JPS60215808A - Spinning system - Google Patents
Spinning systemInfo
- Publication number
- JPS60215808A JPS60215808A JP59065764A JP6576484A JPS60215808A JP S60215808 A JPS60215808 A JP S60215808A JP 59065764 A JP59065764 A JP 59065764A JP 6576484 A JP6576484 A JP 6576484A JP S60215808 A JPS60215808 A JP S60215808A
- Authority
- JP
- Japan
- Prior art keywords
- spinning
- nozzle
- reaction tube
- yarn
- spinning nozzle
- 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
Links
Landscapes
- Optical Fibers, Optical Fiber Cores, And Optical Fiber Bundles (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の利用分野〕
本発明は紡糸装置に係り・光ファイバの製造に好適な紡
糸装置に関する・
〔発明の背景〕
従来の熱町塑性樹脂肪糸装置は・第１図に示されるよう
に、樹脂溶融槽２内の紡糸原液３を計計吐出ボング４で
紡糸ノズル５に送り・この紡糸ノズル５から糸条を吐ｄ
させ、冷却区間６で冷却させて硬化させた後・巻取装置
７で巻取るようＫなっている。[Detailed Description of the Invention] [Field of Application of the Invention] The present invention relates to a spinning device and relates to a spinning device suitable for manufacturing optical fibers. [Background of the Invention] A conventional thermoplastic resin fiber fiber device is As shown in the figure, the spinning dope 3 in the resin melting tank 2 is sent to the spinning nozzle 5 with a metered discharge bong 4, and the yarn is discharged from the spinning nozzle 5.
After cooling and hardening in a cooling section 6, the material is wound up in a winding device 7.
しかし・紡糸ノズル５から吐ｄさｔｌ、た糸条Ｋｉｄ自
重により・あるいは巻取装ａ７の引張力により張力が作
用して繊維長手方向に分子が配向し、糸状を元ファイバ
として利用しようとすると、複屈折、光散乱等の光学的
ひず４が問題となり好ましくないという問題があった。However, if the molecules are oriented in the longitudinal direction of the fibers due to the weight of the yarn Kid discharged from the spinning nozzle 5 or due to the tensile force of the winding device a7, and when trying to use the filament as a source fiber, , birefringence, light scattering, and other optical distortions, which are undesirable.
また・この分子の配向を防ぐ［は非常にゆつ（Ｖと紡糸
せねばならず曖産性も悪いという欠点もあり、さらに、
分子蕾の高いものほど分子が配向し易いので、従来の装
置では・高分子量の熱可塑性樹脂の光ファイバを製造す
ることはできず、低分子量のもの°に限られていた口
また、従来の第１図に示すような紡糸装置は、熱可塑性
樹脂を対象とするもので、熱硬化性樹脂のファイバーを
紡糸しようとすると・紡糸ノズル５の上流側では紡糸原
液を硬化させないために加熱しなければならないが・溶
融槽２内で加熱すると、計量吐出ポンプ４での粘性発熱
もあって重合反応が著しく進行し糸条が吐呂できず、ま
た紡糸ノズル５だけを加熱すると、ノズル５の上下長さ
は短いため温度制備が離しく、ゲル化が不十分であった
り、反応しすぎて糸状が吐出できなかったり・あるいは
糸状の径が均一とならなかったり等の問題が生じていた
。そのため・従来の熱ｏＪ１ｉｔ１性樹脂肪糸装置を熱
硬化性樹脂の紡糸に実用上適用することはできなかった
〇
〔発明の目的〕
本発明の目的は・熱可塑性樹脂および熱硬化性樹脂のい
ずれをも光学ひずみを生ずることなく紡糸できる紡糸装
置を提供することにある。In addition, it is very difficult to prevent the orientation of this molecule (it has the disadvantage of having to spin with V and having poor ambiguity, and
The higher the molecular buds, the easier the molecules are to be oriented, so conventional equipment cannot produce optical fibers made of high-molecular-weight thermoplastic resins. The spinning device shown in Fig. 1 is for thermoplastic resin, and when trying to spin thermosetting resin fibers, the spinning dope must be heated upstream of the spinning nozzle 5 to prevent it from hardening. However, if heating is performed in the melting tank 2, the polymerization reaction will proceed significantly due to the viscous heat generated by the metering discharge pump 4, and the yarn will not be able to be spouted, and if only the spinning nozzle 5 is heated, the upper and lower parts of the nozzle Since the length is short, it is difficult to control the temperature, resulting in problems such as insufficient gelation, too much reaction and failure to discharge filaments, or non-uniform filament diameters. Therefore, the conventional thermal oJ1it1 resin fiber yarn device could not be practically applied to spinning thermosetting resin. It is an object of the present invention to provide a spinning device capable of spinning fibers without causing any optical distortion.
