JPS5840933B2 - Method for producing 2,4,2',4'-tetrabromidiphenyl ether - Google Patents

Method for producing 2,4,2',4'-tetrabromidiphenyl ether

Info

Publication number
JPS5840933B2
JPS5840933B2 JP52040971A JP4097177A JPS5840933B2 JP S5840933 B2 JPS5840933 B2 JP S5840933B2 JP 52040971 A JP52040971 A JP 52040971A JP 4097177 A JP4097177 A JP 4097177A JP S5840933 B2 JPS5840933 B2 JP S5840933B2
Authority
JP
Japan
Prior art keywords
ether
bromine
reaction
tetrabromidiphenyl
catalyst
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
Application number
JP52040971A
Other languages
Japanese (ja)
Other versions
JPS53127428A (en
Inventor
勝好 笹川
一徳 田辺
良昭 野口
栄一 野田
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP52040971A priority Critical patent/JPS5840933B2/en
Publication of JPS53127428A publication Critical patent/JPS53127428A/en
Publication of JPS5840933B2 publication Critical patent/JPS5840933B2/en
Expired 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)

Description

【発明の詳細な説明】 本発明は2・4・2・4′−テトラフロムジフェニルエ
ーテルの製造法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing 2,4,2,4'-tetrafluoromdiphenyl ether.

テトラブロムジフェニルエーテルの製法とじてジブロム
エタン、テトラクロルエタン、四塩化炭素等の有機溶媒
中で臭素とジフェニルエーテルのモル比を4として反応
させるか、もしくは発煙硫酸中で臭素とジフェニルエー
テルのモル比を2として反応させる方法が知られている
The method for producing tetrabromidiphenyl ether involves reacting bromine and diphenyl ether in an organic solvent such as dibromoethane, tetrachloroethane, or carbon tetrachloride with a molar ratio of 4, or in fuming sulfuric acid with a molar ratio of bromine and diphenyl ether of 2. There are known ways to do this.

しかしこれらの方法では有機溶媒の臭素化有機溶媒の回
収、精製、廃硫酸の処理等が必要であり、また同一規模
の製造に対して大きな製造装置を必要とする等、工業的
に不利な点が多く、そのうえ、副生物としてテトラブロ
ムジフェニルエーテルの異性体や、トリフロムジフェニ
ルエーテル、ペンタブロムジフェニルエーテル等カ生成
し、2・4・/・4′−テトラブロムジフエニルエーテ
ルのみを選択的に製造することは出来なかった。
However, these methods require recovery and purification of the brominated organic solvent, treatment of waste sulfuric acid, etc., and also have industrial disadvantages such as the need for large production equipment for the same scale of production. In addition, isomers of tetrabromidiphenyl ether, trifluoromdiphenyl ether, pentabromidiphenyl ether, etc. are produced as by-products, and only 2,4/4'-tetrabromidiphenyl ether can be selectively produced. I couldn't do it.

一方、臭素中でジフェニルエーテルを臭素化してテトラ
ブロムジフェニルエーテルを製造する方法は、これまで
、前記の製造法以上に反応制御が困難であり、臭素化率
の異る巾広い臭素化ジフェニルエーテルの生成が起ると
考えられていた。
On the other hand, the method of producing tetrabrominated diphenyl ether by brominating diphenyl ether in bromine has hitherto been more difficult to control the reaction than the above-mentioned production method, resulting in the production of a wide range of brominated diphenyl ethers with different bromination rates. It was thought that

