JPH11323729A - Polyamide yarn having small fineness and large strength and its production - Google Patents

Polyamide yarn having small fineness and large strength and its production

Info

Publication number
JPH11323729A
JPH11323729A JP13793198A JP13793198A JPH11323729A JP H11323729 A JPH11323729 A JP H11323729A JP 13793198 A JP13793198 A JP 13793198A JP 13793198 A JP13793198 A JP 13793198A JP H11323729 A JPH11323729 A JP H11323729A
Authority
JP
Japan
Prior art keywords
yarn
oil
stretching
agent
interlacer
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
Application number
JP13793198A
Other languages
Japanese (ja)
Inventor
Takeshi Nishiyama
武史 西山
Yukio Manabe
幸夫 真鍋
Azusa Tanaka
あずさ 田中
Yoshinori Tsukada
吉則 塚田
Masahiro Hosoda
雅弘 細田
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.)
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 JP13793198A priority Critical patent/JPH11323729A/en
Publication of JPH11323729A publication Critical patent/JPH11323729A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To obtain the subject yarn having good strengths and a good touch and useful for sports wears, clothes, etc., by melt-spinning a polyamide resin, subjecting the spun yarn to interlacing treatments and oiling treatments before and after a drawing treatment, and subsequently winding up the treated yarn. SOLUTION: This polyamide yarn having a total fineness of <=35 denier, a strength of >=6.0 g/denier and an interlacing number of >=35 interlaced points/ m is obtained by melt-spinning a polyamide resin from a spinneret 1, cooling the spun filaments, imparting a non-aqueous oiling agent to the cooled filaments and simultaneously bundling the filaments in a slit nozzle 2, simultaneously treating the obtained yarn with a fluid in an interlacer 3 to subject the yarn to the first interlacing treatment, drawing the yarn between rollers 4, 5, subjecting the yarn to the second interlacing treatment in an interlacer 6, imparting an oiling agent containing a dioctylsulfosuccinate salt and a polyoxyethylene alkyl ether and/or a polyoxyethylene alkylphenyl ether as an after oil having a high sizing agent-conjugating property in a slit nozzle 7, and subsequently winding up the treated yarn on a package 9 with a winder 8.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、特にスポーツ用
途、一般衣料用途に好適な、強度及び風合いに優れた高
密度織物を得ることができる細繊度で高強力のポリアミ
ド繊維及びその製造方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fine and high-strength polyamide fiber capable of obtaining a high-density woven fabric excellent in strength and texture, particularly suitable for sports use and general clothing use, and a method for producing the same. It is.

【0002】[0002]

【従来の技術】近年、スポーツ用途やアウトドア用途に
おいて、薄く、かつ高強度の織物が求められている。こ
の要求を満たすために、トータル繊度が35デニール
(d)以下の細繊度で、フィラメント数が30本以下で6.
0 g/d以上の強度を有する高強力の繊維が開発されて
いる。
2. Description of the Related Art In recent years, thin and high-strength woven fabrics have been required for sports and outdoor applications. In order to satisfy this requirement, the total fineness is 35 denier (d) or less, and the number of filaments is 30 or less.
High-strength fibers having a strength of 0 g / d or more have been developed.

【0003】このような繊維は、製造する際に、エマル
ジョン油剤では十分に満足できる強伸度等の物性のもの
とならないため、非水系の油剤を付与している。しかし
ながら、非水系の油剤が付与されていると、この繊維を
製織時に経糸用に使用すると、繊維に付着させる糊剤が
繊維内部まで浸透しにくく(糊剤の抱合性が悪く)な
り、製織時に糊落ちし、ひいては糸条の開繊を引き起こ
すために製織性が悪化したり、得られた織物の品位が悪
くなるという問題点があった。
[0003] In the production of such a fiber, a non-aqueous oil agent is provided since an emulsion oil agent does not have properties such as sufficiently high elongation at the time of production. However, if a non-aqueous oil agent is applied, if this fiber is used for warp during weaving, the sizing agent to be attached to the fiber will not easily penetrate into the fiber (poor binding of the sizing agent), and during weaving. There is a problem in that the paste is degreased and eventually the yarn is opened, so that the weaving property is deteriorated and the quality of the obtained woven fabric is deteriorated.

【0004】この問題点を解決するためには、糸条の交
絡数を多くして糊剤との絡みをよくし、繊維の開繊を抑
える方法が一般的な手法として考えられる。しかしなが
ら、直接紡糸延伸法では、交絡数を増やすためにインタ
ーレーサでの流体処理のエアー圧を上げすぎると、糸条
に毛羽が発生しやすくなるという問題があった。また、
交絡数を多くするために糸条を一度巻き取った後に再度
交絡を付与すると、十分な数の交絡を糸条に付与するこ
とが可能であるが、手間がかかる上にコストも高くなる
という問題があった。
In order to solve this problem, a general method is considered in which the number of entangled yarns is increased to improve the entanglement with the sizing agent and to suppress fiber opening. However, in the direct spinning and drawing method, if the air pressure of the fluid treatment in the interlacer is too high in order to increase the number of entanglements, there is a problem that fluff is likely to be generated on the yarn. Also,
If the confounding is applied again after winding the yarn once to increase the number of confounds, it is possible to impart a sufficient number of confounds to the yarn, but it takes time and costs. was there.

