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JPS5817924B2 - Manufacturing method of synthetic resin body for optical transmission - Google Patents
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JPS5817924B2 - Manufacturing method of synthetic resin body for optical transmission - Google Patents

Manufacturing method of synthetic resin body for optical transmission

Info

Publication number
JPS5817924B2
JPS5817924B2 JP52016404A JP1640477A JPS5817924B2 JP S5817924 B2 JPS5817924 B2 JP S5817924B2 JP 52016404 A JP52016404 A JP 52016404A JP 1640477 A JP1640477 A JP 1640477A JP S5817924 B2 JPS5817924 B2 JP S5817924B2
Authority
JP
Japan
Prior art keywords
synthetic resin
resin body
refractive index
plasticizer
optical transmission
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
Application number
JP52016404A
Other languages
Japanese (ja)
Other versions
JPS53101441A (en
Inventor
円満字公衛
高橋健造
草川英昭
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.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric Corp
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 Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP52016404A priority Critical patent/JPS5817924B2/en
Publication of JPS53101441A publication Critical patent/JPS53101441A/en
Publication of JPS5817924B2 publication Critical patent/JPS5817924B2/en
Expired legal-status Critical Current

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  • Polymerisation Methods In General (AREA)
  • Optical Fibers, Optical Fiber Cores, And Optical Fiber Bundles (AREA)

Description

【発明の詳細な説明】 この発明は光共重合反応を利用した光伝送用合成樹脂体
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 a synthetic resin body for optical transmission using a photocopolymerization reaction.

従来、ガラスまたはプラスチックより成る光伝送体が知
られており、例えば医療機器、ディスプレイ装置、光表
示装置などの分野で利用されている。
2. Description of the Related Art Optical transmission bodies made of glass or plastic have been known in the past, and are used, for example, in fields such as medical equipment, display devices, and optical display devices.

将来は情報伝達機器分野でその利用価値が極めて高くな
るものと期待されている。
It is expected that its utility value will become extremely high in the field of information communication equipment in the future.

これらの光伝送体のなかでも像を伝送し得るものは、そ
の周辺部より中心部に向って連続的に増大する屈折率分
布を有する構造を成すものであり、その製造方法は極め
て難しく、特に合成樹脂を用いた光伝送体を一定品質で
歩留り良く工業的に製造する方法は未だ確立されていな
い。
Among these optical transmitters, those capable of transmitting images have a structure with a refractive index distribution that increases continuously from the periphery toward the center, and the manufacturing method thereof is extremely difficult. A method for industrially manufacturing optical transmitters using synthetic resins with constant quality and high yield has not yet been established.

これまでに開発された光伝送用合成樹脂体の製造法とし
ては1例えはイオン架橋した合成樹脂体の周辺より中心
部に向って、異なる金属イオンを拡散置換することによ
り、屈折率を連続的に変化させる方法、屈折率の異なる
2種類以上の透明な重合体混合物より成形された合成樹
脂体を特定組成の溶剤で処理し、合成樹脂体を構成する
組成の内、特定成分の濃度がその中心部より周辺に向っ
て連゛続的に変化するように選択的に抽出する方法、線
状の合成樹脂体を母体材料として、その表面から屈折率
の異なる単量体を拡散させて重合し、周辺から中心部に
向って連続的に変化する組成分布を与えることにより屈
折率分布を形成する方法、或いは屈折率の異なる2種類
の単量体を混合して予備重合させ、その表面より半重合
量体を選択的に表面から揮発させた後再び重合を完結さ
せて屈折率分布を形成する方法などの製法が知られてい
る。
One method of producing synthetic resin bodies for optical transmission that has been developed so far is to continuously change the refractive index by diffusing and replacing different metal ions from the periphery to the center of an ionically crosslinked synthetic resin body. A synthetic resin body formed from a mixture of two or more transparent polymers with different refractive indexes is treated with a solvent of a specific composition, and the concentration of the specific component in the composition constituting the synthetic resin body is changed to that level. A method of selective extraction in which the refractive index changes continuously from the center to the periphery.A linear synthetic resin body is used as the base material, and monomers with different refractive indexes are diffused from the surface and polymerized. , a method of forming a refractive index distribution by giving a composition distribution that changes continuously from the periphery toward the center, or a method of forming a refractive index distribution by mixing two types of monomers with different refractive indexes and prepolymerizing them, Manufacturing methods are known, such as a method in which a polymer is selectively volatilized from the surface and then the polymerization is completed again to form a refractive index distribution.

しかしこれらの製造方法は−■成形された合成樹脂体を
再び溶剤や単量体の溶液に浸したり、重合の4中で未だ
十分成形されていない合成樹脂体を型から取り出して次
の工程を施したりするため、合成樹脂体が変形を起こし
易いという問題があった。
However, these manufacturing methods involve immersing the molded synthetic resin body in a solvent or monomer solution again, or taking out the synthetic resin body that has not yet been sufficiently molded during polymerization step 4 and carrying out the next process. There was a problem in that the synthetic resin body was easily deformed due to the application.

