JPH0597978A - Hydrogenated polymer - Google Patents
Hydrogenated polymerInfo
- Publication number
- JPH0597978A JPH0597978A JP3290700A JP29070091A JPH0597978A JP H0597978 A JPH0597978 A JP H0597978A JP 3290700 A JP3290700 A JP 3290700A JP 29070091 A JP29070091 A JP 29070091A JP H0597978 A JPH0597978 A JP H0597978A
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- hydrogenated polymer
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Abstract
(57)【要約】
【構成】 (1) 特定のノルボルネン系誘導体を開環重合
して得られる重合体をさらに水素添加して得られ、重量
平均分子量が2000以下のオリゴマーを0.01〜5
重量%含有する水素添加重合体。
【効果】 成形時の粘性制御が容易であり、低複屈折
率、かつ耐熱性にも優れる。(57) [Summary] [Structure] (1) 0.01 to 5 of an oligomer having a weight average molecular weight of 2000 or less, which is obtained by further hydrogenating a polymer obtained by ring-opening polymerization of a specific norbornene derivative is used.
Hydrogenated polymer containing wt%. [Effect] It is easy to control the viscosity during molding, has a low birefringence and is excellent in heat resistance.
Description
【0001】[0001]
【産業上の利用分野】本発明は、成形時の粘性制御が容
易な低複屈折の耐熱性光学材料として好適な水素添加重
合体に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hydrogenated polymer suitable as a heat-resistant optical material having a low birefringence, whose viscosity can be easily controlled during molding.
【0002】[0002]
【従来の技術】近年、レンズ用材料として、ガラスに代
って加工性、軽量化の面からプラスチックが採用されて
いる。特にプラスチック非球面レンズの主流材料は、ポ
リメチルメタクリレートである。ポリメチルメタクリレ
ートは、光線透過率が高く、成形時の樹脂の粘性挙動も
制御しやすく、複屈折がほとんどなく、その上コストが
安いため、据え置き型CDではほとんどこのポリメチル
メタクリレートの光ピックアップレンズが使用されてい
る。しかし、ポリメチルメタクリレートは、耐熱性が約
80℃と用途によっては不十分で、飽和吸水率も大き
く、ガラス製レンズに比べて信頼性が劣る。2. Description of the Related Art In recent years, plastic has been adopted as a lens material instead of glass in terms of workability and weight saving. In particular, the mainstream material for plastic aspherical lenses is polymethylmethacrylate. Polymethylmethacrylate has a high light transmittance, it is easy to control the viscous behavior of the resin during molding, there is almost no birefringence, and the cost is low. It is used. However, polymethylmethacrylate has a heat resistance of about 80 ° C., which is insufficient depending on the application, has a large saturated water absorption rate, and is inferior in reliability to a glass lens.
【0003】[0003]
【本発明が解決する課題】本発明は上記問題点を解決
し、光線透過率が高く、成形時の樹脂の粘性挙動も制御
しやすく、複屈折がほとんどなく、飽和吸水率も大き
く、耐熱性にも優れる光学材料として好適な重合体を提
供するものである。The present invention solves the above problems, has a high light transmittance, is easy to control the viscous behavior of the resin during molding, has almost no birefringence, has a large saturated water absorption, and has a high heat resistance. A polymer suitable for use as an optical material having excellent properties is also provided.
【0004】[0004]
【課題を解決するための手段】すなわち本発明は、下記
一般式(I)で表わされる少なくとも1種のノルボルネ
ン誘導体または該ノルボルネン誘導体とこれと共重合可
能な単量体を開環重合して得られる開環重合体をさらに
水素添加して得られる固有粘度0.35〜0.8の水素
添加重合体であって、重量平均分子量2000以下の重
合体の割合が0.01〜5重量%であることを特徴とす
る水素添加重合体 一般式(I)That is, the present invention is obtained by ring-opening polymerization of at least one norbornene derivative represented by the following general formula (I) or the norbornene derivative and a monomer copolymerizable therewith. Which is a hydrogenated polymer having an intrinsic viscosity of 0.35 to 0.8 and further having a weight average molecular weight of 2000 or less in an amount of 0.01 to 5% by weight. Hydrogenated polymer characterized by having general formula (I)
【0005】[0005]
【化2】 (式中、AおよびBは水素原子または炭素数1〜10の
炭化水素基であり、XおよびYは水素原子、ハロゲン原
子または一価の有機基であって、mは0または1であ
る。)を提供するものである。以下、本発明について具
体的に説明する。[Chemical 2] (In the formula, A and B are a hydrogen atom or a hydrocarbon group having 1 to 10 carbon atoms, X and Y are a hydrogen atom, a halogen atom or a monovalent organic group, and m is 0 or 1. ) Is provided. Hereinafter, the present invention will be specifically described.
