JP3259498B2 - Norbornene derivative compositions for metathesis ring-opening polymerization - Google Patents
Norbornene derivative compositions for metathesis ring-opening polymerizationInfo
- Publication number
- JP3259498B2 JP3259498B2 JP34571593A JP34571593A JP3259498B2 JP 3259498 B2 JP3259498 B2 JP 3259498B2 JP 34571593 A JP34571593 A JP 34571593A JP 34571593 A JP34571593 A JP 34571593A JP 3259498 B2 JP3259498 B2 JP 3259498B2
- Authority
- JP
- Japan
- Prior art keywords
- norbornene derivative
- opening polymerization
- polymerization
- metathesis ring
- group
- 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
Links
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Polyoxymethylene Polymers And Polymers With Carbon-To-Carbon Bonds (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、メタセシス開環重合用
のノルボルネン誘導体組成物に関するものである。The present invention relates to a norbornene derivative composition for metathesis ring-opening polymerization.
【0002】[0002]
【従来の技術】近年においては、下記一般式(3)で表
されるノルボルネン誘導体は、優れた光学特性および耐
熱性を有する透明樹脂の原料として非常に有用なもので
あることが知られている。2. Description of the Related Art In recent years, it has been known that a norbornene derivative represented by the following general formula (3) is very useful as a raw material for a transparent resin having excellent optical properties and heat resistance. .
【0003】[0003]
【化3】 Embedded image
【0004】(式中、R1 〜R12は、それぞれ水素原
子、ハロゲン原子および一価の有機基のいずれかであ
り、それぞれ同一または異なっていてもよい。R9 とR
10またはR11とR12は、一体化して二価の炭化水素基を
形成してもよく、R9 またはR10と、R11またはR12と
は、互いに結合して環状構造を形成するものであっても
よい。mは0〜2の整数である。)[0004] (wherein, R 1 to R 12 are each hydrogen atom, an halogen atom and monovalent organic radicals, which may be the same or different from each .R 9 and R
10 or R 11 and R 12 may be combined to form a divalent hydrocarbon group, and R 9 or R 10 and R 11 or R 12 are bonded to each other to form a cyclic structure It may be. m is an integer of 0 to 2. )
【0005】このノルボルネン誘導体は、シクロペンタ
ジエン類および/またはジシクロペンタジエン類と、ジ
エノフィル化合物とを反応原料としてディールス・アル
ダー型の熱付加反応を行った後、蒸留等による精製を行
って得られるものである。このノルボルネン誘導体は、
メタセシス触媒を用いた開環重合(以下、「メタセシス
開環重合」という。)のための原料モノマーとして用い
られる。The norbornene derivative is obtained by subjecting a cyclopentadiene and / or dicyclopentadiene to a dienophile compound as a reaction raw material to a Diels-Alder type heat addition reaction, followed by purification by distillation or the like. It is. This norbornene derivative is
It is used as a raw material monomer for ring-opening polymerization using a metathesis catalyst (hereinafter, referred to as “metathesis ring-opening polymerization”).
【0006】[0006]
【発明が解決しようとする課題】上記ノルボルネン誘導
体は、通常、窒素ガス等の不活性ガスによってシールさ
れたタンク等の容器内に導入され、保管される。しか
し、通常、シール用の不活性ガスにも微量の酸素が含有
されるため、保管期間が長期間となると、当該ノルボル
ネン誘導体の一部が酸化され、色相の黄変が生じて透明
性の良好な重合体を製造することができず、また、メタ
セシス開環重合反応における重合転化率が低下する、と
いう問題がある。The above norbornene derivative is usually introduced and stored in a container such as a tank sealed with an inert gas such as nitrogen gas. However, usually, since a small amount of oxygen is also contained in the inert gas for sealing, when the storage period is long, a part of the norbornene derivative is oxidized, yellowing of the hue occurs, and good transparency is obtained. However, there is a problem that a polymer cannot be produced, and a polymerization conversion rate in a metathesis ring-opening polymerization reaction is reduced.
【0007】本発明は、以上の問題を解決し、保存安定
性に優れ、従って長期間の保存後においても、色相に変
化がみられず、しかも十分に高い重合転化率でメタセシ
ス開環重合反応を行うことのできるノルボルネン誘導体
組成物を提供することを目的とする。The present invention solves the above problems and has excellent storage stability. Therefore, even after long-term storage, there is no change in hue, and the metathesis ring-opening polymerization reaction has a sufficiently high polymerization conversion. An object of the present invention is to provide a norbornene derivative composition capable of performing the following.
【0008】[0008]
【課題を解決するための手段】本発明は、上記目的を達
成するため鋭意研究を重ねた結果、ノルボルネン誘導体
に特定の酸化防止剤を含有させることによって、保存安
定性が大幅に改良されると共に、当該ノルボルネン誘導
体組成物は、長期間にわたる保存後においてもメタセシ
ス開環重合のための原料として用いた場合に十分に高い
重合転化率で重合することが見出されたことによって完
成されたものである。Means for Solving the Problems As a result of intensive studies to achieve the above object, the present invention has shown that storage stability is greatly improved by adding a specific antioxidant to a norbornene derivative. The norbornene derivative composition has been completed by being found to polymerize at a sufficiently high polymerization conversion rate when used as a raw material for metathesis ring-opening polymerization even after long-term storage. is there.