【0005】[0005]

【発明が解決しようとする課題】本発明は、上述した問
題点を解決し、細繊度かつ高強力であり、製織時に糊落
ちせずに品位良好な高密度織物を得ることができる細繊
度高強力ポリアミド繊維と、この繊維を直接紡糸延伸法
によって、毛羽等の問題がなく効率的に製造する製造方
法を提供することを技術的な課題とするものである。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems and provides a high-density woven fabric which is fine and high in strength, and which can obtain a high-quality high-density woven fabric without falling off during weaving. An object of the present invention is to provide a high-strength polyamide fiber and a production method for producing the fiber efficiently by a direct spinning and drawing method without problems such as fluff.

【0006】[0006]

【課題を解決するための手段】本発明者らは、上記課題
を解決するために鋭意検討した結果、本発明に到達し
た。すなわち、本発明は次の(1)〜(2)を要旨とす
るものである。 (1)トータル繊度35デニール以下、強度6.0 g/デニ
ール以上、交絡数35個/m以上であって、ジオクチルス
ルホサクシネート塩と、ポリオキシエチレンアルキルエ
ーテル及び/又はポリオキシエチレンアルキルフェニル
エーテルを含有する油剤が付与されていることを特徴と
する細繊度高強力ポリアミド繊維。 (2)ポリアミド樹脂を溶融紡糸し、紡糸糸条を冷却し
た後、ローラ間で延伸し、3000m/分以上の速度で巻き
取る直接紡糸延伸法により製造する方法であって、延伸
の前及び後にインターレーサで糸条を流体処理して交絡
を付与し、かつ延伸前には非水油剤を付与し、延伸後に
はアフターオイルとして、ジオクチルスルホサクシネー
ト塩と、ポリオキシエチレンアルキルエーテル及び/又
はポリオキシエチレンアルキルフェニルエーテルを含有
する油剤を付与することを特徴とする(1)記載の細繊
度高強力ポリアミド繊維の製造方法。
Means for Solving the Problems The present inventors have made intensive studies to solve the above problems, and as a result, have reached the present invention. That is, the present invention provides the following (1) and (2). (1) Total fineness of 35 denier or less, strength of 6.0 g / denier or more, entanglement number of 35 / m or more, containing dioctyl sulfosuccinate salt and polyoxyethylene alkyl ether and / or polyoxyethylene alkyl phenyl ether And a high-strength polyamide fiber having a fine fineness. (2) A method of producing by a direct spin drawing method in which a polyamide resin is melt-spun and the spun yarn is cooled, then drawn between rollers, and wound at a speed of 3000 m / min or more, before and after drawing. The yarn is subjected to fluid treatment with an interlacer to impart entanglement, and a non-hydraulic agent is applied before stretching, and after stretching, as an after oil, dioctyl sulfosuccinate salt, polyoxyethylene alkyl ether and / or polyoxyethylene alkyl ether. The method for producing a polyamide fiber having high fineness and fineness according to (1), wherein an oil agent containing oxyethylene alkylphenyl ether is provided.

【0007】なお、本発明における繊維の強伸度は、島
津製作所製オートグラフAGS−50Dを用い、試料長
25cm、引っ張り速度25cm/分で測定した。また、交絡数
は、JIS-L-1013 7 13 記載の方法で測定を実施し、糸条
1mあたりの交絡数を算出した。
[0007] The strength and elongation of the fiber in the present invention was measured using an autograph AGS-50D manufactured by Shimadzu Corporation and the sample length was measured.
The measurement was performed at 25 cm and a pulling speed of 25 cm / min. The number of entanglements was measured by the method described in JIS-L-1013 713 to calculate the number of entanglements per 1 m of yarn.

【0008】[0008]

【発明の実施の形態】次に、本発明について詳細に説明
する。本発明のポリアミド繊維は、ナイロン6、ナイロ
ン11、ナイロン12、ナイロン46、ナイロン66、
ナイロン610等からなるものが挙げられるが、これら
に限定されるものではなく、また、これらを2種類以
上、共重合又は混合したものでもよい。そして、本発明
のポリアミド繊維の特性を損なわない範囲であれば、各
種の添加剤(艶消剤、着色剤、安定剤、制電剤等)を含
んでいるものでもよい。
Next, the present invention will be described in detail. The polyamide fiber of the present invention is nylon 6, nylon 11, nylon 12, nylon 46, nylon 66,
Examples thereof include nylon 610 and the like, but the present invention is not limited thereto. Two or more of these may be copolymerized or mixed. As long as the properties of the polyamide fiber of the present invention are not impaired, the polyamide fiber may contain various additives (such as a matting agent, a coloring agent, a stabilizer, and an antistatic agent).

【0009】本発明のポリアミド繊維は、製織すると、
高密度で高強力の織物が得られるものであり、トータル
繊度35d以下、強度6.0 g/d以上であることが必要で
ある。繊度が35dを超えると、高密度で風合いの良好
な織物が得られなくなり、強度6.0 g/d未満では、織
物としたときの強度が不足する。
When the polyamide fiber of the present invention is woven,
A high-density and high-strength woven fabric can be obtained, and it is necessary that the total fineness is 35 d or less and the strength is 6.0 g / d or more. If the fineness exceeds 35d, a woven fabric having a high density and good texture cannot be obtained, and if the strength is less than 6.0 g / d, the strength of the woven fabric is insufficient.

