JPH0675125B2 - Manufacturing method for plastic optical fiber - Google Patents
Manufacturing method for plastic optical fiberInfo
- Publication number
- JPH0675125B2 JPH0675125B2 JP60227093A JP22709385A JPH0675125B2 JP H0675125 B2 JPH0675125 B2 JP H0675125B2 JP 60227093 A JP60227093 A JP 60227093A JP 22709385 A JP22709385 A JP 22709385A JP H0675125 B2 JPH0675125 B2 JP H0675125B2
- Authority
- JP
- Japan
- Prior art keywords
- polymer
- optical fiber
- plastic optical
- manufacturing
- core
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Landscapes
- Optical Fibers, Optical Fiber Cores, And Optical Fiber Bundles (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は、光伝送損失が低いプラスチック光ファイバを
製造する方法に関する。TECHNICAL FIELD The present invention relates to a method for producing a plastic optical fiber having a low optical transmission loss.
[従来技術] プラスチック光ファイバは、可撓性などの利点から頻繁
に用いられている。[Prior Art] Plastic optical fibers are frequently used because of their advantages such as flexibility.
第2図は、従来のプラスチック光ファイバ製造設備を示
す概略図である。この製造設備は、単量体を精製する蒸
留塔11′、単量体を触媒などと混合する混合器12′、単
量体を重合する重合反応器13′、および揮発物除去装置
14を有する。揮発物除去装置14はスクリュー押出機であ
り、これにより、ファイバ形成に有害である揮発物を除
去し、および重合体のファイバ化を行う。重合体をスク
リュー押出機14の入口21から供給し、スクリュー押出機
内で減圧ライン22により重合体中の揮発物を除去した
後、重合体を移送し、ファイバ化する。ファイバ化され
た重合体は出口23から出てくる。FIG. 2 is a schematic diagram showing a conventional plastic optical fiber manufacturing facility. This production facility includes a distillation column 11 'for purifying the monomer, a mixer 12' for mixing the monomer with a catalyst, a polymerization reactor 13 'for polymerizing the monomer, and a devolatilizer.
Have 14. The devolatilizer 14 is a screw extruder, which removes the volatilizers that are harmful to fiber formation and fiberizes the polymer. The polymer is supplied from the inlet 21 of the screw extruder 14, the volatile matter in the polymer is removed by the decompression line 22 in the screw extruder, and then the polymer is transferred to form a fiber. The fiberized polymer emerges from outlet 23.
しかし、この製造設備では、光伝送損失に優れるプラス
チック光ファイバを製造することができない。揮発物除
去装置においてスクリューおよび押出機シリンダが摺動
することによって、これらを構成する金属(通常、遷移
金属、例えば、鉄)粒子が重合体に混入して散乱損失お
よび吸収損失を生じさせるからである。However, this manufacturing facility cannot manufacture a plastic optical fiber having excellent optical transmission loss. The sliding of the screw and extruder cylinder in the devolatilizer removes the metal (usually transition metal, eg, iron) particles that make them up into the polymer, causing scattering and absorption losses. is there.
[発明の構成] 本発明の要旨は、コア重合体を多孔板から減圧案内にス
トランド状に押し出すことにより重合体から揮発物を除
去し、重合体をファイバ化してコアを形成した後、クラ
ッドをコアのまわりに形成することを特徴とするプラス
チック光ファイバの製造方法に存する。本発明の製造方
法は、重合体を多孔板から減圧室内にストランド状に押
し出すことにより、プラスチック光ファイバ用重合体か
ら揮発物を除去することを特徴とする。[Structure of the Invention] The gist of the present invention is to remove volatiles from a polymer by extruding the core polymer from a perforated plate into a reduced pressure guide in a strand shape, forming a core by fiberizing the polymer, and then forming a clad. A plastic optical fiber manufacturing method is characterized in that it is formed around a core. The production method of the present invention is characterized in that a volatile matter is removed from a polymer for a plastic optical fiber by extruding the polymer from a porous plate into a decompression chamber in a strand shape.
本発明のプラスチック光ファイバ製造方法において重合
体からの揮発物除去は、主としてコア形成用重合体に用
いるが、クラッド形成用重合体にも用いてよい。In the method for producing a plastic optical fiber of the present invention, the removal of volatiles from the polymer is mainly used for the core-forming polymer, but it may also be used for the clad-forming polymer.
