JPS60112808A - Preparation of hydroxyl group-containing diene polymer - Google Patents

Preparation of hydroxyl group-containing diene polymer

Info

Publication number
JPS60112808A
JPS60112808A JP58220674A JP22067483A JPS60112808A JP S60112808 A JPS60112808 A JP S60112808A JP 58220674 A JP58220674 A JP 58220674A JP 22067483 A JP22067483 A JP 22067483A JP S60112808 A JPS60112808 A JP S60112808A
Authority
JP
Japan
Prior art keywords
hydrogen peroxide
conjugated diene
polymer
hydroxyl group
diene monomer
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
JP58220674A
Other languages
Japanese (ja)
Other versions
JPS6228964B2 (en
Inventor
Hidetoshi Shimada
英俊 島田
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.)
Idemitsu Petrochemical Co Ltd
Original Assignee
Idemitsu Petrochemical 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 Idemitsu Petrochemical Co Ltd filed Critical Idemitsu Petrochemical Co Ltd
Priority to JP58220674A priority Critical patent/JPS60112808A/en
Publication of JPS60112808A publication Critical patent/JPS60112808A/en
Publication of JPS6228964B2 publication Critical patent/JPS6228964B2/ja
Granted legal-status Critical Current

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  • Polymerization Catalysts (AREA)
  • Polyurethanes Or Polyureas (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

PURPOSE:To obtain the titled polymer useful for improving urethane foam, etc. in a short in high yield, by reacting a conjugated diene monomer with hydrogen peroxide (time catalyst) by the use of sulfobenzimide or naphthylacetic acid as a cocatalyst. CONSTITUTION:(B) A conjugated diene monomer (e.g., chloroprene, etc.) is reacted with (C) a catalyst of hydrogen peroxide by the use of (A) sulfobenzimide and/or naphthylacetic acid as a cocatalyst in a reaction medium (preferably methanol, etc.) to give the desired polymer. The compound A used is preferably 0.05-10wt% based on the component C. The polymerization is preferably carried out at 100-150 deg.C at 10-50 atmospheric pressure for 30min-5hr.

Description

【発明の詳細な説明】 本発明は水酸基含有ジエンポリマーの効率の良い製造方
法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an efficient method for producing a hydroxyl group-containing diene polymer.

従来より過酸化水素を触媒として共役ジエンモノマーを
重合させて末端に水酸基を有するジエン系重合体を製造
する方法は知られている。しかし、従来法は該重合体を
得るために、130°C前後の反応温度で比較的長時間
反応を行なう必要があった。また収率も十分なものでは
なかった。
BACKGROUND ART Conventionally, a method for producing a diene polymer having a hydroxyl group at the terminal by polymerizing a conjugated diene monomer using hydrogen peroxide as a catalyst has been known. However, in the conventional method, in order to obtain the polymer, it was necessary to conduct the reaction at a reaction temperature of about 130° C. for a relatively long time. Moreover, the yield was not sufficient.

そこで本発明者は、短時間で収率良くジエン系重合体を
製造する方法について鋭意研究した結果、過酸化水素と
ともに特定の助触媒を用いて重合反応を行なうと、短時
間で収率良く水酸基含有ジエン系重合体を製造すること
ができることを見い出し本発明を完成した。
Therefore, as a result of intensive research into a method for producing diene polymers in a short time and with high yield, the present inventor found that when a polymerization reaction is carried out using hydrogen peroxide and a specific co-catalyst, hydroxyl groups can be produced in a short time and with high yield. The present invention was completed by discovering that it is possible to produce a diene-containing polymer.

すなわち、本発明は共役ジエンモノマーを反応媒体中で
過酸化水素と反応させて水酸基含有ジエン系重合体を製
造する方法において、助触媒としてスルホベンズイミド
および/またはす7チル酢酸を用いることを特徴とする
水酸基含有ジエン系重合体の製造方法を提供するもので
ある。
That is, the present invention is characterized in that a method for producing a hydroxyl group-containing diene polymer by reacting a conjugated diene monomer with hydrogen peroxide in a reaction medium uses sulfobenzimide and/or 7-tyl acetic acid as a cocatalyst. The present invention provides a method for producing a hydroxyl group-containing diene polymer.

木兄11に用いる共役ジエンモノマーとしては特に制限
されないが、通常は炭素数4〜12個のジオレフィン形
不飽和の非置換−12−置換−もしくは2.3−置換−
1,3−ジエンが用いられる。
The conjugated diene monomer used for Kinoe 11 is not particularly limited, but is usually a diolefinically unsaturated unsubstituted-12-substituted or 2,3-substituted-carbon atom having 4 to 12 carbon atoms.
1,3-diene is used.

