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JPH0226201B2 - - Google Patents
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JPH0226201B2 - - Google Patents

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Publication number
JPH0226201B2
JPH0226201B2 JP58018650A JP1865083A JPH0226201B2 JP H0226201 B2 JPH0226201 B2 JP H0226201B2 JP 58018650 A JP58018650 A JP 58018650A JP 1865083 A JP1865083 A JP 1865083A JP H0226201 B2 JPH0226201 B2 JP H0226201B2
Authority
JP
Japan
Prior art keywords
methyl methacrylate
monomer
plastic optical
core component
optical fiber
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
JP58018650A
Other languages
Japanese (ja)
Other versions
JPS59143104A (en
Inventor
Yoshio Iki
Kazunori Yokoyama
Kazumasa Hashimoto
Masataka Ikeno
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 JP58018650A priority Critical patent/JPS59143104A/en
Publication of JPS59143104A publication Critical patent/JPS59143104A/en
Publication of JPH0226201B2 publication Critical patent/JPH0226201B2/ja
Granted legal-status Critical Current

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  • Optical Fibers, Optical Fiber Cores, And Optical Fiber Bundles (AREA)

Description

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

本発明は、芯成分としてメタクリル酸メチル重
合体を用いるプラスチツクオプテイカルフアイバ
ーにおいて、高度に精製されたメタクリル酸メチ
ル単量体を芯成分メタクリル酸メチル重合体の原
料として用いた光伝送効率が向上したプラスチツ
クオプテイカルフアイバーに関する。 プラスチツクオプテイカルフアイバーは、無機
ガラス、特に石英ガラスフアイバーに比較して大
口径にしても可とう性に優れ、軽量で、かつ高開
口数のものが容易に得られるので光源との接続損
失が少なく、また工業的に大量生産が可能なので
極めて安価であるという特徴を有し、その向上の
ための技術的努力が種々試みられてきた。 メタクリル酸メチル重合体を芯成分とするプラ
スチツクオプテイカルフアイバーの光伝送効率低
下要因の一つとして、可視光領域での吸収と紫外
部吸収のすそひきに起因するものである。 我々は光伝送効率低下を起すこれらの吸収が、
芯成分メタクリル酸メチル重合体原料の単量体中
に含まれる微量の不純物が従来の精製法では十分
除去されず残存するため、あるいは不純物それ自
体に可視、紫外領域波長の吸収能がない場合にお
いても重合体を形成する過程において、可視、紫
外領域波長を吸収する化合物、官能基を形成する
ために生ずると考え、単量体の高度な精製法につ
いて種々鋭意検討を重ね、本発明に示されるよう
な高度に精製されたメタクリル酸メチル単量体を
芯成分メタクリル酸メチル重合体の原料として用
いることにより光伝送効率が飛躍的に向上すると
いう驚くべき事実を見出し、本発明に到達したも
のである。 すなわち本発明の要旨とするところは、芯成分
としてメタクリル酸メチル重合体を用いるプラス
チツクオプテイカルフアイバーにおいて、還元性
化合物で前処理をしたメタクリル酸メチル単量体
を芯成分メタクリル酸メチル重合体の原料として
用いることを特徴とするプラスチツクオプテイカ
ルフアイバーである。以下詳細に説明する。 本発明の精製法である還元性化合物でメタクリ
ル酸メチル単量体を前処理する効果の理論は充分
明白ではないが、メタクリル酸メチル単量体中に
残存する微量の酸化物質が重合体形成時に副反応
を起し、可視、紫外波長光を吸収する化合物また
は官能基を形成し、これが光伝送効率の低下を引
き起すものと推定され、還元性化合物で処理する
ことにより酸化性物質が還元されて不活性物質と
なり、その結果光伝送効率を向上させるものと推
定される。 本発明に用いられる還元性化合物は、通常一般
的に知られている任意の還元性化合物を用いるこ
とができる。好ましくは還元性化合物が水の存在
下、水素を発生る化合物を用いるのがよく、特に
好ましくは還元性化合物として水素化化合物を用
いるのがよい。例示すれば、水素化リチウム、水
素化カルシウム、水素化マグネシウム、水素化バ
リウム、水素化ホウ素、等があげられる。使用還
元性化合物の量は、処理される単量体に対して
0.01〜10重量%、更に好ましくは0.1〜5重量%
が望ましい。 前処理法としては、所定量の還元性化合物存在
下でメタクリル酸メチル単量体を処理するか、処
理効率を向上させるため攪拌混合を行なつてもよ
く、あるいは水の存在下、水素を発生する還元性
物質を用いる場合は若干の水を添加して前処理を
なうのが好ましい。このようにして前処理された
メタクリル酸エステル単量体は減圧蒸留により精
製され、メタクリル酸メチル重合体原料として用
いられる。 本発明に用いられる芯成分メタクリル酸メチル
重合体は、他のアクリル酸メチル、アクリル酸エ
チル、メタクリル酸メチル、メタクリル酸ブチル
等の共重合性単量体との共重合体でもよく、その
場合、共重合を行なう単量体も本発明で用いる同
一の精製処理を行なうことが必要である。その場
合、メタクリル酸メチル以外の他の単量体成分
は、重合体中に10重量%以下である事が望まし
い。重合方法としては、いずれの方法にてもよい
が、ゴミ、不純物等の混入をさけるためにも塊状
重合法が好ましい。適当な開始剤、連鎖移動剤を
用い、適当な重合温度条件で重合し、重合体を得
る。 このようにして得られた重合体を用いて、芯成
分より屈折率の低いさや成分樹脂と紡糸を行なう
が、紡糸方法としてはコーテイグ方式、溶融紡糸
方式と任意の方法を選択すればよいが、工業的観
点からは溶融紡糸法が好ましい。 以上のようにして得られたプラスチツクオプテ
イカルフアイバーは光伝送効率が飛躍的に向上し
ており、機械的強度にもすぐれているので、短距
離伝送システムへ適用の範囲を拡大することが可
能である。 以下実施例により本発明を説明する。 光伝送効率はオペレツクス社製、光フアイバー
損失分光測定器を用いて、400〜700nm間を自動
測定し、(dB/Km)にて表示した。 実施例1および比較例1 メタクリル酸メチル重合体1000c.c.と水素化カル
シウム5gを2000c.c.ガラス容器で攪拌しつつ約6
時間処理を行つた。残存水素化カルシウムを過
したのち減圧蒸留を行ない、精製メタクリル酸メ
チル単量体を得た。 精製単量体500gとAIBN0.1g、n―ブチルメ
ルカプタン1gを完全密閉系で仕込み、60℃で6
時間、100℃で1時間重合を行ない、重合を完結
させた。 このようにして得たメタクリル酸メチル重合体
を芯成分とし、フツ素化メタクリル酸エステル共
重合体をさや成分として、複合溶融紡糸を行な
い、フアイバーを得た。 比較例として前処理を行なわず、減圧蒸留のみ
により精製したメタクリル酸メチル単量体を用
い、実施例と同様にして重合、フアイバー化し
た。
The present invention is a plastic optical fiber that uses a methyl methacrylate polymer as a core component, and the light transmission efficiency is improved by using a highly purified methyl methacrylate monomer as a raw material for the core component methyl methacrylate polymer. Regarding plastic optical fibers. Compared to inorganic glass, especially quartz glass fiber, plastic optical fiber has excellent flexibility even when made to a large diameter, is lightweight, and can easily be obtained with a high numerical aperture, so it has low connection loss with the light source. Moreover, it has the characteristic of being extremely inexpensive because it can be industrially mass-produced, and various technical efforts have been made to improve it. One of the factors that reduces the light transmission efficiency of plastic optical fibers whose core component is methyl methacrylate polymer is due to the difference in absorption in the visible light region and absorption in the ultraviolet region. We believe that these absorptions, which cause a decrease in optical transmission efficiency,