以下に、添付図面を参照して本発明の製造方法を説明す
る。尚、本発明の製造方法は以下の態様に限定されるも
のではない。The manufacturing method of the present invention will be described below with reference to the accompanying drawings. The manufacturing method of the present invention is not limited to the following modes.
第1図は、本発明の製造方法の一態様を示すプラスチッ
ク光ファイバ製造設備の概略図である。この製造設備
は、蒸留塔11、混合器12、重合反応器13および揮発物除
去装置19を有する。揮発物除去装置10を除く蒸留塔11、
混合器12および重合反応器13は、従来の製造設備におい
て用いるものと同様であってよく、あるいは添付図面の
とおりでなくてよく、装置10に重合体を供給できる装置
であればよい。揮発物除去装置10は、多孔板3および減
圧ライン2を有する。多孔板3の細孔径は、0.5〜3.0mm
であることが好ましい。この製造設備は、ジョイント部
の漏れが0.5lusec以下である密閉系であることが好まし
い。以下に、プラスチック光ファイバの製造における揮
発物除去装置10での工程を説明する。FIG. 1 is a schematic view of a plastic optical fiber manufacturing facility showing one embodiment of the manufacturing method of the present invention. This manufacturing facility has a distillation column 11, a mixer 12, a polymerization reactor 13 and a volatile matter removing device 19. A distillation column 11 excluding the volatile matter removal device 10,
The mixer 12 and the polymerization reactor 13 may be the same as those used in the conventional manufacturing facility, or may not be as shown in the accompanying drawings, and may be any device capable of supplying the polymer to the device 10. The volatile matter removal device 10 has a perforated plate 3 and a decompression line 2. The pore diameter of the perforated plate 3 is 0.5 to 3.0 mm
Is preferred. This manufacturing facility is preferably a closed system in which the leak in the joint is 0.5 lusec or less. The process in the volatile matter removing device 10 in the production of the plastic optical fiber will be described below.
揮発物を含む重合体をガス圧により移送し、入口1から
揮発物除去装置10に供給する。揮発物除去装置10は、減
圧ライン2により減圧状態に保たれている。重合体は、
多孔板3を通過することによって、第1図に示すような
ストランド4の形状で減圧容器内に押出され、重合体中
の揮発物は除去される。重合体の粘度を小さくするよう
に、重合体移送路および装置10の内部は高温、例えば20
0〜300℃に保たれていることが好ましい。装置10の下部
に一時的に重合体を貯蔵し、ガス圧により出口5から重
合体を押出し、重合体を(要すれば出口5において)フ
ァイバ化してコアを形成する。The polymer containing volatile matter is transferred by gas pressure and supplied from the inlet 1 to the volatile matter removing apparatus 10. The volatile matter removal device 10 is kept in a reduced pressure state by the reduced pressure line 2. The polymer is
By passing through the porous plate 3, the strands 4 as shown in FIG. 1 are extruded into the decompression container, and the volatile substances in the polymer are removed. The polymer transfer path and the interior of the device 10 are heated to a high temperature, e.g.
It is preferably maintained at 0 to 300 ° C. The polymer is temporarily stored in the lower part of the apparatus 10, the polymer is extruded from the outlet 5 by gas pressure, and the polymer is fiberized (if necessary at the outlet 5) to form a core.
次いで、装置10から出てきたコアのまわりにクラッドを
形成する。クラッドの形成は溶融被覆または溶液被覆な
どの方法によって行える。A cladding is then formed around the core emerging from the device 10. The clad can be formed by a method such as melt coating or solution coating.
[発明の効果] 本発明の製造方法を用いる場合、金属と金属の摺動がな
く金属が重合体に混入しないので、光伝送損失に優れた
プラスチック光ファイバが製造される。ガス圧により重
合体を移送し、および脱揮発物効果を向上するため重合
体を多孔板に通し重合体の表面積を大きくしているから
である。[Advantages of the Invention] When the production method of the present invention is used, a plastic optical fiber having excellent optical transmission loss is produced because there is no sliding of metal to metal and the metal is not mixed in the polymer. This is because the polymer is transferred by gas pressure and the surface area of the polymer is increased by passing the polymer through the porous plate in order to improve the devolatilization effect.
[実施例] 以下に実施例および比較例を示す。[Examples] Examples and comparative examples are shown below.
