JPS5836102B2 - Fushiyokufunoseizouhouhou - Google Patents

Fushiyokufunoseizouhouhou

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Publication number
JPS5836102B2
JPS5836102B2 JP50038157A JP3815775A JPS5836102B2 JP S5836102 B2 JPS5836102 B2 JP S5836102B2 JP 50038157 A JP50038157 A JP 50038157A JP 3815775 A JP3815775 A JP 3815775A JP S5836102 B2 JPS5836102 B2 JP S5836102B2
Authority
JP
Japan
Prior art keywords
pva
nonwoven fabric
fibers
hydrophobic thermoplastic
mixed
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP50038157A
Other languages
Japanese (ja)
Other versions
JPS51112979A (en
Inventor
正雄 鷲見
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.)
Unitika Ltd
Original Assignee
Unitika 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 Unitika Ltd filed Critical Unitika Ltd
Priority to JP50038157A priority Critical patent/JPS5836102B2/en
Publication of JPS51112979A publication Critical patent/JPS51112979A/en
Publication of JPS5836102B2 publication Critical patent/JPS5836102B2/en
Expired legal-status Critical Current

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  • Nonwoven Fabrics (AREA)

Description

【発明の詳細な説明】 本発明は疎水性熱可塑性樹脂とポリビニルアルコール(
以下PVAという)との混合溶融高速紡糸によるスパン
ボンド不織布の製造方法に関するものであり、吸湿性、
吸水性を有する疎水性熱可塑性繊維スパンボンド不織布
をはじめ、高温熱処理やバインダー付着による損傷のな
いスパンボンド不織布の製造方法を提供するものである
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a hydrophobic thermoplastic resin and polyvinyl alcohol (
This article relates to a method for producing spunbond nonwoven fabric by mixing it with PVA (hereinafter referred to as PVA), and it has hygroscopicity,
The present invention provides a method for producing spunbond nonwoven fabrics made of hydrophobic thermoplastic fibers having water absorbing properties, as well as spunbond nonwoven fabrics that are not damaged by high temperature heat treatment or binder adhesion.

従来から、溶融紡糸可能な疎水性熱可塑性樹脂からスパ
ンボンド不織布を製造する方法は広く知られているが、
かかる方法で得られる不織布は構戒材料が疎水性熱可塑
性繊維であるため衛生材料あるいは下着などの用途でセ
ルロース系繊維なみの吸湿性、吸水性が要求されても、
かかる性質を付与することは不可能であった。
Conventionally, methods for producing spunbond nonwoven fabrics from melt-spun hydrophobic thermoplastic resins have been widely known;
The nonwoven fabric obtained by this method is made of hydrophobic thermoplastic fibers, so even if it is required to have hygroscopicity and water absorption comparable to cellulose fiber for sanitary materials or underwear,
It was not possible to provide such properties.

さらに、疎水性熱可塑性繊維で形或したスパンボンド不
織布は、不織布の機械的性能を向上せしめるため加熱圧
着して構戊繊維を相互に熱融着させるか、あるいはバイ
ンダーで構戒繊維を相互に接着せしめていたが、前者の
方法は構威繊維を高温熱処理するため繊維が収縮するだ
けでなく、本来の可撓性、風合が損われ、また後者の方
法もバインダー付着により風合が損われる欠点があった
Furthermore, spunbond nonwoven fabrics formed from hydrophobic thermoplastic fibers can be produced by heat-pressing to heat-fuse the structural fibers to each other, or by bonding the structural fibers to each other using a binder to improve the mechanical performance of the nonwoven fabric. However, the former method not only shrinks the fibers but also loses their original flexibility and texture due to the high-temperature heat treatment of the Guangwei fibers, while the latter method also causes the texture to be damaged due to binder adhesion. There were some drawbacks.

