JP2001354642A - Method for producing bis(3,5-dibromo-4- dibromopropoxyphenyl) sulfone granule - Google Patents

Method for producing bis(3,5-dibromo-4- dibromopropoxyphenyl) sulfone granule

Info

Publication number
JP2001354642A
JP2001354642A JP2000171425A JP2000171425A JP2001354642A JP 2001354642 A JP2001354642 A JP 2001354642A JP 2000171425 A JP2000171425 A JP 2000171425A JP 2000171425 A JP2000171425 A JP 2000171425A JP 2001354642 A JP2001354642 A JP 2001354642A
Authority
JP
Japan
Prior art keywords
tbs
sulfone
dibromo
dibromopropoxyphenyl
bis
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
JP2000171425A
Other languages
Japanese (ja)
Inventor
Kiyohide Murata
清秀 村田
Kazuhiro Mitome
一浩 三留
Kazuaki Noike
一秋 野池
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.)
Sanko Kagaku Kogyo KK
Sanko Chemical Industry Co Ltd
Original Assignee
Sanko Kagaku Kogyo KK
Sanko Chemical Industry 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 Sanko Kagaku Kogyo KK, Sanko Chemical Industry Co Ltd filed Critical Sanko Kagaku Kogyo KK
Priority to JP2000171425A priority Critical patent/JP2001354642A/en
Publication of JP2001354642A publication Critical patent/JP2001354642A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a method for industrially advantageously producing a granule of bis(3,5-dibromo-4-dibromopropoxyphenyl)sulfone excellent in handleability. SOLUTION: In this method for producing bis(3,5-dibromo-4- dibromopropoxyphenyl)sulfone as a granule produced by a bromination reaction of a bis(4-allyloxy-3,5-dibromophenyl)sulfone, the method is characterized in that a solution of bis(3,5-dibromo-4-dibromopropoxyphenyl)sulfone obtained by the production process is dripped into a heated poor solvent and simultaneously cold water is added to bis(3,5-dibromo-4-dibromopropoxyphenyl)sulfone dispersed into the poor solvent while distilling away the solvent to give the granule of bis(3,5-dibromo-4-dibromopropoxyphenyl)sulfone.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、ビス(3,5−ジ
ブロモ−4−ジブロモプロポキシフェニル)スルホン
(以下、TBS−BPと略記する)を、その製造工程か
ら得られた溶液を原料とし、これから顆粒として製造す
る方法に関するものである。TBS−BPは、ポリオレ
フィン樹脂等、特にポリプロピレン等の難燃剤として極
めて有用である(特公昭50−23693号、特公昭5
0−35103号等)。
TECHNICAL FIELD The present invention relates to a method for producing bis (3,5-dibromo-4-dibromopropoxyphenyl) sulfone (hereinafter abbreviated as TBS-BP) using a solution obtained from the production process as a raw material, The present invention relates to a method for producing granules. TBS-BP is extremely useful as a flame retardant for polyolefin resins and the like, particularly polypropylene and the like (Japanese Patent Publication No. 50-23693, Japanese Patent Publication No. Sho 5).
No. 0-35103).

【0002】[0002]

【従来の技術】通常、TBS−BPを製造する方法とし
ては、その前駆物質であるビス(4−アリルオキシ−
3,5−ジブロモフェニル)スルホン(以下、TBS−
BAと略記する)と臭素とを特定の溶媒中で反応させて
得られるTBS−BPの溶液を、貧溶媒中に添加し、T
BS−BPを析出させる方法が一般的に行われている。
しかし、これにより得られたTBS−BPの粉体は、粒
子が細かく取扱性に劣り、また高温、加重条件下で塊化
が起こりやすく、長期保存時ブロッキング等の現象が発
生しやすい。
2. Description of the Related Art Generally, as a method for producing TBS-BP, bis (4-allyloxy-
3,5-dibromophenyl) sulfone (hereinafter referred to as TBS-
BA) and a solution of TBS-BP obtained by reacting bromine with a specific solvent are added to a poor solvent, and T
A method of precipitating BS-BP is generally performed.
However, the TBS-BP powder thus obtained has fine particles and is inferior in handleability, and tends to agglomerate under high-temperature and weighted conditions, and tends to cause phenomena such as blocking during long-term storage.

