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JPH0225483B2 - - Google Patents
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JPH0225483B2 - - Google Patents

Info

Publication number
JPH0225483B2
JPH0225483B2 JP57186369A JP18636982A JPH0225483B2 JP H0225483 B2 JPH0225483 B2 JP H0225483B2 JP 57186369 A JP57186369 A JP 57186369A JP 18636982 A JP18636982 A JP 18636982A JP H0225483 B2 JPH0225483 B2 JP H0225483B2
Authority
JP
Japan
Prior art keywords
optical transmission
fiber
weight
methyl methacrylate
sheath
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
Application number
JP57186369A
Other languages
Japanese (ja)
Other versions
JPS5975202A (en
Inventor
Minoru Shioda
Yoshio Iki
Eiichi Ooki
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.)
Kanegafuchi Chemical Industry Co Ltd
Original Assignee
Kanegafuchi Chemical Industry Co 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 Kanegafuchi Chemical Industry Co Ltd filed Critical Kanegafuchi Chemical Industry Co Ltd
Priority to JP57186369A priority Critical patent/JPS5975202A/en
Publication of JPS5975202A publication Critical patent/JPS5975202A/en
Publication of JPH0225483B2 publication Critical patent/JPH0225483B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29DPRODUCING PARTICULAR ARTICLES FROM PLASTICS OR FROM SUBSTANCES IN A PLASTIC STATE
    • B29D11/00Producing optical elements, e.g. lenses or prisms
    • B29D11/00663Production of light guides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/05Filamentary, e.g. strands
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2027/00Use of polyvinylhalogenides or derivatives thereof as moulding material
    • B29K2027/12Use of polyvinylhalogenides or derivatives thereof as moulding material containing fluorine
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2033/00Use of polymers of unsaturated acids or derivatives thereof as moulding material
    • B29K2033/04Polymers of esters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29LINDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2009/00Layered products

Landscapes

  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Ophthalmology & Optometry (AREA)
  • Mechanical Engineering (AREA)
  • Optical Fibers, Optical Fiber Cores, And Optical Fiber Bundles (AREA)

Description

【発明の詳細な説明】 本発明は、光伝送性に優れた繊維の製造法に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing fibers with excellent light transmission properties.

光を伝送する繊維は古くから知られており、す
でにガラス特に石英を利用した光伝送繊維が実用
化されている。しかし、このガラスあるいは石英
でつくられた光伝送繊維は光伝送性には優れるも
のの可撓性に乏しく、かつ重い、また非常に高価
であるといつた欠点がある。かかる背景から、ガ
ラス系光伝送繊維よりも光伝送性は劣るものの、
取扱いが容易でかつ安価であるプラスチツク系光
伝送繊維を短距離通信用として使用しようとする
試みが最近活発に行なわれている。
Fibers that transmit light have been known for a long time, and optical transmission fibers made of glass, especially quartz, have already been put into practical use. However, although optical transmission fibers made of glass or quartz have excellent optical transmission properties, they have drawbacks such as poor flexibility, heavy weight, and very high cost. Against this background, although the optical transmission properties are inferior to that of glass-based optical transmission fibers,
Recently, attempts have been made to use plastic optical transmission fibers, which are easy to handle and inexpensive, for short-distance communications.

プラスチツク系光伝送繊維は、ガラス系光伝送
繊維に比べて、大口径化及び高開口数化が容易な
ため、光源との、あるいは繊維同志の結合効率が
高く、接続が簡単であり、大口径であつても軽量
かつ可撓性に富み、また工業的に大量生産が可能
であることもあつて極めて安価である等の特微を
有している。このため、コンピユーター周辺の屋
内配線用等への適用が期待されている。
Compared to glass-based optical transmission fibers, plastic optical transmission fibers can easily be made larger in diameter and have a higher numerical aperture, so they have higher coupling efficiency with light sources or between fibers, and are easy to connect. However, it has the characteristics of being lightweight and highly flexible, being able to be industrially mass-produced, and being extremely inexpensive. Therefore, it is expected to be applied to indoor wiring around computers, etc.

