JPH0241001B2 - - Google Patents
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- Publication number
- JPH0241001B2 JPH0241001B2 JP60011617A JP1161785A JPH0241001B2 JP H0241001 B2 JPH0241001 B2 JP H0241001B2 JP 60011617 A JP60011617 A JP 60011617A JP 1161785 A JP1161785 A JP 1161785A JP H0241001 B2 JPH0241001 B2 JP H0241001B2
- Authority
- JP
- Japan
- Prior art keywords
- tube
- refractive index
- monomer
- light irradiation
- formula
- 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
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- Optical Fibers, Optical Fiber Cores, And Optical Fiber Bundles (AREA)
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
Description
〔産業上の利用分野〕
本発明は屈折率が次第に変化するような屈折率
分布を有する合成樹脂光伝送体を製造する方法に
関する。
〔従来の技術〕
屈折率分布型光伝送体は周知のように光軸と直
交する方向に中心から周辺に向けて屈折率が次第
に変化する分布をもつ透明体から成り、ロツド状
のレンズ、光伝送フアイバ等として広く使用され
ている。
上記の自己集束性光伝送体は、中心軸上の屈折
率をNo、Aを定数として中心軸からXの距離に
おける屈折率Nが
N=No(1−1/2AX2) ……(1)
の式で表わされる分布をもつ。
そして定数Aが正のとき上記伝送体は凸レンズ
作用を有し、Aが負の場合には凹レンズ作用を有
する。
また中心近傍において(1)式のA>0の屈折率分
布を有し、それよりも外周側において次第に外側
に向けて屈折率が増加しているような分布をもつ
屈折率分布型光伝送体も提案されている。
このような屈折率分布型の光伝送体を合成樹脂
で製造する代表的な方法として以下の二つの方法
がある。1つの方法は、三次元網目構造を形成す
るような単量体の一部を重合させて透明なゲル状
体から成る例えば円柱状の母材をつくり、この母
材の表面から、重合体の屈折率が上記単量体とは
異なる他の単量体を拡散させた後重合を完結させ
る方法である。他の方法として、重合体屈折率と
単量体反応性比が互いに異なる複数の単量体の混
合物を透明管に充填し、成形型の外側から光照射
および加熱の少なくとも一方を行なうことにより
成形型内の混合物の外層より徐々に重合反応を進
めて単量体ユニツトの分布すなわち屈折率分布を
形成させる方法がある。
本発明は上記後者方法の改良に関する。以下光
照射による方法を例にとり詳しく説明する。
まず単量体混合物を光透過性の成形型に充填す
る。単量体混合物中の単量体相互の間の反応性比
の関係は次の様になる。
一般に多元共重合反応において下記生長反応
Mi*+Mj→Mj*
の速度定数をKijとすれば、任意の単量体Miの単
量体Mjに対する反応性比Rijは
Rij≡Kii/Kij ……(2)
と定義される。同様に単量体Miに対する単量体
Mjの反応性比Rjiは
Rji≡Kjj/Kji ……(3)
と定義される。
X元共重合にはX(X−1)個の反応性比があ
る。また単量体MiとMjの混合比を(Mi/Mj)
mとすると、このとき生成する共重合体成分組成
比(Mi/Mj)pは下記(4)式で表わされることが
知られている。
(Mi/Mj)p=(Mi/Mj)mRij(Mi/Mj)m+1/(M
i/Mj)m+Rji……(4)
ここで
Rij(Mi/Mj)m+1/(Mi/Mj)m+Rji≡Q ……(5)
とおくと、Q>1であれば常に下記(6)式が成立す
る。
(Mi/Mj)p>(Mi/Mj)m ……(6)
すなわち生成する共重合体中のMi成分の含有
比は単量体混合物のMiの混合比よりも常に高く
なるがQ≧1.1であることが好ましい。
重合時間とともに残存している単量体混合物中
のMiの混合比は次第に減少し、逆にMjの混合比
は次第に増加する。したがつて重合初期に生成す
る共重合体中のMi成分の含有比は高いが、重合
時間と共にその時点で生成する共重合体のMi成
分の含有比は減少する。逆に生成する共重合体中
のMj成分の含有比は重合の進行とともに次第に
増加する。このようにして得られる共重合体は組
成の異なる共重合体の混合物である。
またQ<1(好ましくはQ≦0.9)であれば常に
(Mi/Mj)p<(Mi/Mj)m ……(7)
となるから、Q>1の場合とは逆に、共重合体中
のMi成分の含有比は単量体混合物中のMiの混合
比よりも常に小さくなる。
Q=1であれば
(Mi/Mj)p=(Mi/Mj)m ……(8)
となり、単量体混合比と等しい組成を持つた共重
合体が生成し、共重合体は組成分布を示さない。
従つて前記(5)式におけるQが1以外の数(好まし
くはQ≧1.1またはQ≦0.9)であつて、この様な
単量体混合物を透明管内に充填して外側から光を
照射するとき、外側から中心軸方向に向けて重合
が進行すれば反応性比の大きい単量体ほど外側へ
偏つた単量体組成分布が形成される。
例えば単量体混合物が単量体M1、M2……Mx
のX種の単量体より成つており、1≦i<j≦X
であるようなiおよびjを選んだ時に前記(5)式に
おけるQが1よりも大きい数であれば共重合体中
におけるMi成分の量が最大または極大である部
分は、Mj成分の量が最大または極大である部分
よりも先に重合した部分にある。
すなわちこの場合に共重合体の組成分布を外側
から中心方向に向けて調べた場合には、M1成分
がまず最大または極大値に達し次にM2成分、M3
成分……と、順に極大値が見られて、中心におい
てMx成分が極大値をとることになる。
従つて単量体M1、M2……Mxの重合体P1、P2
……Pxの屈折率N1、N2……Nxが異なつていれ
ば半径方向に何らかの屈折率分布が得られる。
上記の光共重合法で使用する単量体としては、
本発明者らの先行出願特願昭50−11723、特願昭
