JPS63277218A - Production of monodisperse polymer - Google Patents

Production of monodisperse polymer

Info

Publication number
JPS63277218A
JPS63277218A JP62310743A JP31074387A JPS63277218A JP S63277218 A JPS63277218 A JP S63277218A JP 62310743 A JP62310743 A JP 62310743A JP 31074387 A JP31074387 A JP 31074387A JP S63277218 A JPS63277218 A JP S63277218A
Authority
JP
Japan
Prior art keywords
polymerization
cyanoacrylate
polymerization initiator
monomer
anionic polymerization
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
JP62310743A
Other languages
Japanese (ja)
Other versions
JPH0670105B2 (en
Inventor
Masaji Yonezawa
米澤 正次
Takeo Sugiura
杉浦 猛雄
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.)
Toppan Inc
Original Assignee
Toppan Printing Co Ltd
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 Toppan Printing Co Ltd filed Critical Toppan Printing Co Ltd
Priority to JP62310743A priority Critical patent/JPH0670105B2/en
Publication of JPS63277218A publication Critical patent/JPS63277218A/en
Publication of JPH0670105B2 publication Critical patent/JPH0670105B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • GPHYSICS
    • G03PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
    • G03FPHOTOMECHANICAL PRODUCTION OF TEXTURED OR PATTERNED SURFACES, e.g. FOR PRINTING, FOR PROCESSING OF SEMICONDUCTOR DEVICES; MATERIALS THEREFOR; ORIGINALS THEREFOR; APPARATUS SPECIALLY ADAPTED THEREFOR
    • G03F7/00Photomechanical, e.g. photolithographic, production of textured or patterned surfaces, e.g. printing surfaces; Materials therefor, e.g. comprising photoresists; Apparatus specially adapted therefor
    • G03F7/004Photosensitive materials
    • G03F7/039Macromolecular compounds which are photodegradable, e.g. positive electron resists

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  • Physics & Mathematics (AREA)
  • Spectroscopy & Molecular Physics (AREA)
  • General Physics & Mathematics (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Exposure And Positioning Against Photoresist Photosensitive Materials (AREA)

Abstract

PURPOSE:To obtain the titled copolymer having extremely narrow molecular weight distribution range in high yield and good reproducibility, by polymerizing alpha-cyanoacrylate with a specific monomer using a specific polymerization initiator at a specific reaction temperature. CONSTITUTION:alpha-cyanoacrylate is polymerized with a monomer expressed by the formula [X is CN, NO2, etc.; Y is CN, H, etc.; R is (halogenated) alkyl] while cooling to -120-20 deg.C in the presence of an anionic polymerization initiator consisting of a weak anion of organic amine, organic amide, phosphine, thiourea, thioalcohol, ether, etc., to provide the aimed polymer. As the monomer expressed by the formula, e.g. vinylidenecyanide is used. As the anionic polymerization initiator, e.g. diethylamine is preferably used.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はα−シ、アノアクリル酸エステルの単分散共重
合体を再現性良く製造する方法に関するものである。さ
らに詳しくは、本発明は特定の重合開始剤を用い特定の
反応温度で溶媒中で重合することによって放射線感応性
レジスト材料を特徴とする特に重量平均分子量/数平均
分子Il(以下M w/ M n と略す)の値がほぼ
1になるような、分子量分布の幅の極めて狭いα−シア
ノアクリル酸エステル共重合体を、好収率且つ再現性良
く製造する方法を提供するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing a monodisperse copolymer of α-cy, anoacrylic acid ester with good reproducibility. More specifically, the present invention features a radiation-sensitive resist material by polymerizing in a solvent at a specific reaction temperature using a specific polymerization initiator. The present invention provides a method for producing an α-cyanoacrylic acid ester copolymer having an extremely narrow molecular weight distribution and a value of approximately 1 (abbreviated as n) in good yield and with good reproducibility.

〔発明の技術的背景〕[Technical background of the invention]

半導体大規8I集積回路の製造において更に高い集積度
が求められており、光学式露光の限界である線幅0.5
μ−以下のレベルのリソグラフィー技術として、電子ビ
ーム直接描画、X線リソグラフィーさらには集束イオン
ビームによる露光技術が提案されており、実現化しつつ
あるが、これに対応して実用化できるレジストが極めて
少ない。
A higher degree of integration is required in the manufacture of semiconductor large-scale 8I integrated circuits, and the line width is 0.5, which is the limit of optical exposure.
Electron beam direct writing, X-ray lithography, and exposure technology using focused ion beams have been proposed as sub-μ-level lithography technologies, and are being realized, but there are very few resists that can be put into practical use. .

これらレジスト材料には放射線を照射することにより架
橋反応を起こし、現像液に不溶化するネガ型と放射線を
照射することによりレジストの主剤ポリマーが分解反応
を起し、現像液に易溶化するポジ型とある。
These resist materials include negative type, which causes a crosslinking reaction by irradiation with radiation and becomes insoluble in the developer, and positive type, in which the main polymer of the resist causes a decomposition reaction and becomes easily soluble in the developer by irradiation with radiation. be.

