JPS5941326A - Polymer having excellent rigidity - Google Patents
Polymer having excellent rigidityInfo
- Publication number
- JPS5941326A JPS5941326A JP15211182A JP15211182A JPS5941326A JP S5941326 A JPS5941326 A JP S5941326A JP 15211182 A JP15211182 A JP 15211182A JP 15211182 A JP15211182 A JP 15211182A JP S5941326 A JPS5941326 A JP S5941326A
- Authority
- JP
- Japan
- Prior art keywords
- polymer
- ring
- norbornene
- formula
- added
- 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.)
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- Polyoxymethylene Polymers And Polymers With Carbon-To-Carbon Bonds (AREA)
Abstract
Description
【発明の詳細な説明】
技術分野
本発明は重自体主鎖中に五員環と二重結合を持った剛性
や剪断強度等の機椋的特性に優れしかも耐熱レベルの高
い重合イ4に関する。DETAILED DESCRIPTION OF THE INVENTION Technical Field The present invention relates to a polymer 4 having a five-membered ring and a double bond in its main chain, which has excellent mechanical properties such as rigidity and shear strength, and has a high level of heat resistance.
現在、石油化学工業においては、ナフサの分解後+のう
ち展索数5のC5留分はほとんど利用されておらず、わ
ずかにインプレンが合成ゴム原料として工業的に利用さ
れているにすぎなく、その大半は燃料として消費されて
いる1、先行技術
これらC5留分の中で最も含有量が多いのはシクロペン
タジェンであり、この7クロペンタジエンは反応性が高
いためシクロペンテンあるいは、ノルボルネン誘導体な
どの新規な高付加価値製品としての利用展囲が期待でき
るものである。Currently, in the petrochemical industry, the C5 fraction with an extrusion number of 5 is hardly used after decomposition of naphtha, and only a small amount of imprene is used industrially as a raw material for synthetic rubber. Most of it is consumed as fuel1.Prior Art Among these C5 fractions, the highest content is cyclopentadiene, and this 7-clopentadiene is highly reactive, so it can be used as cyclopentene or norbornene derivatives. It is expected that it will be used extensively as a new high value-added product.
なかでもノルボルネン誘導体をモノマーとしてメタセン
ス触媒により開環重合させた重合体は、新規なエンジニ
アリングプラスチックトシて興味gHい。Among these, polymers produced by ring-opening polymerization using a norbornene derivative as a monomer using a metasense catalyst are of interest as novel engineering plastics.
十νにシクロペンタジェンとアクリル酸をディールス・
アルダ−反応させた5−ノルボルネン−2−カルボン酸
の開環重合体は耐熱性の旨いエンジニアリングプラスチ
ックとなる可能性をイ]するが、強い極性のために開環
重合しない。Diels cyclopentadiene and acrylic acid in ten ν
Alder-reacted ring-opening polymers of 5-norbornene-2-carboxylic acid have the potential to become good heat-resistant engineering plastics, but due to their strong polarity, ring-opening polymerization does not occur.
そこで特開昭56−65018は、ノルボルネン誘導体
をニスデル化合物としておき、これを開環重合させた移
加水分解し目的とする5−ノルボルネン−2−カルボン
re #f5m体の開環重合体を得る方法を提案してい
る。この重合体は剛性が高くかつ耐価撃性、耐熱性のバ
ランスに優れた樹脂であるが、ハウジング分野・構造材
分野等では、樹脂単体としての剛性・耐熱性の向上が望
まれている。Therefore, Japanese Patent Application Laid-Open No. 56-65018 discloses a method for obtaining a target ring-opening polymer of 5-norbornene-2-carboxylic compound re #f5m by ring-opening polymerization and transfer hydrolysis of a norbornene derivative as a Nisder compound. is proposed. This polymer is a resin with high rigidity and an excellent balance of impact resistance and heat resistance, but in the housing field, structural material field, etc., it is desired to improve the rigidity and heat resistance of the resin alone.
そこで本発明者らは、樹脂の製造研ダヒをさらに一歩進
めることによって上記の様な侠求に対応した樹脂を開発
するに至った。Therefore, the inventors of the present invention have developed a resin that meets the above-mentioned demands by taking the manufacturing research of the resin one step further.
