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JPH06330403A - Oil agent application method - Google Patents

Oil agent application method

Info

Publication number
JPH06330403A
JPH06330403A JP12274293A JP12274293A JPH06330403A JP H06330403 A JPH06330403 A JP H06330403A JP 12274293 A JP12274293 A JP 12274293A JP 12274293 A JP12274293 A JP 12274293A JP H06330403 A JPH06330403 A JP H06330403A
Authority
JP
Japan
Prior art keywords
oil agent
emulsion
amount
oil
tow
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
JP12274293A
Other languages
Japanese (ja)
Inventor
Toshiya Hotta
敏哉 堀田
Akira Kimura
章 木村
Osamu Abe
修 安部
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.)
Teijin Ltd
Original Assignee
Teijin 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 Teijin Ltd filed Critical Teijin Ltd
Priority to JP12274293A priority Critical patent/JPH06330403A/en
Publication of JPH06330403A publication Critical patent/JPH06330403A/en
Pending legal-status Critical Current

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  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)

Abstract

PURPOSE:To provide a process for uniformly and quantitatively applying an oil emulsion to a running synthetic fiber bundle. CONSTITUTION:An oil emulsion is foamed to a density of preferably 0.001-0.1g/cm<3> and applied to a running synthetic fiber bundle.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ポリエステルやポリア
ミド等の合成繊維束に油剤を付与する方法に関する。更
に詳しくは、走行する該繊維束に均一かつ定量的に油剤
エマルジョンを付与する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for applying an oil agent to synthetic fiber bundles such as polyester and polyamide. More specifically, it relates to a method of uniformly and quantitatively applying an oil emulsion to the running fiber bundle.

【0002】[0002]

【従来の技術】ポリエステルやポリアミド等の合成繊維
を製造するに当っては、紡績や不織布化等の後工程を円
滑に通過させるため、又は最終製品に有益な表面特性を
付与するため、平滑成分、制電成分、集束成分等を含有
する油剤を付与することが通常行われている。そして、
かかる油剤の付与方法としては、従来キスロール法、計
量吐出法、ディップ法、シャワー法、スプレー法等が採
用されてきた。
2. Description of the Related Art In the production of synthetic fibers such as polyester and polyamide, smooth components are used in order to smoothly pass through post-processes such as spinning and non-woven fabric, or to impart useful surface characteristics to the final product. It is customary to apply an oil agent containing an antistatic component, a focusing component and the like. And
As a method of applying such an oil agent, conventionally, a kiss roll method, a metering and discharging method, a dipping method, a shower method, a spray method and the like have been adopted.

【0003】しかしながら、これらの方法はいずれも均
一定量付着の点で問題点を有している。すなわち、キス
ロール法は、オイリングローラー部を油剤エマルジョン
に浸漬させて一定速度で回転させ、ローラー表面に均一
な油剤エマルジョン層を形成させ、次いでこのローラー
に走行糸を接触させる方法であるが、この方法ではロー
ラーの回転速度を変更することによって油剤付着量を定
量的に制御できるものの、走行糸が太い繊維束である場
合には内層に油剤エマルジョンが浸透し難く付着斑が発
生し易い。
However, all of these methods have a problem in terms of uniform fixed amount adhesion. That is, the kiss roll method is a method in which the oiling roller portion is dipped in an oil agent emulsion and rotated at a constant speed to form a uniform oil agent emulsion layer on the roller surface, and then a running yarn is brought into contact with this roller. However, although the amount of oil agent adhered can be quantitatively controlled by changing the rotation speed of the roller, when the running yarn is a thick fiber bundle, the oil agent emulsion hardly penetrates into the inner layer and adhesion spots are likely to occur.

【0004】計量吐出法は、油剤吐出孔を設けた特殊な
形状のガイドに走行糸を接触させ、油剤エマルジョン
(又はストレート油剤)を計量しながら吐出して油剤を
付与する方法であるが、この方法では付着量制御の定量
性はキスロール法よりも更に高くなっているものの、キ
スロール法と同様に走行糸が太い繊維束である場合には
油剤が浸透し難く付着斑が発生し易い。
The metering and discharging method is a method in which a running yarn is brought into contact with a guide of a special shape having an oil agent discharging hole, and the oil agent emulsion (or straight oil agent) is metered and discharged to apply the oil agent. According to the method, the quantitative control of the adhesion amount is higher than that of the kiss roll method, but like the kiss roll method, when the running yarn is a thick fiber bundle, the oil agent hardly penetrates and adhesion spots easily occur.

