JPS601211A - Polyethynylphenylacetylene and its production - Google Patents

Polyethynylphenylacetylene and its production

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Publication number
JPS601211A
JPS601211A JP10932183A JP10932183A JPS601211A JP S601211 A JPS601211 A JP S601211A JP 10932183 A JP10932183 A JP 10932183A JP 10932183 A JP10932183 A JP 10932183A JP S601211 A JPS601211 A JP S601211A
Authority
JP
Japan
Prior art keywords
structural formula
catalyst
formula
linear polymer
represented
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.)
Granted
Application number
JP10932183A
Other languages
Japanese (ja)
Other versions
JPS6254329B2 (en
Inventor
Yosuke Koizumi
洋介 小泉
Hideo Ai
愛 英夫
Naohiro Tsuruta
鶴田 直宏
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Asahi Kasei Corp
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry Co Ltd
Asahi Kasei Kogyo KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Asahi Chemical Industry Co Ltd, Asahi Kasei Kogyo KK filed Critical Asahi Chemical Industry Co Ltd
Priority to JP10932183A priority Critical patent/JPS601211A/en
Publication of JPS601211A publication Critical patent/JPS601211A/en
Priority to US06/899,631 priority patent/US4667006A/en
Priority to US06/899,650 priority patent/US4767797A/en
Publication of JPS6254329B2 publication Critical patent/JPS6254329B2/ja
Granted legal-status Critical Current

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  • Polymerization Catalysts (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)

Abstract

PURPOSE:To obtain a polyethynylphenylacetylene suitable for use in electron beam resists, photopolymers, etc., by polymerizing diethynylbenzene in the presence of a specified catalyst in a solvent such as an aromatic hydrocarbon or a halohydrocarbon. CONSTITUTION:The purpose linear polymer represented by formula II (wherein the ethynyl group is m- or p- to the main chain of the molecule, and n is a number corresponding to a weight-average MW of 1,000-100,000) is obtained by polymerizing a compound of formula I (wherein the ethynyl groups are m- or p- to each other) at 0-80 deg.C in a solvent such as an aromatic hydrocarbon or a halohydrocarbon in the presence of a catalyst obtained by exposing tungsten hexacarbonyl or molybdenum hexacarbonyl to light in the presence of an organic halide. In order to obtain the above polymer in good yields, it is preferred that the concentration of the monomer of formula I in the solvent is 10mol/1 or below, and the catalyst is used in an amount 1/10-1/100 time that of the monomer.

Description

【発明の詳細な説明】 本発明は新規でかつ電子線レジスト等の用途に有用なポ
リエチニルフェニルアセチレン及びその製造法に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to polyethynylphenylacetylene which is novel and useful for applications such as electron beam resists, and a method for producing the same.

本発明におけるポリエチニルフェニルアセチレンとは構
造式(I)で表わされる線状重合体である。
Polyethynylphenylacetylene in the present invention is a linear polymer represented by structural formula (I).

(式中、エチニル基は、分子主鎖に対してメタ位ないし
はパラ位に結合しており、nは重量平均分子量が100
0ないし10θ万になる数である。) 芳香環に結合するエチニル基を含む重合体が、特公昭&
4’−4コao号ないし特公昭kA −4’ !;デ3
9号公報等に1開示されているが、これらはエチニル基
を環化三量体化する触媒を用いて重合しているため、分
子主鎖が本発明における重合体のごとく共役二重結合に
よって構成されているもの”でitなく、本発明による
重合体とは全く異なるものである。
(In the formula, the ethynyl group is bonded to the meta or para position with respect to the main chain of the molecule, and n is the weight average molecular weight of 100
It is a number ranging from 0 to 100,000. ) A polymer containing an ethynyl group bonded to an aromatic ring was developed by
4'-4ko ao or special public Sho kA-4'! ;De3
9, etc., but since these are polymerized using a catalyst that cyclizes and trimerizes ethynyl groups, the molecular main chain is formed by conjugated double bonds like the polymer in the present invention. It is completely different from the polymer according to the present invention.

本発明における重合体は新規なものであり、かっ主鎖の
二重結合とエチニル基が共役しているため、種々の用途
において極めて有用なものである。
The polymer of the present invention is novel, and because the double bond in the main chain and the ethynyl group are conjugated, it is extremely useful in various uses.

