JPS5929174B2 - Purification method of prominated diphenyl ether - Google Patents

Purification method of prominated diphenyl ether

Info

Publication number
JPS5929174B2
JPS5929174B2 JP9543876A JP9543876A JPS5929174B2 JP S5929174 B2 JPS5929174 B2 JP S5929174B2 JP 9543876 A JP9543876 A JP 9543876A JP 9543876 A JP9543876 A JP 9543876A JP S5929174 B2 JPS5929174 B2 JP S5929174B2
Authority
JP
Japan
Prior art keywords
diphenyl ether
bromine
brominated
solution
inorganic acid
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
JP9543876A
Other languages
Japanese (ja)
Other versions
JPS5321129A (en
Inventor
良昭 野口
栄一 野田
一徳 田辺
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 JP9543876A priority Critical patent/JPS5929174B2/en
Publication of JPS5321129A publication Critical patent/JPS5321129A/en
Publication of JPS5929174B2 publication Critical patent/JPS5929174B2/en
Expired legal-status Critical Current

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Fireproofing Substances (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Description

【発明の詳細な説明】 本発明はブロム化ジフェニルエーテルの精製法に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for purifying brominated diphenyl ether.

最近、国内および諸外国においてプラスチック類の難燃
化に対する規制が強化される傾向があり、各種の難燃剤
についての研究が盛んになされている。
Recently, there has been a tendency for regulations regarding flame retardant plastics to be tightened in Japan and other countries, and research on various flame retardants has been actively conducted.

デカブロムジフェニルエーテルまたはこれを主成分とす
るプロム化ジフェニルエーテルは難燃剤として有効な臭
素の含有量が高く、固体でかつ熱分解温度も高い等、添
加型難燃剤として極めて優れた性能を有しており、各種
プラスチック用難燃剤として非常に有用であることは既
に知られている。特にポリオレフィン類例えばポリエチ
レン、ポリプロピレン、ポリスチレン等の難燃化には極
めて有効な難燃剤である。デカブロムジフェニルエーテ
ルまたはこれを主成分とするブロム化ジフェニルエーテ
ルの製造法については種々知られているものの回収精製
が必要となる有機溶媒を反応に用いないことから臭素溶
媒による製造が最も有利である。
Decabromidiphenyl ether or prominated diphenyl ether containing it as the main component has a high content of bromine, which is effective as a flame retardant, is solid, and has a high thermal decomposition temperature, so it has extremely excellent performance as an additive flame retardant. , is already known to be very useful as a flame retardant for various plastics. In particular, it is an extremely effective flame retardant for making polyolefins such as polyethylene, polypropylene, and polystyrene flame retardant. Although various methods for producing decabromidiphenyl ether or brominated diphenyl ether containing decabrominated diphenyl ether as a main component are known, production using a brominated solvent is most advantageous since an organic solvent that requires recovery and purification is not used in the reaction.