しかし、現在最も光伝送性の優れたプラスチツ
ク系光伝送繊維であると言われている、芯成分物
質にメタクリル酸メチル系重合体、さや成分物質
にフツ素含有重合体を使用したものでも、繊維径
や波長にもよるが高々300dB/Kmの光伝送性能で
あり、短距離通信用に使用するためには光伝送性
能を更に向上させる必要がある。
However, even with plastic fibers that use a methyl methacrylate polymer for the core component and a fluorine-containing polymer for the sheath component, which is currently said to have the best optical transmission properties, the fiber Although it depends on the diameter and wavelength, the optical transmission performance is at most 300 dB/Km, and it is necessary to further improve the optical transmission performance in order to use it for short-distance communication.

光伝送性能を向上させるために、これまでに、
芯成分中の塵埃や、遷移金属、着色物質等を徹底
的に除去し高純度化することが試みられてきた。
光伝送繊維の光伝送性能を低下させる今一つの大
きな要因は、芯成分物質中に存在する気泡であ
り、また芯成分物質とさや成分物質との界面にお
ける接着不良であると考えられる。
In order to improve optical transmission performance, so far,
Attempts have been made to thoroughly remove dust, transition metals, colored substances, etc. from the core component to improve its purity.
Another major factor that reduces the optical transmission performance of optical transmission fibers is considered to be air bubbles present in the core component material and poor adhesion at the interface between the core component material and the sheath component material.

本発明者らは、これらの要因のうち、芯成分物
質に存在する気泡が光伝送性能を低下させるに最
も大きな要因であると考え、芯成分物質中に気泡
を発生させない製造法を鋭意検討した結果、光伝
送性能が著しく向上したプラスチツク系光伝送繊
維が得られることを見出し本発明に到達した。
Among these factors, the present inventors believe that air bubbles present in the core component material are the most significant factor in deteriorating optical transmission performance, and have diligently investigated a manufacturing method that does not generate air bubbles in the core component material. As a result, it was discovered that a plastic optical transmission fiber with significantly improved optical transmission performance could be obtained, and the present invention was achieved.

すなわち本発明の要旨とするところは、芯成分
物質としてメタクリル酸メチル系重合体、さや成
分物質としてフツ素を少なくとも30重量%含むフ
ツ素含有重合体からなる芯−さや構造を有する光
伝送繊維を製造するに際し、紡糸ノズルの直下の
連続する区域中に溶融押出された繊維を通過させ
て冷却する工程において、加圧下に冷却すること
を特徴とする光伝送繊維の製造法にある。
That is, the gist of the present invention is to provide an optical transmission fiber having a core-sheath structure consisting of a methyl methacrylate-based polymer as a core component material and a fluorine-containing polymer containing at least 30% by weight of fluorine as a sheath component material. A method for producing a light transmitting fiber is characterized in that during the production, the melt-extruded fiber is passed through a continuous area immediately below a spinning nozzle and cooled under pressure.

以下に、本発明を更に詳細に説明する。 The present invention will be explained in more detail below.

本発明で用いられる芯成分物質であるメタクリ
ル酸メチル系重合体は、メタクリル酸メチル単独
重合体であつてもよく、アクリル酸メチルやアク
リル酸エチル等の共重合成分を20重量%以下含む
メタクリル酸メチル系共重合体であつてもよい。
メタクリル酸メチル系重合体は、光伝送性能を高
めるために塵埃や遷移金属、着色物質等の不純物
が極力含まれないようにモノマーを精製、重合す
る必要がある。そのような点から塊状重合法で重
合するのが好ましい。
The methyl methacrylate-based polymer, which is the core component material used in the present invention, may be a methyl methacrylate homopolymer, and may be a methacrylic acid containing 20% by weight or less of a copolymer component such as methyl acrylate or ethyl acrylate. It may also be a methyl copolymer.
In order to improve the optical transmission performance of methyl methacrylate polymers, it is necessary to purify and polymerize the monomer so that impurities such as dust, transition metals, and colored substances are contained as little as possible. From this point of view, bulk polymerization is preferred.