【0006】本発明の水素添加重合体は、上記の一般式
(I)で表わされるノルボルネン誘導体よりなる単量体
(以下「特定単量体」という)を単独で、または特定単
量体をこれと共重合可能な共重合性単量体とともにメタ
セシス重合触媒を用いて開環共重合させることによって
得られる水素添加重合体であり、以下において「水素添
加重合体」という。本発明において、特定単量体のう
ち、上記一般式(I)におけるXまたはYが式−(CH
2 )n COOR1 で表わされる基である特定単量体は、
得られる重合体が高いガラス転移温度と低い吸湿性を有
するものとなる点が好ましい。また、式−(CH2 )n
COOR1 で表わされる基は、特定単量体の1分子当た
りに1個含有されることが、得られる重合体の吸湿性が
低くなる点で好ましい。The hydrogenated polymer of the present invention comprises a monomer comprising the norbornene derivative represented by the general formula (I) (hereinafter referred to as "specific monomer") alone or a specific monomer. It is a hydrogenated polymer obtained by ring-opening copolymerization using a metathesis polymerization catalyst together with a copolymerizable monomer copolymerizable with, and is referred to as a “hydrogenated polymer” below. In the present invention, among the specific monomers, X or Y in the general formula (I) is represented by the formula — (CH
2 ) The specific monomer which is a group represented by n COOR 1 is
It is preferable that the obtained polymer has a high glass transition temperature and low hygroscopicity. Moreover, the formula - (CH 2) n
It is preferable that one group represented by COOR 1 be contained per molecule of the specific monomer, since the resulting polymer has low hygroscopicity.
【0007】また、式−(CH2 )n COOR1 で表わ
される基のうち、nの値が小さいものほど得られる重合
体のガラス転移温度が高くなるので好ましく、さらにn
が0である特定単量体は、その合成が容易である点で、
また得られる重合体に良好な特性が得られる点で好まし
い。上記の式において、R1 は炭素数1〜20の炭化水
素基であるが、炭素数が多くなるほど得られる重合体の
吸湿性が小さくなる点で好ましい。しかし、得られる重
合体のガラス転移温度とのバランスの点から、炭素数が
1〜4の鎖状アルキル基または炭素数が5以上の(多)
環状アルキル基であることが好ましく、特にメチル基で
あることが好ましい。さらに、式−(CH2 )n COO
R1 で表わされる基が結合した炭素数原子に、同時に炭
素数1〜10の炭化水素基が置換基として結合されてい
る特定単量体は、得られる重合体のガラス転移温度を低
下させずに吸湿性を低下させるので好ましい。そして、
特にこの置換基がメチル基である特定単量体は、その合
成が容易な点で好ましい。Further, among the groups represented by the formula — (CH 2 ) n COOR 1 , the smaller the value of n, the higher the glass transition temperature of the polymer obtained, which is preferable.
