JPS6147474A - Preparation of brominated oxirane derivative - Google Patents

Preparation of brominated oxirane derivative

Info

Publication number
JPS6147474A
JPS6147474A JP59169790A JP16979084A JPS6147474A JP S6147474 A JPS6147474 A JP S6147474A JP 59169790 A JP59169790 A JP 59169790A JP 16979084 A JP16979084 A JP 16979084A JP S6147474 A JPS6147474 A JP S6147474A
Authority
JP
Japan
Prior art keywords
brominated
epichlorohydrin
oxirane derivative
oxirane
reaction
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
JP59169790A
Other languages
Japanese (ja)
Inventor
Minoru Hishinuma
稔 菱沼
Junji Takemoto
竹本 淳司
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.)
Sanyo Kokusaku Pulp Co Ltd
Original Assignee
Sanyo Kokusaku Pulp 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 Sanyo Kokusaku Pulp Co Ltd filed Critical Sanyo Kokusaku Pulp Co Ltd
Priority to JP59169790A priority Critical patent/JPS6147474A/en
Publication of JPS6147474A publication Critical patent/JPS6147474A/en
Pending legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

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  • Epoxy Compounds (AREA)

Abstract

PURPOSE:To produce the titled compound useful as an electronic material, etc., in high yield and purity and low hydrolyzable chlorine content, by reacting a brominated alkylphenol with epichlorohydrin, and carrying out dehydrochlorination reaction with an alkali in two steps. CONSTITUTION:A brominated alkylphenol of formula I (R is >=1C alkyl; n is 1-3) is subjected to the addition reaction with epichlorohydrin in the presence of a catalyst such as tetraethyl ammonium bromide, and the obtained brominated alkylphenyl chlorohydrin ether is subjected to the dehydrochlorination reaction with excess epichlorohydrin using an aqueous solution of an alkaline compound while removing the water together with epichlorohydrin by azeotropic distillation under reduced pressure. After removing the excess epichlorohydrin, the resultant brominated oxirane derivative is dissolved in an organic solvent, and the second dehydrochlorination reaction of the residual hydrolyzable chlorine is carried out with an alkaline compound to obtain the objective compound of formula II.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は臭素化オキシラン誘導体の製造法、特に高純度
臭素化オキシラン誘導体を右利に製造する方法に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing brominated oxirane derivatives, and particularly to a method for producing high purity brominated oxirane derivatives in an efficient manner.

本発明の実施により得られる高純度臭素化オキシラン誘
導体は、電気・電子材料、塗料樹脂として有用である。
High purity brominated oxirane derivatives obtained by carrying out the present invention are useful as electrical/electronic materials and paint resins.

〔従来の技術〕[Conventional technology]

従来知られている芳香族ヒドロキシ化合物よりオキシラ
ン誘導体を製造する方法としては、1段法と2段法とが
ある。1段法はアルカリ又はアルカリ土類金属水酸化物
を添加し、ヒドロキシ化合物とエピクロルヒドリンを反
応させ、エーテル化と脱塩化水素化を同時に行うオキシ
ラン誘導体の製造法である。
Conventionally known methods for producing oxirane derivatives from aromatic hydroxy compounds include a one-stage method and a two-stage method. The one-stage method is a method for producing oxirane derivatives in which an alkali or alkaline earth metal hydroxide is added, a hydroxy compound and epichlorohydrin are reacted, and etherification and dehydrochlorination are carried out simultaneously.

2段法は、芳香族ヒドロキシ化合物にエピクロルヒドリ
ンを加え、少量のアルカリ化合物や触媒等を添加し、ま
ず伺加反応を行わせ、次いでアルカリ化合物を加え、脱
塩化水素化を行わせる方法である。
The two-step method is a method in which epichlorohydrin is added to an aromatic hydroxy compound, a small amount of an alkali compound, a catalyst, etc. is added, and a reaction is first carried out, and then an alkali compound is added to carry out dehydrochlorination.

収率及び製品の純度等の点から、後者の2段法が一般的
である。
The latter two-stage method is common in terms of yield and product purity.

これらを反応式で説明すると次の様になる。These reactions can be explained using the following reaction formula.