しかしながらこの方法では得られる反応生成物結晶が淡
褐色に着色しているため精製が必要である。精製法とし
ては従来トルエンキシレン等の芳香族化合物、ジブロム
エタン、ジクロルエタン等の脂肪族ハロゲン化物、ある
いはブロムベンゼン、クロルベンゼン等の芳香族ハロゲ
ン化物を用いた再結晶による精製法が知られていた。し
かし、この従来法では再結晶に用いた有機溶媒の回収、
精製が必要であり、反応に際して有機溶媒を必要としな
い臭素溶媒による製造法の利点が減殺され、そのうえ、
再結晶に用いた有機溶媒の一部が、反応生成物中に含有
されている臭素によつて臭素化されることもあるので、
回収、精製がさらに複雑となり、好ましい方法ではなか
つた。本発明者らは水溶液によるデカブロムジフェニル
エーテルまたはこれを主成分とするブロム化ジフェニル
エーテルの精製法について検討を行つた結果、反応生成
物を含有する臭素溶液に無機酸水溶液を加えて過剰の臭
素を蒸留除去しながら無機酸水溶液で処理することによ
り無色のデカブロムジフェニルエーテルまたはこれを主
成分とするブロム化ジフェニルエーテルが得られること
を見出した。
However, this method requires purification because the reaction product crystals obtained are pale brown in color. Conventionally known purification methods include recrystallization using aromatic compounds such as toluene xylene, aliphatic halides such as dibromoethane and dichloroethane, or aromatic halides such as bromobenzene and chlorobenzene. However, this conventional method requires recovery of the organic solvent used for recrystallization,
Purification is required, and the advantage of the brominated solvent production method, which does not require an organic solvent during the reaction, is negated;
A part of the organic solvent used for recrystallization may be brominated by bromine contained in the reaction product.
Recovery and purification became more complicated, and this was not a preferred method. The present inventors investigated a method for purifying decabrominated diphenyl ether or brominated diphenyl ether containing decabrominated diphenyl ether as a main component using an aqueous solution. As a result, excess bromine was distilled by adding an inorganic acid aqueous solution to a bromine solution containing the reaction product. It has been found that colorless decabromidiphenyl ether or brominated diphenyl ether containing decabrominated diphenyl ether as a main component can be obtained by treating with an aqueous inorganic acid solution while removing the decabromidiphenyl ether.

しかし、この方法では得られたデカブロム、ジフェニル
エーテルまたはこれを主成分とするブロム化ジフェニル
エーテルの脱色がまだ不十分でありそのうえ精製工程で
析出する製品結晶の容器壁への付着が起り、なお問題が
あつた。本発明者らは、更に検討を行つた結果、反応生
成物を含有する臭素溶液を無機酸水溶液で洗浄すること
により製品の脱色を十分にすると同時に容器壁への結晶
付着を防止出来ることを見出し本発明に達したものであ
る。
However, with this method, the decolorization of the obtained decabrome, diphenyl ether, or brominated diphenyl ether containing these as the main component is still insufficient, and furthermore, product crystals that precipitate during the purification process adhere to the container wall, resulting in problems. Ta. As a result of further studies, the present inventors discovered that by washing the bromine solution containing the reaction product with an inorganic acid aqueous solution, it is possible to sufficiently decolorize the product and at the same time prevent crystals from adhering to the container wall. This invention has been achieved.

而して本発明は臭素中で触媒の存在下にジフエニルエー
テルを臭素化してデカプロムジフエニルエーテルまたは
これを主成分とするブロム化ジフエニルエーテルを製造
するに際して反応生成物を含有する臭素溶液に無機酸水
溶液を加え、30℃〜臭素の沸点の温度で、臭素の全還
流下に、一定時間攪拌を行なつた後、過剰の臭素を蒸留
除去しながら前記無機酸水溶液で処理することを特徴と
するブロム化ジフエニルエーテルの精製法である。つぎ
に本発明について詳述する。
Therefore, the present invention provides a bromine solution containing a reaction product for producing decaprom diphenyl ether or a brominated diphenyl ether containing decaprom diphenyl ether as a main component by brominating diphenyl ether in the presence of a catalyst in bromine. Add an inorganic acid aqueous solution to the mixture, stir for a certain period of time under total reflux of bromine at a temperature between 30°C and the boiling point of bromine, and then treat with the inorganic acid aqueous solution while removing excess bromine by distillation. This is a characteristic method for purifying brominated diphenyl ether. Next, the present invention will be explained in detail.