ネガ型レジストの特徴は高感度で耐エツチング性に優れ
ているが、解像度が低いことである。
Negative resists are characterized by high sensitivity and excellent etching resistance, but low resolution.

一方、ポジ型レジストの特徴は高解像度であるが低感度
で耐エツチング性が劣ることである。
On the other hand, positive resists are characterized by high resolution but low sensitivity and poor etching resistance.

大規模集積回路の高集積化に対する産業界の要求は、最
近ますますニスカレートしており、高感度で耐エツチン
グ性の優れたネガレジストも、解像度が劣るので対応で
きなくなり、ポジ型が主流になりつつある。
Recently, industrial demands for higher integration of large-scale integrated circuits have been increasing, and even negative resists with high sensitivity and excellent etching resistance can no longer meet the demand due to their inferior resolution, and positive resists have become mainstream. It's coming.

〔従来技術と問題点〕[Prior art and problems]

従来、ポジ型の放射線感応性レジストの主剤としては、
ポリメチルメタクリレート(P−MMA)が代表的ポリ
マーであった。このP−MMAは、0.3〜0.5μ晴
程度の高解像度が得られる優れたレジストであるが、放
射線に対する感度が低く、電子ビームに対する感度が5
 X 10−’C/cl程度である。この低感応性を改
善する為に電子吸引基の導入が試みられ、実用感度を得
るに至っているレジストも散見される。
Conventionally, the main ingredients for positive radiation-sensitive resists are:
Polymethyl methacrylate (P-MMA) was the representative polymer. This P-MMA is an excellent resist that can provide a high resolution of about 0.3 to 0.5 microns, but its sensitivity to radiation is low and its sensitivity to electron beams is 5.
It is about X 10-'C/cl. In order to improve this low sensitivity, attempts have been made to introduce electron-withdrawing groups, and there are some resists that have achieved practical sensitivity.

しかし乍ら、電子吸引基の導入は耐エツチング性の低下
を招くケースが多い。
However, the introduction of electron-withdrawing groups often leads to a decrease in etching resistance.

α−シアノアクリル酸エステルを主剤とするレジストは
分子内に電子吸引基をもち、高感度の放射線感応性を有
するばかりでなく解像度も高(、優れたレジストである
が、64メガビンl−D−RAM以降の大規模集積回路
用レジストとしては感度も解像度も更に改善し、安定し
た実用性能をもつことが必須条件である。
The resist based on α-cyanoacrylic acid ester has an electron-withdrawing group in the molecule, and has not only high radiation sensitivity but also high resolution (64 megabin l-D- As a resist for large-scale integrated circuits after RAM, it is essential to further improve sensitivity and resolution and to have stable practical performance.

このため、感度改善にはより感度特性の優れたモノマー
との共重合を、解像度向上には単分散ポリマーを志向す
ることにより、この難問の打開を図る必要がある。
Therefore, it is necessary to overcome this difficult problem by aiming at copolymerization with a monomer having better sensitivity characteristics to improve sensitivity, and by aiming at monodisperse polymers to improve resolution.

〔発明の目的〕[Purpose of the invention]

本発明はα−シアノアクリル酸エステルに放射線に対し
て極めて優れた感応性を持っており、しか、もアニオン
重合挙動が酷似している一般式(I)のモノマーを単分
散共重合することにより、例えば64メガピッI−D−
RAM以降の大規模集積回路用として適合する高解像度
・高感度ポジ型放射線感応性レジストの主剤ポリマーを
提供することを目的としている。
The present invention is made by monodisperse copolymerizing monomers of the general formula (I) which have extremely excellent sensitivity to radiation and have very similar anionic polymerization behavior to α-cyanoacrylic acid esters. , for example, 64 megapith ID-
The object of the present invention is to provide a main polymer for a high-resolution, high-sensitivity positive-working radiation-sensitive resist suitable for large-scale integrated circuits after RAM.

〔発明の構成〕[Structure of the invention]

即ち、本発明はα−シアノアクリル酸エステルと一般式
(I) (ただし、式中のXはCN、 No□、C0OR,Yは
CN。
That is, the present invention relates to α-cyanoacrylic acid ester and general formula (I) (wherein, X is CN, No□, COOR, and Y is CN).

+I、 C0ORでRはアルキル基、ハロゲン化アルキ
ル基)で表わされるモノマ一群のうちの一種以上のモノ
マーを20〜−120℃に冷却しながら、有機アミン、
有機アミド、ホスフィン、チオ尿素、チオアルコール、
エーテル等の弱アニオンのうちの単独又はこれらを混合
して得られるアニオン重合開始剤の存在下で重合させ、
単分散共重合体を得ることを特徴とする。
While cooling one or more monomers from a group of monomers represented by +I, C0OR and R is an alkyl group or a halogenated alkyl group to 20 to -120°C, an organic amine,
organic amide, phosphine, thiourea, thioalcohol,
Polymerization in the presence of an anionic polymerization initiator obtained from weak anions such as ethers alone or by mixing them,
It is characterized by obtaining a monodisperse copolymer.