【0003】一方、TBS−BPの顆粒を得る方法とし
ては、TBS−BPの粉体を貧溶媒と50℃以上で混合
し、顆粒化する事が知られている(特開平11−158
104号公報)。しかしながら、この方法は、一度粉体
を取り出し顆粒化するため、操作が煩雑なものであり、
工業的方法としては未だ十分に満足出来るものではなか
った。
On the other hand, as a method for obtaining granules of TBS-BP, it is known that TBS-BP powder is mixed with a poor solvent at 50 ° C. or higher and granulated (JP-A-11-158).
No. 104). However, in this method, once the powder is taken out and granulated, the operation is complicated,
It was not yet satisfactory as an industrial method.

【0004】[0004]

【発明が解決しようとする課題】本発明は、このように
製造上煩雑で工業的にも問題のあったTBS−BPの顆
粒を得る方法において、取扱性の優れたTBS−BPの
顆粒を得るために、経済的かつ従来のプロセスを簡略化
した工業的方法を提供することをその課題とする。
DISCLOSURE OF THE INVENTION The present invention provides a method for obtaining granules of TBS-BP which is complicated in production and industrially problematic in such a manner to obtain granules of TBS-BP having excellent handleability. It is therefore an object of the present invention to provide an industrial method that is economical and simplifies conventional processes.

【0005】[0005]

【課題を解決するための手段】本発明者らは、前記課題
を解決すべく、貧溶媒中にTBS−BPの溶液を滴下
し、同時に脱溶媒を行いながらTBS−BPを貧溶媒中
に分散させる方法について、鋭意検討を行ったところ、
これまでは、大量の種結晶の存在下でなければ顆粒を生
成することが出来なかったが、TBS−BPの疎水性が
極めて高いために、種結晶が存在しなくてもTBS−B
Pを貧溶媒中に分散させた後、冷水を加え急激に冷却す
ることで、TBS−BPを顆粒として得ることができ、
しかも操作性が極めて良いことを見いだして、本発明を
完成するに至った。即ち、本発明によれば、ビス(4−
アリルオキシ−3,5−ジブロモフェニル)スルホンの
臭素化反応で製造したビス(3,5−ジブロモ−4−ジ
ブロモプロポキシフェニル)スルホンを顆粒として得る
方法において、該製造工程で得られたビス(3,5−ジ
ブロモ−4−ジブロモプロポキシフェニル)スルホンの
溶液を、加熱された貧溶媒中に滴下し、同時に溶媒を留
去しながら貧溶媒中に分散されたビス(3,5−ジブロ
モ−4−ジブロモプロポキシフェニル)スルホンに、冷
水を加えることによりビス(3,5−ジブロモ−4−ジ
ブロモプロポキシフェニル)スルホンの顆粒を得ること
を特徴とする前記方法が提供される。
Means for Solving the Problems In order to solve the above-mentioned problems, the present inventors dropped a solution of TBS-BP in a poor solvent and dispersed TBS-BP in the poor solvent while simultaneously removing the solvent. After careful study on how to make it work,
Until now, granules could not be produced without the presence of a large amount of seed crystals. However, since TBS-BP is extremely hydrophobic, TBS-B can be produced without the presence of seed crystals.
After dispersing P in a poor solvent, by adding cold water and rapidly cooling, TBS-BP can be obtained as granules,
Moreover, they found that the operability was extremely good, and completed the present invention. That is, according to the present invention, the screw (4-
In a method of obtaining bis (3,5-dibromo-4-dibromopropoxyphenyl) sulfone produced by the bromination reaction of allyloxy-3,5-dibromophenyl) sulfone as granules, the bis (3,5-dibromopropoxyphenyl) sulfone obtained in the production step is obtained. A solution of 5-dibromo-4-dibromopropoxyphenyl) sulfone was dropped into a heated poor solvent, and the bis (3,5-dibromo-4-dibromo) dispersed in the poor solvent was simultaneously distilled off. The above method is provided, wherein granules of bis (3,5-dibromo-4-dibromopropoxyphenyl) sulfone are obtained by adding cold water to (propoxyphenyl) sulfone.