本発明における構造式(I)で表わされる線状重合体の
分子量は重量平均分子量でlOθ0ないし100万であ
り、好ましくはhoooないしょO万Sある。
The molecular weight of the linear polymer represented by the structural formula (I) in the present invention is from lOθ0 to 1,000,000 in terms of weight average molecular weight, preferably from hoooo to 0,000S.

重量平均分子量が1000以下のものは重合体としての
物性に乏しく、例えば電子線レジストとして用いるため
に塗膜を作成した場合に均質な塗膜を形成するのが難し
い。また重量平均分子量がlθ0万以上のものは溶剤に
対する溶解性に乏しくなる。
Those having a weight average molecular weight of 1000 or less have poor physical properties as a polymer, and it is difficult to form a homogeneous coating film for use as an electron beam resist, for example. Moreover, those having a weight average molecular weight of lθ00,000 or more have poor solubility in solvents.

構造式(I)により表わされる線状重合体を得るには種
々の方法を用い得るが、構造式(U)で表わされる化合
物(以下モノマーと称す。)を種々の触媒を用いて重合
する方法が工程の簡便さ及び精製の容易さから好ましい
Various methods can be used to obtain the linear polymer represented by structural formula (I), but methods include polymerizing compounds represented by structural formula (U) (hereinafter referred to as monomers) using various catalysts. is preferable because of the simplicity of the process and the ease of purification.

(式中、エチニル基は互いにパラ位ないしはパラ位にあ
るものである。) 構造式(1)に示される線状重合体を収率よく得るには
、上記モノマー(II)を溶剤中で重合することが好ま
しく、この時のモノマL濃度は好ましくは、/ Om0
V1以下である。また本発明の重合体を得るには触媒の
使用が望ましく、その好ましい触媒濃度は/rrtrl
/l以下である。また重合反応の条件としては、窒素、
アルゴン等のモノマー及び触媒と反応しない不活性ガス
の罪囲気下でo−go℃、好ましくは、yo−go℃の
温度範囲で重合することが好ましい。一般的に触媒は七
ツマ−に対して鴇〜Xooが好ましく、触媒使用量が多
いと重合体の分子量が小さくなり、触媒使用量が少ない
と重合体の収率が低下する。また反応温度は高いほうが
重合の反応速度が大きくなるが、触媒の寿命は短くなる
(In the formula, the ethynyl groups are in the para or para positions with respect to each other.) In order to obtain the linear polymer represented by the structural formula (1) in a high yield, the above monomer (II) is polymerized in a solvent. The monomer L concentration at this time is preferably /Om0
It is below V1. Further, in order to obtain the polymer of the present invention, it is desirable to use a catalyst, and the preferred concentration of the catalyst is /rrtrl
/l or less. In addition, the conditions for the polymerization reaction include nitrogen,
Polymerization is preferably carried out at a temperature range of o-go°C, preferably yo-go°C, under an atmosphere of an inert gas that does not react with the monomer and catalyst, such as argon. Generally, it is preferable that the catalyst be 7 to 10%. If the amount of the catalyst used is large, the molecular weight of the polymer will be small, and if the amount of the catalyst used is small, the yield of the polymer will be reduced. Furthermore, the higher the reaction temperature, the faster the polymerization reaction rate, but the shorter the life of the catalyst.

本発明の重合体を重合するために使用される触媒には、
一般的にエチニル基を重合させるために用いられる触媒
を用いることができるが、その好ましい触媒としては、
構造式(m)と構造式(F/1によって示される化合物
の組み合わせよりなるチーグラー・ナツタ型触媒が挙げ
られる。
Catalysts used to polymerize the polymers of the invention include:
Catalysts commonly used for polymerizing ethynyl groups can be used, and preferred catalysts include:
Examples include Ziegler-Natsuta type catalysts consisting of a combination of compounds represented by structural formula (m) and structural formula (F/1).

Ti (Ql )4 構造式(It) AI(Q2)11 構造式(酌 (式中、Qlは炭素数20以下のアルコキシ基、Q2は
炭素数20以下のアルキル基、ないしアリール基である
。)構造式(N)によって表わされる化合物としては、
例えば、チタニウムテトラ−n−ブトキシド、チタニウ
ムテトラ−1−ブトキシド、チタニウムテトラ−1−ブ
トキシド等が添げられ、また構造式(Mによって表わさ
れる化合物としては、例えば、トリエチルアルミニウム
等が挙げられる。
Ti (Ql ) 4 Structural formula (It) AI (Q2) 11 Structural formula (In the formula, Ql is an alkoxy group having 20 or less carbon atoms, and Q2 is an alkyl group or aryl group having 20 or less carbon atoms.) As a compound represented by structural formula (N),
For example, titanium tetra-n-butoxide, titanium tetra-1-butoxide, titanium tetra-1-butoxide, etc. are added, and examples of compounds represented by the structural formula (M) include triethylaluminum and the like.