また製造工程が多段階を要し、屈折率分布を与える工程
が、イオンの交換、重合体の抽出、単量体の拡散、或い
は単量体の揮発を行なうというように非常に制御の難し
い方法を採っているため、安定した品質の光伝送用合成
樹脂体を製造することが難しいという欠点もあった。
Furthermore, the manufacturing process requires multiple steps, and the process of providing the refractive index distribution involves ion exchange, polymer extraction, monomer diffusion, or monomer volatilization, which is a method that is extremely difficult to control. This method also had the disadvantage that it was difficult to produce a synthetic resin body for optical transmission with stable quality.

これらの欠点を除く新しい製造法として共重合反応にお
ける七ツマ−の反応性比の違いを利用して重合と同時に
屈折率分布を形成させる製造法が報告されている。
As a new production method that eliminates these drawbacks, a production method has been reported in which a refractive index distribution is formed simultaneously with polymerization by utilizing the difference in the reactivity ratio of heptamers in a copolymerization reaction.

〔大塊、千野、中本、電気通信学会予稿(1975年秋
)〕この方法は透明な管状ガラス容器に屈折率と共重合
反応におけるモノマーの反応性比の異なる2種類以上の
単量体及び光重合開始触媒を混合した溶液を満たし、管
壁より光照射することにより管壁部分から重合を開始さ
せ、管状合成樹脂体の周辺部から中心に向かって連続的
に変化する組成分布を形成し、それによって屈折率分布
を有する光伝送用合成樹脂体を製造するものである。
[Ohuma, Chino, Nakamoto, Proceedings of the Institute of Electrical Communication Engineers (Autumn 1975)] This method involves placing two or more types of monomers with different refractive indexes and monomer reactivity ratios in a copolymerization reaction in a transparent tubular glass container, and light. It is filled with a solution containing a polymerization initiation catalyst and irradiated with light from the tube wall to initiate polymerization from the tube wall, forming a composition distribution that continuously changes from the periphery to the center of the tubular synthetic resin body. Thereby, a synthetic resin body for light transmission having a refractive index distribution is manufactured.

この方法をさらに詳述すれば、前記共重合用の単量体の
組み合せとして屈折率の大きい単量体M1と屈折率の小
さい単量体M2を用いた場合、単量体M1及びM2の共
重合反応におけるモノマー反応性比としてはrl〈1及
びr2〉■であることが要求される。
To explain this method in more detail, when a monomer M1 with a large refractive index and a monomer M2 with a small refractive index are used as a combination of monomers for copolymerization, the monomers M1 and M2 are copolymerized. The monomer reactivity ratio in the polymerization reaction is required to be rl<1 and r2>■.

例えはモノマー反応性比がそれぞれr 1 ””0.4
r2=2.0の単量体を組み合わせた場合における単
量体混合液中のM2の組成;f2=M2/(Ml 十M
2)と重合された合成樹脂体中のM2の組成; F2=
dM、/(dM1+dMρ(但し、dMは重合した単量
体量を表わす。
For example, the monomer reactivity ratio is r 1 ""0.4.
Composition of M2 in the monomer mixture when combining monomers with r2=2.0; f2=M2/(Ml 10M
2) Composition of M2 in the synthetic resin body polymerized with F2=
dM, /(dM1+dMρ (however, dM represents the amount of polymerized monomer).

)の関係を第1図に示す。単量体M1とM2ど等量仕込
んだ場合には重合された合成樹脂体中の単量体M1は3
2モル係、M2は68モル係金談れる。
) is shown in Figure 1. When equal amounts of monomers M1 and M2 are charged, the amount of monomer M1 in the polymerized synthetic resin is 3.
2 mole charge, M2 can talk about 68 mole charge.

その結果、単量体混合液中のM2の組成(f2)は重合
が進むに連れて減少し、従って重合時間の経過と共に重
合された合成樹脂体の組成F2も減少する。
As a result, the composition (f2) of M2 in the monomer mixture decreases as the polymerization progresses, and therefore the composition F2 of the polymerized synthetic resin body also decreases as the polymerization time progresses.

次にMlの重合物の屈折率を1.5、M2の重合物の屈
折率を1,4とした時の透明な管状ガラス容器内で光共
重合された合成樹脂体の屈折率分布を第2図に示す。
Next, let us consider the refractive index distribution of the synthetic resin body photocopolymerized in a transparent tubular glass container, assuming that the refractive index of the Ml polymer is 1.5 and the refractive index of the M2 polymer is 1.4. Shown in Figure 2.

図中1,2,3及び4は単量体の仕込み組成;f2がそ
れぞれ0.8 、0.5 、0.3及び0.1の場合を
示す。
In the figure, 1, 2, 3 and 4 indicate the monomer charging composition; f2 is 0.8, 0.5, 0.3 and 0.1, respectively.