〔発明の概要ｊ
本発明に係る紡糸装置ｔは、紡糸原液タンクと紡糸ノズ
ル間の管路内に紡糸原液を層流流れにする整流格子を配
置し、該整流格子と紡糸ノズル間の管路倉駆１の反応管
にて形成するとともに・紡糸ノズル下流側に渠２の反応
管全配設し・渠１の反応管によって重合反応を開始して
紡糸原液が紡糸ノズルから半ゲル化状態で吐出できるよ
うにし、第２の反応管によって紡糸ノズルから吐出され
た半ゲル化状態の糸状を充分に硬化させるように構成し
たことを特徴とするもので、この構成によって前記目的
が達成されるのである。[Summary of the Invention j The spinning apparatus t according to the present invention includes a rectifying grid that makes the spinning dope into a laminar flow in the pipe line between the spinning dope tank and the spinning nozzle, and the pipe line between the rectifying grid and the spinning nozzle. At the same time, the reaction tubes of conduit 2 are all arranged downstream of the spinning nozzle, and the polymerization reaction is started by the reaction tube of conduit 1, so that the spinning stock solution leaves the spinning nozzle in a semi-gelled state. The method is characterized in that it is configured so that the filament in a semi-gelled state discharged from the spinning nozzle is sufficiently hardened by the second reaction tube, and the above object is achieved by this configuration. be.
また、第２の反応管に気流発生装置を設けることによっ
て・紡糸ノズルから吐出された糸条に浮力を与えて糸条
の自重による変形を防止することができる。Further, by providing an airflow generating device in the second reaction tube, it is possible to impart buoyancy to the yarn discharged from the spinning nozzle and prevent deformation of the yarn due to its own weight.
次に１本発明の詳細な説明する。 Next, one aspect of the present invention will be explained in detail.
第２図は本発明に係る紡糸装＠を熱硬化性樹脂の紡糸に
適用した実施例を示す図である口この第２図において、
本実施例に係る紡糸装置は、熱硬化性樹脂の原液１２Ａ
の入ったタンク１２と・糸状１６を吐出する紡糸ノズル
１５・と・タンク１２内の原液を紡糸ノズル１５に送る
管路１３と、管路１３内に設置されている整流器２゜と
・整流″ａ２０と紡糸ノズル１５間に配設された第１の
反応管３０と、ノズル１５下流側に配設された第２の反
応管４０とから構成されている・管路１３には計量吐出
ポンプ１４が設（ａされており、このポンプ１４によっ
て紡糸ノズル１５がら糸条１６ｔ−吐出させるようにな
っている。FIG. 2 is a diagram showing an embodiment in which the spinning device according to the present invention is applied to spinning thermosetting resin.
The spinning device according to this embodiment has a thermosetting resin stock solution of 12A.
A spinning nozzle 15 that discharges a filament 16, a pipe line 13 that sends the stock solution in the tank 12 to the spinning nozzle 15, a rectifier 2° installed in the pipe line 13, and a rectifier. It is composed of a first reaction tube 30 disposed between the a20 and the spinning nozzle 15, and a second reaction tube 40 disposed downstream of the nozzle 15. The pump 14 causes the spinning nozzle 15 to eject 16t of yarn.
