JPH043469B2 - - Google Patents

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Publication number
JPH043469B2
JPH043469B2 JP21509088A JP21509088A JPH043469B2 JP H043469 B2 JPH043469 B2 JP H043469B2 JP 21509088 A JP21509088 A JP 21509088A JP 21509088 A JP21509088 A JP 21509088A JP H043469 B2 JPH043469 B2 JP H043469B2
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JP
Japan
Prior art keywords
nylon
oil
white powder
agent
multifilament
Prior art date
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Expired
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JP21509088A
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Japanese (ja)
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JPH0268363A (en
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Priority to JP21509088A priority Critical patent/JPH0268363A/en
Publication of JPH0268363A publication Critical patent/JPH0268363A/en
Publication of JPH043469B2 publication Critical patent/JPH043469B2/ja
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Description

【発明の詳細な説明】[Detailed description of the invention]

〔産業上の利用分野〕 本発明はナイロン66糸条に関する。更に詳しく
は、3000〜6000m/minの高速で紡糸して得られ
るナイロン66マルチフイラメントに関し、該マル
チフイラメントが長期間保管された後でも後加工
(ユーザー)の工程性能を悪化させないものであ
る。即ち、長期間経時後もワーパー整経、編立て
等において白粉の発生しないナイロン66マルチフ
イラメントに関するものである。 〔従来の技術〕 近年、ナイロン繊維製造に関し、コストダウン
を目的とする高速紡糸が行なわれる様になつた。
ナイロンの高速紡糸は一般に3000〜6000m/min
好ましくは4000〜6000m/minで行なわれるのが
普通である。このようにして製糸されたナイロン
繊維は複屈折率Δnが0.035〜0.045、切断伸度が50
〜100%、好ましくは50〜80%の範囲にあること
が特徴であり、柔軟な風合い、均一な染色性を有
することから、仮撚加工分野のみならず織物、ト
リコツト分野等、幅広い用途に使用されている。
しかしながら、高速紡糸工程でエマルジヨン系の
従来油剤を付与させたナイロン66マルチフイラメ
ントは、トリコツトや織物経糸としてワーパー整
経を行なう時、ナイロン66マルチフイラメントが
ガイドや筬に接触しながら走行するが、その時単
糸の表面に付着している白粉が一部は脱落し、大
半はガイドや筬に付着しワーパー経時と共に付着
量が増加し異常に張力が上昇して糸切れを誘発し
問題となつている。 一方、ポリアミドフイラメントの高速紡糸にお
いて付与される油剤についてはオレイルオレート
を主成分とした油剤による織物欠点(経縞)を改
善の目的として特公昭60−31931号公報に提案さ
れている。又加工操業性が良く高品位の加工糸
(毛羽の少ない)を得るナイロン6POY用油剤組
成物(エチレンオキサイドとプロピレンオキサイ
ドの共重合物を主成分)として特開昭60−215872
号公報に提案されている。しかしながら、これ等
の油剤組成物を高速紡糸工程でナイロン66マルチ
フイラメントに付与させる場合、長期間保管後
(例えば10ケ月)に使用するとワーパーや編立て
工程で白粉が増えるという問題が起こる。以上の
他、高速紡糸ナイロン66マルチフイラメント用の
油剤については、見るべき提案はなく通常の油剤
をそのまま、スライドして高速紡糸に使用すると
やはり長期間保管後、該ナイロン66マルチフイラ
メントを使用すると白粉が発生するという問題が
ある。 高速紡糸の衣料系分野には紡糸工程でストレー
ト油剤(非含水油剤)を付与させる公知技術(特
公昭60−37222号公報)があるが、この場合白粉
の発生を防止することは出来るが紡糸段階で油剤
飛散により油煙が充満し、これを除去する為には
大がかりな回収装置が必要となり、コストアツプ
の問題がある。更に油剤コストも著しく高くなる
問題もある。 〔発明が解決しようとする問題点〕 本発明者等は上記、白粉の発生につき鋭意検討
した結果、高速紡糸によるナイロン66マルチフイ
ラメントの白粉の析出度合は乳化剤のエチレンオ
キサイド(以降EOとする)付加物の含有量と密
接な関係があるという驚くべき事実を見出した。 本発明者等はエマルジヨンが安定で、更に安価
で後加工性能をクリアーしつつ、且つ乳化剤の
EO付加物を極力減らす油剤配合について鋭意検
討した結果、EO付加物を0〜3wt%に減らして
もエマルジヨンが安定である方法を見出し、本発
明を完成するに至つた。本発明の目的は上記のよ
うな、白粉の出ないナイロン66糸条を提供するこ
とにある。 〔問題点を解決するための手段〕 本発明は、複屈折率△nが0.035〜0.045、切断
伸度が50〜100%であるナイロン66マルチフイラ
メントからなり下記油剤をフイラメントに対して
0.3〜1.5wt%有することを特徴とするナイロン66
糸条 (イ) エチレンオキサイド付加物(3wt%以下)、
アルケニルコハク酸、アルキルイミダゾリン両
性化物、アルキルアルキレートスルホン酸Na
又はK塩、アルキルジエタノールアミド、アル
キルホスフエートNa又はK塩の2種〜6種で
構成される乳化剤及び制電剤 (25〜60wt%) (ロ) 鉱物油及び/又はアルキルアルキレートの平
滑剤 (75〜40wt%) 但しアルキル基の炭素数は4〜20 EO付加物とは高級アルコールのEO付加物及び
EO/PO付加物、PEGエステル、ヒマシ油EO付
