JP3941158B2 - Process for producing poly- (1,4-phenylene ether) having hydroxyl groups at both ends - Google Patents

Process for producing poly- (1,4-phenylene ether) having hydroxyl groups at both ends Download PDF

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JP3941158B2
JP3941158B2 JP13339397A JP13339397A JP3941158B2 JP 3941158 B2 JP3941158 B2 JP 3941158B2 JP 13339397 A JP13339397 A JP 13339397A JP 13339397 A JP13339397 A JP 13339397A JP 3941158 B2 JP3941158 B2 JP 3941158B2
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Prior art keywords
hydroxyl groups
phenylene ether
poly
producing poly
ortho
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JP13339397A
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JPH10324743A (en
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淳 寺原
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Sumitomo Chemical Co Ltd
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Sumitomo Chemical Co Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は熱安定性に優れた高分子材料として有用な、両末端に水酸基を有するポリ−(1,4−フェニレンエーテル)の製造方法に関する。
【0002】
【従来の技術】
2,6−ジメチルフェノールの遷移金属錯体触媒を用いた酸化重合によって得られるポリ−(2,6−ジメチルフェニレンエーテル)(以下、PPEと略すことがある。)は有用な樹脂であることが知られている。しかしPPEは、芳香環に置換されたメチル基が酸化劣化を受けやすいため、PPE単独で溶融成形することが難しいという欠点があり、一般にはポリスチレンとのポリマーアロイとして汎用エンプラに位置づけられている。
【0003】
一方、無置換のフェノールの重合体であるポリ−1,4−フェニレンエーテルは、Europ. Polym. J., 4, 275 (1968).に記載されているように融点が298℃(ガラス転移温度は83℃)であり、超高耐熱性の樹脂として、例えば電子部品のコネクタ用途に期待される。
【0004】
しかしながら、このような2位にも置換基を有していない、無置換のフェノールを遷移金属錯体触媒の存在下に酸化重合することによりポリ−1,4−フェニレンエーテルを製造する方法においては、オルト位分岐が生じやすいという欠点があった。
ここでオルト位分岐とは、フェノール重合体中のベンゼン環が1,2,4−三置換ベンゼン構造や1,2−二置換ベンゼン構造、1,2,6−三置換ベンゼン構造、1,2,4,6−四置換ベンゼン構造などをとることを指し、本来望まれる1,4−二置換ベンゼンの連鎖を乱す構造である。
【0005】
ところで、両末端に水酸基を有するポリ−(1,4−フェニレンエーテル)も同様に超高耐熱性樹脂として有用であり、さらには、高分子量化などの目的で共重合反応に用いたり、各種の物性改良を目的として官能基を付加するためなどに非常に有用である。その製造方法について例えば、特開昭59−168029号公報には、フェノール類とビスフェノール類の混合物を有機溶媒中、遷移金属錯体触媒の存在下に酸素と反応させる方法が記載されているが、具体的に開示されているのは2,6−ジ置換フェノール類と、やはり水酸基に対してオルト位に置換基を有するヒドロキシフェニル基を2個有するプロパンまたはメタンから得られる重合体に関する製造方法であり、無置換のポリ−(1,4−フェニレンエーテル)を製造できるか否かについては何も具体的に開示されていない。
【0006】
特開平2−214724号公報には、パラ位がハロゲン化されたフェノールとビスフェノール類またはハイドロキノンとの混合物をCu(I)ハロゲン化物の共存下に極性非プロトン溶媒中で反応させて両末端に水酸基を有するポリ−(1,4−フェニレンエーテル)を製造する方法が開示されているが、実用的にはフェノール性水酸基に対して当量以上のアルカリ金属水酸化物を添加する必要があるという問題があった。
【0007】
また特公昭44−28917号公報には4−(4−ヒドロキシフェノキシ)−フェノール、4,4’−ジヒドロキシジフェニルエーテルまたは4,4’−ビス(4−ヒドロキシフェノキシ)−ジフェニルエーテルを250〜300℃の温度に加熱することによる両末端に水酸基を有するポリ−(1,4−フェニレンエーテル)を製造する方法が示されているが、この場合高温が必要であるという問題があった.