このようなメタクリル酸メチル系重合体を使つ
て溶融紡糸法によつて芯材を形成させた後、メタ
クリル酸メチル系重合体よりも屈折率の低い重合
体をさや材物質として被覆することによつて、あ
るいは複合紡糸ノズルを用いて芯材物質とさや材
物質を複合溶融紡糸することによつて光伝送繊維
が製造される。
After forming a core material using such a methyl methacrylate polymer by a melt spinning method, it is coated with a polymer having a lower refractive index than the methyl methacrylate polymer as a sheath material material. Alternatively, the optical transmission fiber is produced by composite melt spinning of the core material and the sheath material using a composite spinning nozzle.

本発明で用いられるさや材物質としては、フツ
素を少なくとも30重量%含むフツ素含有重合体を
用いるべきである。フツ素含有重合体としては、
フツ化ビニリデンとテトラフルオロエチレンとの
共重合体や、次式で示されるメタクリル酸のフツ
素化エステルの単独重合体あるいはこれらとメタ
クリル酸メチル、アクリル酸ブチル等との共重合
体等が例示される。
The sheath material used in the present invention should be a fluorine-containing polymer containing at least 30% by weight of fluorine. As a fluorine-containing polymer,
Examples include copolymers of vinylidene fluoride and tetrafluoroethylene, homopolymers of fluorinated esters of methacrylic acid represented by the following formula, and copolymers of these with methyl methacrylate, butyl acrylate, etc. Ru.

(式中、n=1〜2、m=1〜10、X=Hまたは
Fである) 芯材物質に用いられるメタクリル酸メチル系重
合体は、多くの場合、塊状重合によつて得られる
が、そのままでは通常数重量%以上の残存モノマ
ーが含まれている。残存モノマー量を出来るだけ
少なくするように、例えば静置塊状重合されたも
のでも通常は0.5〜2重量%の残存モノマーが含
まれる。このような例えば0.5重量%の残存モノ
マーを含むメタクリル酸メチル系重合体を通常の
方法で溶融紡糸すると、繊維中に多数の気泡が発
生し、光伝送性能を著しく低下させる。
(In the formula, n = 1 to 2, m = 1 to 10, and X = H or F) The methyl methacrylate polymer used for the core material is often obtained by bulk polymerization. As it is, it usually contains several weight percent or more of residual monomer. In order to reduce the amount of residual monomer as much as possible, the residual monomer is usually contained in an amount of 0.5 to 2% by weight, even if the polymer is subjected to stationary bulk polymerization. When such a methyl methacrylate-based polymer containing, for example, 0.5% by weight of residual monomer is melt-spun using a conventional method, a large number of bubbles are generated in the fiber, which significantly reduces optical transmission performance.

一般には、繊維形成時に、このような気泡を発
生させないようにするために、予めベント式押出
機や薄膜蒸発機等の脱モノマー装置で残存モノマ
ーを除去する方法が広く行なわれている。このよ
うな方法で残存モノマー量を0.1重量%以下にす
る事が可能である。しかし、ベント式押出機や薄
膜蒸発機等で残存モノマー量を0.1重量%以下に
しようとすると、装置自身から金属粉やシール材
粉等の異物が混入することが避けられないし、過
度の熱履歴を受けて樹脂が劣化することも避けら
れない。
Generally, in order to prevent the generation of such bubbles during fiber formation, a method is widely used in which residual monomer is removed in advance using a demonomer device such as a vented extruder or a thin film evaporator. By such a method, it is possible to reduce the amount of residual monomer to 0.1% by weight or less. However, if you try to reduce the amount of residual monomer to 0.1% by weight or less using a vented extruder or thin film evaporator, it is inevitable that foreign substances such as metal powder and sealing material powder will get mixed in from the equipment itself, and excessive thermal history will occur. It is also unavoidable that the resin will deteriorate due to exposure to heat.