先づ、デカプロムジフエニルエーテルまたはこれを主成
分とするブロム化ジフエニルエーテルは公知の方法でつ
ぎのように製造する。触媒を添加した臭素中にジフエニ
ルエーテルを1〜10時間好ましくは2〜5時間で滴下
し、臭素の沸点以下好ましくは30〜55℃でブロム化
を行わせ、さらに同温度で1〜10時間、好ましくは1
〜5時間熟成を行うことにより製造される。触媒として
はヨウ素、ハロゲン化アルミニウム、ハロゲン化鉄等の
通常知られたハロゲン化触媒を単独に、あるいは数種混
合したものが用いられ、その使用量はジフエニルエーテ
ルに対し、0.5〜20重量%、好ましくは1〜10重
量%である。
First, decaprom diphenyl ether or a brominated diphenyl ether containing decaprom diphenyl ether as a main component is produced by a known method as follows. Diphenyl ether is added dropwise into bromine containing a catalyst over a period of 1 to 10 hours, preferably 2 to 5 hours, and bromination is carried out at a temperature below the boiling point of bromine, preferably 30 to 55°C, and then further maintained at the same temperature for 1 to 10 hours. , preferably 1
It is produced by aging for ~5 hours. As a catalyst, commonly known halogenation catalysts such as iodine, aluminum halide, iron halide, etc. are used alone or in a mixture of several kinds, and the amount used is 0.5 to 20% based on diphenyl ether. % by weight, preferably from 1 to 10% by weight.

臭素は反応当量の2〜10倍量好ましくは3〜5倍量が
用いられる。熟成の終了した時点では反応により生成し
たブロム化ジフエニルエーテルは過剰の臭素に溶解した
状態である。本発明による精製法では上記の如くして得
られたデカプロムジフエニルエーテルまたはこれを主成
分とするブロム化ジフエニルエーテルの臭素溶液に無機
酸水溶液を加え臭素の沸点以下好ましくは30℃〜臭素
の沸点の温度で0.5時間以上、好ましくは1〜5時間
臭素の全還流下に攪拌し、臭素溶液を無機酸水溶液と十
分に接触させて洗浄し、次いで加熱を強めて過剰の臭素
を系外に蒸留除去してデカプロムジフエニルエーテルま
たはこれを主成分とするブロム化ジフエニルエーテルの
結晶を析出させ、得られた結晶を▲過水洗することによ
つて無色のデカプロムジフエニルエーテルまたはこれを
主成分とするブロム化ジフエニルエーテルを得る。
Bromine is used in an amount of 2 to 10 times, preferably 3 to 5 times, the reaction equivalent. At the end of the ripening, the brominated diphenyl ether produced by the reaction is dissolved in excess bromine. In the purification method according to the present invention, an aqueous inorganic acid solution is added to a bromine solution of decaprom diphenyl ether or brominated diphenyl ether containing decaprom diphenyl ether as a main component, and the temperature is below the boiling point of bromine, preferably from 30°C to bromine. The bromine solution is stirred under total reflux for at least 0.5 hours, preferably 1 to 5 hours, at a temperature of the boiling point of The crystals of decaprom diphenyl ether or brominated diphenyl ether containing decaprom diphenyl ether as a main component are precipitated by distillation out of the system, and the resulting crystals are washed with water to obtain colorless decaprom diphenyl ether. Alternatively, a brominated diphenyl ether containing this as a main component is obtained.

上記の如く臭素溶液を無機酸水溶液で十分に洗浄するこ
とによつて無色のデカプロムジフエニルエーテルまたは
これを主成分とするブロム化ジフエニルエーテルを得る
ことが可能になると同時に過剰の臭素を蒸留除去して結
晶を晶析させる際に起る析出結晶の容器器壁への付着を
完全に防止することが出来る。
By thoroughly washing the bromine solution with an aqueous inorganic acid solution as described above, it becomes possible to obtain colorless decaprom diphenyl ether or brominated diphenyl ether containing this as the main component, and at the same time distill excess bromine. It is possible to completely prevent the precipitated crystals from adhering to the walls of the container, which occurs when the crystals are removed and crystallized.

本発明に用いる無機酸としては、塩酸、硫酸、臭化水素
酸等の通常知られた無機酸であり、水溶液の濃度は3〜
40%好ましくは5〜20%のものを使用する。
The inorganic acids used in the present invention are commonly known inorganic acids such as hydrochloric acid, sulfuric acid, and hydrobromic acid, and the concentration of the aqueous solution is 3 to 3.
40%, preferably 5 to 20%.