本発明者は、疎水性熱可塑性繊維にPVAの吸湿性、吸
水性を付与することができ、さらに短繊維不織布の製造
時に使用されるバインダー繊維と同様に低温加熱または
水などにより接着能を発揮する繊維がスパンボンド法に
おける高速紡糸で得られれば、前記従来公知のスパンボ
ンド不織布の問題点が克服できると判断し、鋭意研究し
た結果特定PVAが疎水性熱可塑性樹脂と混合紡糸でき
るだけでなく、高速紡糸も可能であり、ざらにPVAの
添加量により疎水性熱可塑性繊維の吸湿性、吸水性を改
良するだけでなく、接着能をも付与することができる事
実をみいだし本発明を完或した。
The present inventor has demonstrated that it is possible to impart the hygroscopicity and water absorption properties of PVA to hydrophobic thermoplastic fibers, and that they exhibit adhesive ability when heated at low temperatures or with water, similar to the binder fibers used in the production of short fiber nonwoven fabrics. It was determined that if the fibers could be obtained by high-speed spinning in the spunbond method, the problems of the conventionally known spunbond nonwoven fabrics could be overcome, and as a result of intensive research, not only could a specific PVA be mixed with a hydrophobic thermoplastic resin and spun. The present invention was completed by discovering that high-speed spinning is possible, and that it is possible to not only improve the hygroscopicity and water absorbency of hydrophobic thermoplastic fibers but also impart adhesive ability by changing the amount of PVA added. did.

すなわち、本発明は疎水性熱可塑性樹脂と平均重合度5
0〜3 0 01残存酢酸基15〜70モル%(7)P
VAとを混合溶融押出したフィラメント群を単独または
他繊維のフィラメント群と引揃えるか、あるいは別々に
吸引ジェットにて引取り、噴射気流により非織性シート
形戊面上に吹付け堆積することを特徴とする不織布の製
造方法である。
That is, the present invention uses a hydrophobic thermoplastic resin and an average degree of polymerization of 5.
0-3001 residual acetate group 15-70 mol% (7)P
A group of filaments melted and extruded by mixing with VA can be pulled together singly or with a group of filaments of other fibers, or taken separately with a suction jet and sprayed and deposited on the surface of a non-woven sheet using a jet of air. This is a unique method for producing nonwoven fabric.

本発明について詳細に説明する。The present invention will be explained in detail.

本発明に適用する疎水性熱可塑性樹脂とは、一般に知ら
れているポリエステル系、ポリアミド系およびポリオレ
フイン系などの溶融して繊維化することのできる高分子
化合物をいう。
The hydrophobic thermoplastic resin used in the present invention refers to generally known polymeric compounds such as polyester, polyamide, and polyolefin that can be melted into fibers.

また、本発明においてかかる疎水性熱可塑性樹脂と混合
するPVAは平均重合度50〜300、残存酢酸基15
〜70モル俤の熱溶融性のものをいう。
In addition, in the present invention, the PVA to be mixed with the hydrophobic thermoplastic resin has an average degree of polymerization of 50 to 300, and a residual acetate group of 15
It refers to a heat-melting substance with a capacity of ~70 mol.

このような特殊PVAはたとえば重合時の温度のもとて
20X10 ’以上の連鎖移動定数をもつアルコール
類中で酢酸ビニルを平均重合度50〜300に重合し、
加熱下に溶剤を追い出したのちポリ酢酸ビニルを無水メ
タノールに混合溶解し、アルカリを加えて脱酢酸化する
ことにより容易に製造することができる。
Such special PVA is produced by polymerizing vinyl acetate to an average degree of polymerization of 50 to 300 in an alcohol having a chain transfer constant of 20 x 10' or more at the polymerization temperature, for example.
It can be easily produced by expelling the solvent under heating, mixing and dissolving polyvinyl acetate in anhydrous methanol, and adding an alkali to deacetate the mixture.

本発明は疎水性熱可塑性樹脂とPVAとを混合溶融して
高速紡糸するものであるが、疎水性熱可塑性樹脂と混合
するPVAの平均重合度が300より高いと、PVAの
溶融温度が高く、PVAの熱分解を伴い、さらに溶融粘
度も高くなるため混合溶融、高速紡糸が困難となり、ま
た平均重合度が50より低いPVAは熱安定性のよいも
のを製造することが困難であり、混合溶融時に熱分解が
発生し易いので本発明の目的に適合しなくなる。
In the present invention, a hydrophobic thermoplastic resin and PVA are mixed and melted and spun at high speed. However, when the average degree of polymerization of PVA mixed with the hydrophobic thermoplastic resin is higher than 300, the melting temperature of PVA is high; PVA is thermally decomposed and the melt viscosity also increases, making mixing melting and high-speed spinning difficult, and PVA with an average degree of polymerization lower than 50 is difficult to produce with good thermal stability. In some cases, thermal decomposition tends to occur, making it unsuitable for the purpose of the present invention.