55−53920、特願昭58−11954、特願昭58−11956
に列挙した単量体群を使用することができ、これ
ら単量体の使用により凸レンズ作用を有する自己
集束性光伝送体を製造することができる。また特
願昭58−11955に記載した単量体を使用すること
により、中心から周辺に向けて当初屈折率が減少
した後再び増大するようなW型の屈折率分布をも
つた光伝送体が得られる。
以上重合を光照射で行なう場合について述べた
が、光照射の代りに加熱することによつても同様
の効果が得られる。ただし光照射あるいは加熱を
行なう場合に、単量体混合物充填管全長にわたり
同時に光照射または加熱を与えると、管内周壁側
から固形の重合体が当初生成し、その内側にある
未だ液相状態の混合物は時間経過とともに体積収
縮するが、その外周が固形化(ゲル化)している
ため収縮によつて生ずる空隙が埋められないまま
重合が進み、最終的に相当長い部分にわたつて中
心に空洞が生成されてしまうという問題がおこ
る。上記問題を解決した改良方法として、単量体
混合物充填管を、光照射光源を内蔵させるか又は
重合に必要な一定温度に保持した重合処理室を貫
通して相対移動させることにより、上記充填管の
下端側から光照射あるいは加熱を漸進的に進める
方法も提案されている。
〔発明が解決しようとする問題点〕
しかしながら、上記の改良方法によつても次の
ような問題が残されている。
すなわち、成形管全体に単量体混合物を当初か
ら充填しておき、これを前述の重合処理室に通す
ようにすると、重合反応によつて生成した重合体
成分が、重合処理室外上方にある未反応の単量体
混合物中に拡散し、単量体混合物が重合体成分に
よつて汚染され、成形された光伝送体の屈折率分
布が長さ方向に一定でなくなるという問題があ
る。
〔問題点を解決するための手段〕
外部から単量体混合物を前記管内に該管の移動
速度に合せて順次供給することにより、前記管内
の液面レベルを光照射域または加熱域の入口付近
で一定に保つようにした。
〔作用〕
成形管内に存在する未反応単量体混合物は成形
管の移動の間常に光照射(または加熱)が与えら
れない領域と、光照射(または加熱)が与えられ
る領域との境界近くの少量だけとなり、重合体成
分によつて汚染される単量体混合物は重合の起つ
ている付近に限定される。
すなわち、重合反応の進行に合せて重合の管軸
方向進行前端に新鮮な未反応単量体混合物が供給
される。これにより、未反応単量体の重合体成分
による汚染は最小限度に抑制されて長さ方向に屈
折率分布が一定した光伝送体を得ることができ
る。
〔実施例〕
以下本発明を図面に示した実施例につき詳細に
説明する。
まず所定量の重合体屈折率と単量体反応性比が
互いに異なる補数種の単量体M1、M2……Mxを
混合し、これに所定量の重合開始剤、例えば過酸
化ベンゾイル、ベンゾインメチルエーテルなどを
溶解する。
本発明で使用可能な単量体としては、
[Industrial Field of Application] The present invention relates to a method for manufacturing a synthetic resin optical transmission body having a refractive index distribution in which the refractive index gradually changes. [Prior Art] As is well known, a gradient index optical transmission body consists of a transparent body whose refractive index gradually changes from the center to the periphery in the direction orthogonal to the optical axis. Widely used as transmission fiber, etc. The self-focusing optical transmitter described above has a refractive index on the central axis of No and a constant of A, and the refractive index N at a distance of X from the central axis is N=No (1-1/2AX 2 )...(1) It has a distribution expressed by the formula. When the constant A is positive, the transmitter has a convex lens effect, and when A is negative, the transmitter has a concave lens effect. In addition, a refractive index distribution type optical transmission body having a refractive index distribution of A>0 in equation (1) near the center, and a distribution in which the refractive index gradually increases outwards at the outer periphery side. has also been proposed. The following two methods are typical methods for manufacturing such a refractive index distribution type optical transmission body using synthetic resin. One method is to polymerize a portion of a monomer that forms a three-dimensional network structure to create, for example, a cylindrical base material made of a transparent gel-like material. This is a method in which the polymerization is completed after diffusing another monomer