α−シアノアクリル酸エステルの重合方法についてはJ
、^ppl、 Po1yLSei、+土、231 (I
960)、を合化1ユ、280 (昭和44年)に記述
されているとおり、ラジカル重合法とアニオン重合法が
ある。また、−r式(I)で表される七ツマ−のアニオ
ン重合性に関しては「高分子の合成」 (化学同人発行
1961版)の67頁に記述されているとおり、α−シ
アンアクリル酸エステルと酷似した挙動を示すことが知
られている。したがって、これらの七ツマ−のアニオン
重合性の説明を簡素化するため、これらの代表とし°C
α−シアノアクリル酸エステルのアニオン重合性につい
て述べる。
Regarding the polymerization method of α-cyanoacrylic acid ester, please refer to J.
, ^ppl, Po1yLSei, + Sat, 231 (I
There are radical polymerization methods and anionic polymerization methods, as described in 960), 1 Yu, 280 (1962). Regarding the anionic polymerizability of the 7-mer represented by -r formula (I), as described on page 67 of "Synthesis of Polymers" (1961 edition published by Kagaku Dojin), α-cyanacrylic acid ester It is known that the behavior is very similar to that of Therefore, in order to simplify the explanation of the anionic polymerizability of these seven polymers, these representative
The anionic polymerizability of α-cyanoacrylic acid ester will be described.

一般に、ラジカル重合法では分子量分布の極端に狭い重
合体を得ることが困難であることは周知の事実であり、
解像度の改良には余り効果がない。
It is generally known that it is difficult to obtain polymers with an extremely narrow molecular weight distribution using radical polymerization methods.
Improving resolution has little effect.

一方アニオン重合法ではスチレン、p−ジメチルアミノ
メチルスチレン、イソプレン等のアニオン重合に代表さ
れるように分子量分布の非常に狭い重合体が得られるこ
とは公知であるが、α−シアノアクリル酸エステルのア
ニオン重合においてはその非常に高いアニオン重合性の
為、通常のモノマーのアニオン重合に比べ、分子量や分
子量分布を規制することは極めて困難で、上記文献等に
記述されているようなアニオン重合法では所定の分子量
、分子量分布を有する重合体を再現性良く製造すること
はできない。
On the other hand, it is known that the anionic polymerization method yields polymers with a very narrow molecular weight distribution, as typified by the anionic polymerization of styrene, p-dimethylaminomethylstyrene, isoprene, etc.; Due to the extremely high anionic polymerizability in anionic polymerization, it is extremely difficult to control the molecular weight and molecular weight distribution compared to the anionic polymerization of ordinary monomers, and the anionic polymerization method described in the above literature etc. A polymer having a predetermined molecular weight and molecular weight distribution cannot be produced with good reproducibility.

また、この重合体を強いて製造を試みても重合条件等に
多くの操作上の制限が必要となり、実用J二再現性を得
ることは不可能であった。
Further, even if attempts were made to produce this polymer by forcing it, many operational restrictions would be required on polymerization conditions, etc., and it would be impossible to obtain practical reproducibility.

−11にα−シアノアクリル酸エステルが、水やアルコ
ール等の微弱塩基によってさえも重合を開始することは
、これを主剤とした瞬間接着剤が被着体の表面に付着し
ている極微量の水分を硬化剤として常温で瞬間的にアニ
オン重合する機能によって、−液性万能接着剤として賞
用されていることからも明らかである。
-11. The fact that α-cyanoacrylic acid ester initiates polymerization even in the presence of a weak base such as water or alcohol is due to the fact that instant adhesives containing this as the main ingredient can be used in extremely small amounts on the surface of adherends. This is evident from the fact that it is prized as a liquid-based all-purpose adhesive due to its ability to instantaneously undergo anionic polymerization at room temperature using water as a curing agent.

アニオン重合には、理論上は停止反応が無いので、重合
開始剤の量をtI!節することにより、所定の分子量と
分子量分布の極めて狭い(理論的には同一分子量の)重
合体が得られる筈であるが、不純物などにより起る停止
反応等の副反応が併発するケースが多い。
Theoretically, there is no termination reaction in anionic polymerization, so the amount of polymerization initiator should be adjusted to tI! Although it is possible to obtain a polymer with a predetermined molecular weight and extremely narrow molecular weight distribution (theoretically, the same molecular weight) by separating the polymers, side reactions such as termination reactions caused by impurities often occur simultaneously. .

α−シアノアクリル酸エステルのアニオン重合開始剤と
して水、アルコールなどの微弱塩基を使用した場合は、
その重合速度が極めて遅く、瞬間接着剤のように極微量
のモノマーを扱う場合は使えるが、この重合反応は微量
不純物の影響を受は易く、生産性も悪いので工業的製法
としては不適当である。
When a weak base such as water or alcohol is used as an anionic polymerization initiator for α-cyanoacrylic acid ester,
Its polymerization rate is extremely slow, and it can be used when handling extremely small amounts of monomers, such as in instant adhesives, but this polymerization reaction is easily affected by trace impurities and has poor productivity, making it unsuitable as an industrial manufacturing method. be.