【0010】また、本発明の繊維は、ジオクチルスルホ
サクシネート塩と、ポリオキシエチレンアルキルエーテ
ル及び/又はポリオキシエチレンアルキルフェニルエー
テルを含有する油剤、すなわち、次の3種類の油剤のい
ずれかが付与されている。 ・ジオクチルスルホサクシネート塩とポリオキシエチレ
ンアルキルエーテルを含有する油剤 ・ジオクチルスルホサクシネート塩とポリオキシエチレ
ンアルキルフェニルエーテルを含有する油剤 ・ジオクチルスルホサクシネート塩とポリオキシエチレ
ンアルキルエーテルとポリオキシエチレンアルキルフェ
ニルエーテルを含有する油剤 これらの成分は、糊剤との相溶性に優れており、糊剤の
浸透性を向上させる作用がある。これらの成分を含有し
ている上記のような油剤が付与されていることによっ
て、糊剤が糸条の内部まで浸透しやすくなり、製織時に
糊剤が脱落しにくくなる。
Further, the fiber of the present invention is provided with an oil containing a dioctyl sulfosuccinate salt and a polyoxyethylene alkyl ether and / or a polyoxyethylene alkyl phenyl ether, ie, one of the following three oils. Have been.・ Oil containing dioctyl sulfosuccinate and polyoxyethylene alkyl ether ・ Oil containing dioctyl sulfosuccinate and polyoxyethylene alkyl phenyl ether ・ Dioctyl sulfosuccinate and polyoxyethylene alkyl ether and polyoxyethylene alkyl Oils Containing Phenyl Ether These components have excellent compatibility with the sizing agent and have an effect of improving the permeability of the sizing agent. By providing such an oil agent containing these components as described above, the sizing agent easily penetrates into the inside of the yarn, and the sizing agent does not easily fall off during weaving.

【0011】したがって、これらの成分が含有されてい
ないと、製経時に糊剤が表面のみを覆う状態となってし
まい、製織時のわずかな衝撃で糊剤が剥落してしまう。
[0011] Therefore, if these components are not contained, the sizing agent will only cover the surface during the manufacturing process, and the sizing agent will peel off with a slight impact during weaving.

【0012】この糊剤との抱合性に優れる油剤の付着量
は、繊維全体の0.05〜1.0重量%とすることが好
ましい。0.05重量%未満では、糊剤の浸透性を向上
させる効果が不十分となりやすく、1.0重量%を超え
ると、巻き取り時にパッケージの捲き弛みや汚れ等の問
題が発生する可能性が高くなる。
The amount of the oil agent excellent in conjugation with the sizing agent is preferably 0.05 to 1.0% by weight of the whole fiber. If it is less than 0.05% by weight, the effect of improving the permeability of the paste tends to be insufficient, and if it exceeds 1.0% by weight, there is a possibility that problems such as looseness and dirt of the package during winding will occur. Get higher.

【0013】さらに、本発明の繊維には、製経時に付与
する糊剤との絡みをよくし、製織時の糊落ちを防ぐため
に交絡数35個/m以上の交絡が付与されている。交絡数
が35個/m未満であると、糊剤の絡みが不十分となり、
糊落ちが生じる。本発明の繊維の交絡数は、さらに好ま
しくは40個/m以上であるが、本発明の繊維は、上記の
ような糊剤との抱合性に優れる油剤が付与されているた
め、交絡数をあまり多くしなくても糊落ちを防ぐことが
できるので、交絡数は50個/m程度あれば十分であ
る。
Further, the fibers of the present invention are entangled at a rate of 35 entangles / m or more in order to improve the entanglement with the sizing agent to be applied during the production and to prevent the sizing from occurring during weaving. When the number of entanglements is less than 35 / m, the entanglement of the glue becomes insufficient,
Paste occurs. The number of entanglements of the fiber of the present invention is more preferably 40 fibers / m or more, but the number of entanglements of the fiber of the present invention is reduced because an oil agent excellent in conjugation with the sizing agent as described above is provided. Since the amount of glue can be prevented without increasing the number, the number of entanglements should be about 50 / m.

【0014】次に、本発明のポリアミド繊維の製造方法
について説明する。本発明の製造方法は、ポリアミド樹
脂を溶融紡糸し、紡糸糸条を冷却固化した後、ローラ間
で延伸し、3000m/分以上の速度で巻き取る直接紡糸延
伸法により製造する方法であって、ローラ間での延伸の
前後にインターレーサでの交絡の付与と油剤の付与を行
うものである。
Next, a method for producing the polyamide fiber of the present invention will be described. The production method of the present invention is a method of producing by a direct spin drawing method in which a polyamide resin is melt-spun, a spun yarn is cooled and solidified, drawn between rollers, and wound at a speed of 3000 m / min or more, Before and after the stretching between the rollers, the interlacing and the oil agent are applied by the interlacer.