」臥 (1)     (2)         <3)■購 〔発明が解決しようとする問題点〕 しかし、これらは収率70〜85%で純度も低く、電気
・電子材料分野には満足するものではない。
``臥(1) (2) <3) ■Purchase [Problem that the invention aims to solve] However, these have a yield of 70-85% and low purity, which is not satisfactory for the field of electrical and electronic materials. .

本発明の目的は、臭素化アルキルフェノールから臭素化
オキシラン誘導体を高収率でかつ高 。
The object of the present invention is to produce brominated oxirane derivatives from brominated alkylphenols in high yield and at high efficiency.

純度に製造する方法を提供することにある。   I電
気・電子材料等に使用される臭素化オキシラン誘導体は
加水分解性塩素量が高いと、硬化時間を長くし、また金
属等を腐食する欠点を有する。そのため需要家は加水分
解性塩素含有量が少ない臭素化オキシラン誘導体を要求
するのが実情である。
The purpose is to provide a method for manufacturing with high purity. Brominated oxirane derivatives used in electrical and electronic materials etc. have the drawback of prolonging the curing time and corroding metals etc. when the amount of hydrolyzable chlorine is high. Therefore, the reality is that consumers demand brominated oxirane derivatives with a low content of hydrolyzable chlorine.

〔問題点を解決するための手段〕[Means for solving problems]

本発明者は、鋭意検問の結果、下記の一般式(II)で
示される臭素化アルキルフェノール(ただしRは炭素数
1以上のアルキル基、nは1〜3の整数を表わす。) とエピクロルヒドリンとの反応により下記一般式(I) (ただし式中Rおよびnは前記に同じ。)で示される臭
素化オギシラン誘導体の製造法について、高純度臭素化
オキシラン誘導体の製造法を見出した。
As a result of extensive investigation, the present inventors found that the combination of brominated alkylphenol represented by the following general formula (II) (wherein R represents an alkyl group having 1 or more carbon atoms, and n represents an integer of 1 to 3) and epichlorohydrin A method for producing a brominated oxirane derivative represented by the following general formula (I) (wherein R and n are the same as above) by reaction has been found.

具体的には、本発明は次の第1工程乃至第3工程よりな
る臭素化オキシラン誘導体の製造法を提供するものであ
る。
Specifically, the present invention provides a method for producing a brominated oxirane derivative comprising the following first to third steps.

第1工程 臭素化ノフルギルフJノールとエピクロルヒドリンを触
媒の存在下f=I加反応させ、臭素化アルギルフェニル
クロルヒドリンエーテルを得る工程 第2工程 臭素化アルキルフェニルクロルヒドリンエーテルを過剰
のエピクロルヒドリンの存在下で、アルカリ化合物の水
溶液を用い、水をエピクロルヒドリンと共に減圧下、共
沸蒸留しつつ脱塩化水素化反応させ、過剰のエピクロル
ヒドリンを留去する工程 第3工程 上記工程で得られた臭素化Aキシラン誘導体を有機溶剤
に溶解し、該オギシラン誘導イホ中に残存する加水分解
性塩素をアルカリ化合物を用いて、第2回目の脱塩化水
素化反応を行う工程 を経て高1Iii1′!度臭素化オキシラン誘導体を得
るものである。
1st step: Brominated nofurgilf Jnol and epichlorohydrin are reacted with f=I in the presence of a catalyst to obtain brominated alkylphenyl chlorohydrin ether. 2nd step: Brominated alkylphenyl chlorohydrin ether is reacted with excess epichlorohydrin. In the presence of an aqueous solution of an alkaline compound, water is subjected to a dehydrochlorination reaction under reduced pressure with epichlorohydrin while being azeotropically distilled, and excess epichlorohydrin is distilled off.Third step Brominated A obtained in the above step The xylan derivative is dissolved in an organic solvent, and the hydrolyzable chlorine remaining in the xylan derivative is subjected to a second dehydrochlorination reaction using an alkali compound to obtain high 1Iii1'! A highly brominated oxirane derivative is obtained.