一方、より求核性、塩基性の高いホスフィン類やアミン
類を重合開始剤として用いた場合、通常の条件では、重
合速度が極めて速く、暴走反応を起して副反応を生じ、
生成重合体の分子量、分子量分布を容易に規制すること
はできない。
On the other hand, when phosphines and amines, which are more nucleophilic and highly basic, are used as polymerization initiators, the polymerization rate is extremely fast under normal conditions, causing runaway reactions and side reactions.
The molecular weight and molecular weight distribution of the produced polymer cannot be easily controlled.

また、このほかにα−シアノアクリル酸エステル中には
通常、重合禁止剤として二酸化硫黄、プロパンザルトン
等の酸性物質が添加され、これらによりα−シアノアク
リル酸エステルの貯蔵安定性が維持されているが、これ
らによる停止反応の併発が重合の生長反応に影響を与え
ることは明らかである。
In addition, acidic substances such as sulfur dioxide and propanezalton are usually added to α-cyanoacrylic ester as polymerization inhibitors, and these maintain the storage stability of α-cyanoacrylic ester. However, it is clear that the simultaneous occurrence of termination reactions due to these influences the growth reaction of polymerization.

本発明者らは、上記のα−シアノアクリル酸エステルの
特異的なアニオン重合性に着目し、高感度で秀れた解像
度を有するポジ型レジスト用材料として有用な重合体の
製法を提供することを主目的とし、α−シアノアクリル
酸エステルの重合方法について種々検討した結果、これ
らのモノマーのアニオンに対する重合性が極めて激しい
ので、α−シアンアクリル酸エステルをその凝固点乃至
それ以下の反応温度に冷却し、その分子運動を抑制し、
水などの極微弱アニオンに比べ活性が強いa機アミド、
ホスフィン、存機アミン、チオ尿素、チオアルコール、
エーテル等の重合開始剤の存在下で、重合させることに
より、系内の水、その他の不純物により併発する副反応
、二酸化硫黄、プロパンサルトン等の酸性物質による重
合停止反応などが、抑制できる再現性の優れた単分散ポ
リマーの製造方法を見出し、本発明を完成した。
The present inventors have focused on the specific anionic polymerizability of the above-mentioned α-cyanoacrylic acid ester, and provide a method for producing a polymer useful as a positive resist material having high sensitivity and excellent resolution. As a result of various studies on the polymerization method of α-cyanoacrylic acid ester with the main purpose of and suppress the molecular movement,
A-type amide, which is more active than extremely weak anions such as water,
Phosphine, active amine, thiourea, thioalcohol,
By polymerizing in the presence of a polymerization initiator such as ether, side reactions caused by water and other impurities in the system, and polymerization termination reactions caused by acidic substances such as sulfur dioxide and propane sultone can be suppressed. They discovered a method for producing monodispersed polymers with excellent properties and completed the present invention.

以下、本発明について更に詳細に説明する。The present invention will be explained in more detail below.

本発明で用いられる一般式(I)で表されるモノマーは
、具体的いはビニリデンアニド、ニトロエチレン、メチ
レンマロン酸ジエチル等であり、これに対応するα−シ
アノアクリル酸エステルは、次の一般式で表わされるも
のである。
Specific examples of the monomer represented by the general formula (I) used in the present invention include vinylidene anide, nitroethylene, diethyl methylene malonate, etc., and the corresponding α-cyanoacrylate ester is as follows. It is expressed by a general formula.

N 1(よC= C−C0OR ただし、式中Rは炭素数1から12の範囲にあるアルキ
ル基、ハロゲン化アルキル基、シクロアルキル基、アル
ケニル基、アルコキシアルキル基、アルキニル基あるい
はアリル基などであり、具体的にはα−シアノアクリル
酸メチル、α−シアノアクリル酸エチル、α−シアンア
クリル酸n−プロピル、α−シアノアクリル酸イソプロ
ヒル、α−シアノアクリル酸n−ブチル、α−シアノア
クリル酸イソブチル、α−シアノアクリル酸n−ペンチ
ル、α−シアノアクリル酸イソアミル、α−シアノアク
リル酸n−ヘキシル、α−シアンアクリルHn−オクチ
ル、α−シアノアクリル酸シクロヘキシル、α−シアノ
アクリル酸2−エチルヘキシル、α−シアノアクリル酸
アリル、α−シアノアクリル酸ベンジル、α−シアノア
クリル酸2−メトキシエチル、α−シアノアクリル酸プ
ロパギル、α−シアノアクリル酸トリクロロエチル、α
−シアノアクリル酸テトラクロロプロヒル、α−シアノ
アクリル酸トリフルオロエチル、α−シアノアクリル酸
フェニル等である。
N 1 (YoC=C-C0OR However, in the formula, R is an alkyl group, a halogenated alkyl group, a cycloalkyl group, an alkenyl group, an alkoxyalkyl group, an alkynyl group, an allyl group, etc. having a carbon number of 1 to 12. Yes, specifically methyl α-cyanoacrylate, ethyl α-cyanoacrylate, n-propyl α-cyanoacrylate, isoproyl α-cyanoacrylate, n-butyl α-cyanoacrylate, α-cyanoacrylate. Isobutyl, n-pentyl α-cyanoacrylate, isoamyl α-cyanoacrylate, n-hexyl α-cyanoacrylate, Hn-octyl α-cyanoacrylate, cyclohexyl α-cyanoacrylate, 2-ethylhexyl α-cyanoacrylate , α-allyl cyanoacrylate, benzyl α-cyanoacrylate, 2-methoxyethyl α-cyanoacrylate, propargyl α-cyanoacrylate, trichloroethyl α-cyanoacrylate, α
-tetrachloroproyl cyanoacrylate, trifluoroethyl α-cyanoacrylate, phenyl α-cyanoacrylate, and the like.