チーグラー・ナツタ型触媒としては、上記構造式(1)
及び構造式(鴎によって表わされる化合物の組み合わせ
以外に、構造式(7)ないし構造式(P/)のQ1及び
Q、がハロゲンである化合物、例えば、TiCl4 あ
るいはAI (C* H5) CI等の組み合わせが知
られている。
The Ziegler-Natsuta type catalyst has the above structural formula (1)
and Structural Formula (In addition to the combination of compounds represented by O), compounds in which Q1 and Q of Structural Formula (7) to Structural Formula (P/) are halogens, such as TiCl4 or AI (C* H5) CI, etc. combinations are known.

しかし、このようなハロゲンを置換基としてもつ化合物
により構成されるチーグラー・ナツタ型触媒の使用は、
エチニル基を環化三量体化しペンゼ、ン骨格を形成しや
すく、本発明の重合体の製造法としては好ましくない。
However, the use of a Ziegler-Natsuta type catalyst composed of a compound having a halogen as a substituent,
The ethynyl group tends to be cyclized and trimerized to form a penzene skeleton, which is not preferred as a method for producing the polymer of the present invention.

本発明における重合体を重合するための他の好ましい触
媒としては、例えば、六塩化タングステンあるいは五塩
化モリブデンの単独または、テFラフェニルスズ等の有
機スズ化合物や水等の助触媒を併用する触媒が挙げられ
る。
Other preferred catalysts for polymerizing the polymer in the present invention include, for example, tungsten hexachloride or molybdenum pentachloride alone or in combination with an organotin compound such as teF-raphenyltin or a co-catalyst such as water. It will be done.

更に好ましい触媒としては、例えば、タングステンヘキ
サカルボニル、あるいはモリブデンヘキサカルボニルを
四塩化炭素等の有機ハロゲン化物の存在下に高圧水鎖灯
等により光照射することにより得られる触媒が挙げられ
る。この触媒系の場合は触媒調製時(光照射時)の温度
は低いほうが良く、好ましくはO℃〜30℃の温度範囲
で光照射するのが良い。高温で調製した触媒では重合体
の分子量が小さくなるためである。
More preferred catalysts include, for example, catalysts obtained by irradiating tungsten hexacarbonyl or molybdenum hexacarbonyl with light using a high-pressure water chain lamp or the like in the presence of an organic halide such as carbon tetrachloride. In the case of this catalyst system, the temperature at the time of catalyst preparation (at the time of light irradiation) is preferably lower, and preferably the light irradiation is carried out at a temperature range of 0°C to 30°C. This is because catalysts prepared at high temperatures have a small molecular weight.

本発明における重合体を得る重合反応において七ツマ−
を希釈する溶剤としては、ベンゼン、トルエン等の芳香
族炭化水素、四塩化炭素、クロロホルム等のハロゲン化
炭化水素、ジエチルエーテル、テトラヒドロフラン、ジ
オキサン等のエーテル類が用いられる。ただし、上記チ
ーグラー・ナツタ型触媒の場合は芳香族炭化水素を溶剤
として用いるのが好ましい。前記モノマーはこれらの溶
剤により希釈下に重合させることが好ましく、lθmo
l/1以上の高濃度で重合させると三次元架橋反応が進
行しゲル化しやすい。
In the polymerization reaction to obtain the polymer of the present invention, seven polymers are used.
As the solvent for diluting, aromatic hydrocarbons such as benzene and toluene, halogenated hydrocarbons such as carbon tetrachloride and chloroform, and ethers such as diethyl ether, tetrahydrofuran and dioxane are used. However, in the case of the Ziegler-Natsuta type catalyst, it is preferable to use an aromatic hydrocarbon as the solvent. It is preferable that the monomer is polymerized while being diluted with these solvents, and lθmo
If polymerization is carried out at a high concentration of 1/1 or more, a three-dimensional crosslinking reaction will proceed and gelation will occur easily.