【0009】本発明のメタセシス開環重合用ノルボルネ
ン誘導体組成物は、下記一般式(1)で表されるノルボ
ルネン誘導体と、含有割合が10〜10,000ppm
である下記一般式(2)で表されるフェノール系化合物
とよりなることを特徴とする。The norbornene derivative composition for metathesis ring-opening polymerization of the present invention has a content of 10 to 10,000 ppm with a norbornene derivative represented by the following general formula (1).
And a phenolic compound represented by the following general formula (2) .
【0010】[0010]
【化4】 Embedded image
【0011】[0011]
【0012】[0012]
【化5】 Embedded image
【0013】(式中、X、Yは水素原子または炭素数1
〜10の炭化水素基であり、Zは水素原子、炭素数1〜
10の炭化水素基または炭素数1〜20の有機基(炭素
数1〜10の炭化水素基を除く。)である。)[0013] (wherein, X, Y is the number of hydrogen atoms or carbon 1
Z is a hydrogen atom, and has 1 to 10 carbon atoms.
A hydrocarbon group having 10 or an organic group having 1 to 20 carbon atoms (excluding a hydrocarbon group having 1 to 10 carbon atoms). )
【0014】以下、本発明について具体的に説明する。
本発明のメタセシス開環重合用ノルボルネン誘導体組成
物は、上記一般式(1)で表されるノルボルネン誘導体
と、含有割合が10〜10,000ppmである上記一
般式(2)で表されるフェノール系化合物とよりなるも
のである。Hereinafter, the present invention will be described specifically.
Metathesis ring-opening polymerization of norbornene derivative composition of the present invention comprises a norbornene derivative represented by the above general formula (1), the one content is 10~10,000ppm
It comprises a phenolic compound represented by the general formula (2) .
【0015】<ノルボルネン誘導体> 本発明のノルボルネン誘導体組成物の主成分であるノル
ボルネン誘導体は、上記一般式(1)で表される構造を
有する化合物である、8−メチル−8−カルボキシメチ
ルテトラシクロ[4.4.0.1 2,5 .1 7,10 ]−3−
ドデセンである。 <Norbornene Derivative> The norbornene derivative, which is the main component of the norbornene derivative composition of the present invention, is a compound having a structure represented by the above general formula (1) , ie, 8-methyl-8-carboxymethyl.
Letetracyclo [4.4.0.1 2,5 . 1 7,10 ] -3-
Dodecene.
【0016】[0016]
【0017】[0017]
【0018】[0018]
【0019】[0019]
【0020】[0020]
【0021】[0021]
【0022】[0022]
【0023】[0023]
【0024】[0024]
【0025】[0025]
【0026】[0026]
【0027】<ノルボルネン誘導体の合成> 上述のノルボルネン誘導体は、シクロペンタジエン類お
よび/またはジシクロペンタジエン類と、目的とするノ
ルボルネン誘導体の種類に応じて選ばれたジエノフィル
化合物とを反応原料として用いたディールス・アルダー
型の熱付加反応を行うことによって合成することができ
る。この反応温度は80〜250℃の範囲が好ましく、
さらに好ましくは130〜220℃である。また、この
合成の反応系に、反応原料であるシクロペンタジエンお
よび/またはジシクロペンタジエンとジエノフィル化合
物と共に、当該合成の反応における中間生成物である下
記一般式(4)で表されるビシクロヘプテン誘導体を供
給することによって、高い反応選択率でテトラシクロド
デセン誘導体を得ることができる。<Synthesis of Norbornene Derivative> The above-mentioned norbornene derivative is obtained by using Diels using cyclopentadiene and / or dicyclopentadiene and a dienophile compound selected according to the kind of the intended norbornene derivative as reaction raw materials. -It can be synthesized by performing an alder-type heat addition reaction. The reaction temperature is preferably in the range of 80 to 250 ° C,
The temperature is more preferably 130 to 220 ° C. Also this
Under the reaction system of the synthesis, with cyclopentadiene and / or dicyclopentadiene and dienophile compound which is a reaction raw material, an intermediate product in the reaction of the synthesis
By supplying the bicycloheptene derivative represented by the general formula (4) , a tetracyclododecene derivative can be obtained with a high reaction selectivity.
【0028】[0028]
【化6】 Embedded image
【0029】[0029]
【0030】さらに、上記の反応においては、N,N−
ジエチルヒドロキシルアミン、テトラキス[メチレン−
3−(3’.5’−ジ−t−ブチル−4−ヒドロキシフ
ェニル)プロピオネート]メタンなどの重合防止剤を添
加することによって、目的とするノルボルネン誘導体の
反応選択率を向上させることができる。Further, in the above reaction, N, N-
Diethylhydroxylamine, tetrakis [methylene-
By adding a polymerization inhibitor such as [3- (3'.5'-di-t-butyl-4-hydroxyphenyl) propionate] methane, the reaction selectivity of the target norbornene derivative can be improved.
