JPH0687955A - Polymerization of cyclohexene oxide - Google Patents

Polymerization of cyclohexene oxide

Info

Publication number
JPH0687955A
JPH0687955A JP26125791A JP26125791A JPH0687955A JP H0687955 A JPH0687955 A JP H0687955A JP 26125791 A JP26125791 A JP 26125791A JP 26125791 A JP26125791 A JP 26125791A JP H0687955 A JPH0687955 A JP H0687955A
Authority
JP
Japan
Prior art keywords
acid
cyclohexene oxide
hxo
reaction
phosphoric
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.)
Pending
Application number
JP26125791A
Other languages
Japanese (ja)
Inventor
Tetsuo Kobayashi
徹夫 小林
Kenichi Saito
憲一 斉藤
Yoshihisa Suzuki
良久 鈴木
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.)
Nippon Peroxide Co Ltd
Original Assignee
Nippon Peroxide 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 Nippon Peroxide Co Ltd filed Critical Nippon Peroxide Co Ltd
Priority to JP26125791A priority Critical patent/JPH0687955A/en
Publication of JPH0687955A publication Critical patent/JPH0687955A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To polymerize cyclohexene oxide under a mild condition (at a low reaction temperature) in a good yield. CONSTITUTION:Cyclohexene oxide is polymerized in the presence of at least one phosphoric acid compound selected from a group consisting of phosphoric anhydride, orthophosphoric acid, pyrophosphoric acid and polyphosphoric acid at 40-80 deg.C.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明はシクロヘキセンオキサイ
ドの重合方法に関し、更に詳細には、特定のリン酸化合
物の存在下にシクロヘキセンオキサイドを加熱、重合す
る方法に関する。得られる重合物は、潤滑剤、離型剤、
塗料、界面活性剤及びプラスチック等の原料として有用
な化合物である。
TECHNICAL FIELD The present invention relates to a method for polymerizing cyclohexene oxide, and more particularly to a method for heating and polymerizing cyclohexene oxide in the presence of a specific phosphoric acid compound. The obtained polymer is a lubricant, a release agent,
It is a compound useful as a raw material for paints, surfactants and plastics.

【0002】[0002]

【従来の技術】シクロヘキセンオキサイド(以下「HX
O」と略称する)の重合方法に関しては、トリアルキル
アルミニウム等の有機金属化合物、或いは塩化アルミニ
ウム、塩化第二スズ、塩化第二鉄等のルイス酸などを単
独または組合せて使用する方法等が知られている。ま
た、HXOを四ホウ酸および/あるいは無水ホウ酸の存
在下で加熱する方法が知られている。(特開昭64−1
1130号公報)
2. Description of the Related Art Cyclohexene oxide (hereinafter referred to as "HX
Abbreviated as "O"), a method of using an organometallic compound such as trialkylaluminum, or a Lewis acid such as aluminum chloride, stannic chloride, ferric chloride, etc. alone or in combination is known. Has been. Further, a method of heating HXO in the presence of tetraboric acid and / or boric anhydride is known. (Japanese Patent Laid-Open No. 64-1
(1130 publication)

【0003】[0003]

【発明が解決しようとしている課題】有機金属化合物、
或いはルイス酸を用いる方法は、触媒自身が高価であ
り、また取扱に特別な注意を払わなければならない等の
欠点がある。四ホウ酸および/あるいは無水ホウ酸を用
いる方法は、反応温度が130〜140℃と高く、また
使用する触媒は、正ホウ酸、あるいは無水ホウ酸を加熱
脱水するなど触媒調整が煩雑であるという欠点がある。
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention
Alternatively, the method using a Lewis acid has drawbacks in that the catalyst itself is expensive and special handling is required. According to the method using tetraboric acid and / or boric anhydride, the reaction temperature is as high as 130 to 140 ° C., and the catalyst to be used is complicated to adjust by heating or dehydrating orthoboric acid or anhydrous boric acid. There are drawbacks.

【0004】本発明者等は、穏和な反応条件下(低い反
応温度)で反応が進行し、かつ高収率でシクロヘキセン
オキサイドの重合物が得られる方法を見出すべく検討を
重ねた結果、本発明を完成した。
The present inventors have conducted extensive studies to find a method in which the reaction proceeds under mild reaction conditions (low reaction temperature) and a cyclohexene oxide polymer is obtained in a high yield. Was completed.

【0005】[0005]

【課題を解決するための手段】即ち、本発明は、無水リ
ン酸、オルトリン酸、ピロリン酸及びポリリン酸からな
る群から選ばれた少なくとも1種のリン酸化合物の存在
下に、シクロヘキセンオキサイドを加熱、重合すること
を特徴とするシクロヘキセンオキサイドの重合方法であ
る。
That is, the present invention is to heat cyclohexene oxide in the presence of at least one phosphoric acid compound selected from the group consisting of phosphoric anhydride, orthophosphoric acid, pyrophosphoric acid and polyphosphoric acid. The method is a method for polymerizing cyclohexene oxide, characterized in that it is polymerized.