【0006】[0006]

【発明の実施の形態】本発明による顆粒状のTBS−B
Pの製造は、製造工程で得られたTBS−BPの良溶媒
溶液を加熱された貧溶媒中に滴下し、同時に良溶媒を留
去した後、冷水を加え急冷することで達成される。本明
細書でいうTBS−BPの良溶媒とは、TBS−BPを
溶解しかつTBS−BAの臭素化反応において不活性な
溶媒を意味する。このような溶媒としては、例えば、四
塩化炭素、クロロホルム、塩化メチレン、ジクロロエタ
ン、トリクロロエタン、テトラクロロエタン等のハロゲ
ン化炭化水素が挙げられる。この良溶媒の沸点は、通
常、30〜150℃、好ましくは30〜90℃である。
TBS−BPの溶液を得る場合の溶媒量は特に制限ない
が、TBS−BPの1重量部当り、通常1〜5重量部、
好ましくは2.5〜3.5重量部である。TBS−BP
の貧溶媒は、20℃における溶解度が2%未満の溶媒で
ある。具体的には、水、メタノール、エタノール、n−
プロパノール、iso−プロパノール、n−ブタノー
ル、iso−ブタノール、sec−ブタノール、ter
t−ブタノール等が挙げられ、またこれら溶媒の混合物
でもよい。この貧溶媒の沸点は、通常、50〜170
℃、好ましくは50〜100℃である。また、この貧溶
媒は、前記良溶媒よりも、その沸点が高いものであるこ
と、通常、0〜100℃、好ましくは20〜60℃程度
高いものであることが必要である。TBS−BP溶液に
加える溶媒量は、TBS−BPの1重量部当り、通常1
〜5重量部、好ましくは2.0〜3.5重量部である。
DETAILED DESCRIPTION OF THE INVENTION Granular TBS-B according to the invention
The production of P is achieved by dropping a good solvent solution of TBS-BP obtained in the production process into a heated poor solvent, distilling off the good solvent at the same time, adding cold water and quenching. The good solvent for TBS-BP as used herein means a solvent that dissolves TBS-BP and is inactive in the bromination reaction of TBS-BA. Examples of such a solvent include halogenated hydrocarbons such as carbon tetrachloride, chloroform, methylene chloride, dichloroethane, trichloroethane, and tetrachloroethane. The boiling point of this good solvent is usually 30 to 150 ° C, preferably 30 to 90 ° C.
The amount of the solvent for obtaining the solution of TBS-BP is not particularly limited, but usually 1 to 5 parts by weight, per 1 part by weight of TBS-BP,
Preferably it is 2.5 to 3.5 parts by weight. TBS-BP
Is a solvent having a solubility at 20 ° C. of less than 2%. Specifically, water, methanol, ethanol, n-
Propanol, iso-propanol, n-butanol, iso-butanol, sec-butanol, ter
t-butanol and the like, and a mixture of these solvents may be used. The boiling point of this poor solvent is usually 50 to 170
° C, preferably 50 to 100 ° C. The poor solvent must have a boiling point higher than that of the good solvent, and usually need to be higher by about 0 to 100 ° C, preferably by about 20 to 60 ° C. The amount of the solvent to be added to the TBS-BP solution is usually 1 to 1 part by weight of the TBS-BP.
To 5 parts by weight, preferably 2.0 to 3.5 parts by weight.

【0007】本発明を好ましく実施するには、先ず、前
記良溶媒中でビス(4−アリルオキシ−3,5−ジブロ
モフェニル)スルホン(TBS−BA)を臭素化する。
この臭素化工程は、従来公知の方法に従って実施するこ
とができる。この場合、良溶媒の使用割合は特に制約さ
れないが、この反応で生成するTBS−BPの1重量部
当り、1〜5重量部、好ましくは2.5〜3.5重量部
となるような割合である。反応温度は、10〜50℃、
好ましくは20〜30℃である。
In order to carry out the present invention preferably, bis (4-allyloxy-3,5-dibromophenyl) sulfone (TBS-BA) is first brominated in the above-mentioned good solvent.
This bromination step can be performed according to a conventionally known method. In this case, the use ratio of the good solvent is not particularly limited, but is 1 to 5 parts by weight, preferably 2.5 to 3.5 parts by weight, per 1 part by weight of TBS-BP produced by this reaction. It is. The reaction temperature is 10 to 50 ° C,
Preferably it is 20-30 degreeC.