【0031】<ノルボルネン誘導体の精製> 上記の反応により得られた反応液は、目的とするノルボ
ルネン誘導体以外に、未反応のシクロペンタジエン類お
よび/またはジシクロペンタジエン類、ジエノフィル化
合物、当該反応における中間生成物、さらにノルボルネ
ン誘導体よりも分子量の大きい重質分を含んでいるた
め、この反応液について精製処理を行うことによって、
高純度のノルボルネン誘導体を得ることができる。精製
処理の方法としては、通常は、蒸留塔内の温度などの条
件を変化させて蒸留処理を複数回行う方法が採られてお
り、これによって高純度のノルボルネン誘導体を得るこ
とができる。蒸留処理は、蒸留塔内の温度が200℃以
下、好ましくは180℃以下となるように減圧下で行う
ことが好ましい。蒸留塔内が高温の場合には、合成され
たノルボルネン誘導体が分解するおそれがある。<Purification of Norbornene Derivative> In addition to the intended norbornene derivative, unreacted cyclopentadiene and / or dicyclopentadiene, dienophile compound, intermediate product in the reaction are obtained in addition to the intended norbornene derivative. Product, and further contains a heavy component having a molecular weight larger than that of the norbornene derivative.
A highly pure norbornene derivative can be obtained. As a method of the purification treatment, a method of performing the distillation treatment a plurality of times by changing conditions such as the temperature in the distillation column is usually employed, whereby a high-purity norbornene derivative can be obtained. The distillation treatment is preferably performed under reduced pressure so that the temperature in the distillation column is 200 ° C. or lower, preferably 180 ° C. or lower. When the temperature inside the distillation column is high, the synthesized norbornene derivative may be decomposed.
【0032】<特定の酸化防止剤> 上述のようにして得られるノルボルネン誘導体に、上記
一般式(2)表される構造を有するフェノール系化合物
(以下、「特定の酸化防止剤」という。)が含有され
る。上記一般式(2)においてXおよびYは、それぞれ
水素原子、またはメチル基、エチル基、プロピル基、ブ
チル基などの炭素数1〜10のアルキル基に代表される
炭化水素基であり、Zは水素原子、またはメチル基、エ
チル基、プロピル基、ブチル基などの炭素数1〜10の
アルキル基に代表される炭化水素基、またはメトキシ
基、エトキシ基などのアルコキシ基、アルキルエステル
基などの炭素数1〜20のその他の有機基である。上記
一般式(2)で表されるフェノール系化合物の具体例と
しては、2,6−ジ−t−ブチルフェノール、2,6−
ジ−t−ブチル−4−メチルフェノール、4−メトキシ
フェノール、オクタデシル−3−(3,5−ジ−t−ブ
チル−4−ヒドロキシフェニル)プロピオネートなどを
挙げることができる。<Specific antioxidant> The norbornene derivative obtained as described above
A phenolic compound having a structure represented by the general formula (2) (hereinafter, referred to as “specific antioxidant”) is contained. In the general formula (2) , X and Y each represent a hydrogen atom or a hydrocarbon group represented by an alkyl group having 1 to 10 carbon atoms such as a methyl group, an ethyl group, a propyl group, and a butyl group; A hydrogen atom, a hydrocarbon group represented by an alkyl group having 1 to 10 carbon atoms such as a methyl group, an ethyl group, a propyl group, and a butyl group; or a carbon group such as an alkoxy group such as a methoxy group and an ethoxy group and an alkyl ester group. Other organic groups represented by Formulas 1 to 20. the above
Specific examples of the phenolic compound represented by the general formula (2) include 2,6-di-t-butylphenol, and 2,6-di-t-butylphenol.
Examples thereof include di-t-butyl-4-methylphenol, 4-methoxyphenol, and octadecyl-3- (3,5-di-t-butyl-4-hydroxyphenyl) propionate.
【0033】特定の酸化防止剤の含有割合は10〜1
0,000ppmであり、好ましくは20〜1,000
ppmの割合で含有される。10ppm未満である場合
は長期間における保存安定性が不十分となり、一方、1
0,000ppmを超える場合は経済的に不利なばかり
でなく、メタセシス開環重合反応における重合転化率が
却って低下するおそれが生じて好ましくない。The specific antioxidant content is 10 to 1
0.00000 ppm, preferably from 20 to 1,000 ppm.
It is contained in the ratio of ppm. If it is less than 10 ppm, the storage stability over a long period of time will be insufficient.
If it exceeds 000 ppm, not only is it economically disadvantageous, but also the polymerization conversion rate in the metathesis ring-opening polymerization reaction may undesirably decrease, which is not preferable.