これらはいずれも通常の合成法で得られたもので良く、
アニオン重合抑制剤を5〜501+1)I+、ラジカル
重合抑制剤2.000ppm以下含むものであればよい
、 本発明の製造方法においては、特定のアニオン重合
開始剤と反応温度の制′4nが必須条件であり、その重
合開始剤とは有機アミン、有機アミド、ホスフィン、チ
オ尿素、チオアルコール、エーテル等の弱アニオン又は
それらの混合物で、好ましくはジエチルアミン、ジメチ
ル・バラ・トルイジン、アニリン、ジメチルホルムアミ
ド、ジフェニルホスフィン、2.5−キシリジン、チオ
セミカルバジド、チオ尿素、1.3−ジフェニルチオ尿
素、1−プロパンチオール、15クラウン5エーテルな
どである。
All of these can be obtained by ordinary synthetic methods,
It is sufficient that it contains an anionic polymerization inhibitor of 5 to 501+1)I+ and a radical polymerization inhibitor of 2.000 ppm or less. In the production method of the present invention, a specific anionic polymerization initiator and control of the reaction temperature are essential conditions. The polymerization initiator is a weak anion such as organic amine, organic amide, phosphine, thiourea, thioalcohol, ether, or a mixture thereof, preferably diethylamine, dimethyl baro-toluidine, aniline, dimethylformamide, diphenyl. They include phosphine, 2,5-xylidine, thiosemicarbazide, thiourea, 1,3-diphenylthiourea, 1-propanethiol, 15 crown 5 ether, and the like.

これらの重合開始剤の添加量は蒔に限定しないが、好ま
しくはモノマーに対し0.01〜2,0モル%である。
The amount of these polymerization initiators added is not limited to the amount, but is preferably 0.01 to 2.0 mol % based on the monomer.

反応温度はそれぞれのモノマーの凝固点附近か、それ以
下の反応温度が好ましい。この低温下の重合反応は七ツ
マ−の分子運動を極力セーブして、比較的活性の強い開
始剤を使用し、微量不純物による副反応を抑え込むこと
を目的としたものである。使用可能な反応温度は20〜
−120°Cであるが、好ましくは、−30〜−100
’Cである。
The reaction temperature is preferably near or below the freezing point of each monomer. The purpose of this low-temperature polymerization reaction is to minimize the molecular movement of the seven polymers, use a relatively active initiator, and suppress side reactions caused by trace impurities. Usable reaction temperature is 20~
-120°C, preferably -30 to -100°C
'C.

このために使用される溶媒としてはアセトン、メチルエ
チルケトン、酢酸エチル、シクロヘキサノン、メチルイ
ソブチルケトン、アセトニトリル、プロピオニトリル、
トリクロルエチレン、T)!Fなどのほか、これらの混
合溶媒である。
Solvents used for this purpose include acetone, methyl ethyl ketone, ethyl acetate, cyclohexanone, methyl isobutyl ketone, acetonitrile, propionitrile,
Trichlorethylene, T)! In addition to F, etc., these solvents are mixed solvents.

いずれにしても、使用される溶媒は一般式(■)の単独
重合体、共重合体及びα−シアノアクリル酸エステルと
の共重合体の良溶媒で、所定の低温下で一般式(I)の
単独重合体、共重合体及びα−シアノアクリル酸エステ
ルとの共重合体を析出させることのない溶媒でなくては
ならない。
In any case, the solvent used is a good solvent for the homopolymer, copolymer, and copolymer of the general formula (■) and the copolymer with α-cyanoacrylic acid ester, and the general formula (I) is The solvent must not precipitate homopolymers, copolymers, and copolymers with α-cyanoacrylic acid ester.

これらの溶媒は公知の脱水方法で精製したものが使用で
きる。
These solvents can be purified by known dehydration methods.

以上、説明した一般式<1)の単独重合体、共重合体及
びα−シアノアクリル酸エステルとの共重合体の単分散
ポリマーの製造方法により、2万〜100万の任意の分
子量の単分散ポリマーが再現性良く好収率で得られる。
As described above, by the method for producing monodisperse polymers of homopolymers, copolymers, and copolymers with α-cyanoacrylic acid esters of the general formula <1), monodisperse polymers with an arbitrary molecular weight of 20,000 to 1,000,000 are produced. Polymers can be obtained with good reproducibility and good yields.