【0006】本発明で使用するリン酸化合物は、無水リ
ン酸、オルトリン酸、ピロリン酸及びポリリン酸等であ
り、それぞれを単独あるいは組合わせて使用する。尚、
ポリリン酸とは、トリポリリン酸、テトラトリポリン
酸、トリメタリン酸およびヘキサメタリン酸等である。
これらリン酸化合物は、重合触媒として作用するもので
あり、その添加量は、原料であるシクロヘキセンに対し
て0.1重量%以上必要であるが、反応速度および生成
物の重合度等を考慮した場合、1.0〜25重量%が好
ましい。
The phosphoric acid compound used in the present invention is phosphoric anhydride, orthophosphoric acid, pyrophosphoric acid, polyphosphoric acid, etc., which may be used alone or in combination. still,
The polyphosphoric acid includes tripolyphosphoric acid, tetratriphosphoric acid, trimetaphosphoric acid, hexametaphosphoric acid and the like.
These phosphoric acid compounds act as a polymerization catalyst, and the addition amount thereof is required to be 0.1% by weight or more with respect to the cyclohexene as a raw material, but the reaction rate and the degree of polymerization of the product are taken into consideration. In this case, 1.0 to 25% by weight is preferable.

【0007】本発明の重合反応は、室温でも進行する
が、適当な反応速度を得るためには、反応温度を40℃
〜80℃の範囲とすることが好ましい。また、特に望む
場合にはこれ以上の温度に加熱してもかまわない。反応
時間は、反応温度と密接に関連するものであり、一概に
決められないが、1〜6時間の範囲で任意に決めること
ができる。尚、40〜80℃で反応を行う場合には、該
反応は2時間以内に完了する。
The polymerization reaction of the present invention proceeds even at room temperature, but in order to obtain an appropriate reaction rate, the reaction temperature is 40 ° C.
It is preferably in the range of -80 ° C. If desired, it may be heated to a temperature higher than this. The reaction time is closely related to the reaction temperature and cannot be determined unconditionally, but can be arbitrarily determined within the range of 1 to 6 hours. When the reaction is carried out at 40 to 80 ° C, the reaction is completed within 2 hours.

【0008】HXOに上記リン酸化合物を添加してかき
混ぜながら加熱すると、発熱を伴って溶解し、均一溶液
になる。更に攪拌を続けると、重合反応の進行ととも
に、次第に反応液の粘度が増加して反応は完了する。該
反応は、このようにHXOをリン酸化合物の存在下、直
接加熱する方法の他に、HXOをベンゼン、トルエン、
キシレン等の不活性芳香族溶剤に一旦溶解してから行う
こともできる。
When the above phosphoric acid compound is added to HXO and heated while stirring, the HXO is exothermicly dissolved to form a uniform solution. When the stirring is further continued, the viscosity of the reaction solution gradually increases as the polymerization reaction progresses, and the reaction is completed. In this reaction, in addition to the method of directly heating HXO in the presence of a phosphoric acid compound, HXO is converted to benzene, toluene,
It can also be performed after once dissolving in an inert aromatic solvent such as xylene.

【0009】得られる重合物には、触媒として用いたリ
ン酸化合物が不純物として含まれるが、これらリン酸成
分は熱水で洗浄することにより除去することができる。
このようにして得られるHXO重合物の平均分子量は、
900〜1500である。
The obtained polymer contains the phosphoric acid compound used as a catalyst as an impurity, and these phosphoric acid components can be removed by washing with hot water.
The average molecular weight of the HXO polymer thus obtained is
It is 900-1500.

【0010】[0010]

【実施例】【Example】

実施例1 HXO(50グラム;0.51モル)、無水リン酸(8.
9グラム;0.05モル)を還流冷却器付きのガラス製
反応器中でメカニカルスターラーにて攪拌しながら、水
浴にて、50℃に1.5時間保った。その後、減圧下に
て未反応のHXOを留去させ、得られた重合物は熱水と
共にかき混ぜ、分液を数回繰り返してリン酸触媒を分離
した。再び減圧下にて水分を除去すると、無色透明のH
XO重合物(ガラス状重合物)36.8グラム(74
%)が得られた。平均分子量をGPC法(ゲル浸透クロ
マトグラフィー分析(標準:ポリスチレン))により分
析した結果、1130であった。
Example 1 HXO (50 grams; 0.51 mol), phosphoric anhydride (8.
(9 g; 0.05 mol) was kept at 50 ° C. for 1.5 hours in a water bath while stirring with a mechanical stirrer in a glass reactor equipped with a reflux condenser. Then, unreacted HXO was distilled off under reduced pressure, the obtained polymer was stirred with hot water, and liquid separation was repeated several times to separate the phosphoric acid catalyst. When water is removed again under reduced pressure, colorless transparent H
XO polymer (glassy polymer) 36.8 g (74
%)was gotten. The average molecular weight was 1130 as a result of analysis by GPC method (gel permeation chromatography analysis (standard: polystyrene)).