【0034】<メタセシス開環重合>既述のノルボルネ
ン誘導体を原料モノマーとしてメタセシス開環重合が行
われ、重合体が生成される。このメタセシス開環重合
は、通常トルエン、キシレンなどの溶媒の存在下におい
て、触媒として (a)WCl6 、MoCl5 、ReOCl3 などのW、
MoおよびReの化合物から選ばれた少なくとも1種
と、(b)n−C4 H9 Li、(C2 H5 )3 Al、
(C2 H5 )2 AlCl、LiHなどのデミングの周期
律表IA族元素、III A族元素の化合物から選ばれた少
なくとも1種との組合せによる混合物などを用いて行わ
れる。このメタセシス開環重合において、さらに、添加
剤としてアルコール類、アルデヒド類などを好適に用い
ることができ、また、分子量調節剤として反応系に共存
させられるα−オレフィン類などをの量を調整すること
によって、目的とする重合体の分子量を制御することが
できる。<Metathesis Ring-Opening Polymerization> Metathesis ring-opening polymerization is carried out using the above-described norbornene derivative as a raw material monomer to produce a polymer. This metathesis ring-opening polymerization is usually carried out in the presence of a solvent such as toluene or xylene as a catalyst by using (a) W such as WCl 6 , MoCl 5 or ReOCl 3 ,
At least one selected from the compounds of Mo and Re, (b) n-C 4 H 9 Li, (C 2 H 5) 3 Al,
(C 2 H 5 ) 2 AlCl, LiH and the like are used as a mixture of at least one selected from compounds of Group IA elements and Group IIIA elements of the Periodic Table of Deming. In this metathesis ring-opening polymerization, further, alcohols, aldehydes, etc. can be suitably used as additives, and the amount of α-olefins, etc., coexisting in the reaction system as a molecular weight regulator is adjusted. Thereby, the molecular weight of the target polymer can be controlled.
【0035】以下、本発明の実施例について説明する
が、本発明がこれらによって限定されるものではない。Hereinafter, embodiments of the present invention will be described, but the present invention is not limited thereto.
【実施例】〔合成例〕 温度180℃、圧力3.5kg/cm2 ・Gに保った内
容積50リットルの撹拌機付の反応器に、定量ポンプを
用いて、メチルメタクリレートと、ジシクロペンタジエ
ンと、上記一般式(4)で表されるビシクロヘプテン誘
導体である5−メチル−5−カルボキシメチル−ビシク
ロ[2.2.1]−2−ヘプテンとの三者を、これらの
モル比が1:1.2:2.4となるよう供給した。EXAMPLES [Synthesis Example] In a reactor equipped with a stirrer having an inner volume of 50 liter and maintained at a temperature of 180 ° C. and a pressure of 3.5 kg / cm 2 · G, methyl methacrylate and dicyclopentadiene were added using a metering pump. And 5-methyl-5-carboxymethyl-bicyclo [2.2.1] -2-heptene, which is a bicycloheptene derivative represented by the general formula (4) , and their molar ratio is 1: 1.2: 2.4 was supplied.
【0036】[0036]
【0037】これら三者の反応器への供給量は、反応器
内における滞留時間が8時間となるように毎時4kgと
した。さらに、重合防止剤として、N,N−ジエチルヒ
ドロキシルアミンと、テトラキス[メチレン−3−
(3’.5’−ジ−t−ブチル−4−ヒドロキシフェニ
ル)プロピオネート]メタンの各々をメチルメタクリレ
ートに溶解して連続的に添加した。各々の添加量は、上
記三者の全供給量に対し300ppmの割合に相当する
量とした。反応器内で得られた反応液を、毎時4kgの
割合で当該反応器から抜き出し、この反応液を、圧力3
0torr、温度105℃に保ったフラッシュタンクに
連続的に供給し、当該反応液中に存在する未反応のメチ
ルメタクリレート、ジシクロペンタジエンおよびビシク
ロヘプテン誘導体の一部を回収した。その後、充填材
「スルザーパッキンBX(住友重機社製)」(以下にお
いて同じ。)が221cmの高さに充填された塔径3イ
ンチの蒸留塔に、前記フラッシュタンクからの缶出液を
連続的に供給し、塔頂圧力5torr、還流比1、塔底
温度145℃の条件で蒸留を行い、前記フラッシュタン
クで回収されなかった未反応のメチルメタクリレート、
ジシクロペンタジエンおよび上記ビシクロヘプテン誘導
体を塔頂から回収すると共に、上記一般式(1)で示さ
れる67重量%の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
センを含有する缶出液を塔底より回収した。The feed rate of these three to the reactor was 4 kg / hour so that the residence time in the reactor was 8 hours. Further, as polymerization inhibitors, N, N-diethylhydroxylamine and tetrakis [methylene-3-
(3′.5′-Di-tert-butyl-4-hydroxyphenyl) propionate] methane was dissolved in methyl methacrylate and added continuously. Each addition amount was an amount corresponding to a ratio of 300 ppm to the total supply amount of the above three. The reaction solution obtained in the reactor was withdrawn from the reactor at a rate of 4 kg per hour, and the reaction solution was subjected to a pressure of 3 kg / h.