【0008】
【発明が解決しようとする課題】
かかる状況下、本発明が解決しようとする課題、即ち本発明の目的は、オルト位の分岐が少ない両末端に水酸基を有するポリ−(1,4−フェニレンエーテル)を温和な条件で製造する方法を提供することにある。
【0009】
【課題を解決するための手段】
本発明者らは上記目的を達成するべく鋭意研究を行った結果、特定の出発原料を用いる方法を見出し、本発明を完成するに至った。即ち本発明は、遷移金属錯体触媒および酸化剤存在下に有機溶媒中で、4,4’−ジヒドロキシジフェニルエーテルを酸化する、両末端に水酸基を有するポリ−(1,4−フェニレンエーテル)の製造方法にかかるものである。
【0010】
【発明の実施の形態】
以下、本発明を詳細に説明する。
本発明の製造方法における触媒は遷移金属錯体触媒であり、通常フェノール類の酸化反応に活性を有する遷移金属錯体触媒を使用することができる。より好ましくはマンガン、コバルトまたは銅の錯体触媒が用いられ、さらに好ましくは銅錯体触媒が用いられる。遷移金属錯体としては、遷移金属のハロゲン化物、例えばCuClやCuBr等と、ピリジンやイミダゾール、オキサゾール等の含窒素芳香族化合物とを接触させて得られる遷移金属錯体が例示される。
触媒は任意の量で用いることができるが、4,4’−ジヒドロキシジフェニルエーテル(以下、DHPEと略称することがある。)に対して0.01〜50モル%が好ましく、0.02〜10モル%がより好ましい。
【0011】
本発明で用いられる酸化剤としては任意のものが使用されるが、好ましくは酸素が用いられる。酸素源としては任意のものが使用できるが、酸素ガスまたは空気が好適に用いられる。
【0012】
本発明で使用できる有機溶媒はDHPEに対し不活性でかつ反応温度において液体であれば良く特に限定されるものではない。好ましい溶媒の例を示すならば、ベンゼン、トルエン、キシレン、クロロベンゼン、ジクロロベンゼン、クロロホルム、ジオキサン、ジグライム、アニソール等が挙げられる。これらは単独あるいは混合物として使用される。
DHPEの濃度は、好ましくは0.5〜50重量%、より好ましくは1〜30重量%になるような割合で使用される。
【0013】
本発明を実施する反応温度は、反応媒体が液状を保つ範囲であれば特に制限はないが、好ましくは0℃〜150℃である。
【0014】
【実施例】
以下に実施例を挙げて本発明をさらに詳細に説明するが、本発明はこれらの実施例によりその範囲を限定されるものではない。
【0015】
以下の実施例および比較例において、重合体の赤外吸収スペクトルはパーキンエルマー社製1600赤外分光光度計(KBr法)を用いて測定した。
【0016】
重合体のオルト位分岐量を表わす指標(o/p)を重合体の赤外吸収スペクトルから次のようにして求めた。 Europ. Polym., J., 4, 275 (1968) によると、ベンゼン環の1,2,4位に置換基を有する構造は970cm-1にピークが現れ、1,4位に置換基を有する構造では1010cm-1にピークが現れることが示されている。前者をオルト結合由来としてそのピーク面積を後者のピーク面積で除した値をo/pとした。ピーク面積の算出にはパーキンエルマー社製のスペクトル解析ソフト(GRAMS Analyst for 1600 Series)を用い、オルト結合由来ピーク面積を 948〜988cm-1の間、パラ結合由来ピークを994〜1018cm-1の間として求めた。
【0017】
実施例1
電磁撹拌機と還流冷却器を備えた50mlナスフラスコ中に、CuCl 25mg、2−メチルベンズイミダゾール33mgおよびクロロホルム0.5mlを入れて酸素ガスを吹き込みながら室温で15分撹拌した。これにDHPE 1.01gをアニソール15mlとジグライム5mlの混合溶媒に溶解して加え、酸素ガスを吹き込みながら50℃で4時間撹拌を続けた。反応終了後、反応混合物を濃塩酸0.5mlを含むメタノール100ml中に注ぎ込んだ。沈澱物を濾取し、100℃で5時間減圧乾燥した後の重合体の重量から収率を求めたところ53%であった。重合体のオルト位分岐量(o/p)は0.4であった。
【0018】
実施例2
触媒にCuCl 50mgと2−エチルイミダゾール48mgを用い、溶媒にジグライム10mlを用いたほかは実施例1と同様にして酸化重合を行った結果、収率は55%、o/pは0.3であった。
【0019】
比較例1
触媒にCuCl 50mgと2−メチルベンズイミダゾール66mgを用い、モノマーとしてDHPE 404mgとフェノール1887mgを用いたほかは実施例1と同様にして酸化重合を行った。重合体の収率は33%でo/pは0.8であった。
【0020】
実施例1と比較例1で得られた重合体の赤外吸収スペクトルを図1に示す。
以上に示した結果からフェノールとDHPEの混合物をモノマーとして用いた比較例1においては、赤外吸収スペクトルにおいてオルト位分岐量(o/p)が多く認められることと、690cm-1と752cm-1にモノ置換ベンゼン環に由来するピークが認められるのに対して,DHPEのみを用いた実施例1,2においてはオルト位分岐量(o/p)が少なく、かつモノ置換ベンゼン環に由来するピークがまったく観測されないことがわかる。これにより、実施例1、2において得られたポリマーは両末端に水酸基を有し、従来よりもオルト位の分岐が低減されていることが示された。
【0021】
【発明の効果】
以上説明したように,本発明によってオルト位の分岐が従来よりも低減された両末端に水酸基を有するポリ−(1,4−フェニレンエーテル)を温和な条件で製造することができるようになった。
【図面の簡単な説明】
【図1】実施例1および比較例1で得られた重合体の赤外吸収スペクトルである.
