JP2716810B2 - Polyamide resin composition for filament and filament - Google Patents

Polyamide resin composition for filament and filament

Info

Publication number
JP2716810B2
JP2716810B2 JP21601989A JP21601989A JP2716810B2 JP 2716810 B2 JP2716810 B2 JP 2716810B2 JP 21601989 A JP21601989 A JP 21601989A JP 21601989 A JP21601989 A JP 21601989A JP 2716810 B2 JP2716810 B2 JP 2716810B2
Authority
JP
Japan
Prior art keywords
filament
polyamide resin
resin composition
acid
weight
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 - Lifetime
Application number
JP21601989A
Other languages
Japanese (ja)
Other versions
JPH0381364A (en
Inventor
隆一 出口
武純 西尾
茜 岡田
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.)
Toyota Central R&D Labs Inc
Ube Corp
Original Assignee
Ube Industries Ltd
Toyota Central R&D Labs Inc
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Filing date
Publication date
Application filed by Ube Industries Ltd, Toyota Central R&D Labs Inc filed Critical Ube Industries Ltd
Priority to JP21601989A priority Critical patent/JP2716810B2/en
Publication of JPH0381364A publication Critical patent/JPH0381364A/en
Application granted granted Critical
Publication of JP2716810B2 publication Critical patent/JP2716810B2/en
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Expired - Lifetime legal-status Critical Current

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  • Artificial Filaments (AREA)

Description

【発明の詳細な説明】 [発明の目的] (産業上の利用分野) 本発明は、フィラメント用ポリアミド樹脂組成物及び
そのフィラメントに関し、さらに詳しくは優れた強度・
伸度を有し、かつ剛性・引き抜き力に優れ、かつ熱収縮
・熱水収縮性、寸法安定性に優れ、衣料用として良好な
風合を持つモノ及びマルチフィラメント用樹脂組成物並
びにモノ及びマルチフィラメントに関する。
DETAILED DESCRIPTION OF THE INVENTION [Object of the Invention] (Industrial application field) The present invention relates to a polyamide resin composition for filaments and filaments thereof, and more particularly to excellent strength and strength.
Resin compositions for mono- and multi-filaments having excellent elongation, excellent rigidity and pull-out force, excellent heat shrinkage / hot water shrinkage, and dimensional stability, and good texture for clothing, and mono and multi Regarding filament.

(従来の技術) ポリアミド樹脂は、その優れた強度・伸度等の特性か
ら、釣り糸、歯ブラシ、マジックファスナーなどのモノ
フィラメント及びタイヤコード、衣料などのマルチフィ
ラメントに幅広く利用されている。
(Prior Art) Polyamide resins are widely used in monofilaments such as fishing lines, toothbrushes and magic fasteners, and multifilaments such as tire cords and clothing because of their excellent properties such as strength and elongation.

しかしながら、従来のポリアミド樹脂は、一部の釣り
糸、歯ブラシ等に用いられるブリッスル(荒毛)、マジ
ックファスナー、タイヤコード、絨毯、人工芝などの用
途では、その剛性、弾性率が十分でなく、さらに弾性率
の高い材料が望まれている。また衣料用では剛性のある
フィラメントで、つや消し風合のものが望まれている。
また、染色時やアイロン処理等、加熱された時の収縮率
が小さく、寸法の安定した材料が望まれている。
However, conventional polyamide resins have insufficient rigidity and elasticity in applications such as bristles (rough hair), magic fasteners, tire cords, carpets, and artificial turf used for some fishing lines, toothbrushes, and the like. A material having a high elastic modulus is desired. In addition, a stiff filament having a matte texture is desired for clothing.
Further, a material having a small shrinkage ratio when heated, such as during dyeing or ironing, and having stable dimensions is desired.

(発明が解決しようとする課題) 本発明は、従来のポリアミド樹脂組成物からなるフィ
ラメントの問題点を改良し、優れた強度・伸度を有し、
かつ、剛性、引き抜き力、熱収縮、熱水収縮性、寸法安
定性にも優れ、また、衣料用として風合の優れたモノ及
びマルチフィラメント用樹脂組成物並びにモノ及びマル
チフィラメントを提供することを目的とする。
(Problems to be Solved by the Invention) The present invention improves the problems of filaments made of a conventional polyamide resin composition, has excellent strength and elongation,
Also, to provide a mono- and multi-filament resin composition and a mono- and multi-filament excellent in rigidity, pull-out force, heat shrinkage, hot water shrinkage, dimensional stability, and excellent feeling for clothing. Aim.

