of the same composition are used and the intrinsic viscosity is simply changed, the crystallization initiation temperature difference cannot be greater than 40° C. within the range of 115 to (L25).
そこで本発明においては高固有粘度側のポリマーとして
イソフタル酸を8〜12%共重合シたポリエチレンテレ
フタレート系ポリマーヲ使用することにより、固有粘度
差(115〜CL25の範囲におりて結晶化開始温度を
40℃以上異ならしめることを可能にしたものである。Therefore, in the present invention, by using a polyethylene terephthalate-based polymer copolymerized with 8 to 12% isophthalic acid as a polymer on the high intrinsic viscosity side, the crystallization initiation temperature is increased to 40 This makes it possible to have a difference of more than ℃.
イソフタル酸の共重合比率としては高込方がよシ効果的
であるが、イソフタル酸の共重合によシボリマーの融点
も低下するため共重合比が12壬を越えると熱的安定性
の面から好ましくない。また共重合比率が6慢未溝の場
合には実質的忙大きな捲縮が得られな込。本発明の不織
布を熱処理する温度は130〜18′0℃が好ましい。The higher the copolymerization ratio of isophthalic acid, the more effective it is, but copolymerization of isophthalic acid also lowers the melting point of the silimer, so if the copolymerization ratio exceeds 12. Undesirable. In addition, when the copolymerization ratio is 6, it is not possible to obtain substantially large crimp. The temperature at which the nonwoven fabric of the present invention is heat treated is preferably 130 to 18'0°C.
これは150℃未満では低固有粘度側の・ポリエステル
が結晶化しないため2種のポリマーの収縮率差を大きく
することができず、180℃以上では両ポリマーともに
結晶化が充分に進むためやはシ収縮率差を大きくするこ
とができない。また熱分解の面からも18(Ic以下が
好ましb範囲である。This is because at temperatures below 150°C, the polyester with a lower intrinsic viscosity does not crystallize, making it impossible to increase the difference in shrinkage rate between the two polymers, and at temperatures above 180°C, both polymers fully crystallize. It is not possible to increase the difference in shrinkage rate. Also, from the viewpoint of thermal decomposition, the range b is preferably 18 (Ic or less).
また熱処理の方法は130〜180℃の範囲で1段で行
っても良すが、好ましくは熱接着性繊維の接着が可能な
低温で第1段目の熱処理を行った後、高温で複合繊維を
自由収縮させることが望ましboこれは、1段のみで高
温熱処理を行った場合、熱接着繊維の接着と複合繊維の
自由収縮が同時に進行し、収縮斑を生じ美観を損うため
である。The heat treatment may be carried out in one stage at a temperature of 130 to 180°C, but it is preferable to perform the first heat treatment at a low temperature that allows bonding of the thermoadhesive fibers, and then heat the composite fibers at a high temperature. It is desirable to allow free shrinkage of the composite fibers.This is because if high-temperature heat treatment is performed in only one stage, adhesion of the thermally bonded fibers and free shrinkage of the composite fibers will proceed at the same time, causing shrinkage spots and impairing the aesthetics. .
熱接着性繊維の混率は不織布の風合の面からは少ないほ
うが好ましかが、104未満の場合忙は1段目の熱処理
でウェブ中に熱接着性繊維のマトリックスを形成するこ
とができず、また40係を超える場合には製品が固い風
合となシ実用上好ましくない結果となる。From the viewpoint of the texture of the nonwoven fabric, it is preferable that the blending ratio of heat-adhesive fibers is small, but if it is less than 104, a matrix of heat-adhesive fibers cannot be formed in the web during the first heat treatment. If it exceeds 40, the product will have a hard texture, which is not practical.
以下本発明を実施例により更に具体的に説明する。The present invention will be explained in more detail below with reference to Examples.
固有粘度(+y)が0.65のポリエチレンテレフタレ
ートを一成分とし、他成分として〔ワ〕及びイソフタル
酸の共重合比を種々変えたポリエチレンテレフタレート
系ポリマーを用いてサイドバイサイド型に複合紡糸し、
温度60℃、倍率4.06倍で延伸後130℃で定長黙
想・理を行い、機械捲縮付与後切断して単糸繊度2.5
デニール、繊維長51mの複合短繊維を得た。この複合
短繊維に、融点が120’Cのポリエチレンテレフタレ
ート系熱接着性短線ia(五0(lX51111)を2
0チ混合してカードウェブを形成し、該ウェブを回転式
ドラム乾燥器により150℃で第1段熱処理し、引続い
て熱風循環型乾燥器にょυ170℃で第2段熱処理して
目付40’l/m”の乾式不織布を得た。Polyethylene terephthalate with an intrinsic viscosity (+y) of 0.65 is used as one component, and polyethylene terephthalate-based polymers with various copolymerization ratios of [wa] and isophthalic acid are used as other components, and composite spinning is performed in a side-by-side type.