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for producing poly- (1,4-phenylene ether) having hydroxyl groups at both ends, which is useful as a polymer material having excellent thermal stability.
[0002]
[Prior art]
Poly- (2,6-dimethylphenylene ether) (hereinafter sometimes abbreviated as PPE) obtained by oxidative polymerization using a transition metal complex catalyst of 2,6-dimethylphenol is known to be a useful resin. It has been. However, PPE has a drawback that it is difficult to melt-mold with PPE alone because the methyl group substituted on the aromatic ring is susceptible to oxidative degradation, and is generally positioned as a general-purpose engineering plastic as a polymer alloy with polystyrene.
[0003]
On the other hand, poly-1,4-phenylene ether, which is a polymer of unsubstituted phenol, has a melting point of 298 ° C. (glass transition temperature) as described in Europ. Polym. J., 4, 275 (1968). Is expected to be used as a connector for electronic parts, for example, as an ultra-high heat-resistant resin.
[0004]
However, in the method of producing poly-1,4-phenylene ether by oxidative polymerization of an unsubstituted phenol having no substituent at the 2-position in the presence of a transition metal complex catalyst, There was a drawback that ortho branching was likely to occur.
Here, the ortho-position branching means that the benzene ring in the phenol polymer has a 1,2,4-trisubstituted benzene structure, a 1,2-disubstituted benzene structure, a 1,2,6-trisubstituted benzene structure, , 4,6-tetrasubstituted benzene structure and the like, and is a structure that disrupts the originally desired 1,4-disubstituted benzene chain.
[0005]
By the way, poly- (1,4-phenylene ether) having hydroxyl groups at both ends is also useful as an ultra-high heat-resistant resin, and further used for copolymerization for the purpose of increasing the molecular weight, It is very useful for adding functional groups for the purpose of improving physical properties. Regarding the production method, for example, JP-A-59-168029 describes a method in which a mixture of phenols and bisphenols is reacted with oxygen in an organic solvent in the presence of a transition metal complex catalyst. Specifically disclosed is a process for producing a polymer obtained from 2,6-disubstituted phenols and propane or methane having two hydroxyphenyl groups having a substituent at the ortho position relative to the hydroxyl group. Nothing is specifically disclosed as to whether or not an unsubstituted poly- (1,4-phenylene ether) can be produced.