本発明者らは臭素中でテトラブロムジフェニルエーテル
を製造する方法について鋭意検討を行なった結果、驚く
べきことに、過剰の臭素中で35℃乃至常圧下の臭素の
沸点の温度に於いて無触媒でジフェニルエーテルの臭素
化を行なうことにより2・4・2・4′−テトラブロム
ジフェニルエーテルが選択的に生成すること及び後記す
るようなある種の触媒の存在下で35℃以下の温度に於
いて過剰の臭素中でジフェニルエーテルの臭素化を行な
うことによりやはり2・4・グ・4′−テトラブロムジ
フェニルエーテルが選択的に生成することを見出し本発
明に達したものである。
The present inventors conducted intensive studies on a method for producing tetrabromidiphenyl ether in bromine, and surprisingly found that it can be produced without a catalyst in excess bromine at a temperature of 35°C to the boiling point of bromine under normal pressure. By brominating diphenyl ether, 2,4,2,4'-tetrabromidiphenyl ether is selectively produced, and in the presence of certain catalysts as described below, at temperatures below 35°C, excess The present invention was achieved by discovering that 2,4,g,4'-tetrabromidiphenyl ether is selectively produced by brominating diphenyl ether in bromine.

本発明によって得られるテトラブロムジフェニルエーテ
ルは、2・4・/・4′−テトラブロムジフェニルエー
テル98〜100%、その異性体、トリブロムジフェニ
ルエーテルおヨヒペンタフロムジフェニルエーテルO〜
2%よりなる極めて純度の高い2・4・/・4′−テト
ラブロムフェニルエーテルである。
The tetrabromidiphenyl ether obtained by the present invention includes 98 to 100% of 2,4/4'-tetrabromidiphenyl ether, its isomers, tribromidiphenyl ether, yohypentafrom diphenyl ether O to
It is extremely pure 2,4./.4'-tetrabromphenyl ether consisting of 2%.

本発明により、2・4・/・4′−テトラフロムジフェ
ニルエーテルを臭素中でしかも極めて高い選択率で製造
することが可能となり、このことは工業的に多くの利点
を有するものである。
The present invention makes it possible to produce 2,4./.4'-tetrafluorodiphenyl ether in bromine with extremely high selectivity, which has many industrial advantages.

本発明は、過剰の臭素を反応溶媒とし、この臭素中に無
触媒あるいは後記するようなある種の触媒の存在下にジ
フェニルエーテルを添加することにより行われる。
The present invention is carried out by using excess bromine as a reaction solvent and adding diphenyl ether to the bromine without a catalyst or in the presence of a certain type of catalyst as described below.

本発明で用いる臭素の量は、反応当量の1.5〜5倍量
、好ましくは2〜4倍量である。
The amount of bromine used in the present invention is 1.5 to 5 times the reaction equivalent, preferably 2 to 4 times the reaction equivalent.

反応当量の1.5倍量以下の臭素では反応により臭素が
消費されるにつれて臭素の溶媒効果がうすれ、均一な混
合が保たれなくなるためテトラブロムジフェニルエーテ
ルの選択率が低下し、一方反応当量の5倍量以上では反
応後の臭素の回収等経済的に不利となるので好ましくな
い。
If the amount of bromine is less than 1.5 times the reaction equivalent, the solvent effect of bromine will weaken as the bromine is consumed by the reaction, and homogeneous mixing will no longer be maintained, resulting in a decrease in the selectivity of tetrabrom diphenyl ether. If the amount is more than double the amount, it is not preferable because it causes economic disadvantages such as recovery of bromine after the reaction.

本発明での反応は、触媒を用いなくてもよいが、触媒を
用いない場合には触媒を用いる場合に比べ、高温下でか
つ長時間反応させることが必要であり、従って工業的に
は触媒を用いることが好ましい。
Although the reaction in the present invention does not require the use of a catalyst, in the case of not using a catalyst, it is necessary to carry out the reaction at a higher temperature and for a longer time than in the case of using a catalyst. It is preferable to use

反応は触媒を用いない場合に35℃以上、好ましくは4
0℃以上常圧下の臭素の沸点以下の温度で3時間以上、
触媒を用いる場合には35℃以下好ましくは30℃以下
で1時間以上行う。
The reaction is carried out at temperatures above 35°C, preferably at 4°C when no catalyst is used.
At a temperature of 0°C or higher and lower than the boiling point of bromine under normal pressure for 3 hours or more,
When a catalyst is used, the reaction is carried out at 35°C or lower, preferably 30°C or lower for 1 hour or more.