加物及びEO/PO付加物、ノニルフエノールEO
付加物、ポリエチレングリコール、ポリオキシア
ルキルアミン、トリメチロールプロパンEO付加
物等があげられる。EOのモル数は1〜60で良い。 通常のナイロン66チツプを用いて高速紡糸した
銘柄については油剤中のEO付加物は3〜18wt
%、好ましくは3〜10wt%で充分白粉を防止出
来るが、EO付加物の制電剤を練込んだナイロン
66チツプを用いて高速紡糸した特殊銘柄について
は白粉が多く油剤中のEO付加物は0〜3wt%領
域の白粉が少なく、更に好ましくは0wt%が良
い。つまり平滑剤、乳化剤、制電剤の総ての単品
についてEOを付加していないもので配合すると
いうことである。 油剤成分にはアルケニルコハク酸、オレイルオ
レートスルホン酸Na塩、オレイルジエタノール
アミド、ラウリルイミダゾリン両性化物、オレイ
ルアルコールホスフエートNa塩、等が該当する
がこの他に高級脂肪酸及びそのNa、K塩でも良
い。乳化剤でありながら制電効果を示すものや、
制電剤でありながら乳化の働きをするので乳化剤
と制電剤の区別がむずかしく乳化剤+制電剤を乳
化剤及び制電剤という表現にした。乳化剤及び制
電剤はエマルジヨンの乳化安定性を確保する為に
25〜60wt%が必要であり、25wt%以下では乳化
不良となり60wt%以上では平滑剤が少なくなり
ナイロン66糸条の平滑性が悪化するので好ましく
ない。 平滑剤は鉱物油、脂肪酸エステルであり、それ
ぞれ単独配合でも良く又は混合の配合でも良い。
平滑剤の含有量が40wt%以下ではナイロン66糸
条の平滑性が悪化し紡糸工程や後加工での糸切れ
が増えるので好ましくない。一方75wt%以上で
は乳化剤が少なくなりエマルジヨンの乳化安定性
が悪化するので好ましくない。従つてエマルジヨ
ンの安定性を保ち、且つ紡糸や後加工での糸切れ
を防止する目的で75〜40wt%の領域が好ましい。 紡糸時の油剤付着量は0.3wt%以下では、平滑
性や集束性が保てないので紡糸工程で糸切れが起
こり易く、1.5wt%以上では、白粉が増えるので
好ましくない。従つて油剤付着量はナイロン66マ
ルチフイラメントに対して0.3〜1.5wt%が良く、
更に好ましくは0.5〜1.0wt%が良い。 本発明の高速紡糸によるナイロン66糸条の油剤
組成物は切断伸度が50〜100%保有しているフイ
ラメントに白粉減少効果が有り、通常の(コンベ
ンシヨナル方式)ナイロン6、ナイロン66フイラ
メントは白粉が出にくく従来品のEO付加物を20
〜40wt%含有している油剤で良い。 白粉とはナイロン66特有のオリゴマーで高速紡
糸のマルチフイラメントの非結晶部分の配向がル
ーズである為、油剤中のEO付加物が単糸の表面
から内部へ水と一緒に入り易く、経時変化でオリ
ゴマーを析出するものと考えられる。 油剤付着量とはナイロン66マルチフイラメント
2.06gをジクロルメタン3c.c.にて4回の量で東海
計器株式会社製の迅速残脂抽出装置で(加熱部
110℃)抽出し次の計算式で求めた値をいう。 (残脂量g/2g)×100〔%〕 〔実施例〕 次に実施例により本発明を具体的に説明する。 実施例 1 紡糸孔13個を有する紡糸口金を用いて、通常の
ナイロン66ポリマーを溶融吐出させて紡糸口金下
のチヤンバーで冷風にて冷却し、紡糸工程で次に
示す水エマルジヨン系油剤(10wt%)を糸に対
して0.7wt%付与し延伸することなく4000m/
minのワインダーでチーズ状に捲上げ40d/13fの
ナイロン66マルチフイラメントを造り、白粉発生
状況を調べた。 本発明に用いた配合油剤及び従来の配合油剤を
次に示す。尚油剤名の右欄にEO付加物の含有量
を示し、EO付加物には左欄に※印をした。 配合油剤 No.1 EO付加物 0wt% 2エチルヘキシルパルミテート 65wt% アルケニルコハク酸 6.5wt% ラウリルイミダゾリン両性化物 3.9wt% オレイルオレートスルホン酸Na塩 7.8wt% オレイン酸ジエタノールアミド 10.3wt% オレイルアルコールホスフエートNa塩 6.5wt% 配合油剤 No.2 EO付加物 0wt% 2エチルヘキシルパルミテート 40wt% 鉱物油レツドウツド粘度60秒 30wt% アルケニルコハク酸 6.5wt% ラウリルイミダゾリン両性化物 3.9wt% オレイン酸ジエタノールアミド 5.0wt% オレイルアルコールホスフエートNa塩 6.5wt% オレイルオレートスルホン酸Na塩 8.1wt% 配合油剤 No.3 EO付加物 0wt% 鉱物油レツドウツド粘度60秒 45wt% アルケニルコハク酸 6.5wt% ラウリルイミダゾリン両性化物 5.0wt% オレイン酸ジエタノールアミド 19.5wt% オレイルアルコールホスフエートNa塩 4.0wt% オレイルオレートスルホン酸Na塩 20wt% 配合油剤 No.4 EO付加物 3wt% 2エチルヘキシルパルミテート 62wt% *POE(25)ヒマシ油エーテル 3wt% アルケニルコハク酸 6.5wt% オレイルオレートスルホン酸Na塩 7.8wt% ラウリルイミダゾリン両性化物 3.9wt% オレイン酸ジエタノールアミド 10.3wt% オレイルアルコールホスフエートNa塩 6.5wt% 配合油剤 No.5 EO付加物 6.5wt% 2エチルヘキシルパルミテート 65wt% アルケニルコハク酸 6.5wt% ラウリルイミダゾリン両性化物 3.9wt% オレイルオレートスルホン酸Na塩 7.8wt% *ステアリルアルコール(EO)5ホスフエート
K塩 6.5wt% オレイン酸ジエタノールアミド 10.3wt% 配合油剤 No.6 EO付加物 15wt% オレイルオレート 63wt% *POE(25)ヒマシ油エーテル 10wt% アルケニルコハク酸 5wt% ラウリルイミダゾリン両性化物 3wt% オレイルオレートスルホン酸Na塩 6wt% *ステアリルアルコール(EO)5ホスフエート
K塩 5wt% オレイン酸ジエタノールアミド 8wt% 配合油剤 No.7 EO付加物 25.6wt% 2エチルヘキシルパルミテート 56.9wt% *POE(5)オレイルエーテル 25.6wt% アルケニルコハク酸 3.7wt% ラウリルイミダゾリン両性化物 4.6wt% オレイルオレートスルホン酸Na塩 4.6wt% オレイン酸ジエタノールアミド 4.6wt% <白粉試験> 40d/13fのチーズを第1図に示すドラム缶(金
属容器200)に水3と一緒に入れてゴムシー
ル付のフタで完全密閉する。このドラム缶を50℃
にコントロールされた室内に1ウイーク(week)
放置後ドラム缶を取出し、フタを開けてナイロン
66マルチフイラメントのチーズを取出す。このナ
イロン66マルチフイラメントを第2図の装置でガ
イド7,8を通し更に筬9を通して600m/min
の速度で一定時間(10分間)走らせ脱落した白粉
と筬に付着した白粉を回収して(集めて)メトラ