The specific monomer in which is 0 is easy to synthesize,
It is also preferable in that the obtained polymer can have good characteristics. In the above formula, R 1 is a hydrocarbon group having 1 to 20 carbon atoms, and it is preferable that the carbon number increases so that the hygroscopicity of the resulting polymer decreases. However, from the viewpoint of the balance with the glass transition temperature of the obtained polymer, a chain alkyl group having 1 to 4 carbon atoms or a chain alkyl group having 5 or more carbon atoms (many)
It is preferably a cyclic alkyl group, and particularly preferably a methyl group. Moreover, the formula - (CH 2) n COO
The specific monomer in which the hydrocarbon group having 1 to 10 carbon atoms is simultaneously bonded as a substituent to the carbon atom to which the group represented by R 1 is bonded does not lower the glass transition temperature of the obtained polymer. It is preferable because it lowers hygroscopicity. And
In particular, the specific monomer having a methyl group as the substituent is preferable because the synthesis thereof is easy.
【0008】本発明に用いる水素添加重合体に係る開環
重合体は、特定単量体を単独で開環重合させたものであ
ってもよいが、当該特定単量体と共重合性単量体とを開
環共重合させたものであってもよい。このように共重合
性単量体が使用される場合において、開環重合体におけ
る特定単量体の割合は5モル%以上、好ましくは20モ
ル%以上とされる。使用される共重合性単量体として
は、メタセシス重合触媒によって開環重合し得る単量
体、および重合体の主鎖に炭素−炭素二重結合を有する
一部重合された低重合体を挙げることができる。上記特
定単量体のうちでは、上記一般式(I)においてmが1
であるテトラシクロドデセン誘導体が、ガラス転移点の
高い重合体が得られる点で好ましい。一般式(I)にお
いて、mが1であるテトラトクロドデセン誘導体のう
ち、好ましい化合物としては、8−カルボキシメチルテ
トラシクロ〔4.4.0.12,5 .17,10〕−3−ドデ
セン、8−メチル−8−カルボキシメチルテトラシクロ
〔4.4.0.12,5 .17,10〕−3−ドデセン、5−
カルボキシメチル−ビシクロ〔2.2.1〕−2−ヘプ
テンなどを挙げるとができる。The ring-opening polymer relating to the hydrogenated polymer used in the present invention may be a ring-opening polymer of a specific monomer alone. It may be a compound obtained by ring-opening copolymerization with the body. When the copolymerizable monomer is used as described above, the proportion of the specific monomer in the ring-opening polymer is 5 mol% or more, preferably 20 mol% or more. Examples of the copolymerizable monomer used include monomers that can be ring-opening polymerized by a metathesis polymerization catalyst, and partially polymerized low polymers having a carbon-carbon double bond in the main chain of the polymer. be able to. Among the above specific monomers, m is 1 in the general formula (I).
The tetracyclododecene derivative of is preferable in that a polymer having a high glass transition point can be obtained. Among the tetratoclododecene derivatives in which m is 1 in the general formula (I), preferred compounds include 8-carboxymethyltetracyclo [4.4.0.1 2,5 . 1 7,10 ] -3-dodecene, 8-methyl-8-carboxymethyltetracyclo [4.4.0.1 2,5 . 1, 7, 10 ] -3-dodecene, 5-
Carboxymethyl-bicyclo [2.2.1] -2-heptene and the like can be mentioned.
【0009】特定単量体は環状オレフィン化合物と共重
合することもできる。かかる環状オレフィン化合物の具
体例としては、シクロペンテン、シクロオクテン、1,
5−シクロオクタジエン、1,5,9−シクロドデカト
リエンなどのシクロオレフィン類;ビシクロ〔2.2.
1〕−2−ヘプテン、トリシクロ〔5.2.1.
02,6 〕−8−デセン、トリシクロ〔5.2.1.0
2,6 〕−3−デセン、トリシクロ〔6.2.1.
01,8 〕−9−ウンデセン、トリシクロ〔6.2.1.
01,8 〕−4−ウンデセン、テトラシクロ〔4.4.
0.12,5 .17, 10〕−3−ドデセン、ペンタシクロ
〔6.5.1.13,6 .02,7 .09,13〕−4−ペンタ
デセン、ペンタシクロ〔6.6.1.13,6 .02,7 .
09,14〕−4−ヘキサデセセン、ペンタシクロ〔6.
5.1.13,6 .02,7 .09,13〕−11−ペンタデセ
ン、ジシクロペンタジエン、ペンタシクロ〔6.5.