この第2図から理解されるように管状合成樹脂体の周辺
部は初期に重合するためM2の重合物の比率が高く屈折
率は低いが、後期に重合する中心部程M1の重合部の比
率が高く屈折率も高くなる。
As can be understood from Fig. 2, the peripheral part of the tubular synthetic resin body polymerizes in the early stage and has a high ratio of M2 polymer and a low refractive index, but the central part, which polymerizes in the later stage, has a higher proportion of M1 polymer. is high and the refractive index is also high.

そしてこの屈折率の分布は単量体の仕込み組成によって
変わることがわかる。
It can be seen that this refractive index distribution changes depending on the monomer composition.

また屈折率分布は光重合開始触媒の種類、その濃度にも
依存し、濃度が高い稈屑折率分布は大きくなり、光伝送
用合成樹脂体としての性能が向上する。
The refractive index distribution also depends on the type of photopolymerization initiation catalyst and its concentration, and the higher the concentration, the larger the refractive index distribution of culm waste, and the better the performance as a synthetic resin body for light transmission.

光伝送用合成樹脂体の屈折率分布は(1)式で表わされ
る。
The refractive index distribution of the synthetic resin body for light transmission is expressed by equation (1).

ここでN。N here.

は中心軸の屈折率、Aは屈折率分布定数、rは中心軸か
らの距離であり、Nはrの位置における屈折率を表わす
is the refractive index of the central axis, A is the refractive index distribution constant, r is the distance from the central axis, and N represents the refractive index at the position of r.

屈折率分布定数Aを大きくするには単量体の仕込み組成
f2を小さくし、光重合開始剤濃度を高くする必要があ
る。
In order to increase the refractive index distribution constant A, it is necessary to decrease the monomer charge composition f2 and increase the photopolymerization initiator concentration.

このようにして屈折率と共重合反応におけるモノマーの
反応性比の違いを利用し、管状ガラス容器内の単量体混
合液を管壁から光照射し管壁から重合するように光共重
合を行なって得られた光伝送用合成樹脂体は、屈折率分
布定数を大きくするために光重合開始触媒濃度を高くす
る結果重合体の分子量が小さくなり、非常に脆いという
欠点を併せ持っている。
In this way, by utilizing the difference in refractive index and the reactivity ratio of monomers in the copolymerization reaction, the monomer mixture in the tubular glass container is irradiated with light from the tube wall, and photocopolymerization is carried out so that the polymerization starts from the tube wall. The synthetic resin body for light transmission obtained by this method has the drawback that the molecular weight of the polymer is small as a result of increasing the concentration of the photopolymerization initiation catalyst in order to increase the refractive index distribution constant, and it is extremely brittle.

そしてこの脆いという欠点のために、欠損のない完全な
製品を作ることが難しくこのままでは工業的製法として
満足に使用できるようなものではない。
Due to this disadvantage of brittleness, it is difficult to produce a complete product without defects, and as is, it cannot be satisfactorily used as an industrial manufacturing method.

本発明者らはこれら従来の欠点を除くと共に、更に優れ
た光伝送用合成樹脂体を得ることを目的として鋭意研究
を重ねた結果、屈折率と共重合反応における七ツマー反
応性比の異なる少なくとも2種類の単量体に光重合開始
触媒と共に光重合開始能を有する可塑剤を添加した混合
物を透光性の管に充填し、前記混合物に光を照射して管
壁から光共重合を行なうこと(こより機械的強度に優れ
、しかも屈折率分布定数の大きい光伝送用合成樹脂体を
得ることができることを見い出し、本発明を完成するに
至った。
The present inventors have conducted extensive research with the aim of eliminating these conventional drawbacks and obtaining even better synthetic resin bodies for optical transmission. As a result, we have found that at least A mixture of two types of monomers with a photopolymerization initiation catalyst and a plasticizer capable of initiating photopolymerization is filled into a light-transmitting tube, and the mixture is irradiated with light to perform photocopolymerization from the tube wall. The present inventors have discovered that it is possible to obtain a synthetic resin body for light transmission that has excellent mechanical strength and a large refractive index distribution constant, and has completed the present invention.

光重合開始能を有する可塑剤とは、単量体に均一に溶解
し、かつ光照射によって単量体を重合させる能力と単量
体が重合した結果得られる重合物のガラス転移温度を低
下させる能力を合せもつ物質をいう。
A plasticizer that has the ability to initiate photopolymerization is a plasticizer that is uniformly dissolved in monomers, has the ability to polymerize the monomers by light irradiation, and lowers the glass transition temperature of the polymer obtained as a result of polymerization of the monomers. A substance that has abilities.