重合反応の停止は、チーグラー・ナツタ型触媒及びタン
グステンヘキサカルボニルないしモリブデンヘキサカル
ボニルを有機ノ〜ロゲン化吻の存在下に光照射して得ら
れる触媒を用いた場合は、少量のメタノール等のアルコ
ールにより行ない、六塩化タングステンあるいは五塩化
モリブデンを用いた場合は、少量のアンモニア性アルコ
ール、例えば、アンモニア性メタノールにより行なう。
When using a Ziegler-Natsuta type catalyst and a catalyst obtained by irradiating tungsten hexacarbonyl or molybdenum hexacarbonyl with light in the presence of an organic halogenated proboscis, the polymerization reaction can be terminated by using a small amount of alcohol such as methanol. When tungsten hexachloride or molybdenum pentachloride is used, a small amount of ammoniacal alcohol, such as ammoniacal methanol, is used.

その後不溶性のゲル化物、触媒等を一過した後、大量の
メタノール等の低級アルコールないしはヘキサン等の脂
肪族炭化水素により目的の重合体を析出させる。
Thereafter, insoluble gelled substances, catalysts, etc. are passed through, and then the desired polymer is precipitated with a large amount of lower alcohol such as methanol or aliphatic hydrocarbon such as hexane.

チーグラー・ナツタ型触媒を用いた場合は、更に塩酸/
メタノール混合液により洗浄し触媒を除去することが好
ましい。
When using a Ziegler-Natsuta type catalyst, additional hydrochloric acid/
It is preferable to remove the catalyst by washing with a methanol mixture.

得られた重合体は、一般に暗赤色の粉末であり、ハロゲ
ン化炭化水素、芳香族炭化水素、ケトン系炭化水素等に
可溶で、脂肪族系炭化水素、低級アルコールに不溶であ
る。
The obtained polymer is generally a dark red powder, which is soluble in halogenated hydrocarbons, aromatic hydrocarbons, ketone hydrocarbons, etc., and insoluble in aliphatic hydrocarbons and lower alcohols.

このようにして得られた重合体は、エチニル基をもつこ
とから、電子線レジスト、感光性樹脂、熱硬化型耐熱樹
脂等に用いることが可能であり、特に感光性樹脂及び電
子線レジストとして用いた場合、感度が高く、耐ドライ
エツチ性が高く、また硬化時にガス発生がないため、均
一な皮膜を作る等の有用性がある。
Since the polymer obtained in this way has an ethynyl group, it can be used for electron beam resists, photosensitive resins, thermosetting heat-resistant resins, etc., and is particularly useful as photosensitive resins and electron beam resists. When used, it has high sensitivity, high dry etch resistance, and does not generate gas during curing, so it is useful for producing uniform films.

また、この重合体は主鎖が共役二重結合より構成されて
いることから導電性樹脂材料としても用いることが可能
である。
Furthermore, since the main chain of this polymer is composed of conjugated double bonds, it can also be used as a conductive resin material.

更に、溶剤に溶解した重合体をゲル化溶剤により処理す
ることによりフィルム状、中空糸状等に成型し、選択透
過膜として使用することも可能である。
Furthermore, by treating a polymer dissolved in a solvent with a gelling solvent, it can be formed into a film shape, hollow fiber shape, etc., and used as a selectively permeable membrane.

次に、本発明を実施例により詳しく説明するが、本発明
はこれに限定されるものではない。
Next, the present invention will be explained in detail with reference to Examples, but the present invention is not limited thereto.

実施例/ ジン気流下に加えて触媒溶液とした。これにp−ジエチ
ニルベンゼイン7mmolの20tntトルエン溶液を
室温アルゴン気流下に滴下した。コグ時間後にメタノー
ルIO−を加えて反応を停止し、ゲル化物を一過後、母
液をメタノール/濃塩酸(10:l)の100−に投入
し重合体を析出させる。
Example/ A catalyst solution was prepared under a stream of gin. A 20 tnt toluene solution containing 7 mmol of p-diethynylbenzein was added dropwise to this under an argon stream at room temperature. After the cog time, methanol IO- is added to stop the reaction, and after passing the gelled product, the mother liquor is poured into 100-methanol/concentrated hydrochloric acid (10:l) to precipitate the polymer.

重合体を一過し、更にメタノール/濃塩酸、次いでメタ
ノールで洗浄し、減圧下室源で乾燥した。
The polymer was filtered, further washed with methanol/concentrated hydrochloric acid, then methanol, and dried under vacuum.