having a refractive index different from that of the above monomer. Another method is to fill a transparent tube with a mixture of multiple monomers with different polymer refractive indexes and monomer reactivity ratios, and then perform molding by irradiating light and/or heating from the outside of the mold. There is a method of gradually advancing the polymerization reaction from the outer layer of the mixture in the mold to form a distribution of monomer units, that is, a refractive index distribution. The present invention relates to improvements in the latter method. The method using light irradiation will be explained in detail below, taking as an example. First, a light-transmissive mold is filled with a monomer mixture. The relationship in reactivity ratio between monomers in a monomer mixture is as follows. In general, in a multicomponent copolymerization reaction, if the rate constant of the following growth reaction Mi * + Mj→Mj * is Kij, then the reactivity ratio Rij of any monomer Mi to monomer Mj is Rij≡Kii/Kij...(2 ) is defined as Similarly, monomer for monomer Mi
The reactivity ratio Rji of Mj is defined as Rji≡Kjj/Kji (3). There are X (X-1) reactivity ratios in the X element copolymerization. Also, the mixing ratio of monomers Mi and Mj is (Mi/Mj)
It is known that the copolymer component composition ratio (Mi/Mj)p produced at this time is expressed by the following formula (4), where m is represented by the following formula (4). (Mi/Mj)p=(Mi/Mj)mRij(Mi/Mj)m+1/(M
i/Mj)m+Rji...(4) Here, Rij(Mi/Mj)m+1/(Mi/Mj)m+Rji≡Q...(5) If Q>1, the following equation (6) is always satisfied. To establish. (Mi/Mj)p>(Mi/Mj)m...(6) That is, the content ratio of the Mi component in the resulting copolymer is always higher than the mixing ratio of Mi in the monomer mixture, but Q≧1.1 It is preferable that As the polymerization time increases, the mixing ratio of Mi in the remaining monomer mixture gradually decreases, and conversely, the mixing ratio of Mj gradually increases. Therefore, the content ratio of the Mi component in the copolymer produced at the initial stage of polymerization is high, but as the polymerization time increases, the content ratio of the Mi component in the copolymer produced at that point decreases. Conversely, the content ratio of the Mj component in the produced copolymer gradually increases as the polymerization progresses. The copolymer thus obtained is a mixture of copolymers having different compositions. Also, if Q<1 (preferably Q≦0.9), (Mi/Mj)p<(Mi/Mj)m...(7), so contrary to the case of Q>1, the copolymer The content ratio of Mi components in the monomer mixture is always smaller than the mixing ratio of Mi in the monomer mixture. If Q=1, (Mi/Mj)p=(Mi/Mj)m...(8), a copolymer with a composition equal to the monomer mixing ratio is produced, and the copolymer has a composition distribution. does not indicate.