1.13,6 .02,7 .09,13〕−ペンタデカ−4,11
−ジエンなどのポリシクロアルケンを挙げることができ
る。The specific monomer can also be copolymerized with a cyclic olefin compound. Specific examples of the cyclic olefin compound include cyclopentene, cyclooctene, 1,
Cycloolefins such as 5-cyclooctadiene and 1,5,9-cyclododecatriene; bicyclo [2.2.
1] -2-heptene, tricyclo [5.2.1.
0 2,6 ] -8-decene, tricyclo [5.2.1.0]
2,6 ] -3-decene, tricyclo [6.2.1.
0 1,8 ] -9-undecene, tricyclo [6.2.1.
0 1,8 ] -4-undecene, tetracyclo [4.4.
0.1 2,5 . 1 7, 10 ] -3-dodecene, pentacyclo [6.5.1.1 3,6 . 0 2,7 . 0 9,13] -4-pentadecene, pentacyclo [6.6.1.1 3,6. 0 2,7 .
0 9,14] -4-Hekisadesesen, pentacyclo [6.
5.1.1 3,6 . 0 2,7 . 0 9,13 ] -11-pentadecene, dicyclopentadiene, pentacyclo [6.5.
1.1 3,6 . 0 2,7 . 0 9, 13] - pentadeca -4,11
Mention may be made of polycycloalkenes such as dienes.
【0010】さらに特定単量体は、ポリブタジエン、ポ
リイソプレン、スチレン−ブタジエン共重合体、エチレ
ン−プロピレン非共役ジエン共重合ゴム、ポリノルボル
ネン、ポリペンテナマーなどの重合体の主鎖に、炭素−
炭素二重結合を含んだ不飽和炭化水素重合体の存在下で
開環重合することもできる。特定単量体とこれと共重合
可能な共重合性単量体との開環重合の方法および水素添
加の方法は、特開平1−132626号公報に記載され
る方法と同様の方法を挙げることができる。得られる水
素添加重合体の水素添加率は、通常50%以上、好まし
くは70%以上、さらに好ましくは80%以上とされ
る。水素添加率が50%未満の重合体は耐光性が悪くな
る。Further, the specific monomer is a polymer such as polybutadiene, polyisoprene, styrene-butadiene copolymer, ethylene-propylene non-conjugated diene copolymer rubber, polynorbornene, polypentenamer, and the like.
Ring-opening polymerization can also be carried out in the presence of an unsaturated hydrocarbon polymer containing a carbon double bond. For the ring-opening polymerization method and the hydrogenation method of the specific monomer and the copolymerizable monomer copolymerizable therewith, the same method as the method described in JP-A-1-132626 can be mentioned. You can The hydrogenation rate of the obtained hydrogenated polymer is usually 50% or more, preferably 70% or more, more preferably 80% or more. A polymer having a hydrogenation rate of less than 50% has poor light resistance.