無機酸水溶液の使用量は結晶の理輪生成量に対し、0.
5〜10重量倍量好ましくは1〜5倍量である。無機酸
水溶液の酸濃度が3%以下では精製効果が低く、40%
以上では実用的でない。また無機酸水溶液の使用量は結
晶量の0.5倍量以下では結晶が析出した後の攪拌が困
難であり、10倍量以上では実用的でない。結晶を▲過
分離した無機酸水溶液は、溶解している臭素を水と共沸
除去して臭素を回収した後その一部または全量を再使用
することも可能である。
The amount of the inorganic acid aqueous solution to be used is 0.00% relative to the amount of crystal formation.
The amount is 5 to 10 times by weight, preferably 1 to 5 times by weight. If the acid concentration of the inorganic acid aqueous solution is less than 3%, the purification effect will be low;
The above is not practical. Further, if the amount of the inorganic acid aqueous solution used is less than 0.5 times the amount of crystals, stirring after the crystals have precipitated will be difficult, and if the amount is more than 10 times the amount, it is not practical. The inorganic acid aqueous solution from which the crystals have been over-separated can be azeotropically removed with water to recover the bromine, and then part or all of the bromine can be reused.

本発明による精製処理を行なつて得られるデカプロムジ
フエニルエーテルまたはこれを主成分とするブロム化ジ
フエニルエーテルは、無色の結晶であり、有機溶媒によ
る再結晶によつて得た結晶に比べ着色品質共に何ら遜色
は認められなかつた。以下に例をあげて説明する。実施
例 1 フラスコに臭素480fおよび塩化アルミニウム1yを
仕込み、温度50〜55℃で攪拌しながらジフエニルエ
ーテル17tを約2時間かけて滴下し、その温度で更に
2時間熟成を行なつた。
Decaprom diphenyl ether obtained by the purification process according to the present invention or brominated diphenyl ether containing it as a main component is a colorless crystal, which is more colored than the crystal obtained by recrystallization with an organic solvent. No inferiority was observed in terms of quality. This will be explained below using an example. Example 1 A flask was charged with 480f of bromine and 1y of aluminum chloride, and 17t of diphenyl ether was added dropwise over about 2 hours while stirring at a temperature of 50 to 55°C, and ripening was further carried out at that temperature for 2 hours.

得られた反応液に10%塩酸水溶液200yを加え50
〜55℃で2時間攪拌を行い反応液と塩酸水溶液を十分
に接触させて洗浄した。その後加熱を徐々に強め、過剰
の臭素を蒸留除去した。生成した結晶を▲過、水洗、乾
燥し、白色の結晶95.5yを得た。融点298〜30
7℃、ブロム含量83.2%、なお結晶の容器壁への付
着は全く認められなかつた。比較例 1 実施例1において10%塩酸水溶液のかわりに水200
fを用いて実施例1と同様操作を行ない橙黄色の結晶9
5.7yを得た。
Add 200y of 10% hydrochloric acid aqueous solution to the obtained reaction solution and mix for 50 minutes.
Stirring was carried out at ~55° C. for 2 hours, and the reaction solution was thoroughly brought into contact with an aqueous hydrochloric acid solution for washing. Heating was then gradually increased to distill off excess bromine. The produced crystals were filtered, washed with water, and dried to obtain 95.5y of white crystals. Melting point 298-30
The temperature was 7°C, the bromine content was 83.2%, and no crystals were observed to adhere to the container wall. Comparative Example 1 In Example 1, 200% water was used instead of the 10% aqueous hydrochloric acid solution.
Orange-yellow crystal 9 was obtained by carrying out the same operation as in Example 1 using f.
Obtained 5.7y.