(Ill 発明の概要
要旨
(1)下記の一穀式
で表わされる構成単位(A)と
で表わされる構成単位ω)とから基本的に構成され(但
し、丁(1は水素原子、アルギル基またはフェニル基を
、■ζ2は水素原子またはアルキル基を、R3はアルキ
ルノ、(を表わす。)、かつ次記の(a)〜(c)の要
件を具備する重合体(a)極限粘度が0.3〜4.0で
あること。(Ill Summary of the Invention (1) The structural unit (A) represented by the following monograin formula and the structural unit ω) (provided that 1 is a hydrogen atom, an argyl group, or a phenyl group, ■ζ2 is a hydrogen atom or an alkyl group, R3 is an alkyl group, and (a) a polymer that satisfies the following requirements (a) to (c): (a) has an intrinsic viscosity of 0. Must be between 3 and 4.0.
(b)十6己構成4i位(4)の含有刊が全構成単位中
の90〜100重154%であること。(b) The content of the 16th constituent 4i (4) is 90 to 100 weight 154% of the total constituent units.
(c+#成単位CA)および(B)における二重結合の
トランス含有ばか40%以上であること。The trans content of double bonds in (c+# component CA) and (B) must be 40% or more.
このような構造を有する開環重合体は、従来の汎用エン
ジニアリングでは到達し得ながった高い剛性レベルを述
成し、特に、剪1+f[強度に優れタッピング等の機械
作業性に浚れだ樹脂材料をイiすることができる。Ring-opened polymers with such a structure achieve a high level of rigidity that could not be achieved with conventional general-purpose engineering, and are particularly effective at shearing (1+f) [excellent strength and ease of mechanical work such as tapping]. Resin materials can be used.
1’lll’l 発明の詳細な説明
重合体
本発明の重合体は
で表わされるJIlν成牟位(A)と
で表わされる4t4成単位(13)とから、J+1本的
に構成される重合体であり、上n1ル中R1は水素原子
、炭素数1〜20、好ましくは1〜8のアルキル基また
はフェニル基を、好ましくは水素原子−またはアルキル
基を、R2け水素原子またはR1と同じもしくは異なる
アルギル基を、lえa f#:t R1と同じもしくは
異なるアルキル基を表わすものであり、これら重合体の
剛性、成形性を保持するためには極限粘度が0.3〜4
.()、特に好ましくは0.4〜3.()を会すること
が必振である。極限粘度が0.3未満であれば耐熱性・
剛性・llllI価!1層性が悪く、接眼粘度が4.(
)を越えれば成Jk性が悪化する。1'lll'l Detailed Description of the Invention Polymer The polymer of the present invention is a polymer composed of J+1 units from the JIlν component (A) represented by and the 4t4 component (13) represented by In the above n1, R1 is a hydrogen atom, an alkyl group having 1 to 20 carbon atoms, preferably 1 to 8, or a phenyl group, preferably a hydrogen atom or an alkyl group, and R2 is a hydrogen atom or the same as R1 or Different argyl groups are the same as or different from t R1, and in order to maintain the rigidity and moldability of these polymers, the intrinsic viscosity is 0.3 to 4.
.. (), particularly preferably 0.4 to 3. It is essential to meet (). If the intrinsic viscosity is less than 0.3, the heat resistance
Rigidity/llllI value! One-layer property is poor and ocular viscosity is 4. (
), the quality of JK will deteriorate.
また、上11ニ一般式中41・]成t4i イ)’t
(A)の含有相は全構成単位中の90〜100止M%で
あることが必要である。上記構成単位■の含扇が90重
−B3%未満では剛トド及び剪[υ1仙度のレベルが不
足し、かつ耐熱性のレベルが低下する。Also, in the general formula 11 above, 41.
It is necessary that the phase containing (A) is 90 to 100 M% of the total structural units. If the content of the above-mentioned structural unit (2) is less than 90% by weight and 3% by weight, the level of stiffness and shear [υ1sensity] will be insufficient, and the level of heat resistance will decrease.
さらに、上記構成単位(4)および(B)における二重
結合のトランス含有址が40%以上であることが必要で
ある。トランス型が40%未満では耐熱性および剛性が
態化する。Furthermore, it is necessary that the trans content of double bonds in the structural units (4) and (B) be 40% or more. If the transformer type is less than 40%, heat resistance and rigidity will deteriorate.
11′X合体の製法
本発明で用いられる5−ノルボルネン−2−カルボン酸
エステル誘導体は、一般にシクロペンタジェンとアクリ
ル酸ニスデルKg L”Z体又はα−アルキル装(央ア
クリル酸エステル訪導体とをディールス・アルダ−反応
させて合成される。The 5-norbornene-2-carboxylic acid ester derivative used in the present invention is generally prepared by combining cyclopentadiene and Nisdel acrylate Kg L''Z form or α-alkyl group (center acrylic acid ester visiting conductor). Synthesized by Diels-Alder reaction.