本発明の重合方法を実施する手段としては、重合容器中
に所定の溶媒所定量を導入し、ついで所定の重合開始剤
を所定量加え、所定温度まで冷却する。
As a means for implementing the polymerization method of the present invention, a predetermined amount of a predetermined solvent is introduced into a polymerization container, then a predetermined amount of a predetermined polymerization initiator is added, and the container is cooled to a predetermined temperature.

この重合開始剤溶液を十分かきまぜながら、所定量の一
般式(I)のモノマーを含む所定溶媒の所定量を所定温
度で加えて重合反応を行なう(単独重合の場合)、共重
合の場合はこのようにして得られたりピングポリマーに
、更に所定の七ツマ−を所定量を含む所定溶媒を所定量
加えてブロック重合させ、重合停止剤で反応を停止させ
た。然しながら、この順序に特に限定されるものではな
い。
While thoroughly stirring this polymerization initiator solution, a predetermined amount of a predetermined solvent containing a predetermined amount of the monomer of general formula (I) is added at a predetermined temperature to conduct a polymerization reaction (in the case of homopolymerization), and in the case of copolymerization, this A predetermined amount of a predetermined solvent containing a predetermined amount of a predetermined 7-mer was further added to the thus-obtained orping polymer for block polymerization, and the reaction was terminated with a polymerization terminator. However, this order is not particularly limited.

本発明の方法は重合の規模の大小に無関係に適用可能で
ある。
The method of the present invention is applicable regardless of the scale of the polymerization.

(発明の効果) 本発明は特定のアニオン重合開始剤を用い特定の温度と
特定の溶媒を使用してα−シアノアクリル酸エステルと
一般式(I)の極めてアニオン重合性の強いモノマーの
単分散共重合体を経済的且つ効率よく得る方法を提供す
るものであり、この重合体を主剤とするレジストはD−
RAMにして例えば、64メガビツト以降の半導体大規
模集積回路製造の際の電子ビーム、X線リソグラフィー
用として半導体技術の向上とその経済性に大きく寄与す
るものである。
(Effects of the Invention) The present invention uses a specific anionic polymerization initiator, a specific temperature, and a specific solvent to monodisperse α-cyanoacrylic acid ester and a highly anionically polymerizable monomer of general formula (I). It provides a method for economically and efficiently obtaining a copolymer, and a resist based on this polymer is D-
As a RAM, for example, it is used for electron beam or X-ray lithography in the manufacture of semiconductor large-scale integrated circuits of 64 megabits or higher, and greatly contributes to the improvement of semiconductor technology and its economic efficiency.

実施例1 重合開始剤としてジエチルアミン5X10−’モルを含
む800m+1のトルエン溶液をフラスコ内に導入し、
このフラスコを一55°Cに冷却した。
Example 1 An 800 m+1 toluene solution containing 5×10 −′ moles of diethylamine as a polymerization initiator was introduced into a flask,
The flask was cooled to -55°C.

この溶液を十分かきまぜながら、メチレンマロン酸ジエ
チルを0.1モル含む100m1のトルエン溶液を一5
5°Cを超えないように遂次導入して重合させた後、ア
ニオン重合停止剤を加えてこの重合体を再沈殿法により
精製し、ゲルパーミェーションクロマトグラフィー(c
pc)−光散乱法で分子量を測定したところ、分子量は
37万で分散度は1.04であった。
While thoroughly stirring this solution, add 15 ml of a toluene solution containing 0.1 mol of diethyl methylenemalonate.
After polymerization by sequentially introducing the polymer at a temperature not exceeding 5°C, an anionic polymerization terminator was added and the polymer was purified by reprecipitation method, followed by gel permeation chromatography (c
When the molecular weight was measured by a pc)-light scattering method, the molecular weight was 370,000 and the dispersity was 1.04.