〔作 用〕[For production]

本発明に用いる臭素化アルキルフェノールとしでは、4
,6−ジプロモー〇−クレゾール、4.6−ジプロモー
2−イソプロピルフェノール、2,4.6−ドリブロモ
ー3−イソプロピルフェノール、2,6−ジプロモー4
−tert−ブチルフェノール、2,6−ジプロモー4
−3eC−ブチルフェノール、2−ブロモ−4−イソプ
ロピルフェノール、2.6−シグロモー叶Aクチルフェ
ノール、2.6−ジプロモー4−tert−ドデシルフ
ェノール、4−プロモーO−クレゾール等が挙げられる
The brominated alkylphenol used in the present invention includes 4
, 6-dipromo 〇-cresol, 4,6-dipromo 2-isopropylphenol, 2,4.6-dibromo 3-isopropylphenol, 2,6-dipromo 4
-tert-butylphenol, 2,6-dipromo4
-3eC-butylphenol, 2-bromo-4-isopropylphenol, 2.6-siglomo-Actylphenol, 2.6-dipromo-4-tert-dodecylphenol, 4-promo-O-cresol, and the like.

次に第一工程で臭素化アルキルフェノールとエピクロル
ヒドリンの付加反応に用いられる触媒としては、第4級
アミン塩、塩基性アニオン交換樹脂、ハロゲン化アルカ
リ金属類等を挙げることができる。具体的には第4級ア
ミン塩としては、例えばテ1〜ラエチルアンモニウムブ
ロモド、トリメチルベンジルアンモニウムプロミド、ト
リメチルゼチルアンモニウムクロリド、トリブヂルアン
モニウムブロミド等が挙げられる。塩基性アニオン交換
樹脂としては、市販の塩基性アニオン交換樹脂を使用す
ることができる。
Next, examples of the catalyst used in the addition reaction of brominated alkylphenol and epichlorohydrin in the first step include quaternary amine salts, basic anion exchange resins, and alkali metal halides. Specifically, examples of the quaternary amine salt include te-1-laethylammonium bromide, trimethylbenzylammonium bromide, trimethylzetylammonium chloride, and tribudylammonium bromide. As the basic anion exchange resin, commercially available basic anion exchange resins can be used.

触媒量は、原料の臭素化アルキルフェノール100重量
部に対してo、oi〜5.0重量部程度である。触媒は
、単一あるいは混合して使用することができる。
The amount of the catalyst is approximately 5.0 parts by weight based on 100 parts by weight of brominated alkylphenol as a raw material. A single catalyst or a mixture of catalysts can be used.

付加反応温度は、原料によって異なるが通常30〜12
0℃好ましくは40〜80℃である。反応時問は、実質
的に付加反応が完了するまでであり、反応温度、触媒量
に応じて変えるが、通常0.5−=16時間好ましくは
2−10時間である。
The addition reaction temperature varies depending on the raw materials, but is usually 30 to 12
The temperature is 0°C, preferably 40 to 80°C. The reaction time is until the addition reaction is substantially completed, and varies depending on the reaction temperature and the amount of catalyst, but is usually 0.5-16 hours, preferably 2-10 hours.

第2工程、第3工程で用いられるアルカリとしては、水
酸化ノJリウム、水酸化プ1〜リウム、水酸化カルシウ
ム等が挙げられる。第2工程で用いられるアルカリ量は
、原料に用いた臭素化アルキルフェノール1モルに対し
U O,75〜0.99モルで、このアルカリ化合物の
存在下で脱塩化水素化反応を行う。この脱塩化水素化は
反応系を50〜300T orrの減圧条件下に維持し
ながら水をエピクロルヒドリンと共沸、留去させるが、
反応系中の水含有率は0.1〜5.0重量%に維持しな
がら、アルカリの添加速度と蒸留速度を調整する。アル
カリの添加速度が速いと反応系中のpHが高くなり、重
合を起す原因となり、好ましくない。通常0.5〜8時
間位で、反応系中のpl−(7〜9.5に保つことが好
ましい。
Examples of the alkali used in the second step and the third step include hydroxide, chlorium hydroxide, hydroxide, calcium hydroxide, and the like. The amount of alkali used in the second step is 75 to 0.99 mol of U2O per 1 mol of brominated alkylphenol used as the raw material, and the dehydrochlorination reaction is carried out in the presence of this alkali compound. In this dehydrochlorination, water is azeotropically distilled off with epichlorohydrin while maintaining the reaction system under reduced pressure conditions of 50 to 300 Torr.
The alkali addition rate and distillation rate are adjusted while maintaining the water content in the reaction system at 0.1 to 5.0% by weight. If the alkali addition rate is too fast, the pH in the reaction system will increase, causing polymerization, which is not preferable. It is preferable to maintain pl-(7 to 9.5) in the reaction system, usually for about 0.5 to 8 hours.