これらエステル基を有するノルボルネン訪導体モノマー
、例えば5−ノルボルネン−2−カルボン酸メチル、5
−ノルボルネン−2,2−カルボン酸メチル、5−ノル
ボルネン−2−カルボン酸エチル、5−ノルボルネン−
2−カルボン師オクチル等は、さらに特開昭49−77
999号明細書などに記載されるメタセシス触媒により
容易に開環重合する。Norbornene-conductor monomers having these ester groups, such as methyl 5-norbornene-2-carboxylate, 5
-Methyl norbornene-2,2-carboxylate, Ethyl 5-norbornene-2-carboxylate, 5-norbornene-
2-Carbonist octyl etc. are further disclosed in Japanese Patent Application Laid-Open No. 1983-1977.
Ring-opening polymerization can be easily carried out using a metathesis catalyst described in Japanese Patent No. 999, etc.
メタセシス触媒としては、通常タングステン又はモリブ
テン化合物が遷移金属成分として用いられ、特に、タン
グステン化合物は活性が高いので好ましい。中でもタン
グステンのハロゲン化合物が好適である。有機アルミニ
ウム成分は特に制限がなく、例えばトリエチルアルミニ
ウム、ジエチルアルミニウムモノクロライド、エチルア
ルミニウム士スキクロライドが用いられる。第3成分柚
としくヲ−11、アルコールの様な酸素系配位子、ピリ
ジンの様なチソ累系配位子、トリフェニルホスフィンの
様なリン系配付子が用いられる。As a metathesis catalyst, a tungsten or molybdenum compound is usually used as a transition metal component, and a tungsten compound is particularly preferred because of its high activity. Among these, tungsten halogen compounds are preferred. The organoaluminum component is not particularly limited, and for example, triethylaluminum, diethylaluminum monochloride, and ethylaluminum monochloride are used. As the third component, an oxygen-based ligand such as alcohol, a thiiso-based ligand such as pyridine, and a phosphorus-based ligand such as triphenylphosphine are used.
溶媒としては、ハロゲン化炭化水素、芳香族系炭化水素
、ハロゲン化芳香族炭化水素が用いられるが、’NFに
トルエンの様な芳香族炭化水素、クロルベンゼンの様な
ハロゲン化芳香族炭化水素が高トランス含量体を得るの
に適している。As the solvent, halogenated hydrocarbons, aromatic hydrocarbons, and halogenated aromatic hydrocarbons are used. Suitable for obtaining products with high trans content.
重合圧力は大気Eで充分であり、特に加圧下で重合を行
なうこともできる。Atmospheric pressure E is sufficient for the polymerization pressure, and the polymerization can also be carried out under increased pressure.
重合湯度(d、−2(1℃から70℃の範囲で用いられ
るが、温度が低くすぎると活性が著しく低下し、温度が
高すぎるとトランス含量が低下し、目的物は得られない
。したがってo℃〜40℃位の幅での選択が好まI7い
。Polymerization temperature (d, -2) is used in the range of 1°C to 70°C, but if the temperature is too low, the activity will drop significantly, and if the temperature is too high, the trans content will drop, making it impossible to obtain the desired product. Therefore, it is preferable to select within a range of about 0°C to 40°C.
目的とするトランス含有縫40%以上のIji4 項M
1合体をaするにけ、モノマーに対する剛(媒の址を多
くし、■11合専i庶を低温に保持し、あるいは、第3
成分種としてアルコール系やチッ素系の配イ+’(子を
選択する笠によって可能である。Target Iji4 Item M with 40% or more transformer-containing stitches
In order to carry out the first coalescence, increase the amount of stiffness (medium) for the monomer, (1) keep the coalescence at a low temperature, or
Alcohol-based or nitrogen-based combinations can be used as component types (depending on the type of cap selected).
開環重合[7て得られた重合体は、
(但し、1り]け水素原子、アルキル基またはフェニル
基を、R2は水素原子またはアルキル基を、R3はアル
キル基を表わす。)
で表わされる繰返し単位から構成される5−ノルボルネ
ン−2−カルボン酸エステル誘導体の開環重合体で、極
限粘度は0,4〜4.0のものが好ましい。The polymer obtained by ring-opening polymerization [7] is represented by (where 1 is a hydrogen atom, an alkyl group, or a phenyl group, R2 is a hydrogen atom or an alkyl group, and R3 is an alkyl group). It is a ring-opening polymer of a 5-norbornene-2-carboxylic acid ester derivative composed of repeating units, and preferably has an intrinsic viscosity of 0.4 to 4.0.
しかしながらこの開環重合体自体はニスデル1u換体で
あるために耐熱性は低く、耐熱性樹脂としては実用に供
さない。However, since this ring-opened polymer itself is a Nisdel 1U conversion product, its heat resistance is low and it cannot be used practically as a heat-resistant resin.