本発明で用いる触媒は、亜鉛および錫の塩化物および硫
酸塩;結晶水を有する鉄の塩化物、硫酸塩およびリン酸
塩;並びにアルミニウムの硫酸塩およびリン酸塩である
The catalysts used in the invention are chlorides and sulfates of zinc and tin; chlorides, sulfates and phosphates of iron with water of crystallization; and sulfates and phosphates of aluminum.

触媒の量は、使用する臭素に対して0.01重量%〜5
重量%、好ましくは0.1重量%〜2重量%である。
The amount of catalyst is between 0.01% and 5% by weight based on the bromine used.
% by weight, preferably from 0.1% to 2% by weight.

0.01重量%以下では触媒効果が弱く、5重量%以上
では製品中への触媒の混入等があり好ましくない。
If it is less than 0.01% by weight, the catalytic effect is weak, and if it is more than 5% by weight, the catalyst may be mixed into the product, which is not preferable.

ジフェニルエーテルの臭素中への添加は一度にあるいは
分割して行われるが、分割して加える場合に比べ、一度
に加える場合は反応熱のため、温度制御が困難でありテ
トラブロムジフェニルエーテルの選択率が低下する危険
性があるため、分割して加えることが好ましい。
Diphenyl ether can be added to bromine at once or in parts, but compared to adding in parts, it is difficult to control the temperature due to the reaction heat when adding it all at once, and the selectivity of tetrabrom diphenyl ether decreases. It is preferable to add the mixture in portions, as there is a risk of this.

反応終了後、触媒を用いた場合には反応液中に水又は塩
酸、硫酸等の酸性水溶液を加え触媒を水層に抽出した後
、過剰の臭素を留出除去し、一方触媒を用いなL・場合
をま反応液中に水を加えて後過剰の臭素を留出除去する
ことによって反応生成物を水中に析出させる。
After the reaction is completed, if a catalyst is used, water or an acid aqueous solution such as hydrochloric acid or sulfuric acid is added to the reaction solution to extract the catalyst into the aqueous layer, and excess bromine is removed by distillation. - Occasionally, water is added to the reaction solution, and then excess bromine is removed by distillation to precipitate the reaction product in water.

反応生成物は任意の方法で分離洗浄し乾燥する。The reaction product is separated, washed and dried by any method.

本発明で得られる反応生成物は、2・4・2/・4′−
テトラブロムジフェニルニーデルの含量力98〜100
%と極めて高く、そのまへで十分に使用されうる。
The reaction product obtained in the present invention is 2.4.2/.4'-
Tetrabromodiphenyl needle content 98-100
%, and can be used as is.

必要な場合にはジクロルエタン、ジクロルベンゼン、ト
ルエン、キシレン等の溶媒を用いて再結晶を行う。
If necessary, recrystallization is performed using a solvent such as dichloroethane, dichlorobenzene, toluene, or xylene.

本発明により得られた2・4・2′・4′−テトラブロ
ムジフェニルエーテルはポリスチレン、ホリエチレン等
のポリオレフィン用の耐光性に優れた難燃剤として極め
て有用であり、又、ポリエステル、ナイロン等の繊維類
、ポリウレタンあるいは塗料用の難燃剤として有効であ
ることが本発明者らの検討の結果明らかとなった。
The 2,4,2',4'-tetrabromidiphenyl ether obtained by the present invention is extremely useful as a flame retardant with excellent light resistance for polyolefins such as polystyrene and polyethylene, and also for fibers such as polyester and nylon. As a result of studies conducted by the present inventors, it has become clear that the present invention is effective as a flame retardant for polyurethanes, polyurethanes, and paints.

以下に例をあげて本発明の方法を詳しく説明する。The method of the present invention will be explained in detail with reference to examples below.

なお実施例中の部および%はいずれも重量部、および重
量%を示す。
Note that all parts and % in the examples indicate parts by weight and % by weight.