【0011】本発明の水素添加重合体は、前記特定単量
体を開環重合して得られる開環重合体をさらに水素添加
して得られる固有粘度0.35〜0.8の水素添加重合
体である。特定単量体としては前期と同様のものを挙げ
ることができ、好ましいものも同様である。本発明の水
素添加重合体は、重量平均分子量が2000以下の重合
体を0.01〜5重量%、好ましくは0.01〜4重量
%、さらに好ましくは0.02〜3重量%含有するもの
である。ここで、重量平均分子量が2000以下の重合
体が0.01重量%未満では複屈折を下げることができ
ず、また5重量%を超えると成形品が外観不良となる。
本発明においては、重量平均分子量が2000以下の重
合体は、別途重合しておいて、通常に重合した重合体に
添加することが好ましい。水素添加重合体の分子量およ
び分子量分布の調節は、メタセシス開環重合反応におい
て、メタセシス重合触媒の種類や濃度、重合温度、溶媒
の種類や量ならびに単量体濃度などの反応条件を変える
ことにより行なう。通常は、適宜の分子量調節剤の適当
量を重合反応系に添加することによって開環重合体の分
子量を調節することが好ましい。かかる分子量調節剤と
しては、α−オレフィン類、α,ω−ジオレフィン類ま
たはアセチレン類などの分子内に少なくとも1つの炭素
間二重結合または炭素間三重結合を有する化合物、ある
いは塩化アリル、酢酸アリル、トリメチルアクロキシシ
ランなどの極性アリル化合物を挙げることができる。ま
た、触媒を変えることにより分子量分布を狭くすること
ができる。The hydrogenated polymer of the present invention is a hydrogenated polymer having an intrinsic viscosity of 0.35 to 0.8 obtained by further hydrogenating a ring-opening polymer obtained by ring-opening polymerization of the above-mentioned specific monomer. It is united. As the specific monomer, the same ones as in the above can be mentioned, and the preferable ones are also the same. The hydrogenated polymer of the present invention contains 0.01 to 5% by weight, preferably 0.01 to 4% by weight, and more preferably 0.02 to 3% by weight of a polymer having a weight average molecular weight of 2000 or less. Is. Here, if the polymer having a weight average molecular weight of 2000 or less is less than 0.01% by weight, the birefringence cannot be lowered, and if it exceeds 5% by weight, the molded product has a poor appearance.
In the present invention, the polymer having a weight average molecular weight of 2000 or less is preferably polymerized separately and then added to the normally polymerized polymer. In the metathesis ring-opening polymerization reaction, the molecular weight and molecular weight distribution of the hydrogenated polymer are adjusted by changing the reaction conditions such as the type and concentration of the metathesis polymerization catalyst, the polymerization temperature, the type and amount of the solvent, and the monomer concentration. .. Usually, it is preferable to adjust the molecular weight of the ring-opening polymer by adding an appropriate amount of an appropriate molecular weight regulator to the polymerization reaction system. Examples of the molecular weight regulator include compounds having at least one carbon-carbon double bond or carbon-carbon triple bond in the molecule such as α-olefins, α, ω-diolefins and acetylenes, allyl chloride, and allyl acetate. , A polar allyl compound such as trimethylacryloxysilane. Also, the molecular weight distribution can be narrowed by changing the catalyst.
【0012】[0012]
【実施例】分子量分布の広い水素添加重合体(a−1)の製造方法 窒素ガスで置換した反応容器内に、8−メチル−8−カ
ルボキシメチルテトラシクロ〔4.4.0.12,5 .1
7,10〕−3−ドデセン500gと、1,2−ジクロロエ
タン2000mlと、分子量調節剤である1−ヘキセン
3.8gと、触媒として、六塩化タングステンの濃度
0.05M/リットルのクロロベンゼン溶液91.6ml
と、パラアルデヒドの濃度0.1M/リットルの1,2
−ジクロロエタン溶液68.7mlと、トリイソブチルア
ルミニウムの濃度0.5M/リットルのトルエン溶液3
7mlとを加え、60℃で10時間反応させることにより
開環重合体450gを得た。この開環重合体を9000
mlのテトラヒドロフランに溶解し、パラジウム濃度が5
重量%のパラジウム−アルミナ触媒45gを加え、水素
ガスを圧力が100kg/cm2 となるように仕込んで、1
50℃で5時間水素添加反応させた。水素添加反応後、
触媒を濾別し、濾液を塩酸酸性の大過剰量のメタノール
中に注いで、水素添加された重合体a−1を製造した。
この重合体a−1の水素添加率は実質上100%であっ
た。また、重合体のηinh =0.56で、Mw/Mn=
6.02であった。EXAMPLES Method for producing hydrogenated polymer (a-1) having a wide molecular weight distribution 8-methyl-8-carboxymethyltetracyclo [4.4.0.1 2, 5 . 1
7,10 ] -3-dodecene (500 g), 1,2-dichloroethane (2000 ml), 1-hexene (3.8 g) as a molecular weight regulator, and a hexachlorobenzene solution having a concentration of 0.05 M / liter of tungsten hexachloride as a catalyst 91. 6 ml
And 1,2 with a paraaldehyde concentration of 0.1 M / liter
68.7 ml of a dichloroethane solution and a toluene solution of triisobutylaluminum having a concentration of 0.5 M / liter 3
7 ml was added and reacted at 60 ° C. for 10 hours to obtain 450 g of a ring-opening polymer. This ring-opening polymer was
It is dissolved in tetrahydrofuran (ml) and the palladium concentration is 5
45% by weight of palladium-alumina catalyst was added, and hydrogen gas was charged so that the pressure became 100 kg / cm 2 , and 1
Hydrogenation reaction was carried out at 50 ° C. for 5 hours. After the hydrogenation reaction,
The catalyst was filtered off, and the filtrate was poured into a large excess of hydrochloric acid-acidified methanol to prepare hydrogenated polymer a-1.