[0006]
In JP-A-2-214724, a mixture of a phenol halogenated at the para-position and a bisphenol or hydroquinone is reacted in a polar aprotic solvent in the presence of Cu (I) halide to form hydroxyl groups at both ends. Although a method for producing poly- (1,4-phenylene ether) having an alkyl group is disclosed, there is a problem that it is practically necessary to add an alkali metal hydroxide of an equivalent amount or more with respect to the phenolic hydroxyl group. there were.
[0007]
Japanese Patent Publication No. 44-28917 discloses 4- (4-hydroxyphenoxy) -phenol, 4,4′-dihydroxydiphenyl ether or 4,4′-bis (4-hydroxyphenoxy) -diphenyl ether at a temperature of 250 to 300 ° C. The method for producing poly- (1,4-phenylene ether) having hydroxyl groups at both ends by heating is shown, but in this case, there is a problem that high temperature is required.
[0008]
[Problems to be solved by the invention]
Under such circumstances, the problem to be solved by the present invention, that is, the object of the present invention is to produce a poly- (1,4-phenylene ether) having hydroxyl groups at both ends with few branches at the ortho position under mild conditions. Is to provide.
[0009]
[Means for Solving the Problems]
As a result of intensive studies to achieve the above object, the present inventors have found a method using a specific starting material and have completed the present invention. That is, the present invention relates to a process for producing poly- (1,4-phenylene ether) having hydroxyl groups at both ends by oxidizing 4,4′-dihydroxydiphenyl ether in an organic solvent in the presence of a transition metal complex catalyst and an oxidizing agent. It depends on.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the present invention will be described in detail.
The catalyst in the production method of the present invention is a transition metal complex catalyst, and a transition metal complex catalyst having activity in the oxidation reaction of phenols can be usually used. More preferably, a complex catalyst of manganese, cobalt or copper is used, and a copper complex catalyst is more preferably used. Examples of transition metal complexes include transition metal complexes obtained by contacting transition metal halides such as CuCl and CuBr with nitrogen-containing aromatic compounds such as pyridine, imidazole and oxazole.
The catalyst can be used in any amount, but is preferably 0.01 to 50 mol%, preferably 0.02 to 10 mol based on 4,4′-dihydroxydiphenyl ether (hereinafter sometimes abbreviated as DHPE). % Is more preferable.
[0011]
Any oxidant may be used in the present invention, but oxygen is preferably used. Any oxygen source can be used, but oxygen gas or air is preferably used.
[0012]
The organic solvent that can be used in the present invention is not particularly limited as long as it is inert to DHPE and liquid at the reaction temperature. Examples of preferred solvents include benzene, toluene, xylene, chlorobenzene, dichlorobenzene, chloroform, dioxane, diglyme, anisole and the like. These are used alone or as a mixture.
The concentration of DHPE is preferably 0.5 to 50% by weight, more preferably 1 to 30% by weight.
[0013]
The reaction temperature for carrying out the present invention is not particularly limited as long as the reaction medium is kept in a liquid state, but is preferably 0 ° C to 150 ° C.
[0014]
【Example】
The present invention will be described in more detail with reference to the following examples, but the scope of the present invention is not limited by these examples.
[0015]
In the following examples and comparative examples, the infrared absorption spectrum of the polymer was measured using a 1600 infrared spectrophotometer (KBr method) manufactured by PerkinElmer.