光共重合によって製造された光伝送用合成樹脂体の欠点
である脆さを改善する方法として可塑剤の使用が考えら
れるが、本発明者らの実験では可塑剤として市販のフタ
ル酸エステル類を用いた場合には機械的強度の改善は認
められたが、一方で屈折率分布定数の著しい低下を伴な
うという事実が判明した。
The use of plasticizers can be considered as a way to improve the brittleness that is a drawback of synthetic resin bodies for optical transmission manufactured by photocopolymerization, but in our experiments, we used commercially available phthalate esters as plasticizers. When used, an improvement in mechanical strength was observed, but it was also found to be accompanied by a significant decrease in the refractive index distribution constant.

この事実を詳細に検討した結果、添加された可塑剤か光
重合開始触媒の触媒作用を阻害するために屈折率分布定
数の低下が起こっていることが明らかとなった。
As a result of a detailed study of this fact, it became clear that the refractive index distribution constant decreased because the added plasticizer inhibited the catalytic action of the photopolymerization initiation catalyst.

そこで光重合開始触媒の触媒作用を阻害しない可塑剤或
いはさらに進んで光重合開始能を有する可塑剤の使用に
より屈折率分布定数の低下を防げることができるものと
考え、このような可塑剤の探索を行なった結果、フィト
ールを側鎖に持つトコフェロールもしくはその誘導体の
カルボニル基をエステル化したものまたはフィトールを
側鎖に持つキノンもしくはその誘導体の水酸基をエステ
ル化したものが有効であることを見い出したものである
Therefore, we believe that the decrease in the refractive index distribution constant can be prevented by using a plasticizer that does not inhibit the catalytic action of the photopolymerization initiation catalyst, or a plasticizer that has the ability to further initiate photopolymerization, and we are searching for such a plasticizer. As a result, it was found that esterification of the carbonyl group of tocopherol or its derivatives having phytol in the side chain, or esterification of the hydroxyl group of quinone or its derivatives having phytol in the side chain, is effective. It is.

耶ち、この発明は透光性の管に屈折率と共重合反応にお
ける七ツマー反応性比の異なる2種類以上の単量体に光
重合開始触媒及び光重合開始能を有する可塑剤を添加し
た混合物を充填し、管壁から光共重合を行なわせるとき
により、機械的強度に優れ、しかも屈折率分布定数の大
きい光伝送用合成樹脂体を簡単に得ることを特徴とする
ものである。
Therefore, in this invention, a photopolymerization initiation catalyst and a plasticizer having photopolymerization initiation ability are added to two or more types of monomers having different refractive indexes and 7-mer reactivity ratios in a copolymerization reaction in a light-transmitting tube. The present invention is characterized in that a synthetic resin body for light transmission having excellent mechanical strength and a large refractive index distribution constant can be easily obtained by filling the mixture and performing photocopolymerization from the tube wall.

上記単量体としては、例えはメタクリル酸メチルエステ
ル、スチレン、ビニルナフタレン、ビニル安息香酸、ケ
イ皮酸メチル、ケイ皮酸エチル、4−ビニルピリジン、
ケイ皮酸ニトリル、アクロレイン等が挙げられ、これら
の内から選ばれた少なくとも2種類の単量体の組み合わ
せが用いられる。
Examples of the above monomers include methyl methacrylate, styrene, vinylnaphthalene, vinylbenzoic acid, methyl cinnamate, ethyl cinnamate, 4-vinylpyridine,
Examples include cinnamate nitrile and acrolein, and a combination of at least two types of monomers selected from these is used.

上記光重合開始触媒としては、例えはベンゾフェノン、
ベンゾイン、ベンゾインメチルエーテル等が挙げられ、
これらの少なくとも1種類が用いられる。
Examples of the photopolymerization initiation catalyst include benzophenone,
Examples include benzoin, benzoin methyl ether, etc.
At least one of these is used.

また、前記乎重合開始触媒の添加量は1〜20重量係、
とりわけ5〜10重量係が好ましし)。
In addition, the amount of the polymerization initiation catalyst added is 1 to 20% by weight,
Particularly preferred is a weight ratio of 5 to 10).