得られた重合体は暗赤色の粉末で、りpロホルム等のハ
ロゲン化炭化水素、ベンゼン、トルエン等の芳香族炭化
水素、及びアセトン等のケトン系炭化水素に可溶であり
、メタノール等の低級アルコール、ヘキサン等の脂肪族
炭化水素に不溶である。
The obtained polymer is a dark red powder that is soluble in halogenated hydrocarbons such as polyproform, aromatic hydrocarbons such as benzene and toluene, and ketone hydrocarbons such as acetone, and is soluble in low-grade hydrocarbons such as methanol. Insoluble in aliphatic hydrocarbons such as alcohol and hexane.

ゲルパーミェーションクロマトグラフィー(カラムは5
HODEX AC403+ kC−JOケ)による分子
量測定の結果では、重量平均分子量約コo、oooで鮎
った。
Gel permeation chromatography (column is 5
According to the results of molecular weight measurement using HODEX AC403+ kC-JOke), the weight average molecular weight was approximately 0.00,000.

第1図にこのポリマーの重クロロホルム中のプロトン核
磁気共鳴スペクトル(NMRスペクトル)を示す。
FIG. 1 shows the proton nuclear magnetic resonance spectrum (NMR spectrum) of this polymer in deuterated chloroform.

実施例コ ベンゼン kOdにWCl6の0.!r m mo 1
を加えて触媒溶液を調製し、これにp−ジェチニルベン
ゼン#7mmolの30−ベンゼン溶液を攪拌下に滴下
した。
Example cobenzene 0.0 kOd of WCl6. ! r m mo 1
was added to prepare a catalyst solution, and a 30-benzene solution containing 7 mmol of p-jethynylbenzene # was added dropwise thereto under stirring.

反応は30℃、窒素気流下に行ない、キシレンを内部標
準としてガスクロマトグラフィーにより七ツマー消費速
度を測定した。七ツマ−の消費量は30分〜7時間で平
衡に達し、一方時間と共にゲル化物の析出は顕著になる
。従って、目的とする1合体を収率よく得るためには反
応開始後73〜30分で反応を停止させることが好まし
い。
The reaction was carried out at 30° C. under a nitrogen stream, and the consumption rate of 7mer was measured by gas chromatography using xylene as an internal standard. The consumption amount of Natsuma reaches equilibrium in 30 minutes to 7 hours, while the precipitation of gelled products becomes more noticeable with time. Therefore, in order to obtain the desired monomer in a good yield, it is preferable to stop the reaction 73 to 30 minutes after the start of the reaction.

反応の停止は少量のアンモニア性メタノールを添加する
ことにより行なわれる。その彼ゲル化物をp別し、p液
を300−のn−ヘキサンに投入し、目的とする重合体
を析出する。濾過した重合体はメタノールで洗浄し、室
温真空下に乾燥した。得られた重合体の収率は約コO%
、ゲルパーミェーションクロマトグラフィーの結果では
重量平均分子量約7万であった。NMRスペクトルその
他の物性は実施例1により得られた重合体の結果と一致
した。
The reaction is stopped by adding a small amount of ammoniacal methanol. The gelled product is separated and the p solution is poured into 300% n-hexane to precipitate the desired polymer. The filtered polymer was washed with methanol and dried under vacuum at room temperature. The yield of the obtained polymer was approximately 0%
According to the results of gel permeation chromatography, the weight average molecular weight was approximately 70,000. The NMR spectrum and other physical properties were consistent with the results of the polymer obtained in Example 1.

実施例3 四塩化炭素go−にW (CO)aの2mmolを加え
、300Wの高圧水銀灯により7時間光照射を行ない触
媒溶液とした。これをp−ジェチニルベンゼン/θmm
olのgo−四塩化炭素溶液にqo℃窒素気流−下に滴
下した。1時間後に約10−のメタノールを加え反応を
停止し、固型物を一過した。p液を約コOdに議縮しn
−ヘキサンのコθθ−により重。
Example 3 2 mmol of W (CO)a was added to carbon tetrachloride go-, and the mixture was irradiated with light for 7 hours using a 300 W high-pressure mercury lamp to obtain a catalyst solution. This is p-jethynylbenzene/θmm
The mixture was added dropwise to a go-carbon tetrachloride solution of ol at qo°C under a nitrogen stream. After 1 hour, about 10 methanol was added to stop the reaction, and the solid matter was filtered off. Concentrate the p solution to about
-Heavier due to hexane coθθ-.