【0005】ディップ法は、繊維束を油剤エマルジョン
液に浸るように走行させて油剤エマルジョンを含浸させ
た後、荷重ローラーで過剰の油剤エマルジョンを絞り取
る方法であるが、この方法では油剤の浸透性が良いので
小範囲での付着斑は小さいものの、雰囲気の温湿度や油
剤エマルジョンの温度等、種々の要因で油剤の粘度及び
濃度が変化するために付着量が変動し易く、定量性に乏
しい。
The dipping method is a method in which a fiber bundle is run so as to be immersed in an oil agent emulsion liquid to impregnate the oil agent emulsion, and then an excess oil agent emulsion is squeezed out by a load roller. Although the adhesion unevenness in a small range is small, the adhesion amount easily fluctuates because the viscosity and concentration of the oil agent change due to various factors such as the temperature and humidity of the atmosphere and the temperature of the oil agent emulsion, and the quantitativeness is poor.

【0006】またシャワー法は、油剤エマルジョンを走
行繊維束に注いだ後、上記ディップ法と同じく過剰の油
剤エマルジョンを絞り取る方法であるが、ディップ法よ
りも油剤の付着斑及び付着量の変動が大きい。
Further, the shower method is a method of pouring the oil agent emulsion into the running fiber bundle and then squeezing out the excess oil agent emulsion as in the dip method. large.

【0007】さらにスプレー法は、油剤エマルジョンを
走行繊維束に噴霧する方法で、油剤の浸透性が低く付着
量の変動も大きいので、追油等の補助的なオイリングに
用いられているにすぎない。
Further, the spray method is a method of spraying an oil emulsion onto traveling fiber bundles and has a low permeability of the oil and a large variation in the amount of the oil adhering, so that it is only used for auxiliary oiling such as additional oiling. .

【0008】このように、従来提案され実施されてきた
油剤付与方法には、特に太い繊維束に適用した場合、付
着の均一性と定量性とを同時に満足させ得るものがなか
った。
[0008] As described above, none of the conventionally proposed and practiced oil agent applying methods can satisfy both uniformity and quantitativeness of adhesion at the same time when applied to a thick fiber bundle.

【0009】[0009]

【発明が解決しようとする課題】本発明は、上記従来技
術の問題点を解消し、走行する熱可塑性合成繊維束に油
剤エマルジョンを均一かつ定量的に付与することがで
き、さらには油剤切り替えも簡便にできてロスの少ない
油剤付与方法を提供することを目的とする。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems of the prior art, and can uniformly and quantitatively apply an oil agent emulsion to a running thermoplastic synthetic fiber bundle, and also change the oil agent. It is an object of the present invention to provide a method for applying an oil agent which is simple and has little loss.

【0010】[0010]

【課題を解決するための手段】上記目的は、走行する熱
可塑性合成繊維束に油剤エマルジョンを付与するに際し
て、該油剤エマルジョンを泡状にして付与することを特
徴とする油剤付与方法により達成される。
The above object can be achieved by an oil agent applying method characterized in that, when an oil emulsion is applied to a running thermoplastic synthetic fiber bundle, the oil emulsion is applied in the form of foam. .

【0011】本発明の対象とする合成繊維の一般的な製
造方法は、例えばポリエステル短繊維を例にすると以下
の工程で製造される。すなわち、紡糸工程において溶融
ポリマーを紡糸口金ノズルより吐出して紡糸し、原糸サ
ブトウとして収缶する。次いで延伸工程において、上記
サブトウを多数束ねて原糸トウとなし、これを加熱下延
伸した後必要に応じて緊張熱セットし、捲縮付与、弛緩
熱処理、所定繊維長へのカットの各工程を経て製造され
る。そして、かかる工程において油剤は任意の段階で付
与されるが、通常は延伸後又は緊張熱処理後に行なわれ
る。
A general method for producing synthetic fibers to which the present invention is applied is, for example, polyester short fibers are produced by the following steps. That is, in the spinning step, the molten polymer is discharged from the spinneret nozzle to be spun and collected as a raw yarn sub-tow. Next, in the stretching step, a large number of the above-mentioned sub-tows are bundled to form a raw yarn tow, which is stretched under heating and then tension heat set if necessary, crimping, relaxation heat treatment, and each step of cutting to a predetermined fiber length. Manufactured. Then, in this step, the oil agent is applied at an arbitrary stage, but it is usually performed after stretching or after tension heat treatment.