従って、こうしてイ44られだ開環重合体はエステル基
の加水分解処理に付される。Therefore, in this way, the ring-opened polymer of I44 is subjected to a hydrolysis treatment of the ester groups.
加水分解処理に肋に制限+jないが、次に示す方法が工
業的に不利である。Although there are no limitations to the hydrolysis treatment, the following method is industrially disadvantageous.
開演重合体の溶解
前記エステルEW ヲ有−する5−ノルポルイン−2−
カルボン酸エステルの開環重合体をケトノ類、テトラヒ
ドロフラン、ジオキサン、ジメチルホルムアミド
性有機溶媒を用いることによって溶解する。これら有機
溶媒は前記開演重合体を溶解[7、かつ水ど相溶性の廟
槻溶媒であり、これらの有機溶媒を使用することにより
、後記開演重合体を工業的に有利に加水分h・rを行う
ことができる。Dissolution of the starting polymer The ester EW has 5-norpolyne-2-
A ring-opening polymer of a carboxylic acid ester is dissolved by using a ketone, tetrahydrofuran, dioxane, or dimethylformamide organic solvent. These organic solvents dissolve the opening polymer [7] and are compatible with water, and by using these organic solvents, the opening polymer described below can be industrially advantageously hydrolyzed (h/r). It can be performed.
これら有機溶媒の使用h1は、前記開演重合体の種類・
粘度によって異なるが、lL合合体1址址に対し、5〜
50重hj部加えることが一般的である。この程度の旬
を加えることによって均一a液とすることができる。The use h1 of these organic solvents depends on the type of polymer and
Although it varies depending on the viscosity, 5 to 5
It is common to add 50 hj parts. By adding this amount of seasoning, a uniform a liquid can be obtained.
第一段加水分解
次いで開環重合体中のエステル基単位1モルに対し、0
.92〜3モルのアルカリを有機溶媒100重針部に対
し、10〜100重吐部の水に溶解はせ、これを開項重
合体浴蔽に逐次添加し、エステル基の加水分解を行なう
。After the first stage hydrolysis, 0% per mole of ester group units in the ring-opening polymer.
.. 92 to 3 moles of alkali is dissolved in 10 to 100 parts of water per 100 parts of organic solvent, and this is successively added to the polymer bath to effect hydrolysis of the ester groups.
使用されるアルノノリとしては、アルカリ金属又はアル
カリ土類金属との水酸化物及びこれ等の弱酸との塩が用
いられるが、これらアルカリの中で特にアルカリ金属の
水酸化物である水酸化ナトリウム、水酸化カリウム、水
酸化リチウム及び弱酸との塩である炭酸ナトリウム、酢
酸ナトリウム、酢酸カリウム、炭酸カリウムが好ましい
。As the arunonori used, hydroxides of alkali metals or alkaline earth metals and salts of these with weak acids are used, and among these alkalis, sodium hydroxide, which is a hydroxide of alkali metals, is particularly used. Potassium hydroxide, lithium hydroxide, and salts with weak acids such as sodium carbonate, sodium acetate, potassium acetate, and potassium carbonate are preferred.
使用されるアルカリの址は、開環重合体中のエステル基
ユニット1モルに対し第一段と第二段の加水分解工程を
合わせて帆92モル以上必要である。アルカリの添加は
第一段の加水分解工程で全量加えてもよいし、第一段と
第二段に分割して添加してもよい。しかし第一段の加水
分解工程では、エステル基に対してアルカリを0.35
モル以上使用するのが望ま(−い。The amount of alkali used is required to be 92 moles or more in total for the first and second hydrolysis steps per mole of ester group unit in the ring-opening polymer. The alkali may be added in its entirety in the first stage hydrolysis step, or may be added in divided amounts in the first stage and second stage. However, in the first hydrolysis step, 0.35% alkali was added to the ester group.
It is desirable to use more than mol.
0.35モル未満では加水分解率が低くなり、第二段の
加水分解処理の際に開環重合体を水に俗解しか1rくな
る。If it is less than 0.35 mol, the hydrolysis rate will be low, and the ring-opened polymer will be dissolved into water for only 1r during the second-stage hydrolysis treatment.
アルカリは、水溶液として添加するのが一般的であるが
、アルカリの鵬庶は特に制限はなく、水の使用知が前述
の有(i’4m媒と水との比のさ・iχ囲にあればよい
。Alkali is generally added as an aqueous solution, but there are no particular restrictions on the amount of alkali. Bye.