ー天秤で白粉量と走行糸量を測定しナイロン66マ
ルチフイラメント1Kg当たりの白粉量(mg)を算
出する。その結果を第1表及び第3図に示す。
[Industrial Field of Application] The present invention relates to nylon 66 yarn. More specifically, regarding the nylon 66 multifilament obtained by spinning at a high speed of 3000 to 6000 m/min, the process performance of the post-processing (user) is not deteriorated even after the multifilament is stored for a long period of time. That is, it relates to a nylon 66 multifilament that does not generate white powder during warping, knitting, etc. even after a long period of time. [Prior Art] In recent years, high-speed spinning has been used to reduce costs in the production of nylon fibers.
High-speed spinning of nylon is generally 3000 to 6000 m/min.
The speed is preferably 4000 to 6000 m/min. The nylon fiber spun in this way has a birefringence Δn of 0.035 to 0.045 and a cutting elongation of 50.
~100%, preferably in the range of 50 to 80%, and has a flexible texture and uniform dyeability, so it is used not only in the false twisting field, but also in a wide range of applications such as textiles and tricots. has been done.
However, when the nylon 66 multifilament is coated with a conventional emulsion-based oil agent during the high-speed spinning process, the nylon 66 multifilament runs while coming into contact with guides and reeds when it is warped as a tricot or textile warp. Some of the white powder adhering to the surface of the single yarn falls off, but most of it adheres to the guides and reeds, and as the warper ages, the amount of adhesion increases, causing an abnormal increase in tension and causing yarn breakage, causing a problem. . On the other hand, an oil agent applied during high-speed spinning of polyamide filaments has been proposed in Japanese Patent Publication No. 31931/1983 for the purpose of improving textile defects (warp stripes) caused by oil agents mainly containing oleyl oleate. In addition, JP-A-60-215872 describes an oil composition for nylon 6POY (mainly composed of a copolymer of ethylene oxide and propylene oxide) that has good processing operability and yields high-quality processed yarn (with little fuzz).
It is proposed in the Publication No. However, when these oil compositions are applied to nylon 66 multifilament in a high-speed spinning process, a problem arises in that white powder increases in the warper or knitting process if used after long-term storage (for example, 10 months). In addition to the above, there are no proposals regarding oils for high-speed spinning nylon 66 multifilaments. There is a problem that occurs. In the field of high-speed spinning clothing, there is a known technology (Japanese Patent Publication No. 60-37222) that applies a straight oil agent (non-water-containing oil agent) during the spinning process, but in this case, the generation of white powder can be prevented, but the The area is filled with oil smoke due to the scattering of the oil agent, and removing this requires a large-scale collection