また反応系内から水分除去を行なわずに実施することも
可能であるが、反応系中の水によってエピクロルヒドリ
ンが分解するため工業的には不利である。
It is also possible to carry out the reaction without removing water from the reaction system, but this is industrially disadvantageous because epichlorohydrin is decomposed by the water in the reaction system.

反応温度は、30〜130℃好ましくは50−90℃で
ある。次いで過剰のエピクロルヒドリンを減圧蒸留によ
って除去し副生じたハロゲン化アルカリ塩を濾過または
水洗によって除去後臭素化オキシラン誘導体を得る。
The reaction temperature is 30-130°C, preferably 50-90°C. Next, excess epichlorohydrin is removed by distillation under reduced pressure, and the by-produced alkali halide salt is removed by filtration or washing with water to obtain a brominated oxirane derivative.

第3工程では前記の第2工程で得られた臭素化オキシラ
ン誘導体を不1m溶剤に溶解し、原料の臭素化アルキル
フェノール1モルに対してo、oi = 0.15モル
のアルカリを添加し、臭素化オキシラン誘導体中に残存
するクロルヒドリンエーテルを除去することによって、
高純度臭素化Aキシラン誘導体を高収率かつ高純度で得
ることができる。
In the third step, the brominated oxirane derivative obtained in the second step is dissolved in a 1M solvent, and an alkali of o, oi = 0.15 mole is added to 1 mole of brominated alkylphenol as a raw material to dissolve bromine. By removing the chlorohydrin ether remaining in the oxirane derivative,
A highly purified brominated A xylan derivative can be obtained in high yield and purity.

上記の有m溶剤としてはオキシラン基と反応しない溶剤
であり、これにはメチルエチルケトン、トルエン、ジオ
キサン等を挙げることができ、単−又は混合して使用す
ることができる。
The above-mentioned solvent is a solvent that does not react with the oxirane group, such as methyl ethyl ketone, toluene, dioxane, etc., and can be used singly or in combination.

アルカリ水溶液の濃度は通常1〜50重量%であり、好
ましくは10・〜20重伍%である。
The concentration of the alkaline aqueous solution is usually 1 to 50% by weight, preferably 10. to 20% by weight.

反応温度は30〜120℃、好ましくは50〜90°C
である。反応時間は、臭素化オキシラン誘導体中に残存
するクロルヒドリンニーデル体が、消失するまでであり
通常0.5〜10時間である。
Reaction temperature is 30-120°C, preferably 50-90°C
It is. The reaction time is usually 0.5 to 10 hours until the chlorohydrin needles remaining in the brominated oxirane derivative disappear.

〔発明の効果〕〔Effect of the invention〕

このようにして、1@られた高純度臭素化オキシラン誘
導体は、後述の第2表に明らかにしたように、加水分解
性塩素が0.1重量%以下で、特に0.01〜0.05
重Φ%と極めて低いもので、電子・電気工業用樹脂とし
て極めて有用である。
As shown in Table 2 below, the high purity brominated oxirane derivative prepared in this manner contains 0.1% by weight or less of hydrolyzable chlorine, especially 0.01 to 0.05% by weight.
It has an extremely low weight Φ%, making it extremely useful as a resin for the electronic and electrical industries.

〔実施例〕〔Example〕

以下に実施例を挙げて、さらに具体的に説明するが、こ
れらの実施例は例示であり、本発明は実施例によって制
限されるものではない。なお、以下に単に部とあるのは
、いずれもff1fi部を意味する。
The present invention will be described in more detail with reference to Examples below, but these Examples are merely illustrative and the present invention is not limited by the Examples. Note that the term ``section'' hereinafter simply refers to the ff1fi section.

