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JP2549073B2 - Process for producing alkylene oxide adduct of halogenated phenols - Google Patents
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JP2549073B2 - Process for producing alkylene oxide adduct of halogenated phenols - Google Patents

Process for producing alkylene oxide adduct of halogenated phenols

Info

Publication number
JP2549073B2
JP2549073B2 JP62160460A JP16046087A JP2549073B2 JP 2549073 B2 JP2549073 B2 JP 2549073B2 JP 62160460 A JP62160460 A JP 62160460A JP 16046087 A JP16046087 A JP 16046087A JP 2549073 B2 JP2549073 B2 JP 2549073B2
Authority
JP
Japan
Prior art keywords
alkylene oxide
halogenated
oxide adduct
reaction
alkyl group
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.)
Expired - Lifetime
Application number
JP62160460A
Other languages
Japanese (ja)
Other versions
JPS646231A (en
Inventor
克実 内田
祐一 江口
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.)
YOTSUKAICHI GOSEI KK
Original Assignee
YOTSUKAICHI GOSEI 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 YOTSUKAICHI GOSEI KK filed Critical YOTSUKAICHI GOSEI KK
Priority to JP62160460A priority Critical patent/JP2549073B2/en
Publication of JPS646231A publication Critical patent/JPS646231A/en
Application granted granted Critical
Publication of JP2549073B2 publication Critical patent/JP2549073B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Catalysts (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明はハロゲン化フェノール類のアルキレンオキシ
ド付加物の製造方法に関し、特に一価のハロゲン化フェ
ノールのアルキレンオキシド付加物又はハロゲン化ビス
フェノールにアルキレンオキシドを反応させてアルキレ
ンオキシド付加物を製造する方法に関するものである。
Description: TECHNICAL FIELD The present invention relates to a method for producing an alkylene oxide adduct of a halogenated phenol, and particularly to an alkylene oxide adduct of a monovalent halogenated phenol or an alkylene oxide on a halogenated bisphenol. The present invention relates to a method for producing an alkylene oxide adduct by reacting

[従来の技術] 従来、一価のハロゲン化フェノール又はハロゲン化ビ
スフェノールのアルキレンオキシドとを反応させて、一
価のハロゲン化フェノールのアルキレンオキシド付加物
又はハロゲン化ビスフェノールのアルキレンオキシド付
加物を製造するためのアルキレンオキシドとの付加反応
に用いられる触媒としては、一般に水酸化ナトリウム、
水酸化カリウムなどのアルカリ金属水酸化物又はナトリ
ウムメトキシド、ナトリウムエトキシドなどのアルカリ
金属のアルコラートを使用する方法が知られているが、
該アルカリ金属の水酸化物又はアルコラートを使用する
方法は、反応中に反応混合物が着色するといった問題点
がある。
[Prior Art] Conventionally, for producing an alkylene oxide adduct of a monovalent halogenated phenol or an alkylene oxide adduct of a halogenated bisphenol by reacting with an alkylene oxide of a monovalent halogenated phenol or a halogenated bisphenol. The catalyst used in the addition reaction of alkylene oxide with sodium is generally sodium hydroxide,
Although a method using an alkali metal hydroxide such as potassium hydroxide or an alkali metal alcoholate such as sodium methoxide or sodium ethoxide is known,
The method using the alkali metal hydroxide or alcoholate has a problem that the reaction mixture is colored during the reaction.