上記光重合開始能を有する可塑剤としては、例エバα−
トコフェロール酢酸、コハク酸d−α−トコフェロール
、トコフエラミン、α−トコフェロチオール、α−トコ
フェロチオ酢酸、α−トコフエロジスルフイドニ量体、
α−トコフェロセレノ酢酸、ジーα−トコフエロジセレ
ン化合物、α−トコフェニルキノンジアセテート、β−
トコフェニルキノンシアセード、γ−トコフェニルキノ
ンジアセテート、プラストキノンCジアセテート、プラ
ストキノンCジアセテート、プラストキノンCジアセテ
ート プラストキノンDジアセテートユビキノン−n−
ジアセテート、ロドキノンーn−ジアセテート ジメト
キシユビキノン−n−ジアセテート ジメチルユビキノ
ン−n−ジアセテート ジヒドロユビキノン−10−ジ
アセテートエポキシユビキノン−n−ジアセテート、ニ
ブクロメノ−ルーn−ジアセテート、フィロキノン(ビ
タミンに2 )シアセード(即ち、2−メチル−3−フ
ィチル−1,4−ナフトキノンジアセテート)、メナキ
ノンジアセテート(ビタミンに2)(部ち、3−メチル
−2−フィチル−1,4−ナフトキノンジアセテート)
等が挙げられ、これらの内の少なくとも1種類が用いら
れる。
Examples of the plasticizer having photopolymerization initiating ability include EVA α-
Tocopherol acetic acid, d-α-tocopherol succinate, tocopheramine, α-tocopherothiol, α-tocopherothioacetic acid, α-tocopherodisulfide dimer,
α-tocopheroselenoacetic acid, di-α-tocopherodyselene compound, α-tocophenylquinone diacetate, β-
Tocophenylquinone ciacade, γ-tocophenylquinone diacetate, plastoquinone C diacetate, plastoquinone C diacetate, plastoquinone C diacetate plastoquinone D diacetate ubiquinone-n-
Diacetate, rhodoquinone-n-diacetate Dimethoxyubiquinone-n-diacetate Dimethylubiquinone-n-diacetate Dihydroubiquinone-10-diacetate Epoxyubiquinone-n-diacetate, Nibuchromeno-n-diacetate, Phylloquinone (vitamin 2 ) Cyanade (i.e. 2-methyl-3-phytyl-1,4-naphthoquinone diacetate), Menaquinone diacetate (vitamin 2) (i.e. 3-methyl-2-phytyl-1,4-naphthoquinone diacetate)
etc., and at least one of these is used.

また、添加量としては5〜20重量東とりわけ10〜1
5重量係が好ましい。
In addition, the amount added is 5 to 20% by weight, especially 10 to 1% by weight.
5 weight ratio is preferable.

@記添加量が5重量%より少ない場合には改良効果が不
充分であり、また200重量%り多い場合には重合物が
もろくなるという問題があるのでいずれの場合も好まし
くない。
If the amount added is less than 5% by weight, the improvement effect will be insufficient, and if it is more than 200% by weight, there will be a problem that the polymer will become brittle, so either case is not preferred.

上記各成分を配合した混合物はガラス管などの透光性の
管に充填され、公知の従来技術により、光を照射して重
合させることによって工程を簡単にし、機械強度が改善
された光伝送用合成樹脂体を容易に得ることができる。
The mixture of the above components is filled into a transparent tube such as a glass tube, and is polymerized by irradiation with light using known conventional techniques, which simplifies the process and improves mechanical strength. A synthetic resin body can be easily obtained.

なお必要に応じて加熱して重合を完結させることは何ら
差支えない。
Note that there is no problem in completing the polymerization by heating as necessary.

このようにして得られた合成樹脂体は光による情報伝達
媒体、例えば光半導体素子〆光ファイバーとの結合部に
利用するロンチャーなど、として有用なものである。
The synthetic resin body thus obtained is useful as an optical information transmission medium, such as a launcher used as a coupling part between an optical semiconductor element and an optical fiber.

以下参考例および本発明の実施例を挙げ、本発明をさら
に具体的に説明する。
Hereinafter, the present invention will be explained in more detail with reference to Reference Examples and Examples of the present invention.

実施例 1 内径3. Omrrtの一端を閉じた薄いパイレックス
(商品名)製ガラス管に、100重量%ベンゾインメチ
ルエーテルと100重量%α−トコフェロールアセテー
トを含えだケイ皮酸メチルエステル1部に対してメタク
リル酸メチルエステル4部の混合液を満して、ガラス管
の他端を封じた。
Example 1 Inner diameter 3. In a thin Pyrex (trade name) glass tube with one end of Omrrt closed, 1 part methyl cinnamate to 4 parts methyl methacrylate containing 100% by weight benzoin methyl ether and 100% by weight α-tocopherol acetate was added. The other end of the glass tube was sealed.

(なお前記ケイ皮酸メチルエステルの屈折率は1.58
゜メタクリル酸メチルエステルの屈折率は1.49であ
る。
(The refractive index of the cinnamate methyl ester is 1.58.
The refractive index of methacrylic acid methyl ester is 1.49.

又、単量体反応性比はrl =Q、16、r 2 =
6.4である。
Moreover, the monomer reactivity ratio is rl = Q, 16, r 2 =
It is 6.4.

)このものを25°Gの恒温水中でギセノンランプ光を
10時間照射し固化させた。
) This product was solidified by irradiating it with light from a gysenon lamp for 10 hours in constant temperature water at 25°G.

このようにして得られた合成樹脂体は第3図に示す如く
その中心部から周辺部に向って連続的に減少する屈折率
分布を有し、しかも形状の歪みもなく光伝送用合成樹脂
体としてすぐれたものであった。
The synthetic resin body thus obtained has a refractive index distribution that decreases continuously from the center toward the periphery as shown in Figure 3, and has no shape distortion and is a synthetic resin body for light transmission. It was excellent.