【0012】本発明においては、かかる油剤付与を、泡
状にした油剤エマルジョンを用いて行うことが肝要であ
る。特に均一付与及び定量付与の点から泡密度は0.0
01〜0.1g/cm3 の範囲にあることが好ましい。
In the present invention, it is important to apply such an oil agent by using a foamed oil agent emulsion. In particular, the foam density is 0.0 in terms of uniform application and quantitative application.
It is preferably in the range of 01 to 0.1 g / cm 3 .

【0013】以下図面を用いて、延伸工程後に本発明を
適用した場合について、具体的に説明する。図1に示す
ように、第1ローラー1と第3ローラー3の間で温水延
伸され、セットローラー6で緊張熱処理された繊維束
に、泡状にした油剤エマルジョンを付与する。油剤エマ
ルジョンの泡状化は、圧縮空気と液状の油剤エマルジョ
ンをミキシングヘッド10に送り込み攪拌することで均
一な泡状とされ、電磁ポンプ11で一定量計量し泡吐出
ノズル12から吐出される。
The case where the present invention is applied after the stretching step will be specifically described below with reference to the drawings. As shown in FIG. 1, the foamed oil agent emulsion is applied to the fiber bundle that has been stretched in warm water between the first roller 1 and the third roller 3 and subjected to the tension heat treatment by the set roller 6. In the foaming of the oil agent emulsion, compressed air and a liquid oil agent emulsion are fed into the mixing head 10 and stirred to form a uniform foam, and a fixed amount is measured by the electromagnetic pump 11 and discharged from the foam discharge nozzle 12.

【0014】ここで用いられる油剤エマルジョンは、容
易に泡状となすことのできる水性エマルジョンであれば
任意であり、一般にストレート油剤は泡状にすることが
困難なので好ましくない。
The oil agent emulsion used here is arbitrary as long as it is an aqueous emulsion which can be easily foamed. In general, it is difficult to make a straight oil agent into a foam, which is not preferable.

【0015】油剤成分としては、例えば通常の紡績油剤
の成分である、ホスフェートやサルフェート等のアニオ
ン活性剤、ポリエーテル等のノニオン活性剤、第4級ア
ンモニウム塩等のカチオン活性剤、ベタイン等の両性活
性剤を単独あるいは組み合わせて用いれば良い。その他
に平滑剤として、アルキルエステル類やパラフィン系炭
化水素類、ジメチルシリコール類等を乳化系で配合して
も良い。
As the oil agent component, for example, anionic activators such as phosphates and sulfates, nonionic activators such as polyethers, cation activators such as quaternary ammonium salts, and amphoteric amphoteric agents such as betaine, which are components of ordinary spinning oil agents, are used. The activators may be used alone or in combination. In addition, as a leveling agent, alkyl esters, paraffinic hydrocarbons, dimethyl silicols and the like may be blended in an emulsion system.

【0016】[0016]

【発明の作用・効果】本発明の製造方法によれば、油剤
エマルジョンは泡状にされているので比重は軽く、走行
繊維束上に付与してもすぐに滴り落ちることなく繊維束
内部に浸透するため、また泡状となっているので表面積
が大きくなっているため、付着均一性は著しく向上す
る。また、付与される泡状油剤エマルジョンは全て繊維
束に供給されるので付着量の定量性も極めて高くなり、
しかも泡状油剤エマルジョンは見掛けの粘度が低いた
め、濃度の高い油剤エマルジョンを用いても均一に付着
することができるのである。
According to the manufacturing method of the present invention, since the oil emulsion is foamed, the specific gravity is light, and even if it is applied onto the traveling fiber bundle, it does not drip immediately and penetrates into the fiber bundle. In addition, since it is foamy and has a large surface area, the adhesion uniformity is remarkably improved. Further, since the foamed oil agent emulsion to be applied is all supplied to the fiber bundle, the quantification of the attached amount becomes extremely high,
In addition, since the foamy oil agent emulsion has a low apparent viscosity, even if the oil agent emulsion having a high concentration is used, it can be uniformly attached.

【0017】また、ディップ法の如き絞り油剤用回収装
置が不要となり、油剤エマルジョン用のヘッドタンク、
配管等の設備を小さくすることができ、さらにはバス内
に残った油剤を廃棄する必要がないのでロスが極めて少
なくなり、その工業的価値は極めて大である。
Further, a collecting device for the squeezing oil agent such as the dipping method is unnecessary, and a head tank for the oil agent emulsion,
The equipment such as piping can be downsized, and further, since it is not necessary to discard the oil agent remaining in the bath, loss is extremely small, and its industrial value is extremely large.