[発明の構成] (課題を解決するための手段及び作用) 本発明は、ポリアミド樹脂(A)100重量部と(A)
成分中に均一に分散されている層状珪酸塩(B)0.05〜
30重量部のポリアミド樹脂組成物及び該ポリアミド樹脂
組成物からなるフィラメントである。
[Constitution of the Invention] (Means and Actions for Solving the Problems) The present invention relates to a polyamide resin (A) of 100 parts by weight and (A)
Layered silicate (B) uniformly dispersed in the components 0.05 to
30 parts by weight of a polyamide resin composition and a filament comprising the polyamide resin composition.

ポリアミド樹脂(A)は、分子中に酸アミド結合(−
CONH−)を有する重合体であり、具体的には、ε−カプ
ロラクタム、6−アミノカプロン酸、ω−エナントラク
タム、7−アミノヘプタン酸、11−アミノウンデカン
酸、9−アミノノナン酸、α−ピロリドン、α−ピペリ
ドンなどから得られる重合体又は共重合体;ヘキサメチ
レンジアミン、ノナメチレンジアミン、ウンデカメチレ
ンジアミン、ドデカメチレンジアミン、メタキシリレン
ジアミンなどのジアミンとテレフタル酸、イソフタル
酸、アジピン酸、セバシン酸などのジカルボン酸とを重
縮合して得られる重合体若しくは共重合体又はこれらの
ブレンド物を例示することができる。
The polyamide resin (A) has an acid amide bond (-
CONH-), specifically, ε-caprolactam, 6-aminocaproic acid, ω-enantholactam, 7-aminoheptanoic acid, 11-aminoundecanoic acid, 9-aminononanoic acid, α-pyrrolidone, Polymers or copolymers obtained from α-piperidone and the like; diamines such as hexamethylenediamine, nonamethylenediamine, undecamethylenediamine, dodecamethylenediamine, and metaxylylenediamine, and terephthalic acid, isophthalic acid, adipic acid, and sebacic acid Examples of the polymer include a polymer or copolymer obtained by polycondensation with a dicarboxylic acid or a blend thereof.

ポリアミド樹脂(A)の、平均分子量は10,000〜30,0
00が好ましい。
The average molecular weight of the polyamide resin (A) is 10,000 to 30,0
00 is preferred.

平均分子量が10,000以下では、フィラメントの紡糸・
延伸が困難であり、30,000以上になるとポリアミド自体
の生産が難しくなるので好ましくない。
If the average molecular weight is 10,000 or less,
Stretching is difficult, and if it exceeds 30,000, production of polyamide itself becomes difficult, which is not preferable.

層状珪酸塩(B)は、ポリアミド樹脂(A)に、その
優れた引張り伸び特性を損なうことなく、剛性、高弾
性、高引き抜き力特性及び優れた風合を付与するための
成分である。
The layered silicate (B) is a component for imparting rigidity, high elasticity, high pull-out force characteristics, and excellent feeling to the polyamide resin (A) without impairing its excellent tensile elongation characteristics.

層状珪酸塩(B)は、(A)成分中に分散させた際、
平均的に20Å以上の層間距離を保ち、均一に分散するも
のであることが好ましい。ここで層間距離とは層状珪酸
塩の平板の重心間の距離を言い、均一に分散するとは層
状珪酸塩の一枚一枚が、若しくは平均的な重なりが5層
以下の多層物が平行に、またはランダムに、もしくは平
行とランダムが混在した状態で50重量%以上が、好まし
くは70重量%以上が局所的な塊を形成することなく分散
する状態を言う。ここで、層状珪酸塩は、厚みが6〜20
Åで、一辺が0.002〜1μmの層状一単位を示す。
When the layered silicate (B) is dispersed in the component (A),
It is preferable that the interlayer distance is maintained at an average of 20 ° or more on average and the layer is uniformly dispersed. Here, the interlayer distance refers to the distance between the centers of gravity of the plate of the layered silicate, and to uniformly disperse, the layered silicate is one by one, or a multilayer having an average overlap of 5 layers or less is parallel. Or, a state in which 50% by weight or more, preferably 70% by weight or more is dispersed without forming a local mass at random or in a state where parallel and random are mixed. Here, the layered silicate has a thickness of 6 to 20.
Å indicates a layered unit having a side of 0.002 to 1 μm.