合体を析出させた。重合体を一過しメタノールにより洗
浄し減圧下室温で乾燥した。七ツマ−の消費率は実施例
コと同様の方法により測定し、約60−であった。この
方法によれば実施例−よりはるかにゲル化物が少なく、
最終的な重合体の収率はSOチであった。また、ゲルパ
ーミェーションクロマトグラフィーによる分子量は約2
hoooであったが、分子量分布は実施例1及び実施例
コにより得られた重合体より均一であった。NMRスペ
クトルその他の物性は実施例1及び実施例コの結果と一
致した。
The coalescence was precipitated. The polymer was filtered, washed with methanol, and dried under reduced pressure at room temperature. The consumption rate of seven sweet potatoes was measured by the same method as in Example 1, and was about 60. According to this method, there is much less gelled material than in Example-
The final polymer yield was SO. Furthermore, the molecular weight determined by gel permeation chromatography is approximately 2.
However, the molecular weight distribution was more uniform than the polymers obtained in Example 1 and Example 2. The NMR spectrum and other physical properties were consistent with the results of Example 1 and Example 2.

元素分析の結果は、炭素9ふθコチ、水素侶goチであ
った。
The results of elemental analysis were 9 carbon atoms and 9 hydrogen atoms.

実施例ダ p−ジェチニルベンゼンに替えてm−ジェチニルベンゼ
ンを用いる以外は実施例3と同様にして重合体を得た。
Example d A polymer was obtained in the same manner as in Example 3 except that m-jethynylbenzene was used instead of p-jethynylbenzene.

ゲルパーミェーションクロマトクラフィーによれば、得
られた重合体の分子量は約/ 200θであり、色、溶
媒に対する溶解性は実施例1ないし実施例3により得ら
れた重合体と同様であった。
According to gel permeation chromatography, the molecular weight of the obtained polymer was approximately /200θ, and the color and solubility in solvents were similar to those of the polymers obtained in Examples 1 to 3. Ta.

実施例S 実施例コにより得られた重合体をジメチルホルムアミド
に溶解し、プレパラート上にスピンコードした。このも
のにマスクパターンをかぶせて、10OW高圧水銀灯に
より3分間光′照射を行なった。
Example S The polymer obtained in Example A was dissolved in dimethylformamide and spin-coded onto a preparation. This material was covered with a mask pattern and irradiated with light for 3 minutes using a 10 OW high pressure mercury lamp.

このものをメチルエチルケトンにS分間浸漬し、更にヘ
キサンにより洗浄し、乾燥することにより解偉度の高い
画像が得られた。
This product was immersed in methyl ethyl ketone for S minutes, further washed with hexane, and dried to obtain a highly resolved image.

実施例6 実施例3により得られた重合体/重量部と重量平均分子
量1g万のポリスチレンコタ重量部を、1000重量部
のトルエンに溶解し゛、シリコンウェハー上にスピンコ
ードし、真空下室温で乾燥した。
Example 6 Parts by weight of the polymer obtained in Example 3 and parts by weight of polystyrene with a weight average molecular weight of 1 g were dissolved in 1000 parts by weight of toluene, spin-coded onto a silicon wafer, and dried under vacuum at room temperature. did.