Therefore, when Q in the above formula (5) is a number other than 1 (preferably Q≧1.1 or Q≦0.9) and such a monomer mixture is filled in a transparent tube and irradiated with light from the outside. If polymerization proceeds from the outside toward the central axis, a monomer composition distribution will be formed that is more biased toward the outside as the monomer has a larger reactivity ratio. For example, if a monomer mixture contains monomers M 1 , M 2 ...Mx
It is composed of X types of monomers, and 1≦i<j≦X
When i and j are selected such that if Q in the above formula (5) is a larger number than 1, the portion where the amount of the Mi component in the copolymer is maximum or maximum is the amount of the Mj component. It is located in the part that polymerized earlier than the part that is the largest or local maximum. In other words, in this case, when the composition distribution of the copolymer is investigated from the outside toward the center, the M1 component reaches its maximum or local maximum value first, then the M2 component, and the M3 component.
The maximum values of the components are seen in order, and the Mx component takes the maximum value at the center. Therefore, monomers M 1 , M 2 ... polymers P 1 , P 2 of Mx
...If the refractive indices N 1 and N 2 of Px are different, some kind of refractive index distribution can be obtained in the radial direction. The monomers used in the above photocopolymerization method are:
Prior application patent application No. 50-11723 by the present inventors;
55-53920, patent application 1982-11954, patent application 1982-11956
The monomer groups listed in can be used, and by using these monomers, a self-focusing light transmission body having a convex lens action can be manufactured. Furthermore, by using the monomer described in Japanese Patent Application No. 58-11955, an optical transmission material with a W-shaped refractive index distribution in which the refractive index initially decreases from the center to the periphery and then increases again can be produced. can get. Although the case where polymerization is carried out by light irradiation has been described above, the same effect can be obtained by heating instead of light irradiation. However, if light irradiation or heating is applied simultaneously over the entire length of the monomer mixture filled tube, a solid polymer will initially form from the inner circumferential wall of the tube, and the mixture inside it, which is still in a liquid phase, will form. shrinks in volume over time, but because its outer periphery is solidified (gelled), polymerization proceeds without filling the voids caused by shrinkage, and eventually a void forms in the center over a considerable length. The problem arises that it is generated. As an improved method that solves the above problem, the monomer mixture filled tube is moved relatively through a polymerization treatment chamber that has a built-in light irradiation light source or is maintained at a constant temperature necessary for polymerization. A method has also been proposed in which light irradiation or heating is gradually applied from the lower end side. [Problems to be Solved by the Invention] However, even with the above improved method, the following problems remain. In other words, if the entire formed tube is filled with a monomer mixture from the beginning and is passed through the aforementioned polymerization treatment chamber, the polymer component produced by the polymerization reaction will be transferred to the unused material above the outside of the polymerization treatment chamber. There is a problem of diffusion into the monomer mixture of the reaction, contamination of the monomer mixture by the polymer component, and the refractive index distribution of the shaped light transmitter becoming non-uniform along its length. [Means for solving the problem] By sequentially supplying a monomer mixture into the tube from the outside in accordance with the moving speed of the tube, the liquid level in the tube is brought to near the entrance of the light irradiation area or the heating area. I tried to keep it constant. [Function] During the movement of the forming tube, the unreacted monomer mixture existing in the forming tube is constantly removed near the boundary between the area where no light irradiation (or heating) is applied and the area where light irradiation (or heating) is applied. Only a small amount of the monomer mixture is contaminated by the polymer component, and the monomer mixture is confined to the vicinity where polymerization is occurring. That is, as the polymerization reaction progresses, fresh unreacted monomer mixture is supplied to the front end of the polymerization tube in the axial direction. Thereby, contamination by the polymer component of unreacted monomers is suppressed to a minimum, and a light transmitting body having a constant refractive index distribution in the length direction can be obtained. [Embodiments] The present invention will be described in detail below with reference to embodiments shown in the drawings. First, a predetermined amount of complementary monomers M 1 , M 2 , . Dissolve benzoin methyl ether etc. Monomers that can be used in the present invention include:
【式】 [Formula]
【式】【formula】
【式】 [Formula]
【式】【formula】
【式】 [Formula]
【式】【formula】
【式】 [Formula]
【式】【formula】
【式】【formula】
【式】【formula】
【式】【formula】
【式】 CH2=CH−CH2−X[Formula] CH 2 = CH−CH 2 −X
【式】
CH2=C−CH2−X
|
CH3
アクリロニトリル、メタクリルニトリル、塩化ビ
ニル、N−ビニルカルバゾール、N−ビニルフタ
ルイミド、N−ビニルピロリドン、ビニルチオフ
エン、ビニルフラン、ビニルフエニルスルフイ
ド、
R=−CnH2o+1(n=1〜10)
−C6H11、
又は含フツ素脂肪族基[Formula] CH 2 = C-CH 2 -X | CH 3 Acrylonitrile, methacrylnitrile, vinyl chloride, N-vinylcarbazole, N-vinylphthalimide, N-vinylpyrrolidone, vinylthiophene, vinylfuran, vinylphenyl sulfide, R =-CnH 2o+1 (n=1 to 10) -C 6 H 11 or fluorine-containing aliphatic group
【式】 [Formula]
【式】【formula】
【式】 [Formula]
本発明方法によれば、未反応状態にある単量体
混合物が重合体成分によつて汚染されることがほ
とんど無くなり、この汚染に起因するレンズの屈
折率分布のばらつきが大幅に減少して長さ方向お
よび製品間で一定した光学特性をもつ屈折率分布
型合成樹脂光伝送体が得られる。
According to the method of the present invention, the monomer mixture in an unreacted state is almost never contaminated by polymer components, and the dispersion in the refractive index distribution of the lens due to this contamination is greatly reduced. A refractive index distribution type synthetic resin light transmitting body having uniform optical properties in the transverse direction and between products can be obtained.