加水分解温度は40〜200 ℃までの間で任意である
が、50〜80℃で充分に進行する。Although the hydrolysis temperature is arbitrary between 40 and 200°C, the hydrolysis proceeds satisfactorily at 50 to 80°C.
反[Cスが進行すると反応系はIJi環重環体合体出し
て不均一となってくる。As anti-[C] progresses, the reaction system becomes heterogeneous as IJi ring polycycles coalesce.
第二段加水分解
反応系が不均一になったところで、水またはアルカリ水
fd敢を添加する。加熱して有機浩剤を留去しながら添
加してもよいし、壕だ留去せずに直接添加してもよい。When the second stage hydrolysis reaction system becomes non-uniform, water or alkaline water is added. The organic bulking agent may be added while being heated to distill it off, or it may be added directly without distilling it off.
添加する水の量は最低重合体1重置部に対し、31!1
諺部以上必要である。これ以下であると水またはアルカ
リ水溶液を加えても均−k)液にはならない。壕だ有機
溶4vが留去されていない系では第一段加水汁解時に加
えた水との合計量が仕込まれた有+、・メ溶媒に対して
等(辻以−F必要である。The amount of water to be added is at least 31!1 per part of polymer.
More than just a proverb is necessary. If it is less than this, even if water or aqueous alkaline solution is added, it will not become a homogeneous solution. In a system in which 4v of organic solution has not been distilled off, the total amount of water added during the first-stage hydrolyzate decomposition must be equal to the amount of water added, etc. (Tsuji I-F).
加水分解温度は、第一段加水分解と同一範囲であれば、
lトνに問題ない。If the hydrolysis temperature is in the same range as the first stage hydrolysis,
There is no problem with l and v.
、中 和
ついで開狽重合体中のカルボン酸塩を酸を加えることに
よりカルボン酸基に変え、生成物を沈殿として(47る
。酸成分としては、塩酸又は硝酸・酢r夜・硫酸等一般
の酸であれば充分であり、その添加用はカルボン酸塩に
対し1〜10当りである。用いる酸の濃度には鳴に限定
はない1゜生成物をスラリーとして得るには、招件下、
特に高速攪拌下でカルボン酸塩に対し、酸を()、2〜
()、7当惟、好ましくは帆4〜0.6当世入れ、その
まま約0.5〜3時間ti拝し、その後残りの酸成分を
徐々に添加すると良好な粉末状となる。After neutralization, the carboxylic acid salt in the opened polymer is converted into a carboxylic acid group by adding an acid, and the product is precipitated (47). An acid of 1° to 10 parts per carboxylate is sufficient, and the concentration of the acid used is not limited to 1° to obtain the product as a slurry. ,
Especially for carboxylic acid salts under high-speed stirring, acid (), 2~
(), 7 hours, preferably 4 to 0.6 hours, stir as is for about 0.5 to 3 hours, and then gradually add the remaining acid component to form a good powder.
この中和反応で、所定量の酸成分を一度に系中に添加す
ると、中和は可能となるがアルカリ残置が増加し、生成
qをノの汝、動性は低下しかつ着色しゃすいっ
分析・物性測定
生成物の組成比は、赤タ1線吸収スペクトル法により定
lit化した。In this neutralization reaction, if a predetermined amount of acid component is added to the system at once, neutralization is possible, but the amount of alkali remaining increases, the amount of alkali remaining is increased, the kinetics is reduced, and the coloring is difficult to analyze. -Measurement of physical properties The composition ratio of the product was determined to a constant lit value using red-tab 1-ray absorption spectroscopy.
トランス含有祉は、C−N MRスペクトル法の二重結
合領域のスペクトルより宇部化を行った。The trans-containing properties were determined using the spectrum of the double bond region obtained by C-N MR spectroscopy.
極限粘度(ηs/C)はテトラヒドロフラン中(濃度o
、]y/ae)、30℃で測定した。The intrinsic viscosity (ηs/C) in tetrahydrofuran (concentration o
, ]y/ae), measured at 30°C.
−一(脂よ・ノトタ?M ry は JIS ・ K
−7207−1974に、アイゾツト価卸1強庶はJI
S・I(−711(1−1971(2mm厚試験片3枚
重ね法)に、三点曲げ剛性はJIS・K−7203−1
973に、剪断強度けに−7214にもとづいて各々d
国定しだ。-1 (fatty, notota? Mry is JIS/K
-7207-1974, Izotsu price wholesaler was JI
The three-point bending rigidity is JIS K-7203-1 for S・I(-711(1-1971 (3-ply 2mm thick test piece method))
973, respectively based on shear strength -7214
It's nationally established.