このものに電子顕微鏡(日本分光製、コ3S−!型)に
より電子線を照射し、感度を測定したところ、lo−5
〜10”C/cdlの感度であった。なお、現像はlo
チのメタノールを含むメチルエチルケトンに3分間浸漬
することにより行なった。
When this material was irradiated with an electron beam using an electron microscope (manufactured by JASCO Corporation, type 3S-!) and the sensitivity was measured, it was found that lo-5
The sensitivity was ~10"C/cdl.The development was performed at lo
This was done by immersing the sample in methyl ethyl ketone containing methanol for 3 minutes.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、実施例1で得られたポリマーのNMRスペク
トル(l100M七)を示す。 特許出願人 旭化成工業株式会社 代理人弁理士 星 野 透 第1!i 手続補正書(自発) 昭和58年10月11日 昭和58年特許願第109321号 2、発明の名称 ポリエチニルフェニルアセチレンと その製造法 3、補正をする者 事件との関係 特許出願人 大阪府大阪市北区堂島浜1丁目2番6号(003)旭化
成工業株式会社 代表取締役社長 宮 崎 輝 4、代理人 東京都新宿区四谷3丁目7番地がっ新ビル586、補正
により増加する発明の数 なし7、補正の対象 明細書の「発明の詳細な説明Jr図面の簡単な説明」の
欄、及び図面 8、補正の内容(別紙のとおり) 補正の内容 ■、明細書の補正 明細書の記載を次のとおり補正する。 (1)第13頁7行〜9行目の rNMRスペクトル・・・と一致した。」をrNMRス
ペクトルを第2図に示す。得られた重合体の色及び溶媒
に対する熔解性は実施例1ないし実施例2と同様であっ
た。」 と訂正する。 (2)第14頁18行目と19行目の間に次の記載を追
加J−る。 「 実施例7 p−ジェチニルベンゼンに代えてp−ジェチニルベンゼ
ンと1ジエチニルベンゼン50 : 50の混合物を用
いる以外は実施例3と同様にして重合体を得た。 ゲルパーミェーションクロマトグラフィーによる重量平
均分子量は約11,000であり、色、溶媒に対する溶
解性は実施例工ないし実施例4により得られた重合体と
同様であった。」 (3) 第15頁1行目のあとに次の記載を追加する。 「第2図は、実施例3により得られた重合体のプロトン
N M R(100MllzN M R)スペクトルを
示す。」 ■0図面の補正 添イ1の第2図を特徴とする 特許出願人 旭化成工業株式会社 代理人 弁理土星野透
FIG. 1 shows the NMR spectrum (1100M7) of the polymer obtained in Example 1. Patent Applicant: Asahi Kasei Industries Co., Ltd. Representative Patent Attorney Toru Hoshino No. 1! i Procedural amendment (voluntary) October 11, 1988 Patent Application No. 109321 2, Name of the invention Polyethynylphenylacetylene and its manufacturing method 3, Relationship with the person making the amendment Case Patent applicant Osaka Prefecture 1-2-6 Dojimahama, Kita-ku, Osaka (003) Teru Miyazaki, President and Representative Director of Asahi Kasei Industries Co., Ltd. 4, Agent: Gashin Building 586, 3-7 Yotsuya, Shinjuku-ku, Tokyo, Number of inventions increased by amendment None 7, "Detailed Description of the Invention Jr. Brief Explanation of Drawings" column of the specification to be amended, and Drawing 8, Contents of the amendment (as attached) Contents of the amendment ■, Description of the amended specification of the specification shall be corrected as follows. (1) Consistent with the rNMR spectrum on page 13, lines 7 to 9. Figure 2 shows the rNMR spectrum of ``. The color and solubility of the obtained polymer in solvents were the same as in Examples 1 and 2. ” he corrected. (2) Add the following statement between lines 18 and 19 on page 14. Example 7 A polymer was obtained in the same manner as in Example 3 except that a 50:50 mixture of p-jethynylbenzene and 1-diethynylbenzene was used in place of p-jethynylbenzene. The weight average molecular weight determined by chromatography was approximately 11,000, and the color and solubility in solvents were similar to those of the polymers obtained in Examples to Example 4.'' (3) Page 15, line 1 Add the following statement after the eye. "Figure 2 shows the proton NMR (100MllzNMR) spectrum of the polymer obtained in Example 3." ■Patent applicant Asahi Kasei featuring Figure 2 of 0 Correction Attachment A1 of the drawing Kogyo Co., Ltd. Agent Patent Attorney Toru Sahono

Claims (1)