device, resulting in an increase in costs. Furthermore, there is also the problem that the cost of the oil agent increases significantly. [Problems to be Solved by the Invention] As a result of the above-mentioned intensive study on the generation of white powder, the present inventors found that the degree of precipitation of white powder from nylon 66 multifilament produced by high-speed spinning is due to the addition of ethylene oxide (hereinafter referred to as EO) as an emulsifier. We discovered the surprising fact that there is a close relationship with the content of substances. The present inventors have developed an emulsion that is stable, inexpensive, meets post-processing performance, and uses no emulsifier.
As a result of intensive study on the formulation of an oil agent that would reduce the amount of EO adducts as much as possible, they discovered a method that would allow the emulsion to remain stable even when the EO adducts were reduced to 0 to 3 wt%, leading to the completion of the present invention. An object of the present invention is to provide a nylon 66 yarn that does not produce white powder as described above. [Means for solving the problems] The present invention consists of a nylon 66 multifilament having a birefringence △n of 0.035 to 0.045 and a cutting elongation of 50 to 100%, and the following oil agent is applied to the filament.
Nylon 66 characterized by having 0.3~1.5wt%
Yarn (a) Ethylene oxide adduct (3wt% or less),
Alkenylsuccinic acid, alkylimidazoline amphoteric acid, sodium alkyl alkylate sulfonate
or emulsifier and antistatic agent composed of 2 to 6 types of K salt, alkyl diethanolamide, Na alkyl phosphate, or K salt (25 to 60 wt%) (b) Smoothing agent of mineral oil and/or alkyl alkylate (75-40wt%) However, the number of carbon atoms in the alkyl group is 4-20. EO adducts are EO adducts of higher alcohols and
EO/PO adduct, PEG ester, castor oil EO adduct and EO/PO adduct, nonylphenol EO
Examples include adducts, polyethylene glycol, polyoxyalkylamine, trimethylolpropane EO adducts, and the like. The number of moles of EO may be 1 to 60. For brands spun at high speed using regular nylon 66 chips, the amount of EO adducts in the oil is 3 to 18wt.
%, preferably 3 to 10 wt%, can sufficiently prevent white powder.
For special brands spun at high speed using 66 chips, there is a lot of white powder, and the EO adduct in the oil has less white powder in the range of 0 to 3 wt%, more preferably 0 wt%. In other words, all individual components such as smoothing agents, emulsifiers, and antistatic agents are blended with no added EO. Examples of the oil component include alkenyl succinic acid, oleyl oleate sulfonic acid Na salt, oleyl diethanolamide, lauryl imidazoline amphoteric compound, oleyl alcohol phosphate Na salt, etc., but higher fatty acids and their Na and K salts may also be used. Those that are emulsifiers but also have an antistatic effect,