実施例 1〜6 攪拌機、温度計、還流冷却器滴下ロートを付した四ツロ
フラスコに表1に示す臭素、および触媒を入れ、所定の
温度でジフェニルエーテルを滴下した。
Examples 1 to 6 Bromine and a catalyst shown in Table 1 were placed in a four-way flask equipped with a stirrer, a thermometer, a reflux condenser and a dropping funnel, and diphenyl ether was added dropwise at a predetermined temperature.

ジフェニルエーテル滴下後、必要に応じて熟成反応を行
った。
After dropwise addition of diphenyl ether, a ripening reaction was performed as necessary.

その後、水又は塩酸水溶液を加え30分攪拌して触媒を
抽出し、次いで還流冷却器を留出装置にとりかえて過剰
の臭素を留出除去した。
Thereafter, water or an aqueous hydrochloric acid solution was added and the mixture was stirred for 30 minutes to extract the catalyst, and then the reflux condenser was replaced with a distillation device to remove excess bromine by distillation.

(但し実施例1は水を加えた後、直ちに過剰の臭素を留
出除去した。
(However, in Example 1, excess bromine was removed by distillation immediately after adding water.

)冷却後、得られた反応生成物を1過、水洗、乾燥した
) After cooling, the obtained reaction product was filtered once, washed with water, and dried.

乾燥した反応生成物についてガスクロ分析を行い、その
組成を求めた。
Gas chromatography analysis was performed on the dried reaction product to determine its composition.

反応条件および結果を表−1に示した。The reaction conditions and results are shown in Table-1.

なお表−1組成欄の略号は次の通りである。The abbreviations in the composition column of Table 1 are as follows.

2.4−TBDPE: 2・4・/・4′−テトラブロ
ムジフェニルエーテル TBDPE:テトラフロムジフェニルエーテルの異性体
2.4-TBDPE: 2.4./.4'-tetrabromidiphenyl ether TBDPE: isomer of tetrafromdiphenyl ether

Claims (1)

【特許請求の範囲】 1 ジフェニルエーテルを過剰の臭素中で(a)35℃
乃至常圧下の臭素の沸点温度に於いて無触媒で、 もしくは (b) 亜鉛および錫の塩化物および硫酸塩;結晶水
を有する鉄の塩化物、硫酸塩およびりん酸塩:並びにア
ルミニウムの硫酸塩およびりん酸塩の1種又は2種以上
の存在下35℃以下の温度で反応させることを特徴とす
る2・4・/・4′−テトラブロムジフェニルエーテル
の製造法。
[Claims] 1. Diphenyl ether in excess bromine (a) at 35°C
or (b) chlorides and sulfates of zinc and tin; chlorides, sulfates and phosphates of iron with water of crystallization; and sulfates of aluminum; A method for producing 2,4./.4'-tetrabromidiphenyl ether, characterized in that the reaction is carried out at a temperature of 35° C. or lower in the presence of one or more kinds of phosphates.
JP52040971A 1977-04-12 1977-04-12 Method for producing 2,4,2',4'-tetrabromidiphenyl ether Expired JPS5840933B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52040971A JPS5840933B2 (en) 1977-04-12 1977-04-12 Method for producing 2,4,2',4'-tetrabromidiphenyl ether

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52040971A JPS5840933B2 (en) 1977-04-12 1977-04-12 Method for producing 2,4,2',4'-tetrabromidiphenyl ether

Publications (2)

Publication Number Publication Date
JPS53127428A JPS53127428A (en) 1978-11-07
JPS5840933B2 true JPS5840933B2 (en) 1983-09-08

Family

ID=12595333

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52040971A Expired JPS5840933B2 (en) 1977-04-12 1977-04-12 Method for producing 2,4,2',4'-tetrabromidiphenyl ether

Country Status (1)

Country Link
JP (1) JPS5840933B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0384043A3 (en) * 1989-02-21 1991-08-07 The Dow Chemical Company Methods for the preparation of brominated intermediates

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5037735A (en) * 1973-07-13 1975-04-08

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5037735A (en) * 1973-07-13 1975-04-08

Also Published As

Publication number Publication date
JPS53127428A (en) 1978-11-07

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