したがって、本発明に適用するPVAの平均重合度は5
0〜300の範囲であることが必要であるが、特に10
0〜250のPVAがより好ましい。
Therefore, the average degree of polymerization of PVA applied to the present invention is 5.
It needs to be in the range of 0 to 300, especially 10
0-250 PVA is more preferred.

一方、PVAの残存酢酸基が15モル係より低いと水酸
基の分子間、分子内水素結合による分子間力が強力とな
り熱溶融しにくく、前記PVAの平均重合度が300以
上になった場合と同様、疎水性熱可塑性樹脂との混合溶
融紡糸が困難となり、またPVAの残存酢酸基が70モ
ル係を越えるとPVAの水膨潤性が低下し、疎水性熱可
塑性樹脂と混合しても充分な吸湿性、吸水性が付与でき
なくなるので不適当である。
On the other hand, if the residual acetate group of PVA is lower than 15 molar ratio, the intermolecular force due to the intermolecular and intramolecular hydrogen bonds of the hydroxyl group becomes strong, making it difficult to heat melt, similar to the case where the average degree of polymerization of PVA is 300 or more. , it becomes difficult to mix melt-spinning with a hydrophobic thermoplastic resin, and if the residual acetate group of PVA exceeds 70 molar ratio, the water swelling property of PVA decreases, and even when mixed with a hydrophobic thermoplastic resin, it does not absorb enough moisture. It is unsuitable because it cannot impart properties and water absorption properties.

したがって、PVAの残存酢酸基量は15〜70モル俤
の範囲であることが必要であり、とくに20〜60モル
係が好ましい。
Therefore, the amount of residual acetic acid groups in PVA needs to be in the range of 15 to 70 moles, and particularly preferably 20 to 60 moles.

本発明において疎水性熱可塑性樹脂と前記特定PVAと
の混合はあらかじめ溶融混合したチップを利用してもよ
いし、また溶融前あるいは溶融時にチップ状で混合して
もよいが、その混合割合は混合紡糸繊維のみでスパンボ
ンド不織布を製造する場合、PVAと疎水性熱可塑性樹
脂との重量比を5:95〜50 : 50の範囲にする
ことが望ましく、また混合紡糸繊維と他の繊維の混合ス
パンボンド不織布を製造する場合、PVAと疎水性熱可
塑性樹脂との重量比を50:50〜85:15の範囲に
することが望ましい。
In the present invention, the hydrophobic thermoplastic resin and the specific PVA may be mixed in chips that have been melt-mixed in advance, or may be mixed in the form of chips before or during melting, but the mixing ratio is When producing a spunbond nonwoven fabric using only spun fibers, it is desirable that the weight ratio of PVA and hydrophobic thermoplastic resin be in the range of 5:95 to 50:50, and it is preferable that the weight ratio of PVA and hydrophobic thermoplastic resin be in the range of 5:95 to 50:50. When manufacturing a bonded nonwoven fabric, it is desirable that the weight ratio of PVA and hydrophobic thermoplastic resin be in the range of 50:50 to 85:15.

このような混合割合にすることにより、前者の場合は吸
湿性、吸水性を有する熱可塑性繊維スパンボンド不織布
となり、後者の場合はスパンボンド不織布形成1 20
0℃以下の低温熱処理あるいは水蒸気散布後圧着するこ
とにより、風合のすぐれた不織布となる。
By making such a mixing ratio, in the former case, a thermoplastic fiber spunbond nonwoven fabric having hygroscopic and water absorbing properties is obtained, and in the latter case, a spunbond nonwoven fabric is formed.
By applying low-temperature heat treatment at 0° C. or lower or applying pressure after spraying with steam, a nonwoven fabric with excellent texture can be obtained.