After stretching at a temperature of 60°C and a magnification of 4.06 times, constant length meditation and theory was performed at 130°C, mechanical crimp was applied, and cutting was performed to obtain a single yarn fineness of 2.5.
Composite short fibers with a denier and a fiber length of 51 m were obtained. Two polyethylene terephthalate heat-adhesive short wires ia (50 (1X51111)) having a melting point of 120'C were added to this composite short fiber.
0 to form a carded web, which was subjected to a first stage heat treatment at 150°C in a rotary drum dryer, followed by a second stage heat treatment at υ170°C in a hot air circulation type dryer to obtain a carded web with a basis weight of 40'. A dry nonwoven fabric of 1/m" was obtained.
複合紡糸安定性及び複合短繊維の捲縮数を下表にした。The composite spinning stability and the number of crimps of composite short fibers are shown in the table below.
尚、&1〜4及び6は比較例、崖5が実施例である。Note that &1 to 4 and 6 are comparative examples, and cliff 5 is an example.
用いることにより、柔軟で伸縮性の優れた不織布を得る
ことができるのであって、その工業的価値は極めて大で
ある。By using it, a nonwoven fabric with excellent flexibility and stretchability can be obtained, and its industrial value is extremely large.
〔7〕コ固有粘度
Ta” =x D80で測定した結晶化開始のピーク温
度工PA−イソフタル酸の共重合比[7] Intrinsic viscosity Ta” = x Peak temperature at which crystallization starts measured at D80 PA-Isophthalic acid copolymerization ratio
Claims (1)
リエチレンテレフタレート系ポリマーがサイドバイサイ
ド型に接合された複合繊維であつて、高固有粘度側のポ
リマーがイソフタル酸を6〜12モル%共重合したポリ
エチレンテレフタレート系ポリマーからなり、且つ両ポ
リマー間の結晶化開始温度が40℃以上異なる複合短繊
維と、ポリエチレンテレフタレート系低融点ポリマーか
らなる熱接着性短繊維とが60:40〜90:10の割
合で混合され、熱接着及び捲縮発現処理されているポリ
エステル系不織布。It is a composite fiber in which two types of polyethylene terephthalate polymers having an intrinsic viscosity difference in the range of 0.15 to 0.25 are joined side-by-side, and the polymer on the higher intrinsic viscosity side contains 6 to 12 mol% of isophthalic acid. Composite short fibers made of a copolymerized polyethylene terephthalate-based polymer and in which the crystallization initiation temperatures between the two polymers differ by 40°C or more, and heat-adhesive short fibers made of a polyethylene terephthalate-based low melting point polymer are 60:40 to 90: A polyester nonwoven fabric that is mixed at a ratio of 1:10 to 10:1 and is thermally bonded and crimped.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP64000802A JPH02182957A (en) | 1989-01-05 | 1989-01-05 | Polyester nonwoven fabric |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP64000802A JPH02182957A (en) | 1989-01-05 | 1989-01-05 | Polyester nonwoven fabric |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02182957A true JPH02182957A (en) | 1990-07-17 |
Family
ID=11483817
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP64000802A Pending JPH02182957A (en) | 1989-01-05 | 1989-01-05 | Polyester nonwoven fabric |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02182957A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2013136851A (en) * | 2011-12-28 | 2013-07-11 | Kuraray Co Ltd | Polyester-based conjugate binder fiber |
| CN108625043A (en) * | 2017-03-22 | 2018-10-09 | 现代自动车株式会社 | Non-woven fabrics and its manufacturing method and use its vehicle cargo veil |
| JP2022186001A (en) * | 2021-06-04 | 2022-12-15 | 松本油脂製薬株式会社 | Treatment agent for water-repellent fibers and use thereof |
-
1989
- 1989-01-05 JP JP64000802A patent/JPH02182957A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2013136851A (en) * | 2011-12-28 | 2013-07-11 | Kuraray Co Ltd | Polyester-based conjugate binder fiber |
| CN108625043A (en) * | 2017-03-22 | 2018-10-09 | 现代自动车株式会社 | Non-woven fabrics and its manufacturing method and use its vehicle cargo veil |
| JP2022186001A (en) * | 2021-06-04 | 2022-12-15 | 松本油脂製薬株式会社 | Treatment agent for water-repellent fibers and use thereof |
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