上記方法以外に、特開昭50−105638号公報には、活性
水素を有しない極性溶剤の存在下に、トリメチルアミン
を触媒としてテトラブロモビスフェノールAのジオキシ
アルキレンエーテルを製造する方法が、また、特開昭58
−46034号公報には、テトラブロモビスフェノールAの
溶融物にアルキレンオキシドを付加させる際の触媒とし
て、N,N−ジヒドロキシ−N−n−アルキルアミンを用
いる方法が、さらに、特開昭61−148135号公報には、臭
素化ビスフェノール類をアルキレンオキシドでスラリー
状とし、触媒として第三級アミン(アミン類にアルキレ
ンオキシドを付加させたもので、特にジタノールブチル
アミン)を用いる臭素化ビスフェノール類のアルキレン
オキシド付加物の製造方法が開示されているが、これら
の方法はいずれも反応中に反応混合物が着色するといっ
た問題点がある。
In addition to the above-mentioned method, JP-A-50-105638 discloses a method for producing a dioxyalkylene ether of tetrabromobisphenol A using trimethylamine as a catalyst in the presence of a polar solvent having no active hydrogen. Kaisho 58
-46034 discloses a method of using N, N-dihydroxy-N-n-alkylamine as a catalyst for adding alkylene oxide to a melt of tetrabromobisphenol A, further disclosed in JP-A-61-148135. In JP-A No. 1993-242, an alkylene oxide of a brominated bisphenol is prepared by slurrying a brominated bisphenol with an alkylene oxide and using as a catalyst a tertiary amine (an alkylene oxide added to an amine, especially ditanolbutylamine). Although a method for producing an adduct is disclosed, all of these methods have a problem that the reaction mixture is colored during the reaction.

[発明が解決しようとする問題点] ハロゲン化フェノール類のアルキレンオキシド付加物
は、合成樹脂や合成繊維の添加剤、特に添加型又は反応
型難燃剤として有用なものが多く、そのためには着色の
なるべく少ないものが望ましい。しかしながら、前記の
ようなアルカリ金属の水酸化物又はアルコラートを使用
する方法、あるいは、トリメチルアミン、N,N−ジヒド
ロキシ−N−n−アルキルアミン又はジエタノールブチ
ルアミンを触媒として用いる方法は、いずれも反応中に
着色し、この着色した反応混合物を脱色精製するために
は、別途設けられた精製工程が必要で、そのため製品コ
ストが高くなるという問題点があった。
[Problems to be Solved by the Invention] Alkylene oxide adducts of halogenated phenols are often useful as additives for synthetic resins and synthetic fibers, particularly addition-type or reaction-type flame retardants, and for that purpose, coloring It is desirable to have as few as possible. However, the method using an alkali metal hydroxide or alcoholate as described above, or the method using trimethylamine, N, N-dihydroxy-Nn-alkylamine or diethanolbutylamine as a catalyst is not preferable during the reaction. In order to color and purify the colored reaction mixture by decolorization, a separately provided purification step is required, resulting in a problem of high product cost.

[問題点を解決するための手段] 本発明は上記の問題点に鑑みてなされたもので、すな
わち、一価のハロゲン化フェノール又はハロゲン化ビス
フェノールにアルキレンオキシドを反応させてアルキレ
ンオキシド付加物を製造する方法において、 一般式 (ただし、R1、R2、R3のアルキル基のうち、少なくとも
1つが炭素数5〜28のアルキル基であり、その外のアル
キル基が炭素数1〜28のアルキル基である。) で表わされる脂肪族第三級アミンを、一価のハロゲン化
フェノール及び/又はハロゲン化ビスフェノールに対し
て0.05〜3重量%存在させて反応させることを特徴とす
るハロゲン化フェノール類のアルキレンオキシド付加物
の製造方法である。
[Means for Solving the Problems] The present invention has been made in view of the above problems, that is, an alkylene oxide adduct is produced by reacting a monovalent halogenated phenol or halogenated bisphenol with an alkylene oxide. In the method (However, at least one of the alkyl groups of R 1 , R 2 and R 3 is an alkyl group having 5 to 28 carbon atoms, and the other alkyl group is an alkyl group having 1 to 28 carbon atoms.) An alkylene oxide adduct of halogenated phenols, characterized in that the aliphatic tertiary amine represented is reacted in the presence of 0.05 to 3% by weight with respect to the monovalent halogenated phenol and / or halogenated bisphenol. It is a manufacturing method.