実施例2〜6 所定重合溶媒700m1に所定の重合開始剤を所定量加
え、系内温度な−40〜−80°Cに冷却した。この重
合開始剤溶液を十分かきまぜながら、アニオン重合抑制
剤SSO450pp+を含む所定の一般式(I)の所定
モノマー所定量を含む所定重合溶媒100m1 を所定
温度を超えないように遂次導入して重合させ、このよう
にして得られたりピングポリマーにアニオン重合抑制剤
SO□50ppmを含む所定のα−シアノアクリル酸エ
ステルモノマー所定量を含む所定重合溶媒100m! 
を十分かきまぜながら所定温度を超えないように遂次導
入して重合させた後、アニオン重合停止剤で重合反応を
停止させて共重合体を得たにの共重合体を再沈殿法によ
り精製後、GPC−光散乱法で分子量を測定し表1の結
果を得た。(以下余白) 表  1 ゜−シアノアクリル酸エステルと一般式([)のモノマ
ー仕込量の合計モル数0.1モル(α−シアノアクリル
酸エステル/一般式(I)のモノマー−0,07モル1
0.03モル)アニオン重合開始剤の仕込量:5X10
−’モル仕込モノマー/仕込アニオン重合開始剤(モル
比)2.0Of):1比較例1〜4 所定の重合開始剤5XIQ−’モルを含む、700ym
lのアセトントルエン混合溶液をフラスコ内に導入し、
系内温度を30″Cに保った。この系内に十分かきまぜ
ながらアニオン重合抑制剤so工50ppmを含むメチ
レンマロン酸ジエチルo、03モルヲ含ムアセトン・ト
ルエン混合溶媒を遂次導入して重合させた後、このリビ
ングポリマーにアニオン重合抑制剤S08を50ppm
含むα−シアノアクリル酸エチル0.07モルを含むア
セトン・トルエン混合溶媒100m1を十分がきまぜな
がら遂次導入して重合させ、重合停止剤を加えて重合を
停止させて共重合体を得た。
Examples 2 to 6 A predetermined amount of a predetermined polymerization initiator was added to 700 ml of a predetermined polymerization solvent, and the mixture was cooled to an internal temperature of -40 to -80°C. While thoroughly stirring this polymerization initiator solution, 100 ml of a predetermined polymerization solvent containing a predetermined amount of a predetermined monomer of the predetermined general formula (I) including an anionic polymerization inhibitor SSO 450 pp+ is sequentially introduced without exceeding a predetermined temperature to cause polymerization. , 100 m of a predetermined polymerization solvent containing a predetermined amount of a predetermined α-cyanoacrylic acid ester monomer containing an anionic polymerization inhibitor SO□50 ppm in the thus obtained or ping polymer!
The copolymer was purified by the reprecipitation method and the copolymer was obtained by terminating the polymerization reaction with an anionic polymerization terminator. The molecular weight was measured by GPC-light scattering method and the results shown in Table 1 were obtained. (Space below) Table 1 Total number of moles of ゜-cyanoacrylic ester and monomer of general formula ([) charged: 0.1 mol (α-cyanoacrylic ester/monomer of general formula (I) - 0.07 mol) 1
0.03 mol) Amount of anionic polymerization initiator: 5X10
-' moles Charged monomer/charged anionic polymerization initiator (mole ratio) 2.0Of): 1 Comparative Examples 1 to 4 700ym containing 5XIQ-' moles of predetermined polymerization initiator
Introduce 1 of acetone toluene mixed solution into the flask,
The temperature inside the system was maintained at 30"C. While sufficiently stirring, an acetone/toluene mixed solvent containing 3 mol of diethyl methylene malonate containing 50 ppm of an anionic polymerization inhibitor was sequentially introduced into the system and polymerized. After that, 50 ppm of anionic polymerization inhibitor S08 was added to this living polymer.
100 ml of an acetone/toluene mixed solvent containing 0.07 mol of ethyl α-cyanoacrylate was sequentially introduced with sufficient stirring to polymerize, and a polymerization terminator was added to stop the polymerization to obtain a copolymer. .

この共重合体を再沈澱法により精製後、GPC−光散乱
法で分子量を測定し表2の結果を得た。
After purifying this copolymer by reprecipitation method, the molecular weight was measured by GPC-light scattering method, and the results shown in Table 2 were obtained.

この結果は反応温度30 ”Cでは単分散重合体が得ら
れないことを示すものであるや 表  2 (321下余白)
This result shows that a monodisperse polymer cannot be obtained at a reaction temperature of 30"C.Table 2 (bottom margin of 321)

Claims (1)

【特許請求の範囲】 一般式( I ) ▲数式、化学式、表等があります▼ (ただし、式中のXはCN、NO_2、COOR、Yは
CN、H、COOR、Rはアルキル基、ハロゲン化アル
キル基)で表わされるモノマー単独又はこれらのモノマ
ー群のうちの1種以上とα−シアノアクリル酸エステル
を20〜−120℃に冷却しながら、有機アミン、有機
アミド、ホスフィン、チオ尿素、チオアルコール、エー
テル等の弱アニオンのうちの単独又は2種以上を混合し
て得られるアニオン重合開始剤の存在下で重合させ、単
分散重合体を製造する方法。
[Claims] General formula (I) ▲There are mathematical formulas, chemical formulas, tables, etc.▼ (However, in the formula, X is CN, NO_2, COOR, Y is CN, H, COOR, R is an alkyl group, halogenated Alkyl group) monomer alone or one or more of these monomer groups and α-cyanoacrylic acid ester are cooled to 20 to -120°C while organic amine, organic amide, phosphine, thiourea, thioalcohol. , a method of producing a monodisperse polymer by polymerizing in the presence of an anionic polymerization initiator obtained singly or by mixing two or more of weak anions such as ether.
JP62310743A 1986-12-29 1987-12-08 Method for producing monodisperse polymer Expired - Lifetime JPH0670105B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62310743A JPH0670105B2 (en) 1986-12-29 1987-12-08 Method for producing monodisperse polymer

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP61-314224 1986-12-29
JP31422486 1986-12-29
JP62310743A JPH0670105B2 (en) 1986-12-29 1987-12-08 Method for producing monodisperse polymer

Publications (2)

Publication Number Publication Date
JPS63277218A true JPS63277218A (en) 1988-11-15
JPH0670105B2 JPH0670105B2 (en) 1994-09-07