混合溶融押出に際しては該疎水性熱可塑性樹脂と該PV
Aを紡糸の前に適当な温度で減圧下に充分乾燥したのち
、所定の紡糸頭温度に維持された紡糸機に供給し、混合
溶融物を紡糸口金より紡出して繊条体を形或することが
必要である。
During mixed melt extrusion, the hydrophobic thermoplastic resin and the PV
Before spinning, A is sufficiently dried under reduced pressure at an appropriate temperature, and then supplied to a spinning machine maintained at a predetermined spinning head temperature, and the mixed melt is spun from a spinneret to form a filament. It is necessary.

本発明はこのようにして得られる混合紡糸繊条体を紡糸
口金の下方に設けた吸引ジェット装置に通過させ、そこ
で高速度のジェット気流を作用させてその推進力を利用
して繊条体を下方に索引し、該吸引ジェット装置より噴
出した噴流とともに非織性シート形戊面上に均一に吹付
け堆積するものである。
In the present invention, the mixed spun fibrous body obtained in this manner is passed through a suction jet device provided below the spinneret, where a high-velocity jet stream is applied, and the fibrous body is spun using the propulsion force. It is indexed downward and is sprayed and deposited uniformly on the non-woven sheet-shaped surface with the jet stream ejected from the suction jet device.

このとき使用する吸引ジェット装置としては、たとえば
特公昭37−4997号公報、あるいは特公昭41−7
883号公報などにより公知の装置を使用することがで
きる。
As a suction jet device used at this time, for example, Japanese Patent Publication No. 37-4997 or Japanese Patent Publication No. 41-7
A known device such as that disclosed in Japanese Patent No. 883 can be used.

また、ジェット気流の媒体となる気体は通常空気、窒素
ガス、炭酸ガス等が使用されるが、その他活性、不活性
のいずれの気体も目的に応じて使用可能である。
In addition, air, nitrogen gas, carbon dioxide gas, etc. are usually used as the gas serving as a medium for the jet stream, but any other active or inert gas can be used depending on the purpose.

酸素を含む気体を使用する場合、PVAの酸化分解によ
る着色を防止するため、PVAに少量のリン酸、亜リン
酸などのリン酸化合物を加えておくとよい。
When using a gas containing oxygen, it is advisable to add a small amount of a phosphoric acid compound such as phosphoric acid or phosphorous acid to the PVA in order to prevent coloration due to oxidative decomposition of the PVA.

このジェット気流を作用させる装置は紡糸直後の該繊条
体がいまだ固定していない流動領域から完全に冷却固化
し、繊維形態に到達した領域までの間より適当に選定す
ればよく、また吸引ジェット装置に室温程度の空気ある
いは乾熱空気、水蒸気、水蒸気飽和空気などの加熱気体
を供給してジェット気流による索引延伸に引続いて、あ
るいは同時に熱処理、蒸気処理を行ってもよい。
The device that applies this jet airflow may be appropriately selected from the flow area where the filament has not yet been fixed immediately after spinning to the area where the filament has completely cooled and solidified and reached the fiber form, and the suction jet Heat treatment and steam treatment may be performed subsequent to or simultaneously with index stretching using a jet stream by supplying air at about room temperature or a heated gas such as dry hot air, water vapor, or water vapor saturated air to the apparatus.

本発明方法では単糸織度30デニール以下の繊維を10
00m/分以上の高速で、かつ広範囲の紡糸速度で紡糸
することが可能であるが、その際紡糸口金各孔からの吐
出量は0.1〜5.Ogl分にすることが紡糸性より望
ましい。
In the method of the present invention, fibers with a single yarn weave of 30 denier or less are
It is possible to spin at a high speed of 0.00 m/min or more and over a wide range of spinning speeds, but in this case, the discharge rate from each hole of the spinneret is 0.1 to 5.0 m/min. Ogl content is more desirable than spinnability.