管路１３のポンプ１４下流位置には原液の流れを層流に
する整流器２０が設けられている・整流器２０は格子状
の小孔２２Ａの形成されている整流格子２２と・この整
流格子２２上流側・下流側にそれぞれ形成されているア
ダプタ部２４．リザーバ部２６と、整流格子２２下面に
設けられた異物除去用のフィルタ２８とから構成されて
いる。A rectifier 20 is provided downstream of the pump 14 in the conduit 13 to make the flow of the stock solution into a laminar flow.The rectifier 20 is connected to a rectifier lattice 22 in which grid-shaped small holes 22A are formed.Upstream of this rectifier lattice 22. Adapter portions 24 formed on the side and downstream sides, respectively. It is composed of a reservoir section 26 and a filter 28 for removing foreign matter provided on the lower surface of the rectifying grid 22.
原液は整流格子２２の小孔２２Ａを通ることによって流
速が均一化された層流となって紡糸ノズル１５に送られ
る。アダプタ部２４．リザーバ部２６にいずれも整流格
子２２の整流作用を安定させる働きがある。また、アダ
プタ部２４・リザーバ部２６のまわりＩＣはヒータ５０
Ａが設けられており・このヒータ５０Ａによって整流器
２０内の原液にはとんど重合反応が生じない程度に加熱
され・整流器後流側に設けられている第１の反応管３０
内で安定した重合反応（半ゲル化）が進むように配慮さ
れている。The stock solution passes through the small holes 22A of the rectifying grid 22 and is sent to the spinning nozzle 15 as a laminar flow with a uniform flow rate. Adapter part 24. Each of the reservoir parts 26 has a function of stabilizing the rectifying action of the rectifying grating 22. In addition, the IC around the adapter section 24 and reservoir section 26 is connected to a heater 50.
The heater 50A heats the stock solution in the rectifier 20 to such an extent that almost no polymerization reaction occurs.The first reaction tube 30 is provided on the downstream side of the rectifier.
Care has been taken to ensure that a stable polymerization reaction (semi-gelation) progresses within the container.
整流器２０と紡糸ノズル１５間の管路はｇｌ！１の反応
管３０によって形成され、この第１の反応管３０のまわ
りにはヒータ５０Ｂが設けられており・整流器２０から
送られてきた原液をヒータ５０Ｂにて加熱することによ
り・序々に重合反応を進行させて紡糸ノズル１５に送り
、紡糸ノズル１５で半ゲル化状態の糸条１６を吐出でき
るようになっている。The pipe line between the rectifier 20 and the spinning nozzle 15 is gl! A heater 50B is provided around the first reaction tube 30. By heating the stock solution sent from the rectifier 20 with the heater 50B, a polymerization reaction is gradually carried out. is advanced and sent to the spinning nozzle 15, and the spinning nozzle 15 can discharge the yarn 16 in a semi-gelled state.
紡糸ノズル１５まわりにもヒータ５０Ｃが設けられ・さ
らに第２の反応管４０の外周囲にもヒータ４２が設けら
れており・紡糸ノズル１５から吐出された半ゲル化状態
０糸状１６をヒータ４２で加熱して・さらに重合反応を
進行させ２この第２の反応管３０内で糸条１６を充分に
硬化させるよりになっている＠
第２の反応管４０の下端部近傍！ｌｃは熱風送風機４４
が配置されており・その熱風吐出管は反応管４０内にの
びて第４図に示されるような螺線状の上昇気流４５′に
形成するようになっている。この螺線状の上昇気流４５
によって糸条１６は浮揚力を受け・糸状の自重に起因す
る変形が防止されるのである。A heater 50C is also provided around the spinning nozzle 15, and a heater 42 is also provided around the outer circumference of the second reaction tube 40. Near the lower end of the second reaction tube 40 by heating and further advancing the polymerization reaction to sufficiently harden the yarn 16 inside the second reaction tube 30! lc is hot air blower 44
is arranged, and its hot air discharge pipe extends into the reaction tube 40 to form a spiral upward airflow 45' as shown in FIG. This spiral upward airflow 45
As a result, the yarn 16 receives a buoyant force and is prevented from being deformed due to its own weight.