【0018】[0018]

【実施例】固有粘度が0.65のポリエチレンテレフタ
レートチップを300℃で溶融し、孔数が900孔の口
金を通して、吐出量480g/分、紡糸速度1000m
/分で紡糸した。このようにして得られた未延伸糸を束
ねて150万デニールのトウにし、トータル延伸倍率
3.41倍で温水2段延伸を行ない、170℃で緊張熱
処理後、巾80mmのトウとなし、これに油剤エマルジ
ョン濃度、泡吐出量を変化させて種々の条件で油剤を付
与した。この後、捲縮を付与し130℃で弛緩熱処理を
行なって単繊維デニールが1.56deのトウを得た。
付着量のばらつきを見るため、得られたトウを幅方向に
3分割し、長さ方向に沿って3箇所、合計9箇所からサ
ンプリングした。さらにこれらのサンプルトウを表層部
と内層部に分けて油剤付着量を測定した。
EXAMPLE A polyethylene terephthalate chip having an intrinsic viscosity of 0.65 was melted at 300 ° C., passed through a die having 900 holes, a discharge rate of 480 g / min and a spinning speed of 1000 m.
Spinning was carried out at a speed of 1 / min. The undrawn yarn thus obtained was bundled into a tow of 1,500,000 denier, which was drawn in two stages of warm water at a total draw ratio of 3.41 and subjected to tension heat treatment at 170 ° C. to form a tow having a width of 80 mm. The oil agent was applied under various conditions by changing the oil agent emulsion concentration and the foam discharge amount. After that, crimping was applied and relaxation heat treatment was performed at 130 ° C. to obtain a tow having a single fiber denier of 1.56 de.
In order to see the variation in the amount of adhesion, the obtained tow was divided into three in the width direction and sampled from three locations along the length direction, for a total of nine locations. Further, these sample tows were divided into a surface layer portion and an inner layer portion to measure the amount of oil agent adhesion.

【0019】油剤付着量の測定方法は、サンプル10g
をメタノール:ベンゼン(1:1)混合溶媒で2.5時
間抽出し、溶媒を留去した後、抽出物を0.5ccの純
水に再溶解して屈折率を測定し、予め当該油剤エマルジ
ョンで求めておいた検量式に当てはめて付着量を算出す
る方法を採った。本発明の油剤付着方法によるトウの油
剤付着量測定結果を表1に示す。
The method of measuring the amount of oil agent adhered is as follows:
Was extracted with a mixed solvent of methanol: benzene (1: 1) for 2.5 hours, the solvent was distilled off, the extract was redissolved in 0.5 cc of pure water, and the refractive index was measured. A method of applying the calibration formula obtained in step 1 to calculate the amount of adhesion was adopted. Table 1 shows the measurement results of the amount of the oil agent deposited on the tow by the method for depositing the oil agent of the present invention.

【0020】比較のため、上記と同様の延伸条件を採用
し、油剤付与方法としてディップ法とスプレー法を用い
た場合のトウの油剤付着量測定結果を表2と表3に示
す。
For comparison, Table 2 and Table 3 show the results of measuring the amount of the oil agent deposited on the tow when the dipping method and the spray method were used as the oil agent applying method, employing the same stretching conditions as described above.

【0021】また、これらの油剤付着量とエマルジョン
吐出量あるいはトウ絞り後水分率の関係(平均値)を図
2〜図4に図示した。
Further, the relationship (average value) between the amount of adhering oil agent and the amount of ejected emulsion or the water content after tow drawing is shown in FIGS.

【0022】[0022]

【表1】 [Table 1]

【0023】[0023]

【表2】 [Table 2]

【0024】[0024]

【表3】 [Table 3]

【0025】表1及び図2に示すように、本発明の油剤
付与方法によれば、エマルジョン濃度5%から20%の
広い範囲にわたって泡吐出量と油剤付着量はほぼ定量的
な相関が得られ、トウの幅方向、長さ方向、内外層の付
着量のばらつきも極めて小さい。
As shown in Table 1 and FIG. 2, according to the method for applying an oil agent of the present invention, a substantially quantitative correlation can be obtained between the foam discharge amount and the oil agent adhesion amount over a wide range of the emulsion concentration from 5% to 20%. Also, variations in the tow width direction, the length direction, and the adhesion amount of the inner and outer layers are extremely small.

【0026】これに対して、本発明の油剤付与方法とは
異なるディップ法では表2及び図3に示すように、トウ
内の油剤付着量のばらつきは小さいがトウ絞り後水分率
と油剤付着量の間の定量性が低く、付着量の制御が難し
い。
On the other hand, in the dipping method different from the oil applying method of the present invention, as shown in Table 2 and FIG. 3, the variation of the oil adhering amount in the tow is small, but the moisture content after the tow drawing and the oil adhering amount are small. It is difficult to control the adhered amount because the quantitative property between the two is low.