The mixture was continuously supplied to a flash tank maintained at 0 torr and a temperature of 105 ° C. to recover a part of unreacted methyl methacrylate, dicyclopentadiene and bicycloheptene derivatives present in the reaction solution. Thereafter, the bottom liquid from the flash tank was continuously fed to a distillation column having a diameter of 3 inches packed with a filler “Sulzer packing BX (manufactured by Sumitomo Heavy Industries, Ltd.)” (the same applies hereinafter) at a height of 221 cm. And distilled under the conditions of a top pressure of 5 torr, a reflux ratio of 1 and a bottom temperature of 145 ° C., and unreacted methyl methacrylate not recovered in the flash tank;
It is recovered dicyclopentadiene and the bicycloheptene derivatives from the top, of 67% by weight represented by the general formula (1) 8-methyl-8-carboxymethyl tetracyclo [4.4.0.1 2, 5. A bottoms containing [ 17,10 ] -3-dodecene was recovered from the bottom of the column.
【0038】[0038]
【0039】上記のようにして回収された未反応のメチ
ルメタクリレート、ジシクロペンタジエンおよびビシク
ロヘプテン誘導体は、いずれも反応器へ循環させて再び
反応に供した。一方、上記缶出液を、蒸留塔径3イン
チ、充填材を119cmの高さに充填した蒸留塔に連続
的に供給し、塔頂圧力2torr、還流比1、塔底温度
160℃で蒸留を行い、塔底より高沸点成分を除去する
と共に、塔頂より86重量%の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−ドデセンを含有する留出液を回収し、当
該留出液を、さらに塔径3インチ、充填材を340cm
の高さに充填した蒸留塔に連続的に供給し、塔頂圧力2
torr、還流比10、塔底温度150℃で蒸留を行
い、塔頂よりトリシクロペンタジエン留分を回収すると
共に、塔底の蒸気相より純度99.7重量%の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−ドデセンを得、凝縮させて窒素
シール下の容器へ導入した。The unreacted methyl methacrylate, dicyclopentadiene and bicycloheptene derivatives recovered as described above were all circulated to the reactor and used again. On the other hand, the bottom liquid was continuously supplied to a distillation column having a distillation column diameter of 3 inches and a packing material packed at a height of 119 cm, and distillation was performed at a top pressure of 2 torr, a reflux ratio of 1, and a bottom temperature of 160 ° C. The high boiling point component was removed from the bottom of the column, and 86% by weight of 8-methyl-8-carboxymethyltetracyclo [4.4.0.1 2,5 .
The distillate containing the 1,7,10 ] -3-dodecene was recovered, and the distillate was further subjected to a column diameter of 3 inches and a packing material of 340 cm.
To a distillation column packed at a height of
Distillation was carried out at torr, a reflux ratio of 10, and a bottom temperature of 150 ° C., and a tricyclopentadiene fraction was recovered from the top of the column, and 8-methyl-8-carboxymethyl having a purity of 99.7% by weight was obtained from the vapor phase at the bottom of the column. Tetracyclo [4.4.0.
12.5 . 1 7,10 ] -3-dodecene was obtained, condensed and introduced into a vessel under a nitrogen blanket.
【0040】実施例1 上述の合成例で得られた純度99.7重量%の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−ドデセンの一部を窒素シール下
の撹拌機付のフラスコに移し、酸化防止剤としての4−
メトキシフェノールを、当該8−メチル−8−カルボキ
シメチルテトラシクロ[4.4.0.1 2,5 .17,10]
−3−ドデセンに対し100ppmの割合に相当する量
だけ添加し、撹拌して均一化させ、重合用原料Aを得
た。Example 1 8-methyl-2-methylbenzene having a purity of 99.7% by weight obtained in the above synthesis example.
Ru-8-carboxymethyltetracyclo [4.4.0.
12,5. 17,10] -3-Part of dodecene under nitrogen seal
To a flask equipped with a stirrer, and
Methoxyphenol is converted to the 8-methyl-8-carboxy
Cimethyltetracyclo [4.4.0.1 2,5. 17,10]
-3- The amount corresponding to 100 ppm relative to dodecene
And then homogenize by stirring to obtain a raw material A for polymerization.
Was.
【0041】実施例2 上述の合成例で得られた純度99.7重量%の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−ドデセンの一部を窒素シール下
の撹拌機付のフラスコに移し、酸化防止剤としての2,
6−ジ−t−ブチル−4−メチルフェノールを、当該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−ドデセンに対し100
ppmの割合に相当する量だけ添加し、撹拌して均一化
させ、重合用原料Bを得た。Example 2 8-methyl-8-carboxymethyltetracyclo [4.4.0.9% by weight obtained in the above synthesis example and having a purity of 99.7% by weight.