The hydrogenation rate of this polymer a-1 was substantially 100%. Further, η inh of the polymer is 0.56, and Mw / Mn =
It was 6.02.
【0013】オリゴマーの製造方法 窒素雰囲気下において、窒素置換した反応容器内に、8
−メチル−8−カルボキシメチルテトラシクロ〔4.
4.0.12,5 .17,10〕−3−ドデセン800gと、
1−ヘキセン2400gと、触媒であるWCl6 の濃度
0.05M/リッリルのジメトキシエタン溶液34.5
mlと、ジエチルアルミニウムクロライドの濃度1.0M
/リットルのn−ヘキサン溶液3.45mlとを加え、7
0℃で3時間反応させ、重合溶液を得た。 Method for producing oligomer In a reaction vessel purged with nitrogen under a nitrogen atmosphere, 8
-Methyl-8-carboxymethyltetracyclo [4.
4.0.1 2,5 . 1, 7, 10 ] -3-800 g of dodecene,
2400 g of 1-hexene and a solution of WCl 6 as a catalyst in a concentration of 0.05 M / litryl in dimethoxyethane 34.5
ml and diethylaluminum chloride concentration 1.0M
/ Liter of n-hexane solution 3.45 ml was added, and
The reaction was carried out at 0 ° C. for 3 hours to obtain a polymerization solution.
【0014】二層分離した重合溶液の上ずみにメタノー
ルを加え、よく振りまぜた後、静置し、上層部を回収す
る。この操作を3回繰り返し、回収した上層部を再度濃
縮した。この上層部濃縮液をオートクレーブ中でパラジ
ウム/アルミナ水添触媒を加えて、水素圧40kg/c
m3 、温度160℃で水素添加を行なった。水添触媒を
濾過後、触媒より単離し、オリゴマーを得た。平均分子
量1100であった。 GPCのM=1300のところ53重量% M=1000 〃 27重量% M=780 〃 16重量% M=550 〃 4重量% (peak値) であった。Methanol is added to the upper portion of the polymerization solution which has been separated into two layers, and the mixture is shaken well and then allowed to stand to recover the upper layer portion. This operation was repeated 3 times, and the collected upper layer was concentrated again. This upper layer concentrated liquid was added with a palladium / alumina hydrogenation catalyst in an autoclave to obtain a hydrogen pressure of 40 kg / c.
Hydrogenation was carried out at m 3 and a temperature of 160 ° C. After filtering the hydrogenated catalyst, it was isolated from the catalyst to obtain an oligomer. The average molecular weight was 1100. When M = 1300 of GPC, it was 53% by weight M = 1000 〃 27% by weight M = 780 〃 16% by weight M = 550 〃 4% by weight (peak value).