【0008】次に、本発明では、前記のようにして得ら
れたTBS−BPの良溶媒溶液を、加熱された貧溶媒中
に滴下し、その良溶媒を留去させる。この場合、その貧
溶媒の温度は、良溶媒の沸点以上の温度、好ましくは良
溶媒の沸点よりも、20〜60℃程度高い温度である。
TBS−BP良溶媒溶液を滴下する貧溶媒は、攪拌装置
で攪拌しているのが好ましい。貧溶媒中へのTBS−B
P良溶媒溶液の滴下速度は、TBS−BPの固結を防止
するため、良溶媒の留出速度以下、通常、良溶媒の留出
速度の0.2〜1.0倍、好ましくは0.5〜0.8倍
に保持するのがよい。
Next, in the present invention, the good solvent solution of TBS-BP obtained as described above is dropped into a heated poor solvent, and the good solvent is distilled off. In this case, the temperature of the poor solvent is a temperature higher than the boiling point of the good solvent, and preferably about 20 to 60 ° C. higher than the boiling point of the good solvent.
It is preferable that the poor solvent to which the TBS-BP good solvent solution is dropped is stirred by a stirrer. TBS-B in poor solvent
The rate of dropping of the P good solvent solution is equal to or less than the rate of distilling the good solvent, usually 0.2 to 1.0 times the rate of distilling the good solvent, preferably 0.1 to avoid solidification of TBS-BP. It is better to keep it at 5 to 0.8 times.

【0009】貧溶媒に対するTBS−BP良溶媒溶液の
滴下が終了した後、さらに良溶媒を留去するために、一
定時間攪拌を続ける。この場合、良溶媒の留去量は、全
良溶媒量の60%以上、好ましくは70〜95%程度で
ある。前記のようにして良溶媒を留去すると、貧溶媒中
にTBS−BPが、微粒子状で分散した懸濁液が得られ
る。本発明では、この懸濁液に対して冷水を加える。冷
水の添加量は、特に制限はないが、通常TBS−BPの
1重量部に対し、0.1〜5重量部、好ましくは0.5
〜2重量部である。冷水の温度は、20℃以下、好まし
くは10℃以下、より好ましくは5℃以下であり、本発
明では、特に氷水の使用が好ましい。冷水を加えると同
時にTBS−BPは顆粒化され、その顆粒をそのスラリ
ー液から遠心分離、吸引濾過等の慣用の固液分離法で分
離する。
After the dropping of the TBS-BP good solvent solution to the poor solvent is completed, stirring is continued for a certain time in order to further remove the good solvent. In this case, the amount of the good solvent distilled off is at least 60%, preferably about 70 to 95% of the total good solvent amount. When the good solvent is distilled off as described above, a suspension in which TBS-BP is dispersed in the form of fine particles in the poor solvent is obtained. In the present invention, cold water is added to this suspension. The amount of cold water is not particularly limited, but is usually 0.1 to 5 parts by weight, preferably 0.5 to 1 part by weight of TBS-BP.
~ 2 parts by weight. The temperature of the cold water is 20 ° C. or lower, preferably 10 ° C. or lower, more preferably 5 ° C. or lower. In the present invention, use of ice water is particularly preferable. TBS-BP is granulated simultaneously with the addition of cold water, and the granules are separated from the slurry liquid by a conventional solid-liquid separation method such as centrifugation and suction filtration.

【0010】前記のようにして、TBS−BPの製造工
程で得られた反応液から、TBS−BPの顆粒を定量的
に得ることができる。この顆粒の平均粒径は、300〜
500μm、特に400〜500μmである。顆粒の粒
径は、冷水の温度や冷水の添加量等により調節すること
ができる。
As described above, TBS-BP granules can be quantitatively obtained from the reaction solution obtained in the TBS-BP manufacturing process. The average particle size of the granules is 300 to
It is 500 μm, especially 400-500 μm. The particle size of the granules can be adjusted by the temperature of cold water, the amount of cold water added, and the like.

【0011】[0011]

【実施例】本発明を実施例によって更に具体的に説明す
るが、本発明はこの実施例によって限定されるものでは
ない。
EXAMPLES The present invention will be described more specifically with reference to examples, but the present invention is not limited to these examples.