Although it is an antistatic agent, it also acts as an emulsifier, so it is difficult to distinguish between an emulsifier and an antistatic agent, so the expression emulsifier + antistatic agent is used as an emulsifier and an antistatic agent. Emulsifiers and antistatic agents are used to ensure the emulsion stability of the emulsion.
A content of 25 to 60 wt% is required, and if it is less than 25 wt%, emulsification will be poor, and if it is more than 60 wt%, the amount of smoothing agent will decrease and the smoothness of the nylon 66 thread will deteriorate, which is not preferable. The smoothing agent is mineral oil or fatty acid ester, and each may be used alone or in combination.
If the content of the smoothing agent is less than 40 wt%, the smoothness of the nylon 66 yarn will deteriorate and yarn breakage will increase during the spinning process and post-processing, which is not preferable. On the other hand, if it exceeds 75 wt%, the amount of emulsifier decreases and the emulsion stability of the emulsion deteriorates, which is not preferable. Therefore, in order to maintain the stability of the emulsion and prevent yarn breakage during spinning and post-processing, a range of 75 to 40 wt% is preferable. If the amount of oil applied during spinning is less than 0.3 wt%, smoothness and cohesiveness cannot be maintained, so thread breakage is likely to occur during the spinning process, and if it is more than 1.5 wt%, white powder will increase, which is undesirable. Therefore, the amount of oil attached to the nylon 66 multifilament is preferably 0.3 to 1.5 wt%.
More preferably, it is 0.5 to 1.0 wt%. The oil composition for nylon 66 yarn produced by high-speed spinning of the present invention has a white powder reducing effect on filaments that have a breaking elongation of 50 to 100%, and ordinary (conventional method) nylon 6 and nylon 66 filaments have a white powder reduction effect. 20% of the EO additives in conventional products.
An oil containing ~40wt% is fine. White powder is an oligomer unique to nylon 66, and because the orientation of the amorphous part of the multifilament spun at high speed is loose, EO adducts in the oil agent can easily enter the inside of the single filament along with water from the surface of the single filament, resulting in changes over time. It is thought that oligomers are precipitated. What is the amount of oil attached to nylon 66 multifilament?
2.06 g was added 4 times with 3 c.c. of dichloromethane using a rapid residual fat extraction device manufactured by Tokai Keiki Co., Ltd. (heating part
110℃) and calculated using the following formula. (Residual fat amount g/2g) x 100 [%] [Example] Next, the present invention will be specifically explained with reference to Examples. Example 1 Using a spinneret with 13 spinning holes, ordinary nylon 66 polymer was melted and discharged, cooled with cold air in a chamber under the spinneret, and the following water emulsion oil (10 wt%) was added during the spinning process. ) is added to the yarn at 0.7wt% and stretched over 4000m/without stretching.