Core component methyl methacrylate polymer When trace amounts of impurities contained in the raw material monomers are not sufficiently removed by conventional purification methods and remain, or when the impurities themselves do not have the ability to absorb wavelengths in the visible and ultraviolet regions. We believe that this occurs during the process of forming polymers to form compounds and functional groups that absorb wavelengths in the visible and ultraviolet regions, and we have conducted extensive studies on various advanced purification methods for monomers, and have developed the method described in the present invention. The present invention was achieved by discovering the surprising fact that light transmission efficiency is dramatically improved by using highly purified methyl methacrylate monomers as raw materials for core methyl methacrylate polymers. be. That is, the gist of the present invention is that in plastic optical fibers using methyl methacrylate polymer as the core component, methyl methacrylate monomer pretreated with a reducing compound is used as a raw material for the core component methyl methacrylate polymer. This is a plastic optical fiber characterized by being used as a plastic optical fiber. This will be explained in detail below. Although the theory of the effect of pre-treating methyl methacrylate monomer with a reducing compound, which is the purification method of the present invention, is not fully clear, it is believed that trace amounts of oxidizing substances remaining in methyl methacrylate monomer may be absorbed during polymer formation. It is assumed that a side reaction occurs, forming a compound or functional group that absorbs visible and ultraviolet wavelength light, which causes a decrease in light transmission efficiency, and that oxidizing substances are reduced by treatment with a reducing compound. It is presumed that this material becomes an inert substance, thereby improving optical transmission efficiency. As the reducing compound used in the present invention, any generally known reducing compound can be used. Preferably, the reducing compound is a compound that generates hydrogen in the presence of water, and it is particularly preferable to use a hydrogenated compound as the reducing compound. Examples include lithium hydride, calcium hydride, magnesium hydride, barium hydride, and borohydride. The amount of reducing compound used is relative to the monomers being treated.
0.01-10% by weight, more preferably 0.1-5% by weight
is desirable. As a pretreatment method, methyl methacrylate monomer may be treated in the presence of a predetermined amount of reducing compound, stirring and mixing may be performed to improve treatment efficiency, or hydrogen may be generated in the presence of water. When a reducing substance is used, it is preferable to add a small amount of water for pretreatment. The methacrylic acid ester monomer pretreated in this manner is purified by vacuum distillation and used as a raw material for a methyl methacrylate polymer. The core component methyl methacrylate polymer used in the present invention may be a copolymer with other copolymerizable monomers such as methyl acrylate, ethyl acrylate, methyl methacrylate, butyl methacrylate, and in that case, The monomers to be copolymerized must also undergo the same purification treatment used in the present invention. In that case, it is desirable that the amount of monomer components other than methyl methacrylate in the polymer is 10% by weight or less. Although any polymerization method may be used, bulk polymerization is preferred in order to avoid contamination with dust, impurities, and the like. Polymerization is performed using an appropriate initiator and chain transfer agent under appropriate polymerization temperature conditions to obtain a polymer. Using the polymer obtained in this way, spinning is performed with a sheath component resin having a lower refractive index than the core component, and any method such as coating method or melt spinning method may be selected as the spinning method. From an industrial standpoint, melt spinning is preferred. The plastic optical fiber obtained as described above has dramatically improved optical transmission efficiency and excellent mechanical strength, making it possible to expand the scope of its application to short-distance transmission systems. be. The present invention will be explained below with reference to Examples. The optical transmission efficiency was automatically measured between 400 and 700 nm using an optical fiber loss spectrometer manufactured by Operax Co., Ltd., and was expressed in (dB/Km). Example 1 and Comparative Example 1 1000 c.c. of methyl methacrylate polymer and 5 g of calcium hydride were mixed in a 2000 c.c. glass container while stirring.
I did some time processing. After removing residual calcium hydride, vacuum distillation was performed to obtain purified methyl methacrylate monomer. Charge 500 g of purified monomer, 0.1 g of AIBN, and 1 g of n-butyl mercaptan in a completely closed system, and heat at 60℃ for 6 hours.
Polymerization was carried out at 100° C. for 1 hour to complete the polymerization. Composite melt spinning was performed using the thus obtained methyl methacrylate polymer as the core component and the fluorinated methacrylate copolymer as the sheath component to obtain a fiber. As a comparative example, methyl methacrylate monomer purified only by vacuum distillation without pretreatment was used, and polymerization and fiber formation were carried out in the same manner as in the examples.