Family

ID=26566439

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Country Link
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Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02113253A (en) * 1988-10-24 1990-04-25 Toagosei Chem Ind Co Ltd Positive type resist
JPH02264955A (en) * 1989-04-06 1990-10-29 Toppan Printing Co Ltd Positive type resist using electron beams
JPH02264259A (en) * 1989-04-03 1990-10-29 Toppan Printing Co Ltd Positive type resist composition and pattern forming method
WO1998025977A1 (en) * 1996-12-09 1998-06-18 Nippon Soda Co., Ltd. (meth)acrylic ester copolymers and process for producing the same
JP2015518503A (en) * 2012-03-30 2015-07-02 シラス・インコーポレイテッド Composite and laminated articles and polymerization systems for making them
CN105209509A (en) * 2013-05-16 2015-12-30 意大利学院科技基金会 Process for the production of poly(cyanoacrylate) fibres
JP2017527667A (en) * 2014-09-08 2017-09-21 シラス・インコーポレイテッド Solution polymer, solution polymerization method and polymer composition comprising one or more 1,1-disubstituted alkene compounds
JP2022513249A (en) * 2018-12-19 2022-02-07 アルケマ フランス Compositions comprising cyanoacrylates and at least one block copolymer
WO2023224054A1 (en) * 2022-05-20 2023-11-23 株式会社クラレ Resin composition, cured product, laminate, and method for producing laminate
WO2023224053A1 (en) * 2022-05-20 2023-11-23 株式会社クラレ Resin composition, cured product, laminate, and method for producing laminate
WO2024080287A1 (en) * 2022-10-11 2024-04-18 株式会社クラレ Copolymer and resin composition containing copolymer

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4867335A (en) * 1971-12-14 1973-09-14
JPS49116188A (en) * 1973-03-12 1974-11-06
JPS50128790A (en) * 1974-03-27 1975-10-11
JPS53129231A (en) * 1977-04-19 1978-11-11 Toagosei Chem Ind Co Ltd Adhesion composition
JPS5512166A (en) * 1978-07-13 1980-01-28 Nogawa Chem Kk Adhesive composition
JPS58108213A (en) * 1981-12-22 1983-06-28 Toagosei Chem Ind Co Ltd Preparation of polymer of 2-cyanoacrylic acid ester

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4867335A (en) * 1971-12-14 1973-09-14
JPS49116188A (en) * 1973-03-12 1974-11-06
JPS50128790A (en) * 1974-03-27 1975-10-11
JPS53129231A (en) * 1977-04-19 1978-11-11 Toagosei Chem Ind Co Ltd Adhesion composition
JPS5512166A (en) * 1978-07-13 1980-01-28 Nogawa Chem Kk Adhesive composition
JPS58108213A (en) * 1981-12-22 1983-06-28 Toagosei Chem Ind Co Ltd Preparation of polymer of 2-cyanoacrylic acid ester

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02113253A (en) * 1988-10-24 1990-04-25 Toagosei Chem Ind Co Ltd Positive type resist
JPH02264259A (en) * 1989-04-03 1990-10-29 Toppan Printing Co Ltd Positive type resist composition and pattern forming method
JPH02264955A (en) * 1989-04-06 1990-10-29 Toppan Printing Co Ltd Positive type resist using electron beams
WO1998025977A1 (en) * 1996-12-09 1998-06-18 Nippon Soda Co., Ltd. (meth)acrylic ester copolymers and process for producing the same
JP2019151847A (en) * 2012-03-30 2019-09-12 シラス・インコーポレイテッド Composites and laminate articles, and polymerizable systems for producing the same
JP2015518503A (en) * 2012-03-30 2015-07-02 シラス・インコーポレイテッド Composite and laminated articles and polymerization systems for making them
CN105209509A (en) * 2013-05-16 2015-12-30 意大利学院科技基金会 Process for the production of poly(cyanoacrylate) fibres
JP2017527667A (en) * 2014-09-08 2017-09-21 シラス・インコーポレイテッド Solution polymer, solution polymerization method and polymer composition comprising one or more 1,1-disubstituted alkene compounds
JP2017527668A (en) * 2014-09-08 2017-09-21 シラス・インコーポレイテッド Polymers comprising one or more 1,1-disubstituted alkene compounds and polymer compositions thereof
JP2020002369A (en) * 2014-09-08 2020-01-09 シラス・インコーポレイテッド Emulsion polymer containing one or more 1,1-disubstituted alkene compound, emulsion method, and polymer composition
JP2020117721A (en) * 2014-09-08 2020-08-06 シラス・インコーポレイテッド Polymers including one or more 1,1-disubstituted alkene compounds and polymer compositions thereof
JP2022513249A (en) * 2018-12-19 2022-02-07 アルケマ フランス Compositions comprising cyanoacrylates and at least one block copolymer
WO2023224054A1 (en) * 2022-05-20 2023-11-23 株式会社クラレ Resin composition, cured product, laminate, and method for producing laminate
WO2023224053A1 (en) * 2022-05-20 2023-11-23 株式会社クラレ Resin composition, cured product, laminate, and method for producing laminate
WO2024080287A1 (en) * 2022-10-11 2024-04-18 株式会社クラレ Copolymer and resin composition containing copolymer

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