【0012】実施例1 温度計、撹拌機、還流冷却器を取り付けたフラスコに、
TBS−BA182g(純度98.4%)及び塩化メチ
レン544gを仕込、溶解確認後、臭素91gを20〜
30℃で2時間かけて滴下し、滴下終了後30分間その
温度で熟成した。反応後、残存臭素を亜硫酸水素ナトリ
ウム水溶液で還元し、更に水酸化ナトリウム水溶液で洗
浄を行い、TBS−BPを含む塩化メチレン溶液790
gを得た。温度計、撹拌機、蒸留装置を取り付けたフラ
スコに、メタノール440gを仕込み、55℃に加熱し
た。このメタノール液を50〜55℃に調整しながら、
上記の塩化メチレン溶液を約2時間で滴下し同時に、塩
化メチレンを連続的に留去した。塩化メチレンを約55
0g留去した後、冷却しながら5℃の冷水160gを一
度に加え、25℃以下まで冷却した。冷却後、得られた
TBS−BPのスラリー液を濾過し、乾燥させて白色の
顆粒260gを得た。得られた顆粒について、液体クロ
マトグラフィーによる分析を行った結果、TBS−BP
の純度は97.5%、顆粒の平均粒径は401μmであ
った。
Example 1 In a flask equipped with a thermometer, a stirrer, and a reflux condenser,
After charging 182 g of TBS-BA (purity 98.4%) and 544 g of methylene chloride, and confirming dissolution, 91 g of bromine was added to 20 to 90 g of bromine.
The solution was added dropwise at 30 ° C. over 2 hours, and ripened at that temperature for 30 minutes after completion of the addition. After the reaction, the residual bromine is reduced with an aqueous solution of sodium hydrogen sulfite, and further washed with an aqueous solution of sodium hydroxide, and a methylene chloride solution 790 containing TBS-BP is added.
g was obtained. In a flask equipped with a thermometer, a stirrer, and a distillation apparatus, 440 g of methanol was charged and heated to 55 ° C. While adjusting the methanol liquid to 50 to 55 ° C,
The above methylene chloride solution was added dropwise over about 2 hours, and simultaneously, methylene chloride was continuously distilled off. About 55 methylene chloride
After distilling out 0 g, while cooling, 160 g of 5 ° C. cold water was added at once, and the mixture was cooled to 25 ° C. or less. After cooling, the obtained TBS-BP slurry was filtered and dried to obtain 260 g of white granules. The obtained granules were analyzed by liquid chromatography, and as a result, TBS-BP
Was 97.5% and the average particle size of the granules was 401 μm.

【0013】実施例2 ビス(4−ヒドロキシフェニル)スルホンを臭素化し、
その後アリルエーテル化して得られた粗TBS−BAを
反応原料として使用した。この粗TBS−BAの液体ク
ロマトグラフィーによる純度は87%であった。温度
計、撹拌機、還流冷却器を取り付けたフラスコに、前記
粗TBS−BA182g及び塩化メチレン544gを仕
込み、溶解確認後、臭素91gを20〜30℃で2時間
かけて滴下し、滴下終了後30分間その温度で熟成し
た。反応後、残存臭素を亜硫酸水素ナトリウム水溶液で
還元し、更に水酸化ナトリウム水溶液で洗浄を行い、T
BS−BPを含む塩化メチレン溶液770gを得た。温
度計、撹拌機、蒸留装置を取り付けたフラスコに、メタ
ノール440gを仕込み、55℃に加熱した。このメタ
ノール液を50〜55℃に調整しながら、上記の塩化メ
チレン溶液を約2時間で滴下し、同時に塩化メチレンを
連続的に留去した。塩化メチレンを約550g留去した
後、冷却しながら5℃の冷水160gを一度に加え、2
5℃以下まで冷却した。冷却後、得られたTBS−BP
のスラリー液を濾過し、乾燥させて白色の顆粒250g
を得た。得られた顆粒について、液体クロマトグラフィ
ーによる分析を行った結果、TBS−BPの純度は8
5.1%、顆粒の平均粒径は473μmであった。以上
の実施例結果により、種晶を使用することなく、TBS
−BPを効率よく顆粒化し得ることが確認された。
Example 2 Bis (4-hydroxyphenyl) sulfone is brominated,
Thereafter, crude TBS-BA obtained by allyl etherification was used as a reaction raw material. The purity of this crude TBS-BA by liquid chromatography was 87%. Into a flask equipped with a thermometer, stirrer, and reflux condenser, 182 g of the crude TBS-BA and 544 g of methylene chloride were charged, and after confirming dissolution, 91 g of bromine was added dropwise at 20 to 30 ° C. over 2 hours. Aged at that temperature for minutes. After the reaction, the remaining bromine is reduced with an aqueous sodium hydrogen sulfite solution, and further washed with an aqueous sodium hydroxide solution.
770 g of a methylene chloride solution containing BS-BP was obtained. In a flask equipped with a thermometer, a stirrer, and a distillation apparatus, 440 g of methanol was charged and heated to 55 ° C. While adjusting the methanol solution to 50 to 55 ° C., the above methylene chloride solution was dropped in about 2 hours, and simultaneously, methylene chloride was continuously distilled off. After distilling off about 550 g of methylene chloride, 160 g of cold water at 5 ° C. was added all at once while cooling, and
Cooled to below 5 ° C. After cooling, the obtained TBS-BP
Is filtered and dried to obtain 250 g of white granules.
I got The obtained granules were analyzed by liquid chromatography, and as a result, the purity of TBS-BP was 8
5.1%, the average particle size of the granules was 473 μm. According to the results of the above examples, TBS was used without using a seed crystal.
It was confirmed that -BP could be granulated efficiently.