本発明はこのような紡出、ジェット気流で引取られた繊
維を連続フィラメントがランダムループ状に堆積したシ
ート状ウエツブに形成するものであり、このようにして
得られたウエツブに水蒸気を吹付けたり、力口熱圧着す
るかあるいは噴出した繊維が未固化の状態でシート状に
捕集してスパンボンド不織布を形戒することができる。
In the present invention, the fibers drawn by such spinning and jet stream are formed into a sheet-like web in which continuous filaments are deposited in random loops, and the web thus obtained is sprayed with water vapor or A spunbond nonwoven fabric can be formed by force-thermocompression or by collecting the ejected fibers in a sheet form in an unsolidified state.

本発明の方法は、このように疎水性熱可梨性樹脂ど特定
PVAとを混合溶融押出したフィラメント群を高速気流
により引取り、噴射気流により非織性シート形戒面上に
均一に吹付け堆積せしめるものであるが、その際高速気
流により引取るフィラメント群は混合紡糸繊維単独でも
、あるいは他繊維のフィラメント群と引揃えたものでも
よく、さらには2種以上の繊維を別々の吸引ジェットに
より引取り、噴射気流により同一非織性シート形或面上
に均一に吹付け堆積してもよいので、混合紡糸繊維単独
のスパンボンド不織布をはじめ、混合紡糸繊維と他繊維
との混合スパンボンド不織布も製造することができるの
である。
In the method of the present invention, a group of filaments mixed and melted and extruded with a hydrophobic thermoplastic resin or a specific PVA is taken up by a high-speed air stream, and is uniformly sprayed onto a non-woven sheet-shaped surface by a jet air stream. At this time, the filament group taken up by a high-speed air current may be a mixed spun fiber alone or a group of filaments of other fibers, or two or more types of fibers may be collected by separate suction jets. Since it can be uniformly sprayed and deposited on the same non-woven sheet shape or surface by taking up and blowing air, it can be used for spunbond nonwoven fabrics made of mixed spun fibers alone, as well as spunbond nonwoven fabrics mixed spunbond fabrics made of mixed spun fibers and other fibers. can also be manufactured.

このとき、PVAと疎水性熱可塑性樹脂との混合割合を
重量比で5:95〜50:50とした混合紡糸繊維単独
でスパンボンド不織布を製造すると、得られる不織布は
吸湿性、吸水性を有するから衛生材料、下着などにも利
用でき、また該比が50:50〜85:15の混合紡糸
繊維と他繊維との混合スパンボンド不織布は200℃以
下の低温加熱圧着あるいは水蒸気を散布して圧着するだ
けで繊維間を接着することができるので、高温圧着やバ
インダー処理による風合損傷のないすぐれたスパンボン
ド不織布が得られるのである。
At this time, when a spunbond nonwoven fabric is produced solely from mixed spun fibers in which the mixing ratio of PVA and hydrophobic thermoplastic resin is 5:95 to 50:50 by weight, the resulting nonwoven fabric has hygroscopic and water absorbing properties. It can also be used for sanitary materials, underwear, etc., and spunbond nonwoven fabrics made of mixed spun fibers and other fibers with a ratio of 50:50 to 85:15 can be bonded by low-temperature heat compression at 200°C or less or by spraying water vapor. Since the fibers can be bonded together simply by doing this, it is possible to obtain an excellent spunbond nonwoven fabric that does not suffer from damage to its texture due to high-temperature compression bonding or binder treatment.

以下、実施例により本発明をさらに詳細に説明する。Hereinafter, the present invention will be explained in more detail with reference to Examples.

実施例 1 あらかじめ減圧下に十分乾燥した平均重合度1 4 0
,残存酢酸基27モル饅のPVA20重量部に平均分子
量約20.000のナイロン6樹脂80重量部を加えス
クリュー径208、スクリュー長4448の押出機の供
給口に供給し、その際該供給口を乾燥窒素雰囲気とした
Example 1 Average degree of polymerization 1 4 0 sufficiently dried under reduced pressure in advance
, 80 parts by weight of nylon 6 resin having an average molecular weight of about 20,000 was added to 20 parts by weight of PVA containing 27 moles of residual acetic acid groups, and the mixture was fed to the feed port of an extruder having a screw diameter of 208 and a screw length of 4448. A dry nitrogen atmosphere was used.