実施例2 α−トコフェロールアセテート(α−TA)の配合量を
それぞれ0,3,5.10及び15重量%と変えた他は
実施例1と同様にして得た光伝送用合成樹脂体について
測定された屈折率分布定数と機械強度を表1に示す。
Example 2 Measurements were made on synthetic resin bodies for optical transmission obtained in the same manner as in Example 1, except that the blended amounts of α-tocopherol acetate (α-TA) were changed to 0, 3, 5.10, and 15% by weight, respectively. Table 1 shows the refractive index distribution constant and mechanical strength.

ただし、上記表−1に用いた記号はそれぞれ次の事項を
表わす(以下同様) 上記表1かられかるように、α−トコフェロールアセテ
ート(α−TA)を含まないものでは、3機械強度が小
さく、実際の製品として役に立たないが、α−トコフェ
ロールアセテートを含むものでは、機械強度も優れ、か
つ屈折率分布定数も僅か2割程度の減少となっているに
すぎない。
However, the symbols used in Table 1 above each represent the following items (the same applies hereinafter).As seen from Table 1 above, products that do not contain α-tocopherol acetate (α-TA) have a low Although it is not useful as an actual product, those containing α-tocopherol acetate have excellent mechanical strength and the refractive index distribution constant is reduced by only about 20%.

参考例 14 可塑剤としてα−トコフェロールアセテートの代りに一
般的なジ−n−オクチルフタレート(DnOP)を使用
しその配合量をそれぞれ0,3゜5、及び10重量%と
変λ、実施例2と同様にして得た合成樹脂体について測
定された屈折率分布定数と機械強度を・表2に示す。
Reference Example 14 General di-n-octyl phthalate (DnOP) was used as a plasticizer instead of α-tocopherol acetate, and the blending amount was varied to 0, 3°5, and 10% by weight, respectively. Example 2 Table 2 shows the refractive index distribution constant and mechanical strength measured for the synthetic resin body obtained in the same manner as above.

上記表2かられかるように一般的な可塑剤として用いら
れるジ−n−オクチルフタレート15 (DnOP)を
含むものでは機械的強度は添加量と共に増大するが、そ
れに伴って屈折率分布定数も減少し、10重量%の添加
では約7割も屈折率分布定数が低下するという問題があ
る。
As can be seen from Table 2 above, the mechanical strength of those containing di-n-octyl phthalate 15 (DnOP), which is commonly used as a plasticizer, increases with the amount added, but the refractive index distribution constant also decreases accordingly. However, when 10% by weight is added, there is a problem that the refractive index distribution constant decreases by about 70%.

従って一般の可塑剤においては、屈折率分布定数低下の
そわ2θ程著しくない、3〜5重量%にとどめておかね
ばならないし、機械強度の顕著な改善は望めない。
Therefore, in general plasticizers, the amount must be kept at 3 to 5% by weight, which is not as significant as the 2θ decrease in the refractive index distribution constant, and no significant improvement in mechanical strength can be expected.

参考例 2 実施例1とほぼ同じ条件で、可塑剤を加えず、ベンゾイ
ンメチルエーテル(BME)の配合量を250係〜15
重量帽こ変えて得た合成樹脂体について測定された機械
強度と屈折率分布定数を表3に示す。
Reference Example 2 Under almost the same conditions as Example 1, without adding a plasticizer, the amount of benzoin methyl ether (BME) was 250 to 15
Table 3 shows the mechanical strength and refractive index distribution constant measured for the synthetic resin body obtained by changing the weight cap.

上記表3に示すように、ベンゾインメチルエーテル(B
ME)の配合量が少い場合、とりわけ5重量製以下の場
合はレンズ作用がほとんどない。
As shown in Table 3 above, benzoin methyl ether (B
When the blending amount of ME) is small, especially when the weight is less than 5, there is almost no lens effect.

しかし前記配合量が10重量帽こなると急に屈折率分布
定数が増す。
However, when the amount added exceeds 10% by weight, the refractive index distribution constant suddenly increases.

そのため、大きい屈折率分布定数と大きな機械強度を得
ようとする場合には本発明による他に方法はない。
Therefore, if a large refractive index distribution constant and a large mechanical strength are to be obtained, there is no other method than the present invention.

実施例 3 メタクリル酸メチルエステル(MMA)とケイ皮酸メチ
ルエステル(MCI)の配合割合を変えた他は実施例1
さ同様にして得た合成樹脂体について測定された屈折率
分布定数と機械強度を表4に示す。
Example 3 Example 1 except that the blending ratio of methacrylic acid methyl ester (MMA) and cinnamic acid methyl ester (MCI) was changed.
Table 4 shows the refractive index distribution constant and mechanical strength measured for the synthetic resin body obtained in the same manner.

なお比較のために、α−トコフェロールアセテート(α
−TA)を添加しない場合も同様に示した。
For comparison, α-tocopherol acetate (α
-TA) is also shown in the same manner.