第1図は本発明を実施する装置の一例を示す縦
断面図、第2図は本発明の他の実施例を示す縦断
面概略図である。
1……単量体混合物、2……成形管、3……重
合処理室(光照射域)、7……光源ランプ、9…
…エアコンデイシヨナー装置、10……貯蔵槽、
11……液面検出センサー、13……開閉バル
ブ、15……屈折率勾配をもつ共重合体。
FIG. 1 is a vertical cross-sectional view showing an example of an apparatus for implementing the present invention, and FIG. 2 is a schematic vertical cross-sectional view showing another embodiment of the present invention. DESCRIPTION OF SYMBOLS 1... Monomer mixture, 2... Molded tube, 3... Polymerization treatment chamber (light irradiation area), 7... Light source lamp, 9...
...Air conditioner device, 10...Storage tank,
11...Liquid level detection sensor, 13...Opening/closing valve, 15...Copolymer with refractive index gradient.
Claims (1)
異なる複数の単量体の混合物を細長い成形管に充
填し、この管を光照射源または(および)加熱体
に対し相対移動させて前記管の下端から漸進的に
光照射または(および)加熱を与えて管内の混合
物の外層より順次内部に向けておよび管軸方向に
向けて重合反応を進め、外周から中心に向けて屈
折率が変化する光伝送体を製造する方法におい
て、外部から単量体混合物を前記管内に該管の移
動速度に合せて順次供給し、前記管内の液面レベ
ルを前記光照射域または加熱域の上端付近でほぼ
一定に保つことを特徴とする屈折率分布を有する
合成樹脂光伝送体の製造方法。1 A mixture of a plurality of monomers having different polymer refractive indexes and monomer reactivity ratios is filled into an elongated molded tube, and the tube is moved relative to a light irradiation source or (and) a heating element to cool the tube. Light irradiation or (and) heating is applied gradually from the lower end to advance the polymerization reaction from the outer layer of the mixture inside the tube and in the direction of the tube axis, and the refractive index changes from the outer periphery toward the center. In a method for manufacturing an optical transmission body, a monomer mixture is sequentially supplied into the tube from the outside in accordance with the moving speed of the tube, and the liquid level in the tube is brought to approximately near the upper end of the light irradiation area or the heating area. A method for manufacturing a synthetic resin optical transmission body having a refractive index distribution that is maintained constant.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60011617A JPS61170705A (en) | 1985-01-24 | 1985-01-24 | Production of synthetic resin optical transmission body |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60011617A JPS61170705A (en) | 1985-01-24 | 1985-01-24 | Production of synthetic resin optical transmission body |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61170705A JPS61170705A (en) | 1986-08-01 |
| JPH0241001B2 true JPH0241001B2 (en) | 1990-09-14 |
Family
ID=11782879
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60011617A Granted JPS61170705A (en) | 1985-01-24 | 1985-01-24 | Production of synthetic resin optical transmission body |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61170705A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20080091454A (en) * | 2006-01-26 | 2008-10-13 | 후지필름 가부시키가이샤 | Method of manufacturing optical transmission medium |
-
1985
- 1985-01-24 JP JP60011617A patent/JPS61170705A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61170705A (en) | 1986-08-01 |
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