【0015】本発明においては、ローラ間で延伸する前
と後の2段階で流体処理を行う必要がある。すなわち、
直接紡糸延伸法において交絡を付与するに際して、製経
時の糊剤との抱合性を向上させるために、交絡数を多く
しようとして延伸後にのみインターレーサで高圧のエア
ーで流体処理して交絡を付与すると、糸条に毛羽が発生
する。したがって、本発明においては2段階で流体処理
を施し、かつ2段階で油剤を付与することにより、毛羽
の発生を抑えることができる。
In the present invention, it is necessary to perform fluid treatment in two stages before and after stretching between rollers. That is,
When applying confounding in the direct spinning and drawing method, in order to improve conjugation with the sizing agent over time, when increasing the number of confounds, fluid treatment with high-pressure air with an interlacer only after stretching is performed to impart confounding In addition, fluff is generated on the yarn. Therefore, in the present invention, the generation of fluff can be suppressed by performing the fluid treatment in two stages and applying the oil agent in two stages.

【0016】流体処理する際のインターレーサのエアー
圧は、3.0 〜6.0 kg/cm2 程度が好ましく、延伸前
よりも延伸後をやや高めにすることが好ましい。
The air pressure of the interlacer at the time of performing the fluid treatment is preferably about 3.0 to 6.0 kg / cm 2, and is preferably slightly higher after stretching than before stretching.

【0017】さらに、本発明においては、延伸の前と後
に油剤を付与するが、延伸前に付与する油剤は非水油剤
とする。延伸前に非水油剤を付与することによって、延
伸が良好に行われ、高強度の繊維とすることができる。
Further, in the present invention, the oil agent is applied before and after the stretching, and the oil agent applied before the stretching is a non-water-based oil agent. By applying the non-water-based oil agent before stretching, stretching can be performed favorably and a high-strength fiber can be obtained.

【0018】この延伸前の油剤の付与においては、紡糸
された糸条の集束も同時に行うことが好ましいので、イ
ンターレースによる流体処理を行う前に油剤の付与を行
うことが好ましい。この非水油剤の成分は特に限定され
るものではなく、通常、延伸前に集束性や延伸性を向上
させるために付与する油剤であればよい。
In the application of the oil before the drawing, it is preferable that the spun yarn be bundled at the same time, and therefore it is preferable to apply the oil before the fluid treatment by interlacing. The components of the non-water-based oil agent are not particularly limited, and may be any oil agent that is usually applied before stretching to improve convergence and stretchability.

【0019】そして、延伸後に、前記したジオクチルス
ルホサクシネート塩と、ポリオキシエチレンアルキルエ
ーテル及び/又はポリオキシエチレンアルキルフェニル
エーテルを含有する、糊剤との抱合性に優れる油剤をア
フターオイルとして付与する。この油剤は、エマルジョ
ン油剤として付与することが好ましい。これは、エマル
ジョン油剤で付与することにより、糸条内部に水分が浸
透し、糊剤が浸透しやすくなるためである。この油剤を
延伸前に付与すると、ローラの汚れにより操業性が悪化
したり、熱延伸の場合、成分が熱によって変質する可能
性がある。さらに、延伸時に付与成分中の水分が延伸の
際に蒸発してしまい、糊剤との相溶性が低下する。
After the stretching, an oil containing the above-mentioned dioctyl sulfosuccinate salt and polyoxyethylene alkyl ether and / or polyoxyethylene alkyl phenyl ether and having an excellent conjugating property with the paste is applied as an after oil. . This oil agent is preferably provided as an emulsion oil agent. This is because, by applying an emulsion oil, moisture penetrates into the inside of the yarn, and the paste easily penetrates. If this oil agent is applied before stretching, operability may deteriorate due to contamination of the roller, and in the case of thermal stretching, components may be deteriorated by heat. Further, the water in the imparting component evaporates during the stretching at the time of stretching, and the compatibility with the sizing agent is reduced.

【0020】そして、延伸後の油剤の付与は、糸条への
油剤の付着状態をよくするために、2段目のインターレ
ーサによる流体処理の後に行うことが好ましい。
The application of the oil agent after the drawing is preferably performed after the fluid treatment by the second-stage interlacer in order to improve the state of adhesion of the oil agent to the yarn.

【0021】これらの油剤の付与においては、付与手段
は特に限定されるものではなく、オイリングローラやス
リットノズル等を使用すればよい。
In applying these oils, the applying means is not particularly limited, and an oiling roller, a slit nozzle or the like may be used.

【0022】また、延伸方法については特に限定される
ものではないが、高強度で毛羽発生のない繊維を得るた
めに、ローラ間での延伸は熱延伸とすることが好まし
く、延伸倍率も1.5 倍以上とすることが好ましい。
The stretching method is not particularly limited. However, in order to obtain a fiber having high strength and no generation of fluff, it is preferable that stretching between rollers is performed by thermal stretching, and the stretching ratio is 1.5 times. It is preferable to make the above.