【表】 表1に示すごとく、前処理を行なつた実施例の
場合、比較例に比して450nmの短波長側での損失
が大巾に低下し、570,650nmでの損失値も低下
している。 実施例 2 メタクリル酸メチル単量体2000c.c.と水素化リチ
ウム10gを3000c.c.ガラス容器中で内温を5℃に保
持しつつ攪拌し、約5時間処理を行つた。残存水
素化リチウムを化したのち減圧蒸留を行ない、
精製メタクリル酸メチル単量体を得た。 精製単量体1000c.c.とtert―アゾブタン0.5g、n
―ブチルメルカプタン2gを完全密閉系で仕込み
130℃で10時間重合したのち、180℃で5時間重合
して重合を完結させた。 このようにして得たメタクリル酸メチル重合体
を芯成分とし、フツ素化メタクリル酸エステル共
重合体をさや成分として複合溶融紡糸を行ない、
フアイバーを得た。表2に結果を示す。
[Table] As shown in Table 1, in the case of the example in which pretreatment was performed, the loss at the short wavelength side of 450 nm is significantly lower than that of the comparative example, and the loss value at 570 and 650 nm is also lower. are doing. Example 2 2000 c.c. of methyl methacrylate monomer and 10 g of lithium hydride were stirred in a 3000 c.c. glass container while maintaining the internal temperature at 5° C., and treated for about 5 hours. After converting the remaining lithium hydride, vacuum distillation is performed,
Purified methyl methacrylate monomer was obtained. Purified monomer 1000c.c. and tert-azobutane 0.5g, n
-Prepare 2g of butyl mercaptan in a completely closed system
After polymerizing at 130°C for 10 hours, polymerization was completed at 180°C for 5 hours. Performing composite melt spinning using the thus obtained methyl methacrylate polymer as a core component and the fluorinated methacrylate copolymer as a sheath component,
Got fiber. Table 2 shows the results.