この第２の反応管４０を出た糸条１６は、冷却区間６０
を通り充分冷却された後２巻取装置７０で巻取られるよ
うになっている〇
なお、前記実施例では・熱硬化性樹脂の原液に重合反応
を起こさせるエネルギー付与手段としてヒータ５０Ａ、
５０Ｂ、５０Ｃおよび４２を用いたが・その他、赤外線
、紫外線・放射線、電子線等を弗化させる各種機器であ
ってもよく・特に駆足されるものではない。The yarn 16 exiting the second reaction tube 40 is transported to a cooling section 60.
It is designed to be wound up by a two-way winding device 70 after being sufficiently cooled through a heater 50A,
Although 50B, 50C, and 42 were used, various other devices that fluorinate infrared rays, ultraviolet rays/radiation, electron beams, etc. may also be used, and are not particularly required.
また・前記実施例では・本発明に係る装置Ｉｌｔ熱硬化
性樹脂の紡糸に適用しているが・熱可塑性樹脂であって
も・モノ１段階から紡糸過程で重合させて紡糸できるも
のであれば適用できることはいうまでもない。In addition, in the above embodiment, the apparatus according to the present invention is applied to spinning thermosetting resin, but even if it is a thermoplastic resin, as long as it can be polymerized and spun in the spinning process from the first step. Needless to say, it is applicable.
このように、本実施例によれば・重合反応が進まない状
態（重合反応の開始段階である半ゲル化状態）で紡糸す
るので・熱可塑性樹脂・熱硬化性樹脂のいずれを紡糸し
ても光学ひずみの少ないファイバーを得ることができる
。また、半ゲル化状態で紡糸するのでかなり高い分子量
のものも紡糸できるという効果もある。As described above, according to this example, the spinning is carried out in a state where the polymerization reaction does not proceed (semi-gelled state, which is the starting stage of the polymerization reaction), and therefore it is possible to spin the fibers regardless of whether the thermoplastic resin or the thermosetting resin is spun. A fiber with low optical distortion can be obtained. Furthermore, since spinning is performed in a semi-gelled state, it is also possible to spin materials with fairly high molecular weights.
以上の説明から明らかなように１本発明によれば、製造
されたファイバーに光学ひずみを生ずることのない熱硬
化性樹脂および熱可塑性樹脂の紡糸装置ｉ１に一得るこ
とができる口As is clear from the above description, according to the present invention, it is possible to obtain an apparatus for spinning thermosetting resins and thermoplastic resins i1 that does not cause optical distortion in the manufactured fibers.
第１図は従来の熱可塑性樹脂の紡糸装置の概略図、第２
図は本発明に係る紡糸装置の実施例の断−ｒｋＪ契、第
３図はその整流器の要部断面図、第４図はその第２の反
応管内の気流状態を示す断面図である・
１２・・・原液タンク、１３・・・管路、１４・・・計
量吐出ポンプ、１５・・・紡糸ノズル、１６・・・糸条
、２０・・・整流器、２２・・・整流格子、３０・・・
第１の反応管・４０・・・第２の反応管、４２．．５０
Ａ、５０Ｂ。
５０Ｃ・・・ヒータ、４４・・・熱風送風機・６０・・
・冷却区間・７０・・・巻取装置。
代理人 弁理士 高橋明夫Figure 1 is a schematic diagram of a conventional thermoplastic resin spinning device;
The figure is a cross-sectional view of an embodiment of the spinning device according to the present invention, FIG. 3 is a sectional view of the main part of the rectifier, and FIG. 4 is a sectional view showing the airflow state in the second reaction tube. ... Raw solution tank, 13... Pipe line, 14... Metering discharge pump, 15... Spinning nozzle, 16... Yarn, 20... Rectifier, 22... Rectifier grid, 30...・・・
First reaction tube・40...Second reaction tube, 42. ．． 50
A, 50B. 50C... Heater, 44... Hot air blower, 60...