紡糸頭温度240℃、孔径0.3M、12孔の紡糸口金
より1孔当りL897分の吐出量で紡出し、紡糸口金下
40cIrLに設置した吸引ジェット装置をトラバース
運動させながら約9000m/分の紡糸速度で引取り金
網上に吹付けて均一なウエツブを得、これを熱圧着して
目付30g/m2の不織布を得た。
Spinneret temperature was 240°C, hole diameter was 0.3M, and spinning was carried out from a 12-hole spinneret at a discharge rate of 897 minutes per hole, and spinning was carried out at approximately 9000 m/minute while making a traverse motion using a suction jet device installed at 40 cIrL below the spinneret. A uniform web was obtained by spraying at a high speed onto a wire mesh, and this was thermocompressed to obtain a nonwoven fabric having a basis weight of 30 g/m2.

この不織布の経の引張強力は6.5Ky/5cm.で伸
度は80.3%、緯の引張強力7. 4 KP/ 5
crrL、伸度82.5%で、ナイロン6単独の同一条
件で得られた不織布と大差なかった。
The tensile strength of this nonwoven fabric is 6.5Ky/5cm. The elongation is 80.3% and the weft tensile strength is 7. 4 KP/5
crrL and elongation of 82.5%, which were not significantly different from the nonwoven fabric obtained under the same conditions using nylon 6 alone.

本発明の不織布の20℃、65%RH下の水分率は7、
1%であったのに対し、ナイロン6単独の不織布のそれ
は4.2%で、吸水性が改良されていることが明らかで
あった。
The moisture content of the nonwoven fabric of the present invention at 20°C and 65% RH is 7,
It was 1%, whereas that of the nonwoven fabric made of nylon 6 alone was 4.2%, which clearly showed that the water absorbency was improved.

実施例 2 十分に乾燥された平均重合度250、残存酢酸基58モ
ル%のPVA30重量部に平均分子量約8 0 0 0
0,融点165℃のポリプロピレン70重量部加え、
ベント式押出機(スクリュー径D40鵡〆、L/D=2
7 )の供給口に供給し、紡糸頭温度170℃、孔径
0,3嗣、50孔の紡糸口金から1孔当り1. 3 0
gl分の吐出量で紡出した。
Example 2 30 parts by weight of sufficiently dried PVA with an average degree of polymerization of 250 and a residual acetic acid group of 58 mol % and an average molecular weight of about 8000
0. Added 70 parts by weight of polypropylene with a melting point of 165°C,
Vented extruder (screw diameter D40, L/D=2
7), and the spinning head temperature was 170°C, the hole diameter was 0.3 mm, and 1.0 mm per hole was fed from a 50-hole spinneret. 3 0
Spinning was carried out at a discharge rate of 1 gl.

紡糸口金下100crrLに設置した吸引ジェット装置
をトラバース運動させながら約6000m/分の紡糸速
度で引取り金網上に吹付け均一なウエツブとし、これを
熱圧着して約3 0 97m’目付の不織布を得た。
A suction jet device installed at 100 crrL below the spinneret was moved in a traversal motion, and the spinning speed was about 6000 m/min, and the web was sprayed onto a wire mesh to form a uniform web, which was then thermocompressed to form a nonwoven fabric with a fabric weight of about 3097 m'. Obtained.

この不織布の20℃、65SRH下の吸水性は3.8係
でポリプロピレン単独の不織布のそれが0.1%である
のに対し、吸水性が大きく改良されていた。
The water absorbency of this nonwoven fabric at 20° C. and 65 SRH was 3.8, which was 0.1% for the nonwoven fabric made only of polypropylene, but the water absorption was greatly improved.

不織布の機械的強度は大差なかった。There was no significant difference in the mechanical strength of the nonwoven fabrics.

実施例 3 十分乾燥した平均重合度170、残存酢酸基38モル係
のPVA60重量部に平均分子量約20.000のナイ
ロン6樹脂40重量部加え、実施例1と同様に溶融紡糸
した。
Example 3 40 parts by weight of nylon 6 resin having an average molecular weight of about 20,000 was added to 60 parts by weight of sufficiently dried PVA having an average degree of polymerization of 170 and a residual acetic acid group of 38 mol, and melt spinning was carried out in the same manner as in Example 1.