【表】 表2に示すごとく、比較例に比して450nmの短
波長側での損失が大巾に低下し、570,650nmで
も損失値が低下している。 実施例 3 メタクリル酸メチル単量体1000c.c.と水素化リチ
ウム5gを1000c.c.ガラス容器中で攪拌しながら約
5時間処理を行つたのち0℃で一昼夜放置した。
残存水素化リチウムを過したのち減圧蒸留を行
ない、精製メタクリル酸メチル単量体を得た。 精製単量体500c.c.とアゾビスイソバレロニトリ
ル0.1g、n―ブチルメルカプタン1gを完全密
閉系で仕込み60℃で3時間、90℃で1時間重合を
行ない、重合を完結させた。 このようにして得たメタクリル酸メチル重合体
を芯成分とし、フツ素化メタクリル酸エステル共
重合体をさや成分として複合溶融紡糸を行ない、
フアイバーを得た。結果を表3に示す。
[Table] As shown in Table 2, the loss on the short wavelength side of 450 nm is significantly reduced compared to the comparative example, and the loss value is also reduced at 570 and 650 nm. Example 3 1000 c.c. of methyl methacrylate monomer and 5 g of lithium hydride were treated in a 1000 c.c. glass container with stirring for about 5 hours, and then left at 0° C. overnight.
After removing residual lithium hydride, vacuum distillation was performed to obtain purified methyl methacrylate monomer. 500 c.c. of purified monomer, 0.1 g of azobisisovaleronitrile, and 1 g of n-butyl mercaptan were charged in a completely closed system, and polymerization was carried out at 60°C for 3 hours and at 90°C for 1 hour to complete the polymerization. Composite melt spinning is performed using the thus obtained methyl methacrylate polymer as a core component and the fluorinated methacrylate copolymer as a sheath component,
Got fiber. The results are shown in Table 3.