【0015】得られたレンズの物性を以下の方法により
測定した。 全光線透過率 (ASTM D−1003) (%) 複 屈 折 (エリプソメーター 633nm) (nm) 引張強度 (ASTM D−638) (kg/cm2 ) 伸 び (ASTM D−638) (%) 耐 熱 性 (DSC Tg) (℃)The physical properties of the obtained lens were measured by the following methods. Total light transmittance (ASTM D-1003) (%) Double bending (Ellipsometer 633nm) (nm) Tensile strength (ASTM D-638) (kg / cm 2 ) Stretch (ASTM D-638) (%) Resistance Thermal property (DSC Tg) (℃)
【0016】[0016]
【表1】 実施例1〜3、比較例1、2 水素添加重合体(a−1)100重量部に対して、オリ
ゴマー量を表1のとおり変量して得た水素添加重合体を
305℃で射出成形し、厚み2mmのレンズを作製した。
(表1) 実施例4、5 固有粘度の異なるものにオリゴマー量を変えて試料を作
り、これらを用いて成形品を作製した。(表1)[Table 1] Examples 1 to 3, Comparative Examples 1 and 2 A hydrogenated polymer obtained by varying the amount of the oligomer as shown in Table 1 with respect to 100 parts by weight of the hydrogenated polymer (a-1) was injection-molded at 305 ° C. A lens having a thickness of 2 mm was produced.
(Table 1) Examples 4 and 5 Samples were prepared by changing the amount of oligomer to those having different intrinsic viscosities, and molded articles were prepared using these. (Table 1)
【0017】[0017]
【表1】[Table 1]
【0018】[0018]
【発明の効果】本発明は、固有粘度が一定の範囲にあ
り、分子量分布がシャープな水素添加重合体、および固
有粘度が一定範囲によるものにオリゴマー添加した組成
物により、成形時の粘度制御が容易で低い複屈折率にな
る。従って、耐熱性光学部品、例えばプラスチックレン
ズ、球形レンズ、非球形レンズ、複写機レンズ、ビデオ
カメラ用コンバータレンズ、LBP用レンズ、光ティス
ク用ピックアップレンズ、コンタクトレンズ、光ディス
ク、車両部品用レンズ、光ファイバーなどに有効であ
る。INDUSTRIAL APPLICABILITY According to the present invention, a hydrogenated polymer having an intrinsic viscosity within a certain range and a sharp molecular weight distribution, and a composition obtained by adding an oligomer to a polymer having an inherent viscosity within a certain range can control viscosity during molding. Easy and low birefringence. Therefore, heat-resistant optical parts such as plastic lenses, spherical lenses, aspherical lenses, copier lenses, video camera converter lenses, LBP lenses, optical disc pickup lenses, contact lenses, optical disks, vehicle parts lenses, optical fibers, etc. Is effective for.
Claims (1)
も1種のノルボルネン誘導体または該ノルボルネン誘導
体とこれと共重合可能な単量体を開環重合して得られる
開環重合体をさらに水素添加して得られる固有粘度0.
35〜0.8の水素添加重合体であって、重量平均分子
量2000以下の重合体の割合が0.01〜5重量%で
あることを特徴とする水素添加重合体。 一般式(I) 【化1】 (式中、AおよびBは水素原子または炭素数1〜10の
炭化水素基であり、XおよびYは水素原子、ハロゲン原
子または一価の有機基であって、mは0または1であ
る。)1. At least one norbornene derivative represented by the following general formula (I) or a ring-opening polymer obtained by ring-opening polymerization of the norbornene derivative and a monomer copolymerizable therewith is further hydrogenated. Intrinsic viscosity obtained by
A hydrogenated polymer having a weight average molecular weight of 2,000 or less in a proportion of 0.01 to 5% by weight. General formula (I): (In the formula, A and B are a hydrogen atom or a hydrocarbon group having 1 to 10 carbon atoms, X and Y are a hydrogen atom, a halogen atom or a monovalent organic group, and m is 0 or 1. )
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3290700A JP3063311B2 (en) | 1991-10-09 | 1991-10-09 | Hydrogenated polymer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3290700A JP3063311B2 (en) | 1991-10-09 | 1991-10-09 | Hydrogenated polymer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0597978A true JPH0597978A (en) | 1993-04-20 |
| JP3063311B2 JP3063311B2 (en) | 2000-07-12 |
Family
ID=17759385
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3290700A Expired - Lifetime JP3063311B2 (en) | 1991-10-09 | 1991-10-09 | Hydrogenated polymer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3063311B2 (en) |
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-
1991
- 1991-10-09 JP JP3290700A patent/JP3063311B2/en not_active Expired - Lifetime
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