実施例1 4.6−ジプロモー2−イソプロピルフェノール1.0
モル(294部)、エピクロルヒドリン370部、第1
表記載の触媒を温度計、冷却器、撹拌装置を刊した四ツ
ロフラスコ内に仕込み、75±5℃で4時間反応させた
Example 1 4.6-dipromo 2-isopropylphenol 1.0
Mol (294 parts), 370 parts of epichlorohydrin, 1st
The catalyst listed in the table was charged into a four-way flask equipped with a thermometer, a condenser, and a stirrer, and reacted at 75±5° C. for 4 hours.

次いて゛、反応溶液を60℃に冷却し、水分離器を取り
付けた後、50%水酸化ナトリウム水溶液を約3時間に
わたって滴下した。この時、反応系は150±50To
rrの減圧度に保ち、反応温度は、1ピク]コルヒドリ
ンとの共沸温度に保ち、生成する水は除去し、エピクロ
ルヒドリンは反応系に戻し、反応を行った。水酸化す1
ヘリウム水溶液の滴下終了後、系内から残存エピクロル
ヒドリンを減圧下で留去し、副生じた食塩を濾過ないし
水洗によって除去した。得られた臭素化オキシラン誘導
体を、メチルエチルケトンに溶解し、第1表に示した量
の20%水酸化ナトリウム水溶液を1〜3時間か(プて
添加後、有機層を純水500m12で6回洗浄し、最後
に有機層からメチルエチルケトンを減圧留去して、高純
度臭素化オキシラン誘導体を得た。
Next, the reaction solution was cooled to 60° C., a water separator was attached, and a 50% aqueous sodium hydroxide solution was added dropwise over about 3 hours. At this time, the reaction system was 150±50To
The reaction temperature was maintained at an azeotropic temperature with 1 pic] corhydrin, the water produced was removed, and the epichlorohydrin was returned to the reaction system to carry out the reaction. hydroxide 1
After dropping the aqueous helium solution, the remaining epichlorohydrin was distilled off from the system under reduced pressure, and the by-product salt was removed by filtration or washing with water. The obtained brominated oxirane derivative was dissolved in methyl ethyl ketone, and after adding 20% aqueous sodium hydroxide solution in the amount shown in Table 1 for 1 to 3 hours, the organic layer was washed 6 times with 500 ml of pure water. Finally, methyl ethyl ketone was distilled off from the organic layer under reduced pressure to obtain a highly pure brominated oxirane derivative.

このようにして得られた高純度臭素化オキシラン誘導体
の分析値を第2表に示づ。
The analytical values of the highly purified brominated oxirane derivative thus obtained are shown in Table 2.

実施例2〜6 実施例1において4.6−ジプロモー2−イソブ[jビ
ルフェノールの代りに他の臭素化アルキルフェノール1
モルを用いた製造法を実施例1と併せて第1表に示した
。また得られた目的化合物の分析結果を第2表に示した
Examples 2 to 6 In Example 1, 4,6-dipromo-2-isobutylphenol was replaced with other brominated alkylphenol.
The production method using moles is shown in Table 1 together with Example 1. Furthermore, the analysis results of the obtained target compound are shown in Table 2.

比較例1〜2 実施例1〜6に用いたと同様の反応装置で第3工程であ
る精製工程を行わない例を示づ。その結果を第2表に示
す。
Comparative Examples 1 to 2 Examples will be shown in which the third step, the purification step, is not performed using the same reaction apparatus as used in Examples 1 to 6. The results are shown in Table 2.

第1表は実施例及び比較例の触媒の種類とアルカリ量を
示したものである。
Table 1 shows the types of catalysts and amounts of alkali in Examples and Comparative Examples.