[発明の具体的説明] (1)原料成分 一価のハロゲン化フェノール及びハロゲン化ビスフェノ
ール成分 本発明において用いられる一価のハロゲン化フェノー
ル又はハロゲン化ビスフェノールとしては、下記の一般
及び 〔式中、X1〜X4はそれぞれ塩素、臭素、沃素又は弗素か
ら選ばれた原子を表わしYは (R4及びR5は炭素数1〜3のアルキル基)又は を表わす。〕 で表わされる一価のハロゲン化フェノール類又はハロゲ
ン化ビスフェノール類が用いられる。
[Detailed Description of the Invention] (1) Raw material component Monovalent halogenated phenol and halogenated bisphenol component The monovalent halogenated phenol or halogenated bisphenol used in the present invention has the following general formula: as well as [Wherein, X 1 to X 4 each represent an atom selected from chlorine, bromine, iodine or fluorine, and Y represents (R 4 and R 5 are alkyl groups having 1 to 3 carbon atoms) or Represents ] Monovalent halogenated phenols or halogenated bisphenols represented by the following are used.

上記式中において、一価のハロゲン化フェノール類の
X1〜X3は特に塩素又は臭素が好ましい。
In the above formula, a monovalent halogenated phenol
Particularly, X 1 to X 3 are preferably chlorine or bromine.

アルキレンオキシド成分 前記一価のハロゲン化フェノール又はハロゲン化ビス
フェノール成分に付加されるアルキレンオキシドとして
は、エチレンオキシド(以下単にEOと略記する)、プロ
ピレンオキシド(以下単にPOと略記する)、ブチレンオ
キシド(以下単にBuOと略記する)などが挙げられる
が、特にEO、POが好適である。
Alkylene oxide component As the alkylene oxide added to the monovalent halogenated phenol or halogenated bisphenol component, ethylene oxide (hereinafter simply abbreviated as EO), propylene oxide (hereinafter simply abbreviated as PO), butylene oxide (hereinafter simply referred to as (Abbreviated as BuO) and the like, but EO and PO are particularly preferable.

触媒 本発明において触媒として用いられる脂肪族第三級ア
ミンとしては、下記の一般式で表わされるものが用いら
れる。
Catalyst As the aliphatic tertiary amine used as a catalyst in the present invention, those represented by the following general formula are used.

〔ただし、R1、R2、R3のアルキル基のうち少なくとも1
つが炭素数5〜28(好ましくは炭素数8〜22)のアルキ
ル基であり、その外のアルキル基が炭素数1〜28のアル
キル基である。〕 で表わされるものである 上記式中のR1〜R3の炭素数がすべて5未満の場合、あ
るいは、炭素数が28を越える場合は、十分な触媒効果を
得ることができない。すなわち、炭素数がすべて4以下
の場合や炭素数が29以上のものが含まれている場合は、
反応生成物の着色が大きい。
[However, at least 1 of the alkyl groups of R 1 , R 2 and R 3
One is an alkyl group having 5 to 28 carbon atoms (preferably 8 to 22 carbon atoms), and the other alkyl group is an alkyl group having 1 to 28 carbon atoms. ] When all the carbon atoms of R 1 to R 3 in the above formula are less than 5, or the carbon number exceeds 28, a sufficient catalytic effect cannot be obtained. That is, if the carbon number is all 4 or less, or if the carbon number is 29 or more,
The reaction product is highly colored.

上記触媒である脂肪族第三級アミンの添加量は、一価
のハロゲン化フェノール又はハロゲン化ビスフェノール
に対して0.05〜3重量%、好ましくは0.2〜0.8重量%で
ある。添加量が上記範囲より少ない場合には本発明の効
果を十分に発揮することができず、また、多過ぎる場合
は製品の用途によって好ましくない結果を生ずる。
The amount of the aliphatic tertiary amine as the above catalyst added is 0.05 to 3% by weight, preferably 0.2 to 0.8% by weight, based on the monovalent halogenated phenol or halogenated bisphenol. If the added amount is less than the above range, the effect of the present invention cannot be sufficiently exhibited, and if the added amount is too large, unfavorable results are produced depending on the use of the product.

本発明において用いられる触媒は単独で用いることも
できるが、これら触媒を二種類以上併用して用いること
もできる。
The catalyst used in the present invention may be used alone, or two or more kinds of these catalysts may be used in combination.