このような層状珪酸塩の原料としては、珪酸マグネシ
ウム又は珪酸アルミニウムの層から構成される層状フィ
ロ又は珪酸鉱物を例示することができる。具体的には、
モンモリロナイト、サポナイト、バイデライト、ノント
ロナイト、ヘクトライト、スティブンサイトなどのスメ
クタイト系粘土鉱物及びバーミキュライト、ハロイサイ
トなどを例示することができ、これらは天然のものであ
っても、合成されたものであってもよい。これらのなか
でもモンモリロナイトが好ましい。
As a raw material of such a layered silicate, a layered phyllo or a silicate mineral composed of a layer of magnesium silicate or aluminum silicate can be exemplified. In particular,
Examples include smectite-based clay minerals such as montmorillonite, saponite, beidellite, nontronite, hectorite, stevensite, vermiculite, halloysite, and the like, which may be natural or synthesized. You may. Of these, montmorillonite is preferred.

(A)成分と(B)成分の組成は、(A)成分100重
量部に対して(B)成分が0.05〜30重量部である。
(B)成分の組成が0.05重量部未満であると、剛性、弾
性、引き抜き力の向上が顕著でなく、30重量部を超える
と生産が難しくなるため好ましくない。
The composition of the component (A) and the component (B) is such that the component (B) is 0.05 to 30 parts by weight based on 100 parts by weight of the component (A).
If the composition of the component (B) is less than 0.05 parts by weight, the rigidity, elasticity, and pull-out force are not significantly improved, and if it exceeds 30 parts by weight, production becomes difficult, which is not preferable.

本発明の組成物又はフィラメントの製造時に、目的に
応じて、染料、顔料、可塑剤、耐熱剤、透明剤、滑剤、
帯電防止剤などを適宜、適量を配合することができる。
During the production of the composition or filament of the present invention, depending on the purpose, dyes, pigments, plasticizers, heat-resistant agents, clarifiers, lubricants,
An appropriate amount of an antistatic agent or the like can be appropriately compounded.

層状珪酸塩(B)が多層状粘土鉱物である場合には、
(ジ)オクタデシルアミン、フェニレンジアミンのよう
なアミン、4−アミノ−n−酪酸、12−アミノドデカン
酸のようなアミノ酸又はε−カプロラクタムのようなラ
クタム類の膨潤化剤と接触させて、予め層間を拡げて層
間にモノマーを取り込みやすくした後、ポリアミドモノ
マーと混合し、重合する方法(特開昭62−74957号公報
参照)がある。また、膨潤化剤を用い、予め層間を20Å
以上に拡げて、これをポリアミド樹脂若しくはこれを含
む樹脂と溶融混練して均一に分散させる方法によっても
よい。
When the layered silicate (B) is a multilayered clay mineral,
(D) by contacting with a swelling agent of an amine such as octadecylamine or phenylenediamine, an amino acid such as 4-amino-n-butyric acid or 12-aminododecanoic acid or a lactam such as ε-caprolactam, And then mixing with a polyamide monomer and polymerizing (see JP-A-62-74957). Also, use a swelling agent and pre-
It is also possible to adopt a method in which the above is expanded and melt-kneaded with a polyamide resin or a resin containing the same to uniformly disperse them.

本発明のフィラメントは、その原料組成物を単軸など
の溶融押出機にて溶融状態とし、さらに、その吐出量を
定量的に実施するギヤポンプ等により、紡糸口金から押
し出し、空気又は水などで冷却しながら、所定の引き取
り速度で引き取ること等によって製造することができ
る。
The filament of the present invention is obtained by melting the raw material composition in a melt extruder such as a single-screw extruder from a spinneret by a gear pump or the like for quantitatively controlling the discharge amount, and cooling with air or water. Meanwhile, it can be manufactured by taking at a predetermined take-up speed or the like.

さらに得られたフィラメントは、用途によって種々の
倍率で延伸することができるし、また、上記溶融紡糸時
に、同時に延伸することができる。
Further, the obtained filament can be drawn at various magnifications depending on the application, and can be drawn simultaneously with the melt spinning.

フィラメントの形状は、単糸・複数糸又は複数糸の撚
り合わせたものであってもよいし、その断面は、円形に
限らず、中空・星形などの異形断面であってもよい。
The shape of the filament may be a single yarn, a plurality of yarns or a combination of a plurality of yarns, and the cross section thereof is not limited to a circle, and may be an irregular cross section such as a hollow or star shape.