【特許請求の範囲】 (1)、下記構造式(1)で表わされる線状重合体。 (式中、エチニル基は、分子主鎖に対して、メタ位ない
しはパラ位に結合しており、nは重量平均分子量が10
00ないし100万になる数である。) (2)、構造式(ff)で示される化合物を、タングス
テンヘキサカルボニルまたは、モリブデンヘキサカルボ
ニルを有機ハロゲン化物の存在下に光照射して得られる
触媒を用いて、芳香族炭化水素またはハロゲン化炭化水
素の溶剤中でθ℃〜gO℃の温度範囲で、重合すること
を特徴とする構造式(I)で表わされる線状重合体の製
造法。 HCミC (式中、エチニル基は、互いにメタ位ないしはパラ位に
あるものである。) (B)、構造式(ff)で示される化合物を、大塩化タ
ングステン、あるいは五塩化モリブデンのいずれかの単
独あるいは、これらと有機スズ化合物、水等の助触媒の
併用による触媒を用いて、芳香族炭化水素、へpゲシ化
炭化水素、環状エーテル等の溶剤中でθ℃〜ざ0℃の温
度範囲で重合することを特徴とする構造式(1)で表わ
される線状重合体の製造法。 (4)、@造式(I[)で示される化合物を、構造式(
1)及び構造式(酌によって示される化合物の組み合わ
せよりなる触媒を用いて、芳香族炭化水素の溶剤中でθ
℃〜gO℃の温度範囲で重合することを特徴とする構造
式(1)で表わされる線状重合体の製造法。 Ti (Ql )4 (2)) AI ((h )3 (N) (式中、Qlは炭素数コO以下のアルコキシ基、Q2は
炭素数−θ以下のフルキル基ないしアリール基。)
[Scope of Claims] (1) A linear polymer represented by the following structural formula (1). (In the formula, the ethynyl group is bonded to the meta or para position with respect to the main chain of the molecule, and n is the weight average molecular weight of 10
It is a number from 00 to 1 million. ) (2) A compound represented by the structural formula (ff) is converted into an aromatic hydrocarbon or a halogenated compound using a catalyst obtained by irradiating tungsten hexacarbonyl or molybdenum hexacarbonyl with light in the presence of an organic halide. A method for producing a linear polymer represented by structural formula (I), which comprises polymerizing in a hydrocarbon solvent in a temperature range of θ°C to gO°C. HCmiC (In the formula, the ethynyl groups are in the meta or para position with respect to each other.) (B) The compound represented by the structural formula (ff) is replaced with either large tungsten chloride or molybdenum pentachloride. alone or in combination with an organotin compound, water, or other co-catalyst, in a solvent such as an aromatic hydrocarbon, a hegesified hydrocarbon, or a cyclic ether at a temperature of θ°C to 0°C. 1. A method for producing a linear polymer represented by structural formula (1), which is characterized in that the linear polymer is polymerized within a range. (4), @The compound represented by the structural formula (I[) is converted into a compound represented by the structural formula (I[)
1) and the structural formula (θ) in an aromatic hydrocarbon solvent using a catalyst consisting of a combination of compounds represented by
A method for producing a linear polymer represented by structural formula (1), which is characterized in that the polymerization is carried out in a temperature range of 0.degree. C. to gO 0 C. Ti (Ql )4 (2)) AI ((h)3 (N) (wherein, Ql is an alkoxy group with a carbon number of 0 or less, and Q2 is a fulkyl group or an aryl group with a carbon number of -θ or less.)
JP10932183A 1983-06-20 1983-06-20 Polyethynylphenylacetylene and its production Granted JPS601211A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP10932183A JPS601211A (en) 1983-06-20 1983-06-20 Polyethynylphenylacetylene and its production
US06/899,631 US4667006A (en) 1983-06-20 1986-08-25 Poly(ethynylphenyl)acetylene, its copolymer and composition thereof
US06/899,650 US4767797A (en) 1983-06-20 1986-08-25 Photocurable compositions of poly(ethynylphenyl)acetylene, its copolymer and composition thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10932183A JPS601211A (en) 1983-06-20 1983-06-20 Polyethynylphenylacetylene and its production

Publications (2)

Publication Number Publication Date
JPS601211A true JPS601211A (en) 1985-01-07
JPS6254329B2 JPS6254329B2 (en) 1987-11-14

Family

ID=14507258

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10932183A Granted JPS601211A (en) 1983-06-20 1983-06-20 Polyethynylphenylacetylene and its production

Country Status (1)

Country Link
JP (1) JPS601211A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5686027A (en) * 1988-06-15 1997-11-11 Aerojet-General Corporation Process for forming carbon-carbon composite
JP2008179699A (en) * 2007-01-24 2008-08-07 Fujifilm Corp Poly (acetylene) compound-containing composition

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5989310A (en) * 1982-11-12 1984-05-23 Mitsubishi Chem Ind Ltd Production of ethynyl compound polymer

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5989310A (en) * 1982-11-12 1984-05-23 Mitsubishi Chem Ind Ltd Production of ethynyl compound polymer

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5686027A (en) * 1988-06-15 1997-11-11 Aerojet-General Corporation Process for forming carbon-carbon composite
JP2008179699A (en) * 2007-01-24 2008-08-07 Fujifilm Corp Poly (acetylene) compound-containing composition

Also Published As

Publication number Publication date
JPS6254329B2 (en) 1987-11-14

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