Claims (2)

【特許請求の範囲】[Claims] (1)下記の一般式〔II〕で示される臭素化アルキルフ
ェノール ▲数式、化学式、表等があります▼〔II〕 (ただしRは炭素数1以上のアルキル基、nは1〜3の
整数を表わす。) とエピクロルヒドリンとを反応させる下記一般式〔 I
〕 ▲数式、化学式、表等があります▼〔 I 〕 (ただし式中Rおよびnは前記に同じ。) で示される臭素化オキシラン誘導体の製造法。
(1) Brominated alkylphenol represented by the following general formula [II] ▲ Numerical formulas, chemical formulas, tables, etc. are available ▼ [II] (where R is an alkyl group with 1 or more carbon atoms, and n is an integer from 1 to 3. ) and epichlorohydrin are reacted using the following general formula [I
] ▲There are mathematical formulas, chemical formulas, tables, etc.▼ [I] (However, in the formula, R and n are the same as above.) A method for producing a brominated oxirane derivative.
(2)下記の一般式〔II〕で示される臭素化アルキルフ
ェノール ▲数式、化学式、表等があります▼〔II〕 (ただしRは炭素数1以上のアルキル基、nは1〜3の
整数を表わす。) とエピクロルヒドリンとの反応による下記一般式〔 I
〕で示される臭素化オキシラン誘導体、▲数式、化学式
、表等があります▼〔 I 〕 (ただしRおよびnは前記に同じ。) の製造法において、 第1工程 臭素化アルキルフェノールとエピクロルヒ ドリンを触媒の存在下付加反応させ、臭素化アルキルフ
エニルクロルヒドリンエーテルを得る工程 第2工程 臭素化アルキルフエニルクロルヒドリンエ ーテルを過剰のエピクロルヒドリンの存在下で、アルカ
リ化合物の水溶液を用い、水をエピクロルヒドリンと共
に減圧下、共沸蒸留しつつ脱塩化水素化反応させ、過剰
のエピクロルヒドリンを留去する工程 第3工程 上記工程で得られた臭素化オキシラン誘導 体を有機溶剤に溶解し、該オキシラン誘導体中に残存す
る加水分解性塩素をアルカリ化合物を用いて、第2回目
の脱塩化水素化反応を行う工程 を経て高純度臭素化オキシラン誘導体を得ることを特徴
とする臭素化オキシラン誘導体の製造法。
(2) Brominated alkylphenol represented by the following general formula [II] ▲ Numerical formulas, chemical formulas, tables, etc. are available ▼ [II] (where R is an alkyl group with 1 or more carbon atoms, and n is an integer from 1 to 3. ) and epichlorohydrin to form the following general formula [I
] There are brominated oxirane derivatives represented by ▲ mathematical formulas, chemical formulas, tables, etc. ▼ In the production method of [I] (where R and n are the same as above), in the first step, brominated alkylphenol and epichlorohydrin are combined in the presence of a catalyst. Sub-addition reaction to obtain brominated alkyl phenyl chlorohydrin ether Second step Brominated alkyl phenyl chlorohydrin ether is reacted with an aqueous solution of an alkali compound in the presence of excess epichlorohydrin, and water is depressurized together with epichlorohydrin. Step 3: Perform dehydrochlorination reaction with azeotropic distillation to distill off excess epichlorohydrin. Third step: Dissolve the brominated oxirane derivative obtained in the above step in an organic solvent, and dissolve the remaining hydration in the oxirane derivative. A method for producing a brominated oxirane derivative, which comprises obtaining a highly purified brominated oxirane derivative through a second dehydrochlorination reaction of decomposable chlorine using an alkali compound.
JP59169790A 1984-08-14 1984-08-14 Preparation of brominated oxirane derivative Pending JPS6147474A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59169790A JPS6147474A (en) 1984-08-14 1984-08-14 Preparation of brominated oxirane derivative

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59169790A JPS6147474A (en) 1984-08-14 1984-08-14 Preparation of brominated oxirane derivative

Publications (1)

Publication Number Publication Date
JPS6147474A true JPS6147474A (en) 1986-03-07

Family

ID=15892927

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59169790A Pending JPS6147474A (en) 1984-08-14 1984-08-14 Preparation of brominated oxirane derivative

Country Status (1)

Country Link
JP (1) JPS6147474A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02256672A (en) * 1988-12-26 1990-10-17 Kowa Co Production of glycidyl ether
JP2006151854A (en) * 2004-11-29 2006-06-15 Mitsubishi Gas Chem Co Inc Method for producing glycidyl methacrylate

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02256672A (en) * 1988-12-26 1990-10-17 Kowa Co Production of glycidyl ether
JP2006151854A (en) * 2004-11-29 2006-06-15 Mitsubishi Gas Chem Co Inc Method for producing glycidyl methacrylate

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