【0014】比較例1 温度計、撹拌機、還流冷却器を取り付けたフラスコに、
実施例2と同様な方法で得られた粗TBS−BA182
g(純度87%)及び塩化メチレン544gを仕込み、
溶解確認後、臭素91gを20〜30℃で2時間かけて
滴下し、滴下終了後30分間その温度で熟成した。反応
後、残存臭素を亜硫酸水素ナトリウム水溶液で還元し、
更に水酸化ナトリウム水溶液で洗浄を行い、TBS−B
Pを含む塩化メチレン溶液790gを得た。温度計、撹
拌機、蒸留装置を取り付けたフラスコに、メタノール4
40g及び種結晶7gを仕込み、55℃に加熱した。こ
のメタノール液を50〜55℃に調整しながら、上記の
塩化メチレン溶液を約2時間で滴下し、塩化メチレンを
連続的に留去した。塩化メチレンを約550g留去した
後、25℃以下まで冷却した。冷却後、得られたTBS
−BPのスラリー液を濾過し、乾燥させて白色の顆粒2
40gを得た。得られた顆粒について、液体クロマトグ
ラフィーによる分析を行った結果、TBS−BPの純度
は85.5%、顆粒の平均粒径は295μmであった。
Comparative Example 1 In a flask equipped with a thermometer, a stirrer, and a reflux condenser,
Crude TBS-BA182 obtained in the same manner as in Example 2.
g (purity 87%) and 544 g of methylene chloride.
After confirming the dissolution, 91 g of bromine was added dropwise at 20 to 30 ° C over 2 hours, and the mixture was aged at that temperature for 30 minutes after completion of the addition. After the reaction, the remaining bromine is reduced with an aqueous sodium hydrogen sulfite solution,
After washing with sodium hydroxide aqueous solution, TBS-B
790 g of a methylene chloride solution containing P was obtained. In a flask equipped with a thermometer, stirrer, and distillation device, add methanol 4
40 g and 7 g of seed crystals were charged and heated to 55 ° C. While adjusting the methanol solution to 50 to 55 ° C., the above methylene chloride solution was dropped in about 2 hours, and methylene chloride was continuously distilled off. After distilling off about 550 g of methylene chloride, the mixture was cooled to 25 ° C. or lower. After cooling, the obtained TBS
The BP slurry is filtered and dried to give white granules 2
40 g were obtained. The obtained granules were analyzed by liquid chromatography. As a result, the purity of TBS-BP was 85.5%, and the average particle size of the granules was 295 μm.