上記表4かられかるようにα−トコフェロールアセテー
ト(α−TA)を用いた場合ケイ皮酸メチルエステル(
MCI)の割合が増えるに従って、屈折率分布定数の値
は増大するが、機械強度はやや減少する。
As shown in Table 4 above, when α-tocopherol acetate (α-TA) is used, cinnamate methyl ester (
As the ratio of MCI) increases, the value of the refractive index distribution constant increases, but the mechanical strength slightly decreases.

一方α−トコフェロールアセテート(α−TA)無添加
の場合には全ての割合に渡つンて、はとんど使いものに
ならない。
On the other hand, in the case where α-tocopherol acetate (α-TA) is not added, it is almost useless at all ratios.

実施例 4 モノマーの組み合せを変えた他は実施例1と同様の条件
で得られた合成樹脂体について測定された屈折率分布定
数を表5に示す。
Example 4 Table 5 shows the refractive index distribution constants measured for a synthetic resin body obtained under the same conditions as Example 1 except that the combination of monomers was changed.

実施例 5 一端を閉じた、内径3.5朋の薄いパイレックス(商品
名)製ガラス管に、8重量係のベンゾフェノンと5重量
係のビタミンに1ジアセテートを含んだ安息酸ビニル一
部に対して、MMA3部の混合液を満して、ガラス管の
他端を閉じた。
Example 5 A portion of vinyl benzoate containing 8 weight parts of benzophenone, 5 weight parts of vitamins, and 1 diacetate was placed in a thin glass tube made of Pyrex (trade name) with an inner diameter of 3.5 mm and closed at one end. Then, a mixed solution of 3 parts of MMA was filled, and the other end of the glass tube was closed.

(なお、前記安息香酸ビニルあ屈折率は1.57、MM
Aの屈折率は1.49である。
(The refractive index of vinyl benzoate is 1.57, MM
The refractive index of A is 1.49.

また、単量体反応性比はr 1=0.048、r、2=
8.3である。
In addition, the monomer reactivity ratio is r 1 = 0.048, r, 2 =
It is 8.3.

)このものを30°Cの恒温水中でキセノンランプ光を
10時間照射し固化させた。
) This material was irradiated with xenon lamp light for 10 hours in constant temperature water at 30°C to solidify it.

このようにして得られた合成樹脂体はA=1.2 X
10 mm であり、かつ機械強度も充分なもので
あった。
The synthetic resin body thus obtained has A=1.2
10 mm, and had sufficient mechanical strength.

実施例 6 内径2,0mmg;の市販テフロン商品名チューブ中に
MMA8部、ケイ皮酸メチルエステル2部、ベンゾイン
エチルエーテル1部、α−TA1.5部を含む混合液を
満し、500W水銀ランプで2時間光照射した后、80
℃オープン中で24時間後重合して、反応を完結させた
Example 6 A commercially available Teflon (trade name) tube with an inner diameter of 2.0 mm was filled with a mixed solution containing 8 parts of MMA, 2 parts of cinnamate methyl ester, 1 part of benzoin ethyl ether, and 1.5 parts of α-TA, and heated with a 500 W mercury lamp. After 2 hours of light irradiation, 80
The reaction was completed after 24 hours of polymerization in the open air at ℃.

このものの屈折率分布係数は1.8×10−2m7rt
−2であった。
The refractive index distribution coefficient of this material is 1.8×10-2m7rt
-2.

実施例 7 実施例6で得た像伝送用合成樹脂管を80℃の炉中で伸
延して、直径350μmの像伝送用合成樹脂体を得た。
Example 7 The synthetic resin tube for image transmission obtained in Example 6 was stretched in a furnace at 80° C. to obtain a synthetic resin body for image transmission having a diameter of 350 μm.

本方法で得られた像伝送用合成樹脂体は数m程度の距離
では、充分品質のよい像を伝送するものであった。
The synthetic resin body for image transmission obtained by this method was capable of transmitting images of sufficient quality over a distance of several meters.

また、Tgが室温程度にあり、可撓性に優れているので
、他のオプティカル・ファイバー等のように、機械強度
の補強材を必要としないものであった。
In addition, since the Tg is around room temperature and the fiber has excellent flexibility, it does not require reinforcement for mechanical strength like other optical fibers.

以上詳述した如くたの発明によれば、簡単な工程で中心
部から周辺部に向って屈折率が小さくなり、高品質の安
定な光伝送用合成樹脂体を得ることができる。
According to the invention described in detail above, a high-quality and stable synthetic resin body for light transmission can be obtained in which the refractive index decreases from the center toward the periphery through a simple process.