このような脱モノマー方法で残存モノマーを
0.1重量%以下、更には0.05重量%以下にするこ
とは可能であり、その場合には繊維形成中に気泡
の発生はほとんど見られない。しかし一方、脱モ
ノマー工程において、金属粉やシール材粉等の異
物混入や樹脂の劣化を避けられないので繊維の光
伝送性能は著しく低下する。
This demonomerization method removes residual monomers.
It is possible to reduce the content to 0.1% by weight or less, or even 0.05% by weight or less, in which case generation of air bubbles is hardly observed during fiber formation. On the other hand, however, in the demonomerization step, the optical transmission performance of the fibers is significantly reduced because the contamination of foreign substances such as metal powder and sealing material powder and the deterioration of the resin are unavoidable.

本発明者らは、光伝送性能を低下させるような
脱モノマー工程を実施せずに、しかも繊維形成時
に気泡を発生させない方法を鋭意検討した結果、
紡糸ノズルの直下の連続する区域中に溶融押出さ
れた繊維を通過させて冷却する工程において、加
圧下に冷却すれば気泡が全く発生せず、光伝送性
能の極めて優れた光伝送繊維を製造出来ることを
見出した。
As a result of intensive study by the present inventors on a method that does not involve the demonomer process that would degrade optical transmission performance and also does not generate bubbles during fiber formation,
In the process of cooling the molten extruded fiber by passing it through a continuous area directly below the spinning nozzle, if the fiber is cooled under pressure, no air bubbles will be generated, making it possible to produce an optical transmission fiber with extremely excellent optical transmission performance. I discovered that.

なお、本発明で用いられるメタクリル酸メチル
系重合体は残存モノマーが3重量%以下であるこ
とが好ましく、塊状重合後、フラツシング等によ
り残存モノマー量を3重量%以下にする方法や静
置重合で残存モノマー量を3重量%以下にする方
法などが採用される。
In addition, the methyl methacrylate-based polymer used in the present invention preferably has a residual monomer content of 3% by weight or less, and may be treated by a method of reducing the residual monomer amount to 3% by weight or less by flushing etc. after bulk polymerization, or by static polymerization. A method of reducing the amount of residual monomer to 3% by weight or less is adopted.

本発明における加圧の程度は紡糸温度、繊維
径、冷風温度、紡糸速度にもよるが、2Kg/cm2
上、好ましくは3Kg/cm2以上が好ましい。上限圧
力としてはメチルメタアクリレートの紡糸温度に
おける蒸気圧よりやや上(2Kg/cm2程度上)まで
が意味があり、それ以上あげても装置等にコスト
がかかるだけであまり意味がない。
The degree of pressurization in the present invention depends on the spinning temperature, fiber diameter, cold air temperature, and spinning speed, but is preferably 2 kg/cm 2 or more, preferably 3 kg/cm 2 or more. As the upper limit pressure, it is meaningful to set it slightly above the vapor pressure at the spinning temperature of methyl methacrylate (approximately 2 kg/cm 2 above), and raising it higher than that only increases the cost of the equipment and is not very meaningful.

本発明は、種々の形態で具体化され得るが、そ
の代表例を図面を参考に説明する。しかし、これ
らは発明の原理を例示するものであつて、本発明
はこれらの例に限定されるものでない。
Although the present invention can be embodied in various forms, representative examples thereof will be explained with reference to the drawings. However, these are illustrative of the principles of the invention, and the invention is not limited to these examples.