以下実施例にて詳細にFiQ明する。FiQ will be explained in detail in Examples below.
〔実す布例−1〕
乾燥したフラスコを窒素で置換した後、溶媒としてトル
エンを400重量部、単量体として5−ノルボルネン−
2−カルボン酸メチルを100−d+hV部仕込み、R
シ温を15℃とした。こののち六塩化タングステンを2
.6重針部添加し、ついで六塩化タングステンに対し3
倍モルのジエチルアルミニウムモノクロライドを添加し
、さらに六塩化タングステンに対し24ざモルのn−ブ
タノールを添加し、10時間開置型合を行った。重合反
応終了後、仕込みのトルエンに対し3倍各のメタノール
にl 57j’j相°部の濃塩酸を加えて、この酢液を
フラスコに添付し、触媒分解を行った。その稜、テトラ
ヒドロフランを良に9媒とし、メタノールを貧溶媒とし
て再沈精製法を二度行い、乾燥したところ、71i合体
を99重量部得た。この重合体の極限粘度は帆55であ
った。トランス含量は55%であっO
次に開環重合体100重量部を仕込み、その7表アセト
ンを1,000重敵部いれ、温度を56℃に上げ、攪拌
下でポリマーを完全に溶解させる。次いで600重報部
の水に50重針部の苛性カリを溶解させ、これを反応系
の痛度が低下しないように徐々に開環重合体のアセトン
溶液に添加する。[Fruit Fabric Example-1] After purging the dried flask with nitrogen, 400 parts by weight of toluene was added as a solvent, and 5-norbornene was added as a monomer.
Charge 100-d+hV parts of methyl 2-carboxylate, R
The temperature was set at 15°C. After this, 2 tungsten hexachloride
.. Add 6 needles, then add 3 to tungsten hexachloride.
Two times the molar amount of diethylaluminium monochloride was added, and 24 moles of n-butanol relative to tungsten hexachloride were added, followed by an open-type reaction for 10 hours. After the polymerization reaction was completed, concentrated hydrochloric acid of 157j'j phase was added to methanol in an amount of 3 times the amount of toluene used, and the vinegar solution was added to the flask for catalytic decomposition. The ridge was subjected to reprecipitation purification twice using tetrahydrofuran as a good solvent and methanol as a poor solvent, and then dried to obtain 99 parts by weight of 71i combined product. The intrinsic viscosity of this polymer was 55. The trans content was 55%.Next, 100 parts by weight of the ring-opening polymer was charged, and 1,000 parts by weight of acetone was added thereto, the temperature was raised to 56°C, and the polymer was completely dissolved under stirring. Next, 50 parts of caustic potash is dissolved in 600 parts of water, and this is gradually added to the acetone solution of the ring-opening polymer so as not to reduce the degree of pain in the reaction system.
エステル加水分解の進行とともに開環重合体は系中に析
出する。As ester hydrolysis progresses, the ring-opened polymer precipitates in the system.
次に600 ’iJf’rj’i部の水を系中に加え、
反応温度を一定に保ち1時間反応を継続する。水の添加
後析出してい友開m=合体け(f471& VC#tけ
均−系となる。Next, 600 'iJf'rj'i parts of water was added to the system,
The reaction temperature is kept constant and the reaction is continued for 1 hour. After adding water, it precipitates and becomes a uniform system.
ついで94重体部の酢酸を17070重針水で希釈して
開環重合体の水浴液に添加する。生能まで添加した段階
で添加を一旦停止し、1時間攪拌を角体続し、その後残
りの全舅を添加すると開環1iJ合体は白色の粉末とな
って沈殿する。これを沖過することにより、目的とする
5−ノルボルネン−2−カルボン酸と5−ノルボルネン
−2−カルボン酸メチルの開壌共′!1【合体が得られ
た。Then, 94 parts of acetic acid is diluted with 17070 parts of water and added to the water bath solution of the ring-opening polymer. When the ring-opened 1iJ mixture is added to the final stage, the addition is stopped once, stirring is continued for 1 hour, and then the remaining whole ring is added, and the ring-opened 1iJ mixture becomes a white powder and precipitates. By filtering this, the desired 5-norbornene-2-carboxylic acid and methyl 5-norbornene-2-carboxylate can be released! 1 [Coalescence was obtained.
生成物の物性値を〔表1〕に示す。The physical property values of the product are shown in [Table 1].
〔実施例−2〕
実紬例−1の条件で苛性カリの俸を50市9部から37
重量部に減少させた以りiは実施例−1と同様の手法で
反応させた。[Example-2] Under the conditions of Example-1, 37 doses of caustic potash were distributed from 50 cities and 9 parts.