【0023】次に、図面を用いて本発明の製造方法の一
例を説明する。図1は、本発明の製造方法の一実施態様
を示す概略工程図である。まず、紡糸口金1より溶融紡
糸を行い、冷却装置にて糸条を冷却固化した後、スリッ
トノズル2で非水系油剤を付与すると同時に集束を行
い、インターレーサ3で第1段目の交絡を付与する。続
いてローラ4、5間で延伸し、インターレーサ6で第2
段目の交絡を付与し、さらにスリットノズル7で糊剤抱
合性の高い油剤を付与し、巻取機8でパッケージ9に巻
き取る。
Next, an example of the manufacturing method of the present invention will be described with reference to the drawings. FIG. 1 is a schematic process chart showing one embodiment of the production method of the present invention. First, melt spinning is performed from the spinneret 1, and the yarn is cooled and solidified by the cooling device. Then, the non-aqueous oil is applied by the slit nozzle 2, and the bundle is simultaneously formed. I do. Subsequently, the film is stretched between the rollers 4 and 5 and the second
The entanglement of the step is applied, and an oil agent having a high sizing agent conjugation is applied by the slit nozzle 7, and the wound agent 8 winds up the package 9.

【0024】[0024]

【実施例】次に、実施例により本発明を具体的に説明す
る。なお、繊維の油剤付着量、着糊量、毛羽長の測定、
落糊及び製織性の評価は次のようにして行い、繊維の強
伸度、交絡数は前述した方法で測定した。 〔油剤付着量〕JIS-L-1013 7 24 (4)記載の方法で測
定を実施した。 〔糊剤抱合油剤付着量〕得られた繊維(非水油剤と糊剤
抱合性油剤の両方が付与)の油剤付着量(A)と、糊剤
抱合性油剤を付与しない以外は同様の方法で製造して得
た繊維の油剤付着量(B)を上記の測定方法で求め、A
を総油剤付着量とし、A−Bを糊剤抱合油剤付着量とし
て算出した。 〔着糊量〕得られた繊維に糸速60m/分、チャンバー温
度120 ℃、シリンダー温度90℃で糊付けを行った。得ら
れた糊付糸について、精練剤(炭酸ソーダ2g、トリポ
リリン酸ソーダ1g、ノニオン活性剤2gを水1リット
ルに溶解したもの)を用いて80〜90℃で30分間精
練を行い、精練前後の重量差で糊剤の付着量を求め、繊
維全体の重量に対する割合として算出した。 〔毛羽長〕得られた繊維に糸速60m/分、チャンバー温
度120 ℃、シリンダー温度90℃で糊付けを行った。得ら
れた糊付糸50cmに50gの荷重をかけた状態で、糸条の
中央を鋏で切断した。切断した糸条の端部において、糸
が開繊して毛羽状になっている部分の長さを測定した。
これを糊剤の抱合性及び糸条の開繊性の指標とした。 〔落糊〕得られた繊維に糸速60m/分、チャンバー温度
120 ℃、シリンダー温度90℃で糊付けを行った。得られ
た糊付糸をウォータージェットルーム型織機に経糸とし
て掛け、緯糸を打ち込まずに糸速20cm/分、織機回
転数600rpm、走行張力12gで織機を糸長200
0m分稼働させ、糸条からの糊剤の剥離状態を織機へ付
着した糊剤の量及び糸条から落下した糊剤の量で評価し
た。評価は、落下した糊剤の量の少ないものを5として
5段階で評価し、10回評価を行った平均値で示した。 〔製織性〕得られた繊維について、経本数1196本、
糸速100 m/分、チャンバー温度125 ℃、シリンダー温
度100 ℃で整経を行った。そして、緯糸として60d/16
fの井型断面中空糸を用い、織機回転数450 rpm、緯
密度108 本/2.54cm、織品種ハニカムで製織を行った。
このときの製織不良による一日当たりの機台停止回数と
不良反発生率で示した。
Next, the present invention will be described specifically with reference to examples. In addition, measurement of the amount of oil agent attached to the fiber, the amount of gluing, and the fluff length,
Evaluation of the desizing and weaving properties was performed as follows, and the strength and elongation of the fiber and the number of entanglements were measured by the methods described above. [Oil agent adhesion amount] The measurement was carried out by the method described in JIS-L-1013 724 (4). [Attached amount of sizing agent-binding oil agent] In the same manner except that the sizing agent-attached amount (A) of the obtained fiber (both the non-water oil agent and the sizing agent-binding oil agent are applied) and the sizing agent-binding oil agent is not applied. The amount (B) of oil adhering to the fiber obtained by the production was determined by the above-mentioned measuring method.
Was calculated as the total amount of the oil agent attached, and AB was calculated as the adhesive amount of the glue-conjugated oil agent. [Amount of gluing] The obtained fibers were glued at a yarn speed of 60 m / min, a chamber temperature of 120 ° C and a cylinder temperature of 90 ° C. The obtained sized yarn is scoured at 80 to 90 ° C. for 30 minutes using a scouring agent (2 g of sodium carbonate, 1 g of sodium tripolyphosphate, 2 g of nonionic activator dissolved in 1 liter of water), and before and after scouring. The adhesive amount of the sizing agent was determined from the weight difference and calculated as a ratio to the weight of the entire fiber. [Fuzz length] The obtained fibers were glued at a yarn speed of 60 m / min, a chamber temperature of 120 ° C and a cylinder temperature of 90 ° C. With a load of 50 g applied to the obtained glued yarn 50 cm, the center of the yarn was cut with scissors. At the end of the cut yarn, the length of the part where the yarn was opened and became fluff was measured.
This was used as an index of the conjugation property of the sizing agent and the opening property of the yarn. [Glue removal] The obtained fiber has a yarn speed of 60 m / min and a chamber temperature.
Gluing was performed at 120 ° C. and a cylinder temperature of 90 ° C. The obtained glued yarn is wrapped as a warp yarn on a water jet loom type loom.
After operating for 0 m, the peeling state of the glue from the yarn was evaluated by the amount of the glue adhered to the loom and the amount of the glue dropped from the yarn. The evaluation was performed on a scale of 5 on the assumption that the amount of the glue that had fallen was 5 and the average value was evaluated 10 times. [Wovenability] Regarding the obtained fiber, the number of warp was 1196,
Warping was performed at a yarn speed of 100 m / min, a chamber temperature of 125 ° C, and a cylinder temperature of 100 ° C. And as the weft, 60d / 16
Weaving was carried out using a hollow fiber having a cross section of f and a weaving type honeycomb having a weaving machine rotation speed of 450 rpm and a weft density of 108 yarns / 2.54 cm.
At this time, the number of machine stoppages per day due to poor weaving and the rebound rate are shown.