第1図において、1は複合溶融紡糸ノズル、2
は溶融押出された繊維であり、巻き取り機3で巻
き取られる。4は加圧冷却ボツクスであり、5は
冷風入口、6は加圧調節バルブである。更に他の
例を第2図に示す。1は溶融紡糸ノズル、2は溶
融押出された芯材物質からなる繊維である。7は
芯材にさや材物質を被覆するために使われるさや
材物質が入つた浴である。芯材にさや材が被覆さ
れた繊維は巻取り機3によつて巻き取られる。4
は加圧冷却ボツクス、5は冷風入口、6は加圧調
節バルブ、8は冷風出口である。
In FIG. 1, 1 is a composite melt spinning nozzle; 2 is a composite melt spinning nozzle;
is a melt-extruded fiber, which is wound up by a winding machine 3. 4 is a pressurized cooling box, 5 is a cold air inlet, and 6 is a pressurization adjustment valve. Still another example is shown in FIG. 1 is a melt-spinning nozzle, and 2 is a fiber made of a melt-extruded core material. 7 is a bath containing a sheath material used to coat the core material with the sheath material. The fiber whose core material is coated with the sheath material is wound up by a winding machine 3. 4
5 is a pressurized cooling box, 5 is a cold air inlet, 6 is a pressure adjustment valve, and 8 is a cold air outlet.

以上のようにして得られる光伝送繊維は、光伝
送性が著しく優れており、短距離伝送システムへ
の適用範囲を飛躍的に拡大することが可能であ
る。
The optical transmission fiber obtained as described above has extremely excellent optical transmission properties, and can dramatically expand the range of application to short-distance transmission systems.

以下実施例により本発明を説明する。 The present invention will be explained below with reference to Examples.

なお光伝送性能は、ハロゲンランプを光源に使
用して長さL当りの光伝送繊維の入射光強度I0
出射光強度Iから次式により計算される伝送損失
により評価した。
The optical transmission performance is determined by the incident light intensity I 0 of the optical transmission fiber per length L using a halogen lamp as the light source,
Evaluation was made by transmission loss calculated from the output light intensity I using the following formula.

伝送損失(dB/Km)=−10log(I/I0)/L 実施例 1 塵埃、遷移金属、着色物質等の不純物を極力含
まないように注意深く静置塊状重合されたメタク
リル酸メチル重合体と、フツ化ビニリデン・テト
ラフルオロエチレン共重合体(モル比7:3)を
それぞれ芯材、さや材として複合溶融紡糸する際
に、第1図の装置を用いて光伝送繊維を製造し
た。メタクリル酸メチル重合体の残存モノマーは
0.8重量%、紡糸ノズル温度は220℃、加圧は10
Kg/cm2であつた。
Transmission loss (dB/Km) = -10log (I/I 0 )/L Example 1 Methyl methacrylate polymer that was carefully subjected to static bulk polymerization to avoid containing impurities such as dust, transition metals, and colored substances as much as possible. An optical transmission fiber was produced using the apparatus shown in FIG. 1 when composite melt spinning was performed using vinylidene fluoride/tetrafluoroethylene copolymer (molar ratio 7:3) as a core material and a sheath material, respectively. The remaining monomer of methyl methacrylate polymer is
0.8% by weight, spinning nozzle temperature 220℃, pressure 10
It was Kg/ cm2 .

この繊維には気泡が全く観察されず、伝送損失
は570mμの波長で70dB/Kmであつた。
No bubbles were observed in this fiber, and the transmission loss was 70 dB/Km at a wavelength of 570 mμ.

比較のため、冷却時に加圧しなかつた場合(大
気圧)には、繊維には気泡が観察され、伝送損失
は1000dB/Km以上であつた。
For comparison, when no pressure was applied during cooling (atmospheric pressure), bubbles were observed in the fibers, and the transmission loss was over 1000 dB/Km.