A 40D/13F nylon 66 multifilament was made by winding it into a cheese shape using a min winder, and the generation of white powder was investigated. The compounded oil used in the present invention and the conventional compounded oil are shown below. The content of EO adducts is shown in the column to the right of the oil agent name, and EO adducts are marked with * in the left column. Compounded oil No. 1 EO adduct 0wt% 2 Ethylhexyl palmitate 65wt% Alkenyl succinic acid 6.5wt% Lauryl imidazoline amphoteric compound 3.9wt% Sodium oleyl oleate sulfonate 7.8wt% Oleic acid diethanolamide 10.3wt% Sodium oleyl alcohol phosphate Salt 6.5wt% Compounded oil No. 2 EO adduct 0wt% 2-ethylhexyl palmitate 40wt% Mineral oil viscosity 60 seconds 30wt% Alkenylsuccinic acid 6.5wt% Lauryl imidazoline amphoteric compound 3.9wt% Oleic acid diethanolamide 5.0wt% Oleyl alcohol Sodium phosphate 6.5wt% Sodium oleyl oleate sulfonate 8.1wt% Compounded oil No. 3 EO adduct 0wt% Mineral oil viscosity 60 seconds 45wt% Alkenylsuccinic acid 6.5wt% Lauryl imidazoline amphoteric compound 5.0wt% Diethanolamide oleate 19.5wt% Oleyl alcohol phosphate sodium salt 4.0wt% Oleyl oleate sulfonic acid sodium salt 20wt% Compounded oil agent No. 4 EO adduct 3wt% 2-ethylhexyl palmitate 62wt% *POE (25) Castor oil ether 3wt% Alkenyl succinic acid 6.5wt% Oleyl oleate sulfonic acid sodium salt 7.8wt% Lauryl imidazoline amphoteric compound 3.9wt% Oleic acid diethanolamide 10.3wt% Oleyl alcohol phosphate sodium salt 6.5wt% Compounded oil No. 5 EO adduct 6.5wt% 2-ethylhexyl palmitate 65wt% Alkenyl succinic acid 6.5wt% Lauryl imidazoline amphoteric compound 3.9wt% Sodium oleyl oleate sulfonate 7.8wt% *Stearyl alcohol (EO) 5 -phosphate K salt 6.5wt% Oleic acid diethanolamide 10.3wt% Compounded oil No. 6 EO Adducts 15wt% Oleyl oleate 63wt% *POE (25) Castor oil ether 10wt% Alkenylsuccinic acid 5wt% Lauryl imidazoline amphoteric compound 3wt% Oleyl oleate sulfonic acid Na salt 6wt% *Stearyl alcohol (EO) 5- phosphate K salt 5wt% Olein Acid diethanolamide 8wt% Compounded oil No. 7 EO adduct 25.6wt% 2-ethylhexyl palmitate 56.9wt% *POE(5) oleyl ether 25.6wt% Alkenyl succinic acid 3.7wt% Lauryl imidazoline amphoteric compound 4.6wt% Oleyl oleate sulfonic acid Na salt 4.6wt% Oleic acid diethanolamide 4.6wt% <White powder test> Put 40d/13f cheese into the drum (metal container 200) shown in Figure 1 together with 3 parts of water and completely seal it with a lid with a rubber seal. This drum can be heated to 50℃
1 week in a controlled room
After leaving it for a while, take out the drum, open the lid and remove the nylon
66 Remove the cheese from the multifilament. This nylon 66 multifilament is passed through the guides 7 and 8 using the device shown in Figure 2, and then passed through the reed 9 at a speed of 600 m/min.
Collect the white powder that fell off and the white powder that adhered to the reed at the speed of ) is calculated. The results are shown in Table 1 and Figure 3.