12.5 . 1 7,10 ] -3-Dodecene was transferred to a flask equipped with a stirrer under a nitrogen blanket,
6-di-t-butyl-4-methylphenol is converted to 8
-Methyl-8-carboxymethyltetracyclo [4.
4.0.1 2,5 . 1 7,10 ] -3-100 against dodecene
The raw material for polymerization B was obtained by adding an amount corresponding to the ratio of ppm and stirring to homogenize.
【0042】比較例1 上述の合成例で得られた純度99.7重量%の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−ドデセンの一部を窒素シール下
の撹拌機付のフラスコに移し、酸化防止剤を添加せず
に、重合用原料Cを得た。Comparative Example 1 8-methyl-8-carboxymethyltetracyclo [4.4.0.% Having a purity of 99.7% by weight and obtained in the above synthesis example.
12.5 . A portion of [ 17,10 ] -3-dodecene was transferred to a flask equipped with a stirrer under a nitrogen seal, and a raw material C for polymerization was obtained without adding an antioxidant.
【0043】比較例2 上述の合成例で得られた純度99.7重量%の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−ドデセンの一部を窒素シール下
の撹拌機付のフラスコに移し、酸化防止剤としてのハイ
ドロキノンを、当該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
デセンに対し100ppmの割合に相当する量だけ添加
し、撹拌して均一化させ、重合用原料Dを得た。Comparative Example 2 8-methyl-8-carboxymethyltetracyclo [4.4.0.
12.5 . A portion of the 1,7,10 ] -3-dodecene was transferred to a flask equipped with a stirrer under a nitrogen seal, and hydroquinone as an antioxidant was added to the 8-methyl-8-carboxymethyltetracyclo [4.4.0]. .1 2,5 . 1 7,10 ] -3-Dodecene was added in an amount corresponding to 100 ppm, and the mixture was stirred to homogenize, thereby obtaining a raw material D for polymerization.
【0044】比較例3 上述の合成例で得られた純度99.7重量%の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−ドデセンの一部を窒素シール下
の撹拌機付のフラスコに移し、酸化防止剤としての4−
メトキシフェノールを、当該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−ドデセンに対し12,000ppmの割合に相当
する量だけ添加し、撹拌して均一化させ、重合用原料E
を得た。Comparative Example 3 8-methyl-8-carboxymethyltetracyclo [4.4.0.
12.5 . 1 7,10 ] -3-Dodecene was transferred to a flask equipped with a stirrer under a blanket of nitrogen, and 4-dodecene was used as an antioxidant.
Methoxyphenol is converted to the 8-methyl-8-carboxymethyltetracyclo [4.4.0.1 2,5 . 1 7,10 ]
-3-Dodecene was added in an amount corresponding to a ratio of 12,000 ppm, and the mixture was stirred to be homogenized.
I got
【0045】上記実施例1〜2ならびに比較例1〜3で
得られた重合用原料について、色相評価およびメタセシ
ス開環重合反応における重合転化率の測定を行った。以
下、具体的に説明する。With respect to the raw materials for polymerization obtained in Examples 1 and 2 and Comparative Examples 1 to 3, the hue was evaluated and the polymerization conversion in the metathesis ring-opening polymerization reaction was measured. Hereinafter, a specific description will be given.
【0046】<試験> ・色相評価 実施例1で得られた重合用原料Aについて、目視により
色相観察をおこない、評価した。結果を表1に示す。 ・メタセシス開環重合 上記重合用原料A80gと、水分が5ppmの割合で含
有されるトルエン240gと、分子量調節剤である1−
ヘキセン5.8gと、濃度0.96モル/リットルのジ
エチルアルミニウムクロライドのトルエン溶液1.4g
とを、窒素によりシールされた撹拌機付のフラスコに仕
込み、80℃まで昇温した後、濃度0.05モル/リッ
トルの六塩化タングステンのトルエン溶液1.4gを仕
込んで3時間メタセシス開環重合を行った。 ・重合転化率の測定 上記メタセシス開環重合により得られた重合反応液につ
いてガスクロマトグラフィー分析を行い、メタセシス開
環重合反応における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
デセンの重合転化率を測定した。結果を表1に示す。<Test> Evaluation of Hue The raw material A for polymerization obtained in Example 1 was evaluated by visually observing the hue. Table 1 shows the results. -Metathesis ring-opening polymerization 80 g of the raw material for polymerization A, 240 g of toluene containing 5 ppm of water, and 1- being a molecular weight regulator
5.8 g of hexene and 1.4 g of a toluene solution of diethylaluminum chloride having a concentration of 0.96 mol / l.
Was charged into a flask equipped with a stirrer sealed with nitrogen, heated to 80 ° C., and charged with 1.4 g of a toluene solution of tungsten hexachloride having a concentration of 0.05 mol / l for 3 hours for metathesis ring-opening polymerization. Was done. -Measurement of polymerization conversion The gas chromatography analysis was performed on the polymerization reaction solution obtained by the above-mentioned metathesis ring-opening polymerization, and 8-methyl-8-carboxymethyltetracyclo [4.4.0.1 in the metathesis ring-opening polymerization reaction was performed. 2,5 . The polymerization conversion of 1,7,10 ] -3-dodecene was measured. Table 1 shows the results.