【0025】実施例1 図1に示す工程図に従って行った。相対粘度(96%硫酸
を溶媒とし、濃度1g/dl、温度25℃で測定した。)3.
51のナイロン6ペレットをエクストルーダーに供給し、
紡糸温度280 ℃で溶融紡糸した。紡出した糸に非水油剤
を付与し、油剤の付与と集束を行った後、インターレー
サを用いてエアー圧3.0 kg/cm2 で糸条を流体処理
し、ローラ間で1.5 倍に延伸した。続いて、インターレ
ーサを用いてエアー圧5.0 kg/cm2 で糸条を流体処
理し、糊剤抱合油剤(表1に示す成分を含有する油剤を
水で希釈し、10%のエマルジョン油剤としたもの)を
付与してから4150m/分の速度で巻き取り、ポリアミド
繊維(30d/24f)を得た。
Example 1 An experiment was performed according to the process chart shown in FIG. Relative viscosity (measured at a concentration of 1 g / dl and a temperature of 25 ° C. using 96% sulfuric acid as a solvent) 3.
Supply 51 nylon 6 pellets to the extruder,
Melt spinning was performed at a spinning temperature of 280 ° C. After applying the non-water-based oil to the spun yarn, applying and bundling the oil, the yarn was subjected to fluid treatment at an air pressure of 3.0 kg / cm 2 using an interlacer and stretched 1.5 times between rollers. . Subsequently, the yarn was subjected to fluid treatment at an air pressure of 5.0 kg / cm 2 using an interlacer, and a sizing agent-binding oil agent (an oil agent containing the components shown in Table 1 was diluted with water to obtain a 10% emulsion oil agent). ) And wound up at a speed of 4150 m / min to obtain a polyamide fiber (30d / 24f).

【0026】[0026]

【表1】 [Table 1]

【0027】実施例2 延伸後のインターレーサでの流体処理のエアー圧を4.
0kg/cm2 とした以外は、実施例1と同様に行っ
た。
Example 2 The air pressure for fluid treatment in the interlacer after stretching was set to 4.
The procedure was performed in the same manner as in Example 1 except that the pressure was set to 0 kg / cm 2 .

【0028】比較例1 延伸後に糊剤抱合油剤を付与しなかった(延伸後は油剤
の付与を行わなかった)以外は、実施例1と同様に行っ
た。
Comparative Example 1 The same procedure as in Example 1 was carried out except that the sizing agent-containing oil agent was not applied after the stretching (the oil agent was not applied after the stretching).

【0029】比較例2 延伸前のインターレーサでの流体処理のエアー圧を0.5
kg/cm2 とし、延伸後のインターレーサでの流体処
理及び糊剤抱合油剤の付与を行わずに巻き取った以外
は、実施例1と同様に行った。
Comparative Example 2 The air pressure of the fluid treatment in the interlacer before stretching was 0.5
kg / cm 2, and the same procedure as in Example 1 was carried out, except that the film was wound up without performing fluid treatment with an interlacer after stretching and without applying a sizing agent-binding oil agent.

【0030】比較例3 延伸前のインターレーサでの流体処理と延伸後の糊剤抱
合油剤の付与を行わず、延伸後の流体処理をエアー圧7.
0 kg/cm2 で行った以外は、実施例1と同様に行っ
た。
COMPARATIVE EXAMPLE 3 The fluid treatment after stretching was performed by air pressure without applying the fluid treatment with the interlacer before stretching and the application of the glue-binding oil after stretching.
The same procedure as in Example 1 was performed except that the test was performed at 0 kg / cm 2 .

【0031】比較例4 延伸後のインターレーサでの流体処理のエアー圧を2.
0kg/cm2 とした以外は、実施例1と同様に行っ
た。
Comparative Example 4 The air pressure of the fluid treatment in the interlacer after stretching was set to 2.
The procedure was performed in the same manner as in Example 1 except that the pressure was set to 0 kg / cm 2 .

【0032】比較例5 延伸後に、ジオクチルスルホサクシネート塩を含有しな
い油剤(表2に示す成分を含有する油剤を水で希釈し、
10%のエマルジョン油剤としたもの)を付与し、延伸
後のインターレーサでの流体処理のエアー圧を4.0k
g/cm2 とした以外は、実施例1と同様に行った。
Comparative Example 5 After stretching, an oil solution containing no dioctyl sulfosuccinate salt (an oil solution containing the components shown in Table 2 was diluted with water,
10% emulsion oil) was applied, and the air pressure of the fluid treatment in the interlacer after stretching was increased to 4.0 k.
The procedure was performed in the same manner as in Example 1 except that g / cm 2 was used.