ここで置換基としてはアルキル基、アリール基。Here, the substituent is an alkyl group or an aryl group.

ハロゲン、シアノ基、ニトロ基などがある。具体的なモ
ノマーを例示すると、1,3−ブタジェン。
Examples include halogen, cyano group, and nitro group. A specific example of a monomer is 1,3-butadiene.

イソプレン、クロロプレン、2−シアノ−1,3−ブタ
ジェン、2,3−ジメチル−1,3−ブタジェンなどが
ある。
Examples include isoprene, chloroprene, 2-cyano-1,3-butadiene, and 2,3-dimethyl-1,3-butadiene.

前記重合体の製造においては、基本的には上記共役ジエ
ンモノマーを単独もしくは2種以上組合せて用いるが、
必要に応じて共役ジエンモノマーの一部をエチレン性不
飽和モノマーで置き換えることができ、炭素数2〜22
個のα−オレフィン性付加重合性モノマーが用いられる
。具体的にはスチレン、α−メチルスチレン、ビニルト
ルエン。
In the production of the above polymer, the above conjugated diene monomers are basically used alone or in combination of two or more, but
If necessary, a part of the conjugated diene monomer can be replaced with an ethylenically unsaturated monomer, and the conjugated diene monomer has 2 to 22 carbon atoms.
α-olefinic addition polymerizable monomers are used. Specifically, styrene, α-methylstyrene, and vinyltoluene.

メタアクリル酸メチル、アクリル酸、塩化ビニル。Methyl methacrylate, acrylic acid, vinyl chloride.

塩化ビニリデン、アクリロニトリル、アクリルアミド、
2−エチルへキシルアクリレート、n−オクタデシルア
クリレート、無水マレイン酸、ブテン、2−ヒドロキシ
エチルメタクリレートなどがある。このモノオレフィン
不飽和モノマーは好ましくは0〜75重量%の範囲で共
役ジエンモノマーと併用できる。
vinylidene chloride, acrylonitrile, acrylamide,
Examples include 2-ethylhexyl acrylate, n-octadecyl acrylate, maleic anhydride, butene, and 2-hydroxyethyl methacrylate. This monoolefinically unsaturated monomer can be used in combination with the conjugated diene monomer, preferably in a range of 0 to 75% by weight.

共役ジエンモノマーの重合反応は反応媒体中で行なわれ
、反応媒体としては該ジエンモノマーと過酸化水素の両
方に対して相溶性の良好な溶媒が好ましい。このような
溶媒としてメタノール、エタノール、n−プロパツール
、イソプロパツール。
The polymerization reaction of the conjugated diene monomer is carried out in a reaction medium, and the reaction medium is preferably a solvent having good compatibility with both the diene monomer and hydrogen peroxide. Such solvents include methanol, ethanol, n-propanol, isopropanol.

ブタノール、プロピルエーテル、テトラヒドロフラフ、
hNIkエチル、セロソルブ、セロソルブアセテート、
エチルセロソルブ、N、N−ジメチルホルムアミド、ア
セトンなどやこれらの混合物をあげることができる。溶
媒の使用量は全仕込み量(モノマー、過酸化水素、助触
媒および溶媒)の5〜90重量%、好ましくは30〜7
0重量%である。
butanol, propyl ether, tetrahydrofuraf,
hNIk ethyl, cellosolve, cellosolve acetate,
Examples include ethyl cellosolve, N,N-dimethylformamide, acetone, and mixtures thereof. The amount of solvent used is 5 to 90% by weight of the total amount charged (monomer, hydrogen peroxide, cocatalyst and solvent), preferably 30 to 7% by weight.
It is 0% by weight.

また、触媒として作用する過酸化水素は通常、30〜8
0%水溶液として用い、いずれにしても過酸化水素とし
て共役ジエンモノマーの0.5重量%以上、好ましくは
1〜12重量%添加する。
In addition, hydrogen peroxide, which acts as a catalyst, is usually 30 to 8
It is used as a 0% aqueous solution, and in any case, 0.5% by weight or more, preferably 1 to 12% by weight of the conjugated diene monomer is added as hydrogen peroxide.

さらに、本発明においては助触媒としてスルホベンズイ
ミドおよびナフチル酢酸のいずれかを用いる。この助触
媒は過酸化水素の触媒効果をより促進させる役割を果す
ものである。本発明においてスルホベンズイミドおよび
/またはナフチル酢酸を助触媒として用いることにより
、ジエン系重合体の収率の向上を図ることができ、また
反応時間を短縮することができるのである。
Furthermore, in the present invention, either sulfobenzimide or naphthyl acetic acid is used as a cocatalyst. This promoter serves to further promote the catalytic effect of hydrogen peroxide. By using sulfobenzimide and/or naphthyl acetic acid as a cocatalyst in the present invention, it is possible to improve the yield of the diene polymer and shorten the reaction time.