(発明の効果) 本発明のフィラメントは、各種のモノ及びマルチフィ
ラメントに用いることができ、特に、ブラシ用ブリッス
ル、釣り糸、マジックファスナー、タイヤコード、人工
芝、絨毯、自動車座席用シート、魚網、ロープ、ザイ
ル、フィルター用糸などの用途に剛性の強い製品を与え
る。また染色やアイロン処理等、加熱された時の収縮率
が小さく、寸法及び織物としての形状の安定した製品を
与える。また腰の強い特殊な風合いを持つ衣料用の繊維
としても用いることができる。
(Effect of the Invention) The filament of the present invention can be used for various types of monofilaments and multifilaments. In particular, bristles for brushes, fishing lines, magic fasteners, tire cords, artificial turf, carpets, car seats, fishnets, ropes Gives products with high rigidity to applications such as yarn, filter, and yarn for filters. In addition, the shrinkage ratio when heated such as dyeing or ironing is small, and a product having a stable size and shape as a woven fabric is provided. Also, it can be used as a fiber for clothing having a strong and special texture.

(実施例) 実施例1 層状珪酸塩の一単位の厚みが平均的に9.5Åで一辺の
平均長さが約0.1μmのモンモリロナイト100gを10lの水
に分散させ、これに51.2gの12−アミノドデカン酸と24m
lの濃塩酸を加え、5分間攪拌したのち、過した。さ
らにこれを十分洗浄したのち、真空乾燥した。この操作
により、12−ドデカン酸アンモニウム[NH3 +(CH2)11COO
-]とモンモリロナイトの複合体を調製した。複合体中
の層状珪酸塩分は80重量%となった。
(Example) Example 1 100 g of montmorillonite having an average thickness of one unit of the layered silicate of 9.5 mm and an average length of one side of about 0.1 μm is dispersed in 10 l of water, and 51.2 g of 12-amino acid is added thereto. 24m with dodecanoic acid
l of concentrated hydrochloric acid was added, and the mixture was stirred for 5 minutes and then passed. After sufficiently washing this, it was vacuum-dried. By this operation, ammonium 12-dodecanoate [NH 3 + (CH 2 ) 11 COO
- ] And montmorillonite were prepared. The layered silicate content in the composite was 80% by weight.

次に、攪拌機付の反応容器に、10kgのε−カプロラク
タム、1kgの水及び90gの前記複合体を入れ、100℃で反
応系内が均一な状態になるように攪拌した。さらに温度
を260℃に上昇させ、15kg/cm2の加圧下で1時間攪拌し
た。その後、放圧し、水分を反応容器から揮散させなが
ら、常圧下で2時間反応させた。反応終了後、反応容器
の下部ノズルから、ストランド状に取り出した反応物を
水冷し、カッティングを行い、ポリアミド樹脂(平均分
子量15,000)及びモンモリロナイトからなるペレットを
得た。このペレットを熱水中に浸漬し、未反応のモノマ
ー(約10%)を抽出、除去したのち、真空中で乾燥し
て、ポリアミド樹脂組成物を得た。
Next, 10 kg of ε-caprolactam, 1 kg of water and 90 g of the complex were placed in a reaction vessel equipped with a stirrer, and stirred at 100 ° C. so that the inside of the reaction system became uniform. The temperature was further raised to 260 ° C., and the mixture was stirred under a pressure of 15 kg / cm 2 for 1 hour. Thereafter, the pressure was released, and the reaction was carried out at normal pressure for 2 hours while evaporating water from the reaction vessel. After completion of the reaction, the reaction product taken out in a strand form from the lower nozzle of the reaction vessel was water-cooled and cut to obtain a pellet comprising a polyamide resin (average molecular weight 15,000) and montmorillonite. The pellet was immersed in hot water to extract and remove unreacted monomer (about 10%), and then dried in vacuum to obtain a polyamide resin composition.

このようにして得られた材料について、次のような評
価試験を行った。
The materials thus obtained were subjected to the following evaluation tests.