【0015】比較例2 温度計、撹拌機、還流冷却器を取り付けたフラスコに、
実施例2と同様な方法で得られた粗TBS−BA182
g(純度87%)及び塩化メチレン544gを仕込み、
溶解確認後、臭素91gを20〜30℃で2時間かけて
滴下し、滴下終了後30分間その温度で熟成した。反応
後、残存臭素を亜硫酸水素ナトリウム水溶液で還元し、
更に水酸化ナトリウム水溶液で洗浄を行い、TBS−B
Pを含む塩化メチレン溶液790gを得た。温度計、撹
拌機、蒸留装置を取り付けたフラスコに、メタノール4
40gを仕込み、55℃に加熱した。このメタノール液
を50〜55℃に調整しながら、上記の塩化メチレン溶
液を約2時間で滴下し、塩化メチレンを連続的に留去し
た。塩化メチレンを約550g留去した後、25℃以下
まで冷却した。冷却後、得られたTBS−BPのスラリ
ー液を濾過し、乾燥させて白色の粉体235gを得た。
得られた粉体について、液体クロマトグラフィーによる
分析を行った結果、TBS−BPの純度は85.3%、
粉体の平均粒径は80μmであり、顆粒は得られなかっ
た。
Comparative Example 2 In a flask equipped with a thermometer, a stirrer, and a reflux condenser,
Crude TBS-BA182 obtained in the same manner as in Example 2.
g (purity 87%) and 544 g of methylene chloride.
After confirming the dissolution, 91 g of bromine was added dropwise at 20 to 30 ° C over 2 hours, and the mixture was aged at that temperature for 30 minutes after completion of the addition. After the reaction, the remaining bromine is reduced with an aqueous sodium hydrogen sulfite solution,
After washing with sodium hydroxide aqueous solution, TBS-B
790 g of a methylene chloride solution containing P was obtained. In a flask equipped with a thermometer, stirrer, and distillation device, add methanol 4
40 g was charged and heated to 55 ° C. While adjusting the methanol solution to 50 to 55 ° C., the above methylene chloride solution was dropped in about 2 hours, and methylene chloride was continuously distilled off. After distilling off about 550 g of methylene chloride, the mixture was cooled to 25 ° C. or lower. After cooling, the obtained TBS-BP slurry was filtered and dried to obtain 235 g of a white powder.
The obtained powder was analyzed by liquid chromatography. As a result, the purity of TBS-BP was 85.3%,
The average particle size of the powder was 80 μm, and no granules were obtained.

【0016】[0016]

【発明の効果】本発明の方法によれば、TBS−BAの
臭素化反応で製造したTBS−BPを、大量の種結晶を
必要とすることなく、また一度粉体にした後顆粒化する
こともなく、顆粒化させることができる。更には製造過
程で得られたTBS−BPの純度に関係なく反応生成物
を容易に取り出すことができるもので、経済的な工業的
製造方法として好適のものである。
According to the method of the present invention, TBS-BP produced by the bromination reaction of TBS-BA can be granulated after once forming a powder without requiring a large amount of seed crystals. No, it can be granulated. Furthermore, the reaction product can be easily taken out regardless of the purity of TBS-BP obtained in the production process, and is suitable as an economical industrial production method.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 野池 一秋 神奈川県高座郡寒川町一之宮7−10−1 三光化学工業株式会社内 Fターム(参考) 4H006 AA02 AD11 AD15 AD17 BB12 BB14 BB31 BC51 TA02 TB13 ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Kazuaki Noike 7-10-1 Ichinomiya, Samukawa-cho, Koza-gun, Kanagawa F term (reference) in Sanko Chemical Industry Co., Ltd. 4H006 AA02 AD11 AD15 AD17 BB12 BB14 BB31 BC51 TA02 TB13