【表】 表3に示すごとく、実施例1,2と同様に、比
較例に比して、450nmの短波長側での損失が大巾
に低下し、570,650nmでも損失値が低下してい
る。 実施例 4 メタクリル酸メチル単量体1000c.c.と水素化カル
シウム5gを1000c.c.ガラス容器中で内温を5℃に
保しつつ攪拌を行ない、約1c.c.の水を徐々に滴下
しつつ5時間処理を行つた。残存素化カルシウム
を過したのち減圧蒸留を行ない、精製メタクリ
ル酸メチル単量体を得た。 精製単量体500c.c.とtert―アゾブタン0.5g、n
―ブチルメルカプタン2gを完全密閉系で仕込み
130℃で10時間重合したのち180℃で5時間重合し
て、重合を完結させた。 このようにして得たメタクリル酸メチル重合体
を芯成分とし、フツ素化メタクリル酸エステル共
重合体をさや成分として複合溶融紡糸を行ない、
フアイバーを得た。表4に結果を示す。
[Table] As shown in Table 3, as in Examples 1 and 2, the loss on the short wavelength side of 450 nm was significantly reduced compared to the comparative example, and the loss value also decreased on the short wavelength side of 570 and 650 nm. There is. Example 4 1000 c.c. of methyl methacrylate monomer and 5 g of calcium hydride were stirred in a 1000 c.c. glass container while maintaining the internal temperature at 5°C, and about 1 c.c. of water was gradually added. The treatment was carried out for 5 hours while dripping. After removing residual calcium, distillation was carried out under reduced pressure to obtain purified methyl methacrylate monomer. Purified monomer 500c.c. and tert-azobutane 0.5g, n
-Prepare 2g of butyl mercaptan in a completely closed system
Polymerization was carried out at 130°C for 10 hours and then at 180°C for 5 hours to complete the polymerization. Performing composite melt spinning using the thus obtained methyl methacrylate polymer as a core component and the fluorinated methacrylate copolymer as a sheath component,
Got fiber. Table 4 shows the results.

【表】 表4に示すごとく、少量の水を添加して単量体
の処理を行なうと、比較例はもとより他の実施例
に比較してもさらに損失値の低下したフアイバー
が得られる。
[Table] As shown in Table 4, when the monomer is treated by adding a small amount of water, a fiber with a further reduced loss value is obtained when compared to the comparative example as well as the other examples.

Claims (1)

【特許請求の範囲】 1 芯成分としてメタクリル酸メチル重合体を用
いるプラスチツクオプテイカルフアイバーにおい
て、還元性化合物で前処理をしたメタクリル酸メ
チル単量体を芯成分メタクリル酸メチル重合体の
原料として用いることを特徴とするプラスチツク
オプテイカルフアイバー。 2 還元性化合物が水の存在下に水素を発生する
化合物である特許請求の範囲1項記載のプラスチ
ツクオプテイカルフアイバー。 3 還元性化合物が水素化化合物である特許請求
の範囲1項記載のプラスチツクオプテイカルフア
イバー。
[Scope of Claims] 1. In a plastic optical fiber using a methyl methacrylate polymer as a core component, a methyl methacrylate monomer pretreated with a reducing compound is used as a raw material for the core component methyl methacrylate polymer. A plastic optical fiber featuring: 2. The plastic optical fiber according to claim 1, wherein the reducing compound is a compound that generates hydrogen in the presence of water. 3. The plastic optical fiber according to claim 1, wherein the reducing compound is a hydrogenated compound.
JP58018650A 1983-02-07 1983-02-07 Plastic optical fiber Granted JPS59143104A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58018650A JPS59143104A (en) 1983-02-07 1983-02-07 Plastic optical fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58018650A JPS59143104A (en) 1983-02-07 1983-02-07 Plastic optical fiber

Publications (2)

Publication Number Publication Date
JPS59143104A JPS59143104A (en) 1984-08-16
JPH0226201B2 true JPH0226201B2 (en) 1990-06-08

Family

ID=11977484

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58018650A Granted JPS59143104A (en) 1983-02-07 1983-02-07 Plastic optical fiber

Country Status (1)

Country Link
JP (1) JPS59143104A (en)

Also Published As

Publication number Publication date
JPS59143104A (en) 1984-08-16

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