(1)モノフィラメント評価試験 試験材料を、下記条件の押出機に投入し、直径1.47mm
8穴のノズルから溶融押し出し、7℃の冷却水中で冷却
し、第1ローラーで引張り、さらに、第2ローラーの引
き取り速度を第1ローラーの3.9倍として延伸し(延伸
温度250℃)、さらに第3ローラーの引き取り速度を、
第1ローラーの5倍とし、さらに延伸し(延伸温度300
℃)、最後に、第4ローラーを第3ローラーと同一の引
き取り速度で引き取り、その間を雰囲気温度220℃と
し、熱固定してモノフィラメントを得た。
(1) Monofilament evaluation test The test material was charged into an extruder under the following conditions, and the diameter was 1.47 mm.
It is melted and extruded from an 8-hole nozzle, cooled in 7 ° C. cooling water, pulled by the first roller, and further stretched at a take-up speed of the second roller 3.9 times that of the first roller (stretching temperature 250 ° C.). The take-up speed of the three rollers
5 times as large as the first roller and stretched further (stretching temperature 300
° C), and finally, the fourth roller was pulled at the same pulling speed as the third roller. During that time, the ambient temperature was set to 220 ° C, and heat-fixed to obtain a monofilament.

(押出し機条件) スクリュー径:30mm シリンダー設定温度:C1 C2 C3 C4 N ℃ 220 240 260 270 260 得られたモノフィラメントにつき次の評価試験を行っ
た。
(Extruder conditions) Screw diameter: 30 mm Cylinder set temperature: C1 C2 C3 C4 N ° C 220 240 260 270 260 The following evaluation test was performed on the obtained monofilament.

1)繊度 2)引張り強度・伸度・弾性率 JIS L1070、L1073に準
じて測定 3)引き抜き力 第1図に示す治具を作成し、10mm径の孔よりフィラメ
ントをカギ状治具で引き抜く時の力をロードセルで測定
し、その最大値を引き抜き力とした。
1) Fineness 2) Tensile strength, elongation, and elastic modulus Measured according to JIS L1070, L1073 3) Pulling force When a jig shown in Fig. 1 is created and a filament is pulled out from a 10mm diameter hole with a hook-shaped jig Was measured with a load cell, and the maximum value was defined as the pull-out force.

4)熱水収縮率 試料を23℃相対湿度65%中に重量が一定になるまで静
置し、その後、長さ1,000mmに切断する。これを100℃水
中に15分間浸漬し、その直後の寸法を測定する。そして
この熱水収縮率を百分率にて算出する。
4) Hot water shrinkage The sample is allowed to stand at 23 ° C. and a relative humidity of 65% until the weight becomes constant, and then cut into a length of 1,000 mm. This is immersed in water at 100 ° C. for 15 minutes, and the dimensions immediately after that are measured. Then, this hot water shrinkage is calculated in percentage.

(2)マルチフィラメント評価試験 試料を(株)島津製作所製 紡糸機(スクリュー直径
30mm、L/D=23、圧縮比3.5)、同社製巻取機(STS−
1、表面駆動方式、1錘1ボビン)、同社製延伸撚糸機
(SD−4)にて、紡糸・延伸撚糸を行いマルチフィラメ
ントを得た。詳細条件は、下記のとおりである。
(2) Multifilament evaluation test A sample was prepared using a spinning machine (screw diameter, manufactured by Shimadzu Corporation).
30mm, L / D = 23, compression ratio 3.5), Company's winding machine (STS-
1, a surface drive system, a single bobbin and a bobbin), and a spinning / drawing and twisting yarn was used to obtain a multifilament. The detailed conditions are as follows.

(紡糸条件) 1)押出機設定温度:℃ C1 C2 C3 AD H D 210 230 250 260 260 250 2)ノズル:径0.45mm×30孔 3)引き取り速度:700m/min 4)フィルター:40/40/75/125/250/325メッシュ 5)冷却風速度:0.6m/s 6)油剤:丸菱油化(株)製 spinner F−160TS (延伸撚糸条件) 1)延伸温度:170℃(ホットピン) 2)延伸倍率:4倍 3)延伸速度:100m/min 以上のようにして、240d/30f目標のマルチフィラメン
トを作成した。
(Spinning conditions) 1) Set temperature of extruder: ° C C 1 C 2 C 3 ADHD 210 230 250 260 260 250 2) Nozzle: 0.45mm diameter x 30 holes 3) Take-off speed: 700m / min 4) Filter: 40 / 40/75/125/250/325 mesh 5) Cooling air velocity: 0.6m / s 6) Oil agent: spinner F-160TS manufactured by Marubishi Yuka Co., Ltd. (Drawing and twisting conditions) 1) Drawing temperature: 170 ° C ( Hot pin) 2) Stretching ratio: 4 times 3) Stretching speed: 100 m / min As described above, a multifilament with a target of 240d / 30f was prepared.

得られたマルチフィラメントにつき、次の評価試験を
行った。
The following evaluation test was performed on the obtained multifilament.