一方、前記のナイロン6樹脂を紡糸頭温度250℃、孔
径0.3#〆、60孔の紡糸口金より1孔当り1.89
7分の吐出量で紡糸し、紡出フィラメントを前記のP
V A/ナイロン6混合溶融紡糸フィラメントと両者の
・紡糸口金下60crfLのところで引揃え、そこに設
置された吸引ジェット装置をトラバースさせながら約9
000m/分の紡糸速度で引取り、噴射気流により金網
状の非織性シート形或面上に均一に吹付け、ウエツブを
堆積した。
On the other hand, the above-mentioned nylon 6 resin was spun at a spinning head temperature of 250°C, a hole diameter of 0.3#, and a spinneret of 60 holes at a rate of 1.89 mm per hole.
The spun filament was spun at a discharge rate of 7 minutes, and the spun filament was
VA/Nylon 6 mixed melt spun filament and both were aligned at 60 crfL below the spinneret, and the suction jet device installed there was traversed for about 9
The web was taken up at a spinning speed of 1,000 m/min and sprayed uniformly onto a non-woven sheet shaped like a wire mesh using a jet air stream to deposit a web.

これを水蒸気処理後100℃の加熱ローラー間で圧着し
、乾燥してPVA−ナイロン混合紡糸フィラメント/ナ
イロン6フィラメントの重量比が約1/5の不織布を得
た。
After steam treatment, this was pressed between heating rollers at 100°C and dried to obtain a nonwoven fabric having a weight ratio of PVA-nylon mixed spun filament/nylon 6 filament of about 1/5.

得られた不織布の風合は良好であり、20℃、65ZR
H下の水分率は6.8係であったのに対し、ナイロン6
単独の不織布のそれは4.1%で、吸水性が改良されて
いることが明らかであった。
The texture of the obtained nonwoven fabric was good, and it was
The moisture content under H was 6.8%, while the moisture content under nylon 6
That of the nonwoven fabric alone was 4.1%, and it was clear that the water absorption was improved.

Claims (1)

【特許請求の範囲】[Claims] 1 疎水性熱可塑性樹脂と平均重合度50〜300残存
酢酸基15〜70モル係のポリビニルアルコールとを混
合溶融押出したフィラメント群を単独または他繊維のフ
ィラメント群と引揃えるか、あるいは別々に吸引ジェッ
トにて引取り、噴射気流により非織性シート形戒面上に
吹付け堆積することを特徴とする不織布の製造方法。
1 A group of filaments obtained by mixing and melt-extruding a hydrophobic thermoplastic resin and polyvinyl alcohol having an average degree of polymerization of 50 to 300 and a residual acetic acid group of 15 to 70 mols is used singly or with a group of filaments of other fibers, or separately by a suction jet. 1. A method for producing a nonwoven fabric, which comprises taking the nonwoven fabric in a vacuum cleaner, and spraying and depositing it onto a nonwoven sheet-shaped surface using a jet of air.
JP50038157A 1975-03-29 1975-03-29 Fushiyokufunoseizouhouhou Expired JPS5836102B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP50038157A JPS5836102B2 (en) 1975-03-29 1975-03-29 Fushiyokufunoseizouhouhou

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP50038157A JPS5836102B2 (en) 1975-03-29 1975-03-29 Fushiyokufunoseizouhouhou

Publications (2)

Publication Number Publication Date
JPS51112979A JPS51112979A (en) 1976-10-05
JPS5836102B2 true JPS5836102B2 (en) 1983-08-06

Family

ID=12517563

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50038157A Expired JPS5836102B2 (en) 1975-03-29 1975-03-29 Fushiyokufunoseizouhouhou

Country Status (1)

Country Link
JP (1) JPS5836102B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6394701U (en) * 1986-12-11 1988-06-18
JPH0427606Y2 (en) * 1987-11-24 1992-07-02

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4935104A (en) * 1972-08-08 1974-04-01

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4935104A (en) * 1972-08-08 1974-04-01

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6394701U (en) * 1986-12-11 1988-06-18
JPH0427606Y2 (en) * 1987-11-24 1992-07-02

Also Published As

Publication number Publication date
JPS51112979A (en) 1976-10-05

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