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 ビス(4−アリルオキシ−3,5−ジブ
ロモフェニル)スルホンの臭素化反応で製造したビス
(3,5−ジブロモ−4−ジブロモプロポキシフェニ
ル)スルホンを顆粒体として得る方法において、該製造
工程で得られたビス(3,5−ジブロモ−4−ジブロモ
プロポキシフェニル)スルホンの溶液を、加熱された貧
溶媒中に滴下し、同時に溶媒を留去しながら貧溶媒中に
分散されたビス(3,5−ジブロモ−4−ジブロモプロ
ポキシフェニル)スルホンに、冷水を加えることにより
ビス(3,5−ジブロモ−4−ジブロモプロポキシフェ
ニル)スルホンの顆粒を得ることを特徴とする前記方
法。
1. A method for obtaining bis (3,5-dibromo-4-dibromopropoxyphenyl) sulfone produced by a bromination reaction of bis (4-allyloxy-3,5-dibromophenyl) sulfone as a granule. A solution of bis (3,5-dibromo-4-dibromopropoxyphenyl) sulfone obtained in the production process is dropped into a heated poor solvent, and the bis (3,5-dibromo-4-dibromopropoxyphenyl) sulfone is dispersed in the poor solvent while simultaneously distilling off the solvent. The above method, wherein bis (3,5-dibromo-4-dibromopropoxyphenyl) sulfone granules are obtained by adding cold water to (3,5-dibromo-4-dibromopropoxyphenyl) sulfone.
JP2000171425A 2000-06-08 2000-06-08 Method for producing bis(3,5-dibromo-4- dibromopropoxyphenyl) sulfone granule Pending JP2001354642A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000171425A JP2001354642A (en) 2000-06-08 2000-06-08 Method for producing bis(3,5-dibromo-4- dibromopropoxyphenyl) sulfone granule

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000171425A JP2001354642A (en) 2000-06-08 2000-06-08 Method for producing bis(3,5-dibromo-4- dibromopropoxyphenyl) sulfone granule

Publications (1)

Publication Number Publication Date
JP2001354642A true JP2001354642A (en) 2001-12-25

Family

ID=18673977

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000171425A Pending JP2001354642A (en) 2000-06-08 2000-06-08 Method for producing bis(3,5-dibromo-4- dibromopropoxyphenyl) sulfone granule

Country Status (1)

Country Link
JP (1) JP2001354642A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017100069A (en) * 2015-11-30 2017-06-08 トヨタ自動車株式会社 Method for producing particles

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017100069A (en) * 2015-11-30 2017-06-08 トヨタ自動車株式会社 Method for producing particles

Similar Documents

Publication Publication Date Title
JP2020520361A (en) Separation of 1,4-bis(4-phenoxybenzoyl)benzene-Lewis acid complex in aqueous solution
KR102219152B1 (en) Crystal polymorph of 2,2'-bis(2-hydroxyethoxy)-1,1'-binaphthalene and method for producing same
JPH1045655A (en) Production of fluorene derivative
JPS638926B2 (en)
KR100943872B1 (en) Method for producing trans-1,4-cyclohexane dicarboxylic acid
JPH10505084A (en) Method for producing tetrabromobisphenol-A by reducing formation of methyl bromide
JP2001354642A (en) Method for producing bis(3,5-dibromo-4- dibromopropoxyphenyl) sulfone granule
JPH0482142B2 (en)
JPH1045656A (en) Production of fluorene derivative
JP2001187760A (en) Method for purifying 1,1,1,5,5,5-hexafluoroacetylacetone
JP2890846B2 (en) Method for separating and recovering bis (3,5-dibromo-4-dibromopropoxyphenyl) propane
CN108863862B (en) Method for refining crude bisphenol S by using pseudocumene mixed solvent
JP3890642B2 (en) Continuous production method of alkali metal styrene sulfonate
JPH1045654A (en) Purification of fluorine derivative
JP2000053658A (en) Production of tris(dibromopropyl) isocyanurate
US5382725A (en) Process for the purification of 1,3-dihalobenzene from an isomeric mixture of dihalobenzenes
JPH0321011B2 (en)
JP2770512B2 (en) Method for purifying alkali metal salts of aminoethylsulfonic acid
KR100407856B1 (en) Preparation Method of Tetrabromocyclooctane
JPS63130557A (en) Recovering method of biphenyltetracarboxylic acid
JP2590206B2 (en) Method for producing 8-hydroxyquinoline-7-carboxylic acid
WO2001038286A1 (en) PROCESS FOR PRODUCING t-BUTYL ESTERS OF BRIDGED-RING POLYCARBOXYLIC ACIDS
JPH0632757A (en) Tetrabromobisphenol a having large particle diameter and its production
JPS609699B2 (en) Separation method of naphthoquinone and phthalic acid
CN108084011A (en) A kind of crystallization and purification method of 3,5- di-tert-butyl-4-hydroxybenzoic acids