【0011】実施例2 HXO(50グラム;0.51モル)、トルエン(50
グラム)の入った300mlのガラス製反応器をメカニ
カルスターラーにて攪拌し、HXOを溶解した後、水浴
にて50℃に保ちつつピロリン酸(12.5グラム、0.
07モル)を1.0時間掛けて滴下した。1.5時間後、
純水と共に攪拌し、水相に溶けだしたリン酸触媒を分離
する。その後、減圧下で、トルエンを蒸留除去すると、
ほととど無色透明のHXO重合物が49.4グラム(9
8.8%)得られた。平均分子量は1100であった。
Example 2 HXO (50 grams; 0.51 mol), toluene (50
(300 g) containing 300 g of a glass reactor was stirred with a mechanical stirrer to dissolve HXO, and then pyrophosphoric acid (12.5 g, 0.1 g) was added while maintaining the temperature at 50 ° C. in a water bath.
(07 mol) was added dropwise over 1.0 hour. 1.5 hours later
The phosphoric acid catalyst dissolved in the water phase is separated by stirring with pure water. Then, under reduced pressure, when toluene is distilled off,
49.4 g (9%) of colorless and transparent HXO polymer.
8.8%) was obtained. The average molecular weight was 1100.

【0012】実施例3 HXO(50グラム;0.51モル)、99%オルトリ
ン酸(8.2グラム;0.1モル)を還流冷却器付きのガ
ラス製反応器に入れ、攪拌しながら、80℃に保った。
2時間経過後、減圧下にて未反応のHXOを留去させ、
得られた重合物を熱水と共にかき混ぜ、分液を数回繰り
返してリン酸触媒を分離した。再び減圧下にて水分を除
去すると、無色透明のHXO重合物(ガラス状重合物)
39.3グラム(78.6%)が得られた。GPC法によ
る平均分子量は990であった。
Example 3 HXO (50 grams; 0.51 mole) and 99% orthophosphoric acid (8.2 grams; 0.1 mole) were placed in a glass reactor equipped with a reflux condenser and stirred at 80 It was kept at ℃.
After 2 hours, unreacted HXO was distilled off under reduced pressure,
The obtained polymer was stirred with hot water, and liquid separation was repeated several times to separate the phosphoric acid catalyst. When water is removed again under reduced pressure, a colorless transparent HXO polymer (glassy polymer)
39.3 grams (78.6%) were obtained. The average molecular weight by GPC method was 990.

【0013】[0013]

【発明の効果】本発明によれば、穏和な反応条件下(低
い反応温度)で、シクロヘキセンオキサイドの重合物を
高収率で得ることができ、また、使用する触媒は、安価
で、且つ容易に入手できるものであるため、本発明は産
業上極めて有利な方法となる。
INDUSTRIAL APPLICABILITY According to the present invention, a polymer of cyclohexene oxide can be obtained in a high yield under mild reaction conditions (low reaction temperature), and the catalyst used is inexpensive and easy. The present invention is an industrially extremely advantageous method because it is available to the public.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 無水リン酸、オルトリン酸、ピロリン酸
及びポリリン酸からなる群から選ばれた少なくとも1種
のリン酸化合物の存在下に、シクロヘキセンオキサイド
を加熱、重合することを特徴とするシクロヘキセンオキ
サイドの重合方法。
1. Cyclohexene oxide characterized by heating and polymerizing cyclohexene oxide in the presence of at least one phosphoric acid compound selected from the group consisting of phosphoric anhydride, orthophosphoric acid, pyrophosphoric acid and polyphosphoric acid. Polymerization method.
JP26125791A 1991-09-13 1991-09-13 Polymerization of cyclohexene oxide Pending JPH0687955A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26125791A JPH0687955A (en) 1991-09-13 1991-09-13 Polymerization of cyclohexene oxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26125791A JPH0687955A (en) 1991-09-13 1991-09-13 Polymerization of cyclohexene oxide

Publications (1)

Publication Number Publication Date
JPH0687955A true JPH0687955A (en) 1994-03-29

Family

ID=17359319

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26125791A Pending JPH0687955A (en) 1991-09-13 1991-09-13 Polymerization of cyclohexene oxide

Country Status (1)

Country Link
JP (1) JPH0687955A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4883114A (en) * 1988-01-28 1989-11-28 Clecim Oscillation method and apparatus for a continuous casting mold

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4883114A (en) * 1988-01-28 1989-11-28 Clecim Oscillation method and apparatus for a continuous casting mold

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