- Cooling section - 70... Winding device. Agent Patent Attorney Akio Takahashi
Claims (2)
に導き・該紡糸ノズルから糸条を吐出させ・該糸条を硬
化区間にて硬化させて紡糸する紡糸装置において・前記
タンクと紡糸ノズル間の管路内に紡糸原液を層流流れに
する整流格子を配置するとともに・該整流格子と紡糸ノ
ズル間の管路を管内の紡糸原液に序々に重合反応を起こ
させる第１の反応管にて形成し、紡糸ノズル下流側に紡
糸ノズルから吐出された半ゲル化状態の糸条を充分に硬
化させる第２の反応管を配設したことを特徴とする紡糸
装置。(1) In a spinning device that guides the spinning stock solution in a tank to a spinning nozzle through a pipe, discharges a yarn from the spinning nozzle, and cures the yarn in a curing section for spinning. Between the tank and the spinning nozzle. A rectifying grid that causes the spinning stock solution to flow in a laminar flow is arranged in the pipe, and a pipe line between the straightening grid and the spinning nozzle is a first reaction tube that gradually causes a polymerization reaction in the spinning stock solution in the pipe. A spinning device characterized in that a second reaction tube is disposed on the downstream side of the spinning nozzle to fully cure the semi-gelled yarn discharged from the spinning nozzle.
該反応管には管内の糸条を浮揚させるための上昇気流発
生手段が設けられていること′ｆｒ、％徴とする特許請
求の範囲第１項記載の紡糸装置。(2) the second reaction tube extends downward from the lead 11;
2. The spinning apparatus according to claim 1, wherein the reaction tube is provided with an upward air current generating means for levitating the yarn within the tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59065764A JPS60215808A (en) | 1984-04-04 | 1984-04-04 | Spinning system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59065764A JPS60215808A (en) | 1984-04-04 | 1984-04-04 | Spinning system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS60215808A true JPS60215808A (en) | 1985-10-29 |
Family
ID=13296410
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59065764A Pending JPS60215808A (en) | 1984-04-04 | 1984-04-04 | Spinning system |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60215808A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62191506A (en) * | 1986-02-10 | 1987-08-21 | フィリップス エレクトロニクス ネムローゼ フェンノートシャップ | Molecularily oriented synthetic resin fiber and its production |
| WO2017137593A1 (en) * | 2016-02-12 | 2017-08-17 | Poromembrane Gmbh | Filament production device |
-
1984
- 1984-04-04 JP JP59065764A patent/JPS60215808A/en active Pending
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62191506A (en) * | 1986-02-10 | 1987-08-21 | フィリップス エレクトロニクス ネムローゼ フェンノートシャップ | Molecularily oriented synthetic resin fiber and its production |
| WO2017137593A1 (en) * | 2016-02-12 | 2017-08-17 | Poromembrane Gmbh | Filament production device |
| CN108848673A (en) * | 2016-02-12 | 2018-11-20 | 帕尔公司 | Long filament manufacturing equipment |
| JP2019504938A (en) * | 2016-02-12 | 2019-02-21 | ポール・コーポレーションＰａｌｌ Ｃｏｒｐｏｒａｔｉｏｎ | Filament manufacturing equipment |
| US11198952B2 (en) | 2016-02-12 | 2021-12-14 | Pall Corporation | Filament production device |
| CN108848673B (en) * | 2016-02-12 | 2022-03-08 | 帕尔公司 | Filament manufacturing apparatus |
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