[0016]
An index (o / p) indicating the ortho branching amount of the polymer was determined from the infrared absorption spectrum of the polymer as follows. According to Europ. Polym., J., 4, 275 (1968), a structure having a substituent at positions 1, 2, 4 of the benzene ring has a peak at 970 cm -1 and has a substituent at positions 1, 4 The structure shows that a peak appears at 1010 cm- 1 . The value obtained by dividing the peak area by the former peak area from the ortho bond and the latter peak area was defined as o / p. The calculation of the peak areas using spectral analysis software manufactured by Perkin-Elmer Corporation (GRAMS Analyst for 1600 Series), between the ortho bond derived peak area of 948~988cm -1, while the para bond derived peak of 994~1018Cm -1 As sought.
[0017]
Example 1
In a 50 ml eggplant flask equipped with a magnetic stirrer and a reflux condenser, 25 mg of CuCl, 33 mg of 2-methylbenzimidazole and 0.5 ml of chloroform were put and stirred at room temperature for 15 minutes while blowing oxygen gas. To this was added 1.01 g of DHPE dissolved in a mixed solvent of 15 ml of anisole and 5 ml of diglyme, and stirring was continued at 50 ° C. for 4 hours while blowing oxygen gas. After completion of the reaction, the reaction mixture was poured into 100 ml of methanol containing 0.5 ml of concentrated hydrochloric acid. The precipitate was collected by filtration and dried under reduced pressure at 100 ° C. for 5 hours. The yield was determined from the weight of the polymer, and it was 53%. The ortho branching amount (o / p) of the polymer was 0.4.
[0018]
Example 2
As a result of performing oxidative polymerization in the same manner as in Example 1 except that 50 mg of CuCl and 48 mg of 2-ethylimidazole were used as the catalyst and 10 ml of diglyme was used as the solvent, the yield was 55% and o / p was 0.3. there were.
[0019]
Comparative Example 1
Oxidative polymerization was carried out in the same manner as in Example 1 except that 50 mg of CuCl and 66 mg of 2-methylbenzimidazole were used as the catalyst, and 404 mg of DHPE and 1887 mg of phenol were used as the monomers. The yield of the polymer was 33% and o / p was 0.8.
[0020]
Infrared absorption spectra of the polymers obtained in Example 1 and Comparative Example 1 are shown in FIG.
From the results shown above, in Comparative Example 1 using a mixture of phenol and DHPE as a monomer, a large amount of ortho branching (o / p) was observed in the infrared absorption spectrum, and 690 cm −1 and 752 cm −1. In Example 1 and 2 using only DHPE, the peak derived from the mono-substituted benzene ring is small and the amount of ortho-position branching (o / p) is small. Is not observed at all. As a result, it was shown that the polymers obtained in Examples 1 and 2 had hydroxyl groups at both ends, and the ortho-position branching was reduced as compared with the prior art.
[0021]
【The invention's effect】
As described above, according to the present invention, poly- (1,4-phenylene ether) having hydroxyl groups at both ends in which the branching at the ortho position is reduced as compared with the prior art can be produced under mild conditions. .
[Brief description of the drawings]
1 is an infrared absorption spectrum of the polymers obtained in Example 1 and Comparative Example 1. FIG.

Claims (2)

銅のハロゲン化合物とイミダゾール化合物とを接触させて得られる遷移金属錯体触媒および酸化剤存在下に有機溶媒中で、4,4’−ジヒドロキシジフェニルエーテルを酸化することを特徴とする両末端に水酸基を有するポリ−(1,4−フェニレンエーテル)の製造方法。 It has hydroxyl groups at both ends, characterized by oxidizing 4,4'-dihydroxydiphenyl ether in an organic solvent in the presence of a transition metal complex catalyst obtained by contacting a copper halogen compound with an imidazole compound and an oxidizing agent. Production method of poly- (1,4-phenylene ether). 酸化剤が、酸素であることを特徴とする請求項1記載の両末端に水酸基を有するポリ−(1,4−フェニレンエーテル)の製造方法。Method for producing a (1,4-phenylene ether) - oxidizing agent, poly having hydroxyl groups at both terminals according to claim 1, characterized in that the oxygen.
JP13339397A 1997-05-23 1997-05-23 Process for producing poly- (1,4-phenylene ether) having hydroxyl groups at both ends Expired - Fee Related JP3941158B2 (en)

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