【0033】[0033]

【表2】 [Table 2]

【0034】参考例 相対粘度(96%硫酸を溶媒とし、濃度1g/dl、温度25
℃で測定した。)3.51のナイロン6ペレットをエクスト
ルーダーに供給し、紡糸温度280 ℃で溶融紡糸した。紡
出した糸に非水油剤を付与し、インターレーサを用いて
エアー圧0.5 kg/cm2 で糸条を流体処理した後にロ
ーラ間で1.5 倍に延伸し、4150m/分の速度で巻き取っ
た。巻き取った糸条を、再度インターレーサを用いてエ
アー圧2.2 kg/cm2 で流体処理を行い、ポリアミド
繊維を得た。
Reference Example Relative viscosity (concentration: 1 g / dl, 96% sulfuric acid as solvent, temperature: 25
Measured in ° C. 3.) 3.51 nylon 6 pellets were fed to an extruder and melt spun at a spinning temperature of 280 ° C. A non-water-based oil agent was applied to the spun yarn, and the yarn was subjected to fluid treatment at an air pressure of 0.5 kg / cm 2 using an interlacer, and then stretched 1.5 times between rollers and wound at a speed of 4150 m / min. . The wound yarn was again subjected to a fluid treatment at an air pressure of 2.2 kg / cm 2 using an interlacer to obtain a polyamide fiber.

【0035】実施例1〜2、比較例1〜5及び参考例で
得られた繊維の強伸度、交絡数、油剤付着量、糊剤抱合
油剤量、着糊量、毛羽長及び落糊、製織性の評価を表3
に示す。
The fibers obtained in Examples 1 and 2, Comparative Examples 1 to 5 and Reference Example, the elongation, the number of entanglements, the amount of oiling agent, the amount of sizing agent conjugated oil, the amount of gluing, the fluff length and the size of the glue Table 3 shows the evaluation of weaving properties.
Shown in

【0036】[0036]

【表3】 [Table 3]

【0037】表3より明らかなように、実施例1〜2に
よれば、毛羽の発生が少なく品位の高い細繊度で高強度
のポリアミド繊維が得られ、この繊維は、整経時の糊剤
の抱合性も良好で、製織性よく風合いのよい高密度織物
を得ることができた。そして、参考例においては、巻き
取った糸条に再度流体処理して交絡の付与を行ったが、
実施例1〜2の繊維は、参考例により得られた交絡を6
0個/m付与した繊維と同等の糊剤抱合性、製織性等の
特性を有するものであった。一方、比較例1では、糊剤
抱合油剤を付与しなかったため、比較例2では、延伸後
にインターレース処理と糊剤抱合油剤の付与を行わなか
ったため、比較例3では延伸前にインターレース処理と
延伸後に糊剤抱合油剤の付与をしなかったため、比較例
4では交絡数が35個/m未満であったため、比較例5
では、ジオクチルスルホサクシネート塩を含有する油剤
を付与しなかったため、これらの繊維は、製経時の糊剤
との抱合性が悪く、落糊量が多く、製織性も悪かった。
As is clear from Table 3, according to Examples 1 and 2, a high-fineness, high-fineness polyamide fiber having less fluff and high quality can be obtained. Good conjugation properties were obtained, and a high-density woven fabric with good weaving properties and good texture was obtained. And, in the reference example, the wound yarn was again subjected to fluid treatment to impart entanglement,
The fibers of Examples 1 and 2 show the confounding obtained in Reference Example 6
It had properties such as a sizing agent conjugation property and a weaving property, which were equivalent to those of the fiber given 0 fibers / m. On the other hand, in Comparative Example 1, the sizing agent was not applied, and in Comparative Example 2, the interlacing treatment and the application of the sizing agent were not performed after stretching. In Comparative Example 3, the interlacing treatment was performed before stretching and after the stretching. Since no sizing agent was added, the number of entanglements in Comparative Example 4 was less than 35 / m.
However, since no oil agent containing a dioctyl sulfosuccinate salt was given, these fibers had poor conjugation with the sizing agent during production, a large amount of sizing, and poor weavability.

【0038】[0038]

【発明の効果】本発明のポリアミド繊維は、細繊度かつ
高強力であり、糊剤との抱合性がよいので、製織時に糊
落ちせず、風合いのよい、スポーツ用途や衣料用途に好
適な高密度織物を製織性よく得ることが可能となる。ま
た、本発明の製造方法によれば、直接紡糸延伸法によ
り、毛羽等の発生のない品位の高い細繊度高強力ポリア
ミド繊維を生産性よく製造することが可能となる。
Industrial Applicability The polyamide fiber of the present invention has a fine fineness and high strength, and has good conjugation property with a sizing agent. Therefore, it does not fall off during weaving, has a good texture, and is suitable for sports and clothing. It is possible to obtain a high density woven fabric with good weaving properties. Further, according to the production method of the present invention, it is possible to produce a high-quality fine-fiber high-strength polyamide fiber having no fluff or the like with high productivity by the direct spinning and drawing method.