実施例1 第1図に示す設備を用いて、ポリメチルメタクリレート
をコアとし、フッ素含有メチルメタクリレートをクラッ
ドとするコア径0.985mm、クラッド肉厚0.015mmおよびフ
ァイバ外径1.015mmのプラスチック光ファイバを製造し
た。製造設備のジョイント部の漏れは、0.5lusecであっ
た。重合開始剤として、アゾイソブチロニトリル(単量
体に対して0.1重量%)を用いた。揮発物除去装置10に
おいて、多孔板3の細孔径は2.0mmであり、内部圧力は1
0mmHgであり、重合体移送路および揮発物除去装置10の
温度は200℃に保った。Example 1 Using the equipment shown in FIG. 1, a plastic optical fiber having a core of polymethylmethacrylate and a cladding of fluorine-containing methylmethacrylate with a core diameter of 0.985 mm, a cladding thickness of 0.015 mm and a fiber outer diameter of 1.015 mm was manufactured. did. The leak at the joint of the manufacturing equipment was 0.5 lusec. Azoisobutyronitrile (0.1% by weight based on the monomer) was used as a polymerization initiator. In the volatile matter removing device 10, the perforated plate 3 has a pore diameter of 2.0 mm and an internal pressure of 1
It was 0 mmHg, and the temperature of the polymer transfer path and the volatile matter removal device 10 was kept at 200 ° C.
得られたプラスチック光ファイバの光伝送損失は波長56
8nmの光において70dB/kmであった。The optical transmission loss of the obtained plastic optical fiber is 56
It was 70 dB / km at 8 nm light.
比較例1 第2図に示す従来の設備を用いる以外は、実施例1を繰
り返し、同様のプラスチック光ファイバを製造した。え
られたプラスチック光ファイバの光伝送損失は波長568n
mの光において100dB/kmであった。Comparative Example 1 A similar plastic optical fiber was manufactured by repeating Example 1 except that the conventional equipment shown in FIG. 2 was used. The optical transmission loss of the obtained plastic optical fiber has a wavelength of 568n.
It was 100 dB / km at m light.
第1図は、本発明の製造方法の一態様を示すプラスチッ
ク光ファイバ製造設備の概略図、および 第2図は、従来のプラスチック光ファイバ製造設備の概
略図である。 1,21…入口、2,22…減圧ライン、3…多孔板、4…スト
ランド、5,23…出口、10,14…揮発物除去装置、11,11′
…蒸留塔、12,12′…混合器、13,13′…重合反応器。FIG. 1 is a schematic view of a plastic optical fiber manufacturing facility showing one embodiment of the manufacturing method of the present invention, and FIG. 2 is a schematic view of a conventional plastic optical fiber manufacturing facility. 1,21 ... inlet, 2,22 ... decompression line, 3 ... perforated plate, 4 ... strand, 5,23 ... outlet, 10,14 ... volatile matter removing device, 11,11 '
... Distillation column, 12,12 '... Mixer, 13,13' ... Polymerization reactor.
Claims (1)
ンド状に押し出すことにより重合体から揮発物を除去
し、重合体をファイバ化してコアを形成した後、クラッ
ドをコアのまわりに形成することを特徴とするプラスチ
ック光ファイバの製造方法。1. A core polymer is extruded from a porous plate into a vacuum chamber in a strand shape to remove volatiles from the polymer, and the polymer is made into fibers to form a core, and then a clad is formed around the core. A method for manufacturing a plastic optical fiber, characterized in that:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60227093A JPH0675125B2 (en) | 1985-10-11 | 1985-10-11 | Manufacturing method for plastic optical fiber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60227093A JPH0675125B2 (en) | 1985-10-11 | 1985-10-11 | Manufacturing method for plastic optical fiber |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6286305A JPS6286305A (en) | 1987-04-20 |
| JPH0675125B2 true JPH0675125B2 (en) | 1994-09-21 |
Family
ID=16855379
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60227093A Expired - Lifetime JPH0675125B2 (en) | 1985-10-11 | 1985-10-11 | Manufacturing method for plastic optical fiber |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0675125B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107778488B (en) * | 2017-11-16 | 2020-07-21 | 湖北兴瑞硅材料有限公司 | Low molecular remover and method for producing methyl silicone oil with viscosity of 30-1000000cs |
-
1985
- 1985-10-11 JP JP60227093A patent/JPH0675125B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6286305A (en) | 1987-04-20 |
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