実施例 2 芯材物質として実施例1と同じものを用いて、
まず芯材を溶融紡糸し、さや材として10重量%の
メタクリル酸メチルと90重量%の次式 で表わされるメタクリル酸のフツ素化エステルの
共重合体を用いて芯材を被覆するに際し、第2図
の装置を用いて光伝送繊維を製造した。紡糸ノズ
ル温度は220℃、さや材浴温度は120℃、加圧は10
Kg/cm2であつた。
Example 2 Using the same core material as in Example 1,
First, the core material is melt-spun, and as the sheath material, 10% by weight of methyl methacrylate and 90% by weight of the following formula: When coating a core material with a copolymer of a fluorinated ester of methacrylic acid represented by the following formula, an optical transmission fiber was manufactured using the apparatus shown in FIG. The spinning nozzle temperature is 220℃, the pod material bath temperature is 120℃, and the pressure is 10℃.
It was Kg/ cm2 .

この繊維には気泡が全く観察されず、伝送損失
は570mμの波長で65dB/Kmであつた。
No bubbles were observed in this fiber, and the transmission loss was 65 dB/Km at a wavelength of 570 mμ.

比較のため冷却時に加圧しなかつた場合(大気
圧)には、繊維には気泡が観察され、伝送損失は
1000dB/Km以上であつた。
For comparison, when no pressure was applied during cooling (atmospheric pressure), air bubbles were observed in the fibers, and the transmission loss was
It was over 1000dB/Km.

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

第1図、第2図は、ともに本発明を実施するた
めの装置の例の説明図である。 1……紡糸ノズル、2……繊維、2′……繊維
(芯材)、3……巻き取り機、4……加圧冷却ボツ
クス、5……冷風入口、6……加圧調節バルブ、
7……さや材浴、8……冷風出口。
FIG. 1 and FIG. 2 are both explanatory diagrams of an example of an apparatus for carrying out the present invention. 1... Spinning nozzle, 2... Fiber, 2'... Fiber (core material), 3... Winder, 4... Pressure cooling box, 5... Cold air inlet, 6... Pressure adjustment valve,
7...Sheath wood bath, 8...Cold air outlet.

Claims (1)

【特許請求の範囲】[Claims] 1 芯成分物質としてメタクリル酸メチル系重合
体、さや成分物質として、フツ素を少なくとも30
重量%含むフツ素含有重合体からなる芯−さや構
造を有する光伝送繊維を製造するに際し、紡糸ノ
ズルの直下の連続する区域中に溶融押出された繊
維を通過させて冷却する工程において、加圧下に
冷却することを特徴とする光伝送繊維の製造法。
1 Methyl methacrylate-based polymer as the core component material, and at least 30% of fluorine as the sheath component material.
When producing a light transmitting fiber having a core-sheath structure made of a fluorine-containing polymer containing % by weight, the melt-extruded fiber is cooled by passing it through a continuous area directly below the spinning nozzle, under pressure. A method for producing an optical transmission fiber characterized by cooling it to
JP57186369A 1982-10-23 1982-10-23 Manufacture of light transmission fiber Granted JPS5975202A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57186369A JPS5975202A (en) 1982-10-23 1982-10-23 Manufacture of light transmission fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57186369A JPS5975202A (en) 1982-10-23 1982-10-23 Manufacture of light transmission fiber

Publications (2)

Publication Number Publication Date
JPS5975202A JPS5975202A (en) 1984-04-27
JPH0225483B2 true JPH0225483B2 (en) 1990-06-04

Family

ID=16187169

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57186369A Granted JPS5975202A (en) 1982-10-23 1982-10-23 Manufacture of light transmission fiber

Country Status (1)

Country Link
JP (1) JPS5975202A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0646244B2 (en) * 1985-05-17 1994-06-15 三菱レイヨン株式会社 Plastic optical fiber
CN101856570B (en) * 2010-06-03 2012-01-25 西安康本材料有限公司 Dynamic demonomerization and defoaming method and device for carbon fiber spinning solution

Also Published As

Publication number Publication date
JPS5975202A (en) 1984-04-27

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