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

第1図は単量体の組成f2と重合された樹脂の組成F2
の関係を示す説明図、第2図は透光性の管内で共重合さ
れた合成樹脂体の中心部から管壁周辺部までの屈折率の
変化を示す説明図である。 第3図はこの発明の一実施例によって得られた光伝送用
合成樹脂体の屈折率分布を示す特性図である。 なお第1図中12は屈折率および共重合反応におけるモ
ノマー反応性比の異なる単量体M1及びM2の混合液中
の単量体M2の組成、F2は上記混合液を重合した場合
の合成樹脂体中のM2の組成を示す。 また、第2図中1〜4は上記f2がそれぞれ0.8゜0
.5,0.8及び0.1の場合を示す。
Figure 1 shows the monomer composition f2 and the polymerized resin composition F2.
FIG. 2 is an explanatory diagram showing the change in refractive index from the center of a synthetic resin body copolymerized in a light-transmitting tube to the periphery of the tube wall. FIG. 3 is a characteristic diagram showing the refractive index distribution of a synthetic resin body for optical transmission obtained according to an embodiment of the present invention. In Figure 1, 12 is the composition of monomer M2 in a mixed solution of monomers M1 and M2 having different refractive indexes and monomer reactivity ratios in the copolymerization reaction, and F2 is the synthetic resin when the above mixed solution is polymerized. The composition of M2 in the body is shown. In addition, for 1 to 4 in Fig. 2, the above f2 is 0.8°0, respectively.
.. The cases of 5, 0.8 and 0.1 are shown.

Claims (1)

【特許請求の範囲】 1 屈折率および共重合反応における単量体反応性比の
異なる少くとも2種類の単量体、光重合開始触媒ならび
に光重合開始能を有する可塑剤を含有する混合物を透光
性の管に充填する工程、前記混合物に光を照射して重合
せしめる工程を含む光伝送用合成樹脂体の製造法。 2 単体量の総量に対し上記光重合開始触媒を1〜20
重量係重量係上うにした特許請求の範囲第1項記載の光
伝送用合成樹脂体の製造法。 3 単量体の総量に対し上記可塑剤を5〜20重量係重
量係上うにした特許請求の範囲第1項または第2項記載
の光伝送用合成樹脂体の製造法。 4 可塑剤としてフィトールを側鎖に持つトコフェロー
ル類の水酸基をエステル化したものを用いるようにした
特許請求の範囲第1項ないし第3項のいずれかに記載の
光伝用合成樹脂体の製造法。 5 可塑剤としてフィトールを側鎖に持っキノンのカル
ボニル基を還元して水酸基としその水酸基をさらにエス
テル化したものを用いるようにした特許請求の範囲第1
項ないし第3項のいずれかに記載の光伝送用合成樹脂体
の製造法。
[Claims] 1. A mixture containing at least two types of monomers having different refractive indexes and monomer reactivity ratios in a copolymerization reaction, a photopolymerization initiation catalyst, and a plasticizer capable of photopolymerization initiation. A method for producing a synthetic resin body for light transmission, comprising the steps of filling a light tube with light, and irradiating the mixture with light to polymerize it. 2 The above photopolymerization initiation catalyst is added in an amount of 1 to 20% based on the total amount of single substances.
A method for producing a synthetic resin body for optical transmission according to claim 1, wherein the weight ratio is as follows. 3. The method for producing a synthetic resin body for optical transmission according to claim 1 or 2, wherein the plasticizer is added at a weight ratio of 5 to 20 relative to the total amount of monomers. 4. A method for producing a synthetic resin body for phototransmission according to any one of claims 1 to 3, in which an esterified hydroxyl group of tocopherols having phytol in the side chain is used as a plasticizer. . 5. Claim 1, in which a quinone having phytol in its side chain is reduced to a hydroxyl group by reducing the carbonyl group to form a hydroxyl group and further esterifying the hydroxyl group as a plasticizer.
A method for producing a synthetic resin body for optical transmission according to any one of Items 1 to 3.
JP52016404A 1977-02-16 1977-02-16 Manufacturing method of synthetic resin body for optical transmission Expired JPS5817924B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52016404A JPS5817924B2 (en) 1977-02-16 1977-02-16 Manufacturing method of synthetic resin body for optical transmission

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52016404A JPS5817924B2 (en) 1977-02-16 1977-02-16 Manufacturing method of synthetic resin body for optical transmission

Publications (2)

Publication Number Publication Date
JPS53101441A JPS53101441A (en) 1978-09-04
JPS5817924B2 true JPS5817924B2 (en) 1983-04-11

Family

ID=11915295

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52016404A Expired JPS5817924B2 (en) 1977-02-16 1977-02-16 Manufacturing method of synthetic resin body for optical transmission

Country Status (1)

Country Link
JP (1) JPS5817924B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59127002A (en) * 1983-01-11 1984-07-21 Sumitomo Electric Ind Ltd Production of plastic optical fiber
JPS5974502A (en) * 1982-10-21 1984-04-27 Sumitomo Electric Ind Ltd plastic optical fiber

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5430301B2 (en) * 1975-01-27 1979-09-29

Also Published As

Publication number Publication date
JPS53101441A (en) 1978-09-04

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