(2)反応 反応は加圧下で実施されるのが好ましく、具体的には
触媒量、触媒の種類、アルキレンオキシドの種類、ハロ
ゲン化フェノール類、ハロゲン化ビスフェノール類の種
類などで変化するので、反応圧力は適宜選択されるが、
一般には0〜3.0kg/cm2の圧力である。
(2) Reaction It is preferable to carry out the reaction under pressure. Specifically, the reaction varies depending on the amount of catalyst, type of catalyst, type of alkylene oxide, halogenated phenols, halogenated bisphenols, etc. The pressure is selected appropriately,
Generally, the pressure is 0 to 3.0 kg / cm 2 .

また、反応温度は、一般に80〜200℃、好ましくは100
〜150℃である。反応温度が上記範囲より低い場合には
反応速度が遅くなり、また、高い場合には反応中に分解
が促進され、歩留まりを悪化させるので好ましくない。
The reaction temperature is generally 80 to 200 ° C., preferably 100.
~ 150 ° C. When the reaction temperature is lower than the above range, the reaction rate becomes slow, and when it is high, decomposition is promoted during the reaction and the yield is deteriorated, which is not preferable.

(3)付加反応生成物 上記付加反応によって製造される反応生成物として
は、一価のハロゲン化フェノールのアルキレンオキシド
付加物及び/又はハロゲン化ビスフェノールのアルキレ
ンオキシド付加物であって、このアルキレンオキシド付
加反応生成物はそのまま、あるいは変性した後、合成樹
脂又は合成繊維の難燃剤として配合され、利用すること
ができる。
(3) Addition reaction product The reaction product produced by the addition reaction is an alkylene oxide adduct of a monovalent halogenated phenol and / or an alkylene oxide adduct of a halogenated bisphenol. The reaction product can be used as it is or after being modified and then blended as a flame retardant for synthetic resin or synthetic fiber.

前記アルキレンオキシド成分はこの付加反応によっ
て、付加反応生成物中に1〜6モル程度付加されるのが
普通である。付加の程度は付加反応生成物の難燃の程度
あるいは融点などの用途によって適宜決められる。
The alkylene oxide component is usually added to the addition reaction product in an amount of about 1 to 6 mol by this addition reaction. The degree of addition is appropriately determined according to the degree of flame retardancy of the addition reaction product or the application such as melting point.

[実施例] 実施例1〜11及び比較例1〜7 撹拌機、温度計、ガス導入管を備えた内容積が2の
オートクレーブに、表−1又は表−2に示すハロゲン化
フェノール類及び触媒を加えて、十分に窒素置換した
後、撹拌しながら加熱し、表−1又は表−2に示す反応
温度に達した時点で、表−1又は表−2に示すアルキレ
ンオキシドを徐々に導入して、表−1又は表−2に示す
反応時間だけ反応を行なった。
[Examples] Examples 1 to 11 and Comparative Examples 1 to 7 In an autoclave having an inner volume of 2 equipped with a stirrer, a thermometer, and a gas introduction pipe, halogenated phenols and catalysts shown in Table 1 or Table 2 Was added, and after sufficiently substituting with nitrogen, the mixture was heated with stirring, and when the reaction temperature shown in Table-1 or Table-2 was reached, the alkylene oxide shown in Table-1 or Table-2 was gradually introduced. Then, the reaction was performed for the reaction time shown in Table-1 or Table-2.

なお反応は、アルキレンオキシドの導入の停止後、更
に同じ温度を保ちながら撹拌下に1時間熟成を行なった
ものである。
The reaction was carried out after the introduction of the alkylene oxide was stopped and then aged for 1 hour under stirring while maintaining the same temperature.

熟成が終了した後、60℃まで冷却して、反応生成物を
取り出した。
After the aging was completed, the reaction product was taken out by cooling to 60 ° C.

この反応混合物の色調をガードナー法色調基準(油脂
化学製品便覧第150〜151頁参照:日刊工業新聞社昭和38
年10月30日発行)によって測定した。
The color tone of this reaction mixture is based on the Gardner method color tone standard (Refer to pages 150-151 of the manual for oleochemicals: Showa 38, Nikkan Kogyo Shimbun).
Issued October 30, 2013).