本発明において助触媒の使用量は特に制限されないが、
通常は共役ジエン系モノマーに対して0.01〜15重
景%、好ましくは0.05〜10重量%である。0.0
1重量%未満であると助触媒としての効果が小さく、1
0重量%を超えて加えても相応する効果が期待できず、
かえって過酸化水素の分解などが起こり好ましくない。
In the present invention, the amount of co-catalyst used is not particularly limited, but
The amount is usually 0.01 to 15% by weight, preferably 0.05 to 10% by weight based on the conjugated diene monomer. 0.0
If it is less than 1% by weight, the effect as a cocatalyst will be small;
Even if it is added in excess of 0% by weight, the corresponding effect cannot be expected.
On the contrary, decomposition of hydrogen peroxide may occur, which is undesirable.

本発明に上る共役ジエン系モノマーの重合反応条件は用
いるジエン系モノマー等の種類、使用量などにより異な
り一義的に決定されないが、通常は攪拌上反応温度50
〜200°C1好ましくは100〜150°01反応圧
力5〜工Oo気圧、好ましくは10〜50気圧、反応時
間10分〜24時間、好ましくは30分〜5時間である
The polymerization reaction conditions of the conjugated diene monomer according to the present invention vary depending on the type of diene monomer used, the amount used, etc., and are not uniquely determined, but usually the reaction temperature is 50°C while stirring.
-200° C1, preferably 100-150° C1, reaction pressure 5-100 atm, preferably 10-50 atm, reaction time 10 minutes-24 hours, preferably 30 minutes-5 hours.

このようにして目的とする水酸基含有ジエン系重合体が
得られ、この重合体は水酸基を含めて官能基の含有量が
多く、しかも反応条件に依らずほぼ一定であり、平均1
分子当り1.5個以上、通常1.7〜2.5個である。
In this way, the desired hydroxyl group-containing diene polymer is obtained, and this polymer has a high content of functional groups including hydroxyl groups, and is almost constant regardless of the reaction conditions, with an average of 1
The number is 1.5 or more per molecule, usually 1.7 to 2.5.

また、この重合体の数平均分子量は反応条件により異な
るが、通常は300〜30000である。
Further, the number average molecular weight of this polymer varies depending on the reaction conditions, but is usually 300 to 30,000.

本発明により得られるジエン系重合体は、ポリイソシア
ネートと反応させてポリウレタンを製造するために利用
される。このとき得られるポリウレタン硬化物は高強度
で、かつ伸度が高いという特色を有している。したがっ
て、この重合体はウレタンフオーム、接着剤、塗料、成
形品、樹脂。
The diene polymer obtained by the present invention is used to produce polyurethane by reacting with polyisocyanate. The cured polyurethane product obtained at this time is characterized by high strength and high elongation. Therefore, this polymer is used in urethane foams, adhesives, paints, molded products, and resins.

アスファルト類などの改質に極めて有用である。Extremely useful for modifying asphalts, etc.

また、本発明を製法上の立場からみると、従来法よりも
高収率で目的とする水酸基含有ジエン系重合体を得るこ
とができ、しかも反応時間を短縮できるという特色を有
している。
Furthermore, from the viewpoint of the production method, the present invention has the characteristics that the desired hydroxyl group-containing diene polymer can be obtained in a higher yield than conventional methods, and the reaction time can be shortened.

次に、本発明を実施例により説明する。Next, the present invention will be explained by examples.

実施例1 ステンレス製30ゴ振盪式オートクレーブにインプロパ
ノール100重量部、過酸化水素水(濃度50%)10
重量部および0−スルホベンズイミド0.52重量部を
仕込み、冷却しながらオートクレーブ内部の空気を真空
脱気した。次いで、1.3−ブタジェン100重量部を
供給した後、130°Cに昇温した。その後、60分間
55ストロ一ク/分の振盪攪拌を行ない、反応させた。
Example 1 100 parts by weight of inpropanol and 10 parts of hydrogen peroxide (concentration 50%) were placed in a stainless steel 30° shaking autoclave.
parts by weight and 0.52 parts by weight of 0-sulfobenzimide were charged, and the air inside the autoclave was vacuum degassed while cooling. Next, 100 parts by weight of 1,3-butadiene was supplied, and then the temperature was raised to 130°C. Thereafter, the mixture was shaken and stirred at 55 strokes/min for 60 minutes to cause a reaction.