1)繊度 2)マルチフィラメント引張り弾性率 JIS L1070及び同L1073に準じて測定した。1) Fineness 2) Multifilament tensile elastic modulus Measured according to JIS L1070 and L1073.

3)糸の輝き、てらつきを目視にて評価。3) The shine and flicker of the yarn were visually evaluated.

結果を表に示す。 The results are shown in the table.

実施例2 実施例1において、攪拌機付の反応器に、10kgのε−
カプロラクタム、1kgの水及び180gの12−アミノドデカ
ン酸アンモニウムとモンモリロナイトの複合体を添加し
た以外は、実施例1と同様の実験を行った。結果を表に
示す。
Example 2 In Example 1, 10 kg of ε- was added to a reactor equipped with a stirrer.
The same experiment as in Example 1 was performed except that caprolactam, 1 kg of water and 180 g of a complex of ammonium 12-aminododecanoate and montmorillonite were added. The results are shown in the table.

比較例1 実施例1において、攪拌機付の反応器に10kgのε−カ
プロラクタム、1kgの水のみを装入し、複合体を添加せ
ずに、実施例1と同様の実験を行った。結果を表に示
す。
Comparative Example 1 In Example 1, only 10 kg of ε-caprolactam and 1 kg of water were charged into a reactor equipped with a stirrer, and the same experiment as in Example 1 was performed without adding the complex. The results are shown in the table.

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

第1図は引き抜き力測定用治具の説明図である。 FIG. 1 is an explanatory view of a jig for measuring a pull-out force.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 岡田 茜 愛知県愛知郡長久手町大字長湫字横道41 番地の1 株式会社豊田中央研究所内 (56)参考文献 特開 昭64−11157(JP,A) 特開 昭51−109998(JP,A) 特開 昭63−230766(JP,A) 特開 昭62−170515(JP,A) ────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Akane Okada 41-1, Oku-cho, Yokomichi, Nagakute-cho, Aichi-gun, Aichi Prefecture Inside Toyota Central R & D Laboratories, Inc. (56) References JP-A-51-109998 (JP, A) JP-A-63-230766 (JP, A) JP-A-62-170515 (JP, A)

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】ポリアミド樹脂(A)100重量部と層状珪
酸塩(B)0.05〜30重量部とからなるフィラメント用ポ
リアミド樹脂組成物。
1. A polyamide resin composition for filaments comprising 100 parts by weight of a polyamide resin (A) and 0.05 to 30 parts by weight of a layered silicate (B).
【請求項2】請求項1記載のポリアミド樹脂組成物から
なるフィラメント。
2. A filament comprising the polyamide resin composition according to claim 1.
JP21601989A 1989-08-24 1989-08-24 Polyamide resin composition for filament and filament Expired - Lifetime JP2716810B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21601989A JP2716810B2 (en) 1989-08-24 1989-08-24 Polyamide resin composition for filament and filament

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21601989A JP2716810B2 (en) 1989-08-24 1989-08-24 Polyamide resin composition for filament and filament

Publications (2)

Publication Number Publication Date
JPH0381364A JPH0381364A (en) 1991-04-05
JP2716810B2 true JP2716810B2 (en) 1998-02-18

Family

ID=16682027

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21601989A Expired - Lifetime JP2716810B2 (en) 1989-08-24 1989-08-24 Polyamide resin composition for filament and filament

Country Status (1)

Country Link
JP (1) JP2716810B2 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0683252A1 (en) * 1994-05-16 1995-11-22 AlliedSignal Inc. Polyamide fiber
KR100407219B1 (en) * 1998-06-10 2004-03-12 (주)성신텍스타일 Manufacturing method of illite nylon filament yarn
KR20000018829A (en) * 1998-09-03 2000-04-06 문태수 Method for producing synthetic fiber mixed with illite
KR20000045849A (en) * 1998-12-30 2000-07-25 조정래 Polyamide composition and production method thereof
FR2796086B1 (en) * 1999-07-06 2002-03-15 Rhodianyl ABRASION RESISTANT WIRE ARTICLES
JP4183710B2 (en) * 2003-09-16 2008-11-19 帝人株式会社 Totally aromatic polyamide fiber and method for producing the same
DE102005005023A1 (en) * 2005-02-03 2006-08-10 Trw Automotive Safety Systems Gmbh & Co. Kg airbag

Also Published As

Publication number Publication date
JPH0381364A (en) 1991-04-05

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