その結果を表−1及び表−2に示す。 The results are shown in Table-1 and Table-2.

[発明の効果] 本発明のハロゲン化フェノール類のアルキレン オキシド付加物の製造方法は、従来のハロゲン化フェノ
ール類のアルキレンオキシド付加物の製造方法に比較し
て、著しく製品の着色度が低いハロゲン化フェノールの
アルキレンオキシド付加物、及び/又はハロゲン化ビス
フェノールのアルキレンオキシド付加物を製造すること
ができるので、該製品を合成樹脂及び合成繊維にそのま
ま難燃剤として配合しても、着色の少ない合成樹脂及び
合成繊維とすることができるため、工業的に極めて有用
なものである。
[Effects of the Invention] Alkylene of the halogenated phenols of the present invention The method for producing an oxide adduct is such that an alkylene oxide adduct of a halogenated phenol and / or a halogenated bisphenol of which the coloring degree of the product is significantly lower than the conventional method for producing an alkylene oxide adduct of halogenated phenols. Since an alkylene oxide adduct can be produced, even if the product is directly blended with a synthetic resin and a synthetic fiber as a flame retardant, a synthetic resin and a synthetic fiber with little coloring can be obtained, which is industrially very useful. It is something.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 // C07B 61/00 300 C07B 61/00 300 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location // C07B 61/00 300 C07B 61/00 300

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】一価のハロゲン化フェノール又はハロゲン
化ビスフェノールにアルキレンオキシドを反応させてア
ルキレンオキシド付加物を製造する方法において、一般
(ただし、R1、R2、R3のアルキル基のうち、少なくとも
1つが炭素数5〜28のアルキル基であり、その外のアル
キル基が炭素数1〜28のアルキル基である。) で表わされる脂肪族第三級アミンを、一価のハロゲン化
フェノール及び/又はハロゲン化ビスフェノールに対し
て0.05〜3重量%存在させて反応させることを特徴とす
るハロゲン化フェノール類のアルキレンオキシド付加物
の製造方法。
1. A method for producing an alkylene oxide adduct by reacting a monovalent halogenated phenol or a halogenated bisphenol with an alkylene oxide, wherein: (However, at least one of the alkyl groups of R 1 , R 2 and R 3 is an alkyl group having 5 to 28 carbon atoms, and the other alkyl group is an alkyl group having 1 to 28 carbon atoms.) An alkylene oxide adduct of halogenated phenols, characterized in that the aliphatic tertiary amine represented is reacted in the presence of 0.05 to 3% by weight with respect to the monovalent halogenated phenol and / or halogenated bisphenol. Production method.
JP62160460A 1987-06-26 1987-06-26 Process for producing alkylene oxide adduct of halogenated phenols Expired - Lifetime JP2549073B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62160460A JP2549073B2 (en) 1987-06-26 1987-06-26 Process for producing alkylene oxide adduct of halogenated phenols

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62160460A JP2549073B2 (en) 1987-06-26 1987-06-26 Process for producing alkylene oxide adduct of halogenated phenols

Publications (2)

Publication Number Publication Date
JPS646231A JPS646231A (en) 1989-01-10
JP2549073B2 true JP2549073B2 (en) 1996-10-30

Family

ID=15715420

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62160460A Expired - Lifetime JP2549073B2 (en) 1987-06-26 1987-06-26 Process for producing alkylene oxide adduct of halogenated phenols

Country Status (1)

Country Link
JP (1) JP2549073B2 (en)

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5218101B2 (en) * 1973-06-18 1977-05-19
JPS6161626A (en) * 1984-09-03 1986-03-29 Riken Vitamin Co Ltd Manufacture of emulsifier composition
JPS61148135A (en) * 1984-12-21 1986-07-05 Asahi Glass Co Ltd Alkoxylation of brominated bisphenol
GB8509729D0 (en) * 1985-04-16 1985-05-22 British Petroleum Co Plc Preparation of alkoxy halides

Also Published As

Publication number Publication date
JPS646231A (en) 1989-01-10

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