【表】 第1表及び第3図で明らかな様に白粉発生量は
乳化剤のEO付加物の含有量と強い相関があり、
配合系油剤中にEO付加物が多いと白粉が増えて
いる。従つて白粉析出の主原因はEO付加物と判
断出来る。No.6〜7はEO付加物が多く、これに
伴い白粉が多い致命的欠点がある。 これに対して本発明のNo.1〜4はEO付加物含
有量が少ないため、白粉はNo.7の約1/10で驚異的
な効果である。 実施例 2 紡糸孔10個を有する紡糸口金を用いてEO付加
物制電剤1.0wt%を練込んだナイロン66チツプを
溶融吐出させ紡糸口金下のチヤンバーで冷風にて
冷却し紡糸工程で、上記説明の油剤No.1〜7をそ
れぞれに対して0.7wt%付与し延伸することなく
4500m/minの速度でワインダーでチーズ状に捲
上げ、30d/10fのナイロン66マルチフイラメント
を造り、上記、白粉試験方法により白粉発生状況
を調べた。その結果を第2表及び第3図に示す。
[Table] As is clear from Table 1 and Figure 3, the amount of white powder generated has a strong correlation with the content of EO adducts in the emulsifier.
If there are many EO adducts in the blended oil, white powder will increase. Therefore, it can be concluded that the main cause of white powder precipitation is EO adducts. Nos. 6 and 7 have a fatal disadvantage of having a large amount of EO adducts and, accordingly, a large amount of white powder. On the other hand, Nos. 1 to 4 of the present invention have a small amount of EO adducts, so the white powder is about 1/10 that of No. 7, which is an amazing effect. Example 2 Using a spinneret with 10 spinning holes, nylon 66 chips kneaded with 1.0 wt% of EO adduct antistatic agent were melted and discharged, cooled with cold air in a chamber under the spinneret, and the above-mentioned spinning process was carried out. Add 0.7wt% of each oil agent No. 1 to 7 described above without stretching.
A 30D/10F nylon 66 multifilament was produced by winding it into a cheese shape with a winder at a speed of 4500 m/min, and the generation of white powder was examined using the white powder test method described above. The results are shown in Table 2 and Figure 3.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、高速紡糸によるナイロン66糸
条は安価で、且つ乳化性の良い水エマルジヨン油
剤を紡糸工程でギヤポンプ方式又はオイリングロ
ール方式で糸に対して油剤付着量が0.3〜1.5wt
%、更に好ましくは0.5〜1.0wt%付与させると通
常のナイロン66チツプを用いて高速紡糸した
40d/13fについては従来38〜150mg/Kgの白粉発
生していたものが10〜18mg/Kgに抑えられる。 又EO付加物制電剤1.0wt%練込んだナイロン66
チツプを用いて高速紡糸した30d/10fについては
従来120〜360mg/Kgの白粉発生していたものが45
〜70mg/Kgに抑えられる。 従つてNo.1〜4の油剤を付与してなる高速紡糸
したナイロン66糸条は通常のナイロン66チツプ及
びEO付加物制電剤入りチツプを用いて紡糸され
る両者の銘柄に白粉防止効果があり、織物経糸又
はトリコツト用としてワーパー整経及び編立てを
行うと白粉が少なく、安定な性能が得られる。
According to the present invention, the nylon 66 yarn produced by high-speed spinning is inexpensive, and a water emulsion oil with good emulsifying properties is applied to the yarn using a gear pump system or an oiling roll system in the spinning process, so that the amount of oil applied to the yarn is 0.3 to 1.5wt.
%, more preferably 0.5 to 1.0 wt%, when spun at high speed using ordinary nylon 66 chips.
Regarding 40d/13f, the white powder that was previously generated at 38-150mg/Kg can be reduced to 10-18mg/Kg. Nylon 66 mixed with 1.0wt% EO adduct antistatic agent
For 30d/10f spun at high speed using chips, white powder of 120 to 360 mg/Kg was generated in the past, but 45
It can be suppressed to ~70mg/Kg. Therefore, high-speed spun nylon 66 yarns coated with oil agents No. 1 to 4 have a white powder prevention effect on both brands spun using regular nylon 66 chips and chips containing EO adduct antistatic agent. There is less white powder and stable performance can be obtained when warper warping and knitting are performed for textile warps or tricots.