【0047】<試験> ・重合用原料の保存 実施例1で得られた重合用原料Aを、50℃の恒温室内
に30日間保存した。 ・色相評価 この重合用原料Aについて、試験と同様にして色相評
価を行った。結果を表1に示す。 ・メタセシス開環重合 この重合用原料Aを用い、試験と同様にしてメタセシ
ス開環重合を行った。 ・重合転化率の測定 上記メタセシス開環重合により得られた重合反応液につ
いて、試験と同様にして分析を行い、重合転化率を測
定した。結果を表1に示す。<Test> Storage of Polymerization Raw Material The polymerization raw material A obtained in Example 1 was stored in a constant temperature room at 50 ° C. for 30 days. -Hue evaluation About this raw material A for polymerization, hue evaluation was performed like the test. Table 1 shows the results. -Metathesis ring-opening polymerization Using this raw material A for polymerization, metathesis ring-opening polymerization was carried out in the same manner as in the test. -Measurement of polymerization conversion The polymerization reaction solution obtained by the metathesis ring-opening polymerization was analyzed in the same manner as in the test, and the polymerization conversion was measured. Table 1 shows the results.
【0048】<試験〜試験>重合用原料B〜重合用
原料Eの各々について、試験と同様にして、保存し、
その後色相評価を行い、さらにメタセシス開環重合およ
び重合転化率の測定を行った。結果を表1に示す。<Test to Test> Each of the raw materials for polymerization B to E was stored in the same manner as in the test.
Thereafter, the hue was evaluated, and the metathesis ring-opening polymerization and the polymerization conversion were measured. Table 1 shows the results.
【0049】[0049]
【表1】 [Table 1]
【0050】以上の結果から明らかなように、特定の酸
化防止剤が特定の割合で含有された実施例1および実施
例2に係る本発明のノルボルネン誘導体組成物は、30
日間の保存の前後において色相に変化がみられず、しか
も、当該ノルボルネン誘導体組成物を30日間保存した
後にメタセシス開環重合のための原料として用いた場合
にも、メタセシス開環重合反応における重合転化率が9
8.0%程度と十分に高く、他の酸化防止剤を用いた場
合のように重合転化率の低下を招くことがない。As is clear from the above results, the norbornene derivative compositions of the present invention according to Examples 1 and 2 containing a specific antioxidant at a specific ratio are 30%.
No change in hue was observed before and after storage for a period of days, and when the norbornene derivative composition was used as a raw material for metathesis ring-opening polymerization after storage for 30 days, the polymerization conversion in the metathesis ring-opening polymerization reaction was also observed. Rate 9
It is sufficiently high at about 8.0%, and does not cause a decrease in polymerization conversion unlike the case where another antioxidant is used.
【0051】[0051]
【発明の効果】本発明のメタセシス開環重合用ノルボル
ネン誘導体組成物には特定の酸化防止剤が特定の割合で
含有されるため、保存安定性に優れ、従って、当該ノル
ボルネン誘導体組成物は、長期間が経過した後において
も、メタセシス開環重合反応における重合転化率が十分
に高いため、長期間の保存が可能である。従って、優れ
た光学特性を有する透明樹脂の原料として好適に用いる
ことができる。The norbornene derivative composition for metathesis ring-opening polymerization of the present invention contains a specific antioxidant in a specific ratio, and thus has excellent storage stability. Even after the elapse of the period, the polymerization conversion in the metathesis ring-opening polymerization reaction is sufficiently high, so that long-term storage is possible. Therefore, it can be suitably used as a raw material for a transparent resin having excellent optical properties.