【0027】また、スプレー法では表3及び図4に示す
ように、スプレー吐出量と油剤付着量の間にある程度の
定量性が見られるものの、トウ内の油剤付着量のばらつ
き、特にトウの内外層の付着量のばらつきは大きく均一
性が低くなっている。更に、スプレー吐出量から算出し
た油剤量と油剤付着量の実測値を比較すると後者の方が
大幅に低くなっており、付着効率が低いことが判る。
Further, in the spray method, as shown in Table 3 and FIG. 4, although there is some quantitativeness between the spray discharge amount and the oil agent adhesion amount, variations in the oil agent adhesion amount inside the tow, especially inside and outside the tow. The variation in the amount of the deposited layer is large and the uniformity is low. Furthermore, when comparing the amount of oil agent calculated from the spray discharge amount with the actual value of the amount of oil agent adhered, the latter is significantly lower, and it can be seen that the adhesion efficiency is low.

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

【図1】本発明の油剤付与方法を熱可塑性合成繊維の延
伸工程に適用した例を示す模式側面図である。
FIG. 1 is a schematic side view showing an example in which the method for applying an oil agent of the present invention is applied to a step of drawing a thermoplastic synthetic fiber.

【図2】本発明の実施例によって得られたトウの泡吐出
量に対する油剤付着量の関係を示す図である。
FIG. 2 is a diagram showing the relationship between the amount of foam deposited on a tow obtained according to the example of the present invention and the amount of oil adhered.

【図3】比較例のディップ法によって得られたトウのト
ウ絞り後の水分率に対する油剤付着量の関係を示す図で
ある。
FIG. 3 is a diagram showing the relationship between the water content after tow squeezing of the tow obtained by the dipping method of the comparative example and the amount of oil agent adhesion.

【図4】比較例のスプレー法によって得られたスプレー
吐出量と油剤付着量の関係を締めす図である。
FIG. 4 is a diagram showing a relationship between a spray discharge amount and an oil agent adhesion amount obtained by a spray method of a comparative example.

【符号の説明】[Explanation of symbols]

1 延伸第1ローラー 2 延伸第2ローラー 3 延伸第3ローラー 4 第1温水バス 5 第2温水バス 6 セットローラー 7 油剤ヘッドタンク 8 モーター 9 駆動軸 10 ミキシングヘッド 11 電磁ポンプ 12 泡吐出ノズル 13 クリンパー 14 泡状エマルジョン 15 圧縮空気配管 1 Stretching 1st roller 2 Stretching 2nd roller 3 Stretching 3rd roller 4 1st warm water bath 5 2nd warm water bath 6 Set roller 7 Oil head tank 8 Motor 9 Drive shaft 10 Mixing head 11 Electromagnetic pump 12 Bubble discharge nozzle 13 Crimper 14 Foam emulsion 15 Compressed air piping

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 走行する合成繊維束に油剤エマルジョン
を付与するに際して、該油剤エマルジョンを泡状にして
付与することを特徴とする油剤付与方法。
1. A method for applying an oil agent, which comprises applying the oil agent emulsion in the form of foam when applying the oil agent emulsion to a traveling synthetic fiber bundle.
【請求項2】 泡状油剤エマルジョンの密度が0.00
1〜0.1g/cm 3 である請求項1記載の油剤付与方
法。
2. The density of the foamy oil emulsion is 0.00.
1 to 0.1 g / cm 3The method of applying an oil agent according to claim 1.
Law.
JP12274293A 1993-05-25 1993-05-25 Oil agent application method Pending JPH06330403A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12274293A JPH06330403A (en) 1993-05-25 1993-05-25 Oil agent application method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12274293A JPH06330403A (en) 1993-05-25 1993-05-25 Oil agent application method

Publications (1)

Publication Number Publication Date
JPH06330403A true JPH06330403A (en) 1994-11-29

Family

ID=14843478

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12274293A Pending JPH06330403A (en) 1993-05-25 1993-05-25 Oil agent application method

Country Status (1)

Country Link
JP (1) JPH06330403A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996022409A1 (en) * 1995-01-21 1996-07-25 Rieter Automatik Gmbh Process and device for cooling melt-extruded filaments

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996022409A1 (en) * 1995-01-21 1996-07-25 Rieter Automatik Gmbh Process and device for cooling melt-extruded filaments

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