融点272〜302℃、ブロム含量84.1%、なお得
られた結晶のうち38.27が反応器壁にかたく付着し
ていた。比較例 2 実施例1において反応液に20%塩酸水溶液2007を
加えた後直ちに加熱を強め臭素を蒸留除去し、その後温
度80℃で更に3時間攪拌を続けた。
The melting point was 272 DEG -302 DEG C., the bromine content was 84.1%, and 38.27 of the obtained crystals were firmly attached to the reactor wall. Comparative Example 2 In Example 1, after adding 20% aqueous hydrochloric acid solution 2007 to the reaction solution, heating was immediately increased to distill off bromine, and stirring was continued for an additional 3 hours at a temperature of 80°C.

▲過水洗、乾燥して微黄色の結晶95.3fを得た。融
点296〜305℃、ブロム含量 ※※83.0%、な
お得られた結晶のうち16.17が反応器壁にかたく付
着していた。実施例 2〜8 実施例1に記載の方法で臭素化反応及び熟成を行なつて
得られた反応液に表−1に記載した種類、濃度及び液量
の無機酸水溶液を加え、表−1に記載した温度及び時間
の条件下に実施例1に準じて洗浄処理を行ない、次いで
実施例1と同様な方法で臭素の蒸留除去及び後処理を行
ない、O表−1の結果を得た。
▲Washing with water and drying gave slightly yellow crystals 95.3f. The melting point was 296-305°C, the bromine content was 83.0%, and 16.17 of the obtained crystals were firmly attached to the reactor wall. Examples 2 to 8 An inorganic acid aqueous solution having the type, concentration and liquid amount listed in Table-1 was added to the reaction solution obtained by carrying out the bromination reaction and aging according to the method described in Example 1. A washing treatment was carried out according to Example 1 under the temperature and time conditions described in Example 1, and then bromine was distilled off and post-treated in the same manner as in Example 1, and the results shown in Table O-1 were obtained.

Claims (1)

【特許請求の範囲】[Claims] 1 臭素中で触媒の存在下にジフェニルエーテルを臭素
化してデカブロムジフェニルエーテルまたはこれを主成
分とするブロム化ジフェニルエーテルを製造するに際し
て、反応生成物を含有する臭素溶液に無機酸水溶液を加
え、30℃〜臭素の沸点の温度で、臭素の全還流下に少
なくとも0.5時間以上攪拌し、ついで臭素を蒸留除去
しながら無機酸水溶液で処理することを特徴とするブロ
ム化ジフェニルエーテルの精製法。
1. When producing decabrominated diphenyl ether or brominated diphenyl ether containing this as the main component by brominating diphenyl ether in the presence of a catalyst in bromine, an aqueous inorganic acid solution is added to the bromine solution containing the reaction product, and the mixture is heated at 30°C to A method for purifying brominated diphenyl ether, which comprises stirring at a temperature of the boiling point of bromine for at least 0.5 hours under total reflux of bromine, and then treating with an aqueous inorganic acid solution while removing bromine by distillation.
JP9543876A 1976-08-12 1976-08-12 Purification method of prominated diphenyl ether Expired JPS5929174B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9543876A JPS5929174B2 (en) 1976-08-12 1976-08-12 Purification method of prominated diphenyl ether

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9543876A JPS5929174B2 (en) 1976-08-12 1976-08-12 Purification method of prominated diphenyl ether

Publications (2)

Publication Number Publication Date
JPS5321129A JPS5321129A (en) 1978-02-27
JPS5929174B2 true JPS5929174B2 (en) 1984-07-18

Family

ID=14137693

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9543876A Expired JPS5929174B2 (en) 1976-08-12 1976-08-12 Purification method of prominated diphenyl ether

Country Status (1)

Country Link
JP (1) JPS5929174B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57200322A (en) * 1981-05-27 1982-12-08 Great Lakes Chemical Corp Perbromination of phenol and diphenyl ether carrying out under rising temperature as reactive medium of bromine
JPS6097351U (en) * 1983-12-09 1985-07-03 アイシン精機株式会社 Swirler for Stirling engine

Also Published As

Publication number Publication date
JPS5321129A (en) 1978-02-27

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