フロントページの続き (56)参考文献 特開 平1−149738(JP,A) 特開 平5−262822(JP,A) (58)調査した分野(Int.Cl.7,DB名) C08G 61/06 - 61/08 C08L 65/00 Continuation of front page (56) References JP-A-1-149738 (JP, A) JP-A-5-262822 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) C08G 61 / 06-61/08 C08L 65/00
Claims (1)
ン誘導体と、含有割合が10〜10,000ppmであ
る下記一般式(2)で表されるフェノール系化合物とよ
りなることを特徴とするメタセシス開環重合用ノルボル
ネン誘導体組成物。 【化1】 【化2】 (式中、X、Yは水素原子または炭素数1〜10の炭化
水素基であり、Zは水素原子、炭素数1〜10の炭化水
素基または炭素数1〜20の有機基(炭素数1〜10の
炭化水素基を除く。)である。)1. A composition comprising a norbornene derivative represented by the following general formula (1) and a phenolic compound represented by the following general formula (2) having a content of 10 to 10,000 ppm. Norbornene derivative composition for metathesis ring-opening polymerization. Embedded image Embedded image (In the formula , X and Y are a hydrogen atom or a hydrocarbon group having 1 to 10 carbon atoms, and Z is a hydrogen atom, a hydrocarbon group having 1 to 10 carbon atoms or an organic group having 1 to 20 carbon atoms (1 carbon atom) Excluding hydrocarbon groups of 10 to 10.)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP34571593A JP3259498B2 (en) | 1993-12-22 | 1993-12-22 | Norbornene derivative compositions for metathesis ring-opening polymerization |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP34571593A JP3259498B2 (en) | 1993-12-22 | 1993-12-22 | Norbornene derivative compositions for metathesis ring-opening polymerization |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH07179730A JPH07179730A (en) | 1995-07-18 |
| JP3259498B2 true JP3259498B2 (en) | 2002-02-25 |
Family
ID=18378475
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP34571593A Expired - Lifetime JP3259498B2 (en) | 1993-12-22 | 1993-12-22 | Norbornene derivative compositions for metathesis ring-opening polymerization |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3259498B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100938046B1 (en) * | 2005-07-22 | 2010-01-21 | 제이에스알 가부시끼가이샤 | Cyclic olefin ring-opening copolymer and its use, and method for producing retardation plate comprising the copolymer |
| EP1931746B1 (en) * | 2005-09-12 | 2013-09-04 | FujiFilm Electronic Materials USA, Inc. | Additives to prevent degradation of cyclic alkene derivatives |
| JP2009507834A (en) * | 2005-09-12 | 2009-02-26 | フジフィルム・エレクトロニック・マテリアルズ・ユーエスエイ・インコーポレイテッド | Additives that prevent degradation of cyclic alkene derivatives |
-
1993
- 1993-12-22 JP JP34571593A patent/JP3259498B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH07179730A (en) | 1995-07-18 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Lewis et al. | Copolymerization. IX. A Comparison of Some cis and trans Isomers1, 2 | |
| Nugent et al. | Cyclization of diacetylenes to E, E exocyclic dienes. Complementary procedures based on titanium and zirconium reagents | |
| US4899005A (en) | Method for preparing cycloolefin copolymers with improved heat stability | |
| JP3259498B2 (en) | Norbornene derivative compositions for metathesis ring-opening polymerization | |
| Wegener et al. | New ladder polymers via repetitive Diels-Alder reaction under high pressure | |
| Feast et al. | Metathesis polymerization of 1, 7, 7-trimethylbicyclo [2.2. 1] hept-2-ene using a well defined molybdenum initiator | |
| US4994426A (en) | Catalyst and process for polymerization of norbornene derivatives | |
| JP3106811B2 (en) | Method for purifying cyclic olefin ring-opened polymer | |
| JPH07173085A (en) | Tetracyclododecene derivative composition | |
| JP4503901B2 (en) | Continuous process for the production of tetracyclododecenes | |
| JP2622186B2 (en) | Organic silicon compound distillation method | |
| JP4471322B2 (en) | Continuous process for the production of tetracyclododecenes | |
| US3651112A (en) | Polymeric organo aluminum substances | |
| US20240109984A1 (en) | Catalysts for Olefin Metathesis, Methods of Preparation, and Processes for the use Thereof | |
| WO2000001742A1 (en) | Tetracyclododecene compositions and process for producing the same | |
| Cheng et al. | Synthesis of precision poly (1, 3‐bicyclo [1.1. 1] pentane alkylene) s via acyclic diene metathesis polymerization | |
| bin Alimuniar et al. | Stereoregular fluoropolymers: 1. The ring opening polymerization of 2, 3-bis (trifluoromethyl) bicyclo-[2.2. 1] hepta-2, 5-diene | |
| DE10015452A1 (en) | Processes for the polymerization of polar substituted cycloalkenes, useful for optical applications, are carried out in the presence of at least one tungsten carbyne and/or molybdenum carbyne complex. | |
| EP4227327A1 (en) | An olefin metathesis polymerization catalyst system and curable compositions containing the catalyst system | |
| EP0307041B1 (en) | Sterically hindered amino compounds and processes for their preparation | |
| US4980477A (en) | Sterically hindered 4-oxy-methylene[2-(norborn-5-enyl)]-2,2,6,6-tetramethyl N-substituted-piperidine derivatives | |
| JP2000026328A (en) | Tetracyclododecene composition | |
| JPH05112474A (en) | Production of compound having norbornene ring | |
| JP2019089714A (en) | Process for producing fluorine-containing cyclic olefin monomer | |
| JP2000026329A (en) | Tetracyclododecene composition |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20011113 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20081214 Year of fee payment: 7 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20091214 Year of fee payment: 8 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20091214 Year of fee payment: 8 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20091214 Year of fee payment: 8 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20101214 Year of fee payment: 9 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20101214 Year of fee payment: 9 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20111214 Year of fee payment: 10 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20111214 Year of fee payment: 10 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20121214 Year of fee payment: 11 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20121214 Year of fee payment: 11 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20131214 Year of fee payment: 12 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| EXPY | Cancellation because of completion of term |