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

【図1】本発明の細繊度高強力ポリアミド繊維の製造工
程の一実施態様を示す概略工程図である。
FIG. 1 is a schematic process chart showing one embodiment of a process for producing a fine-fiber high-strength polyamide fiber of the present invention.

【符号の説明】[Explanation of symbols]

1 紡糸口金 2 スリットノズル 3 インターレーサ 4 ローラ 5 ローラ 6 インターレーサ 7 スリットノズル 8 巻取機 9 パッケージ DESCRIPTION OF SYMBOLS 1 Spinneret 2 Slit nozzle 3 Interlacer 4 Roller 5 Roller 6 Interlacer 7 Slit nozzle 8 Winding machine 9 Package

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI D02J 1/22 D02J 1/22 H D06M 15/53 D06M 15/53 // D01D 5/16 D01D 5/16 (72)発明者 塚田 吉則 京都府宇治市宇治戸ノ内5 ユニチカ株式 会社宇治工場内 (72)発明者 細田 雅弘 京都府宇治市宇治戸ノ内5 ユニチカ株式 会社宇治工場内──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification symbol FI D02J 1/22 D02J 1/22 H D06M 15/53 D06M 15/53 // D01D 5/16 D01D 5/16 (72) Inventor Yoshinori Tsukada 5 Unitika, Uji-Tonouchi, Uji-city, Kyoto (72) Inventor Masahiro Hosoda 5 Uji-Tonouchi, Uji-shi, Uji, Kyoto, Japan

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 トータル繊度35デニール以下、強度6.0
g/デニール以上、交絡数35個/m以上であって、ジオ
クチルスルホサクシネート塩と、ポリオキシエチレンア
ルキルエーテル及び/又はポリオキシエチレンアルキル
フェニルエーテルを含有する油剤が付与されていること
を特徴とする細繊度高強力ポリアミド繊維。
1. Total denier 35 denier or less, strength 6.0
g / denier or more, the number of confounds is 35 / m or more, and an oil agent containing dioctyl sulfosuccinate salt and polyoxyethylene alkyl ether and / or polyoxyethylene alkyl phenyl ether is provided. Fine fiber high strength polyamide fiber.
【請求項2】 ポリアミド樹脂を溶融紡糸し、紡糸糸条
を冷却した後、ローラ間で延伸し、3000m/分以上の速
度で巻き取る直接紡糸延伸法により製造する方法であっ
て、延伸の前及び後にインターレーサで糸条を流体処理
して交絡を付与し、かつ延伸前には非水油剤を付与し、
延伸後にはアフターオイルとして、ジオクチルスルホサ
クシネート塩と、ポリオキシエチレンアルキルエーテル
及び/又はポリオキシエチレンアルキルフェニルエーテ
ルを含有する油剤を付与することを特徴とする請求項1
記載の細繊度高強力ポリアミド繊維の製造方法。
2. A method for producing a polyamide resin by a melt spinning method, cooling the spun yarn, stretching the yarn between rollers, and winding the polyamide resin at a speed of 3000 m / min or more. And afterwards the yarn is subjected to fluid treatment with an interlacer to impart confounding, and before drawing, impart a non-water-based oil agent,
An oil containing a dioctyl sulfosuccinate salt and a polyoxyethylene alkyl ether and / or a polyoxyethylene alkyl phenyl ether is provided as an after oil after stretching.
A method for producing the high-fine-strength polyamide fiber according to the above description.
JP13793198A 1998-05-20 1998-05-20 Polyamide yarn having small fineness and large strength and its production Pending JPH11323729A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13793198A JPH11323729A (en) 1998-05-20 1998-05-20 Polyamide yarn having small fineness and large strength and its production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13793198A JPH11323729A (en) 1998-05-20 1998-05-20 Polyamide yarn having small fineness and large strength and its production

Publications (1)

Publication Number Publication Date
JPH11323729A true JPH11323729A (en) 1999-11-26

Family

ID=15210045

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13793198A Pending JPH11323729A (en) 1998-05-20 1998-05-20 Polyamide yarn having small fineness and large strength and its production

Country Status (1)

Country Link
JP (1) JPH11323729A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004050345A1 (en) * 2002-12-04 2004-06-17 Toyo Boseki Kabushiki Kaisya Moisture permeable waterproof woven fabric excelling in tearing strength and process for producing the same
JP2013512354A (en) * 2009-12-03 2013-04-11 インターフェース・オーストラリア・ピーティーワイ・リミテッド Bio-based fibers and yarns
CN110644064A (en) * 2018-06-26 2020-01-03 欧瑞康纺织有限及两合公司 Multifilament conditioning method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004050345A1 (en) * 2002-12-04 2004-06-17 Toyo Boseki Kabushiki Kaisya Moisture permeable waterproof woven fabric excelling in tearing strength and process for producing the same
JP2013512354A (en) * 2009-12-03 2013-04-11 インターフェース・オーストラリア・ピーティーワイ・リミテッド Bio-based fibers and yarns
CN110644064A (en) * 2018-06-26 2020-01-03 欧瑞康纺织有限及两合公司 Multifilament conditioning method
CN110644064B (en) * 2018-06-26 2022-08-02 欧瑞康纺织有限及两合公司 Multifilament conditioning method

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