I was reacted in the same manner as in Example-1 except that the amount was reduced to parts by weight.
生成物の物性値を〔表1〕に示す。The physical property values of the product are shown in [Table 1].
〔実h(口側−3〕
実施例−lで用いた苛性カリの変りに苛性ノーダ3 6
−1i情部に豫・更した以外は実施例−1と同様の仕込
み条件、反応条件でエステルの力[1水分解を行ったO
生成物の物性値を〔表1〕に示す。−
〔実h1);例−4〕
実3i+i例−1で用いた5−ノルボルネン−2−力4
1′
ルボン酔メチル単量体のyりに、5−ノルボルネン−2
−カルボン市オクチル単ハ1体に俊I,I4 L− 、
開鎖重合体をイリた。生成物は97重針部ー乙偵限粘度
帆62で、トランス含量50%であった。[Actual h (mouth side-3)] Caustic Noda 3 6 was used instead of the caustic potash used in Example-1.
Table 1 shows the physical properties of the ester product that underwent water decomposition under the same preparation and reaction conditions as in Example 1, except for changing the content of the ester. - [Actual h1); Example-4] Actual 3i+i 5-norbornene-2-force 4 used in Example-1
1' In the reaction of methyl monomer, 5-norbornene-2
-Carbon City Octyl Monoha, Shun I, I4 L-,
The open chain polymer was removed. The product had a viscosity limit of 62 and a trans content of 50%.
実施例−1と同様の仕込み条件、反応条件で加水分解を
行った。Hydrolysis was carried out under the same charging conditions and reaction conditions as in Example-1.
生成物の物ゼト値を1表1〕に示す。The product values are shown in Table 1.
〔実h111例−5〕
実hiiI例−1で用いた5−ノルボルネン−2−カル
ボン1変メチルLit tit体のイ(ユに、3−フェ
ニル−5−ノルボルネン−2−カルボン酸メチル単量体
に変更し、開環重合体を得た。生成物は37重量部で、
榛眼精度帆43で、トランス合邦53%であった。[Practical Example 111-5] 5-norbornene-2-carboxylic acid methyl 3-phenyl-5-norbornene-2-carboxylate monomer used in Practical Example-1 to obtain a ring-opened polymer.The product was 37 parts by weight,
The accuracy sail was 43, and the trans union was 53%.
実画例−1と同様の什込み条件、反応条件で加水分解を
行った。Hydrolysis was carried out under the same feeding conditions and reaction conditions as in Example 1.
生成物の物性仙を〔表1〕に示す。The physical properties of the product are shown in Table 1.
〔実h11i例−6〕
実施例−1で用いた開型重合条件のうち、n−ブタノー
ルを2,6ルチジンに変Wニジ7た所、87重針部で極
限粘度0.65、トランス含量74%の開環重合体をイ
!Iた。[Actual H11i Example-6] Among the open polymerization conditions used in Example-1, where n-butanol was changed to 2,6-lutidine, the intrinsic viscosity was 0.65 at the 87-heavy needle part, and the trans content was 74% ring-opened polymer! I was.
実7/i+i例−1と同様の仕込み条件、反応条件で加
水分解を行った。Example 7/i+i Hydrolysis was carried out under the same charging conditions and reaction conditions as in Example-1.
生成物の物性f1filを1表1〕に示す。The physical properties of the product f1fil are shown in Table 1.
〔実hAi例−7〕
実施例−1で用いた開環重合条件のうち、六塩化タング
ステンを2.1−t:ti祉部、重合温度を5℃、反応
時間を16時間に変更したところ、65重鼠Wlfで極
限粘度1.2、トランス含bt43%の開猿重合体を得
た。[Actual hAi Example-7] Among the ring-opening polymerization conditions used in Example-1, the tungsten hexachloride was changed to 2.1-t:ti, the polymerization temperature was changed to 5°C, and the reaction time was changed to 16 hours. An open aqueous polymer having an intrinsic viscosity of 1.2 and a trans content of 43% bt was obtained using 65-weight Wlf.
実施例−1と同様の仕込み条件、反応条件で加水分解を
行った。Hydrolysis was carried out under the same charging conditions and reaction conditions as in Example-1.
生成物の物性イ偵を〔表1〕に示す。The physical properties of the product are shown in Table 1.