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

第1図はナイロン66糸条の調湿装置の概略図を
示す。第2図は白粉試験装置の概略図を示す。第
3図はEO付加物含有量と白粉発生量の関係グラ
フを示す。 1……ドラム缶のフタ、2……ドラム缶200、
3……水3、4……ナイロン66糸条、5……金
網、6……ナイロン66糸条、7,8……ガイド、
9……筬22G、10……ワインダー(600m/
min)。
FIG. 1 shows a schematic diagram of a humidity control device for nylon 66 yarn. FIG. 2 shows a schematic diagram of the white powder testing apparatus. Figure 3 shows a graph of the relationship between the content of EO adducts and the amount of white powder generated. 1... Drum lid, 2... 200 drums,
3... Water 3, 4... Nylon 66 thread, 5... Wire mesh, 6... Nylon 66 thread, 7, 8... Guide,
9... Reed 22G, 10... Winder (600m/
min).

Claims (1)

【特許請求の範囲】 1 複屈折率△nが0.035〜0.045、切断伸度が50
〜100%であるナイロン66マルチフイラメントか
らなり、下記、油剤をフイラメントに対して0.3
〜1.5wt%有することを特徴とするナイロン66糸
条 (イ) エチレンオキサイド付加物(3wt%以下)、
アルケニルコハク酸、アルキルイミダゾリン両
性化物、アルキルアルキレートスルホン酸Na
又はK塩、アルキルジエタノールアミド、アル
キルホスフエートNa又はK塩の2種〜6種で
構成される乳化剤及び制電剤 (25〜60wt%) (ロ) 鉱物油及び/又はアルキルアルキレートの平
滑剤 (75〜40wt%) 但しアルキル基の炭素数は4〜20
[Claims] 1. Birefringence △n is 0.035 to 0.045, and cutting elongation is 50.
Consisting of ~100% nylon 66 multifilament, the following oil agent is applied to the filament at 0.3
Nylon 66 yarn characterized by having ~1.5wt% (a) Ethylene oxide adduct (3wt% or less),
Alkenylsuccinic acid, alkylimidazoline amphoteric acid, sodium alkyl alkylate sulfonate
or emulsifier and antistatic agent composed of 2 to 6 types of K salt, alkyl diethanolamide, Na alkyl phosphate, or K salt (25 to 60 wt%) (b) Smoothing agent of mineral oil and/or alkyl alkylate (75-40wt%) However, the number of carbon atoms in the alkyl group is 4-20
JP21509088A 1988-08-31 1988-08-31 Nylon 66 yarn Granted JPH0268363A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21509088A JPH0268363A (en) 1988-08-31 1988-08-31 Nylon 66 yarn

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21509088A JPH0268363A (en) 1988-08-31 1988-08-31 Nylon 66 yarn

Publications (2)

Publication Number Publication Date
JPH0268363A JPH0268363A (en) 1990-03-07
JPH043469B2 true JPH043469B2 (en) 1992-01-23

Family

ID=16666587

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21509088A Granted JPH0268363A (en) 1988-08-31 1988-08-31 Nylon 66 yarn

Country Status (1)

Country Link
JP (1) JPH0268363A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1994019517A1 (en) * 1993-02-23 1994-09-01 Toray Industries, Inc. High-strength polyamide fiber

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1994019517A1 (en) * 1993-02-23 1994-09-01 Toray Industries, Inc. High-strength polyamide fiber

Also Published As

Publication number Publication date
JPH0268363A (en) 1990-03-07

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