反応終了後、反応液にイソプロピルアルコール3 Qm
l、トルxン60meおよび水15111gを加えて油
層を分離した。さらに、油層をエバポレーターにて予備
脱気し、続いてlmmHg、80°Cにて30分間脱気
を行ない蒸発分を除去した。得られた重合体の収率を第
1表に示す。
After the reaction is complete, add 3 Qm of isopropyl alcohol to the reaction solution.
1, Tolxun 60me and 15111 g of water were added and the oil layer was separated. Furthermore, the oil layer was preliminarily degassed using an evaporator, and then degassed at lmmHg and 80°C for 30 minutes to remove evaporated components. Table 1 shows the yield of the obtained polymer.

実施例2 ステンレス製3(1me振盪式オートクレーブにインプ
ロパツール100重量部、過酸化水素水(濃度50%)
およびα−ナフチル酢酸0.50重量部を仕込み、冷却
しながらオートクレーブ内部の空気を真空脱気した。次
いで、1.3−ブタジェン100重量部を供給した後、
130℃に昇温した。
Example 2 100 parts by weight of Impropatool and hydrogen peroxide solution (concentration 50%) in a stainless steel 3 (1me shaking autoclave)
and 0.50 parts by weight of α-naphthyl acetic acid were charged, and the air inside the autoclave was vacuum degassed while cooling. Then, after supplying 100 parts by weight of 1,3-butadiene,
The temperature was raised to 130°C.

その後、60分間55ストロ一ク/分の振盪攪拌を行な
い反応させた。
Thereafter, the mixture was shaken and stirred at 55 strokes/min for 60 minutes to react.

反応終了後、実施例1と同様の操作で重合体を分離、精
製して重合体を得た。重合体の収率を第1表に示す。
After the reaction was completed, the polymer was separated and purified in the same manner as in Example 1 to obtain a polymer. The yield of the polymer is shown in Table 1.

比較例1 実施例1においてスルホベンズイミドを用いないこと以
外は実施例1と同様にして重合体を得た。
Comparative Example 1 A polymer was obtained in the same manner as in Example 1 except that sulfobenzimide was not used in Example 1.

結果を第1表に示す。The results are shown in Table 1.

第 1 表 特許出願人 出光石油化学株式会社Table 1 Patent applicant: Idemitsu Petrochemical Co., Ltd.

Claims (1)

【特許請求の範囲】 (11共役ジエンモノマーを反応媒体中で過酸化水素と
反応させて水酸基含有ジエン系重合体を製造する方法に
おいて、助触媒としてスルホベンズイミドおよび/また
はナフチル酢酸を用いることを特徴とする水酸基含有ジ
エン系重合体の製造方法。 (2) 助触媒の添加拙が共役ジエンモノマーに対して
0.01〜10重量%である特許請求の範囲第1項記載
の製造方法。
[Claims] (11) In a method for producing a hydroxyl group-containing diene polymer by reacting a conjugated diene monomer with hydrogen peroxide in a reaction medium, sulfobenzimide and/or naphthyl acetic acid are used as cocatalysts. A method for producing a hydroxyl group-containing diene polymer characterized by: (2) The method according to claim 1, wherein the cocatalyst is added in an amount of 0.01 to 10% by weight based on the conjugated diene monomer.
JP58220674A 1983-11-25 1983-11-25 Preparation of hydroxyl group-containing diene polymer Granted JPS60112808A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58220674A JPS60112808A (en) 1983-11-25 1983-11-25 Preparation of hydroxyl group-containing diene polymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58220674A JPS60112808A (en) 1983-11-25 1983-11-25 Preparation of hydroxyl group-containing diene polymer

Publications (2)

Publication Number Publication Date
JPS60112808A true JPS60112808A (en) 1985-06-19
JPS6228964B2 JPS6228964B2 (en) 1987-06-23

Family

ID=16754681

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58220674A Granted JPS60112808A (en) 1983-11-25 1983-11-25 Preparation of hydroxyl group-containing diene polymer

Country Status (1)

Country Link
JP (1) JPS60112808A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6286012A (en) * 1985-10-11 1987-04-20 Idemitsu Petrochem Co Ltd Production of liquid diene copolymer
JPS63264601A (en) * 1986-11-14 1988-11-01 エムテーア ケズポンティ ケーミアイ クタトー インテーゼテ Manufacture of polymer

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01154365U (en) * 1988-04-15 1989-10-24
JPH0329767U (en) * 1989-08-01 1991-03-25

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6286012A (en) * 1985-10-11 1987-04-20 Idemitsu Petrochem Co Ltd Production of liquid diene copolymer
JPS63264601A (en) * 1986-11-14 1988-11-01 エムテーア ケズポンティ ケーミアイ クタトー インテーゼテ Manufacture of polymer

Also Published As

Publication number Publication date
JPS6228964B2 (en) 1987-06-23

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