〔比車交1り1− 1 〕
実施例−1で川V・だ開環重合条件のうち、六塩化タン
グステンを0.33+情部に、アルキルアルミニウムの
オIロ類をトリエチルアルミニウムに、浴媒をトルエン
からクロルベンゼンに、重合温1u′を40℃に哀史し
たところ、98 !4E畦部で(タ限枯バF1.4トラ
ンス含駐35%の開ff1.m合体がIHらJした。[Comparative vehicle traffic 1-1] Among the ring-opening polymerization conditions in Example-1, tungsten hexachloride was added to 0.33 + tungsten, aluminum alkyls were added to triethylaluminum, and bath When the medium was changed from toluene to chlorobenzene and the polymerization temperature was changed to 1 u' to 40°C, the result was 98! At the 4E ridge, 35% open ff1.m of F1.4 trans-containing coalesced into IH et al.
実)血j+1J−1と同様の仕込み条件、反応条件で加
水分解を行った。Actual) Blood j+1 Hydrolysis was carried out under the same preparation and reaction conditions as for J-1.
生成物の物性値を〔表2〕に示す。The physical property values of the product are shown in [Table 2].
〔比較例−2〕
実施例−1の開環重合系に分子端R1”J活剤として1
.5−へキサジエンを六塩化タングステンに対シて5.
0モル添加したところ、71重足部で極限粘度0.28
、トランス含け48%の開環重合[トが得られた。[Comparative Example-2] 1 was added to the ring-opening polymerization system of Example-1 as a molecular end R1''J activator.
.. 5-hexadiene to tungsten hexachloride 5.
When 0 mol was added, the intrinsic viscosity was 0.28 at 71 mol.
, 48% ring-opening polymerization including trans was obtained.
実施jyl−+と同様の仕込み条件、反応条件で加水分
解を行った。Hydrolysis was carried out under the same charging conditions and reaction conditions as in the jyl-+ experiment.
生成物の物性値を〔表2〕に示す。The physical property values of the product are shown in [Table 2].
〔比較例−3〕
実7jtjし11−1の条件で苛1生カリの鼠を50′
屯+j部から30沖腓部に減少させた以外は実施例−1
と同様の手法で反応させた。[Comparative Example-3] Rats with 1 raw potash were heated for 50 minutes under the conditions of 7 and 11-1.
Example-1 except that it was reduced from ton + j part to 30 okifubu.
The reaction was carried out in the same manner.
生成物の物性イl:’4を〔表2〕に示す。、(以下余
白)The physical properties of the product I:'4 are shown in [Table 2]. , (margin below)
Claims (1)
但し、R1は水素原子、アルキル基またはフェニル基を
、R2は水素原子またはアルキル基を、R3t、tアル
キル基を表わす。)、かつ次記の(a)〜(c)の硬性
を其イ11bする重合体 値)極限粘度が0.3〜4.0であること。 (b)上記構成学位(A)の含有量が全構成単位中の9
0〜100重柾%であること。 (c)構成単位囚および(B)における二重結合のトラ
ンス含有量が40%以上であること。(1) It is basically composed of 414 structural units (4) represented by the following general formula and structural units (B) represented by (
However, R1 represents a hydrogen atom, an alkyl group or a phenyl group, R2 represents a hydrogen atom or an alkyl group, and R3t,t represents an alkyl group. ), and the following hardness (a) to (c) (11b) Polymer value) The intrinsic viscosity is 0.3 to 4.0. (b) The content of the above constituent degree (A) is 9 in the total constituent units.
Must be 0 to 100%. (c) The trans content of the structural unit and the double bond in (B) is 40% or more.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15211182A JPS5941326A (en) | 1982-09-01 | 1982-09-01 | Polymer having excellent rigidity |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15211182A JPS5941326A (en) | 1982-09-01 | 1982-09-01 | Polymer having excellent rigidity |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5941326A true JPS5941326A (en) | 1984-03-07 |
JPH0242094B2 JPH0242094B2 (en) | 1990-09-20 |
Family
ID=15533294
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15211182A Granted JPS5941326A (en) | 1982-09-01 | 1982-09-01 | Polymer having excellent rigidity |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5941326A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6232718A (en) * | 1985-08-05 | 1987-02-12 | Nippon Telegr & Teleph Corp <Ntt> | Binarization method for analog signal |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04153079A (en) * | 1990-10-18 | 1992-05-26 | Digital Sutoriimu:Kk | Erasable and rewritable paper, printing ink and printing apparatus and erasing apparatus using them |
JPH04202898A (en) * | 1990-11-22 | 1992-07-23 | Fukui Pref Gov | Chromic patterned paper and its production |
-
1982
- 1982-09-01 JP JP15211182A patent/JPS5941326A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6232718A (en) * | 1985-08-05 | 1987-02-12 | Nippon Telegr & Teleph Corp <Ntt> | Binarization method for analog signal |
Also Published As
Publication number | Publication date |
---|---|
JPH0242094B2 (en) | 1990-09-20 |
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