JPH03218330A - Production of hexabromocyclododecane - Google Patents
Production of hexabromocyclododecaneInfo
- Publication number
- JPH03218330A JPH03218330A JP28845290A JP28845290A JPH03218330A JP H03218330 A JPH03218330 A JP H03218330A JP 28845290 A JP28845290 A JP 28845290A JP 28845290 A JP28845290 A JP 28845290A JP H03218330 A JPH03218330 A JP H03218330A
- Authority
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- Japan
- Prior art keywords
- bromine
- reaction
- cdt
- hbcd
- trans
- Prior art date
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、耐熱性に優れた1,2,5,6.910−ヘ
キサブロモシクロドデカンの製造方法に関する。1,2
,5,6,9.10−ヘキサブロモシクロドデカンは、
高分子化合物の難燃剤として有用な化合物である。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for producing 1,2,5,6.910-hexabromocyclododecane, which has excellent heat resistance. 1,2
,5,6,9.10-hexabromocyclododecane is
It is a compound useful as a flame retardant for polymeric compounds.
(従来の技術)
1,2,5,6,9.10−ヘキサブロモシクロドデカ
ン(以下HBCDと略記する)は通常よく知られた難燃
剤であり、ポリスチレン樹脂等に使用されている。この
難燃剤は、1,5.9−シス,トランス、トランス−シ
クロドデカトリエン(以下CDTと略記する)に臭素を
付加させる反応によって合成される。(Prior Art) 1,2,5,6,9.10-hexabromocyclododecane (hereinafter abbreviated as HBCD) is a commonly known flame retardant and is used in polystyrene resins and the like. This flame retardant is synthesized by a reaction in which bromine is added to 1,5.9-cis, trans, trans-cyclododecatriene (hereinafter abbreviated as CDT).
ドイツ特許第1147574号明細書には、エチルアル
コールを反応溶媒としてCDTのエチルアルコール溶液
へ臭素を滴下して、臭素付加反応を行うことが記載され
ている。German Patent No. 1147574 describes that a bromine addition reaction is carried out by dropping bromine into an ethyl alcohol solution of CDT using ethyl alcohol as a reaction solvent.
また同様の反応方法でいくつかの混合溶媒系が提案され
ている。例えば特公昭49−24474号ではアルコー
ルとベンゼンの混合溶媒系、特公昭49−24475号
ではアルコールとエステルの混合溶媒系、USP383
3675ではt−ブチルアルコールとベンゼンの混合溶
媒系、特公昭50−5187号ではアルコールとハロゲ
ン系炭化水素の混合溶媒系、EP181414号ではア
ルコールとジオキサンの混合溶媒系がそれぞれ提案され
ている。Several mixed solvent systems have also been proposed using similar reaction methods. For example, in Japanese Patent Publication No. 49-24474, a mixed solvent system of alcohol and benzene is used, and in Japanese Patent Publication No. 49-24475, a mixed solvent system of alcohol and ester is used, USP383
No. 3675 proposes a mixed solvent system of t-butyl alcohol and benzene, Japanese Patent Publication No. 50-5187 proposes a mixed solvent system of alcohol and a halogenated hydrocarbon, and EP 181414 proposes a mixed solvent system of alcohol and dioxane.
この他に、特公昭53−12510号には、反応器に溶
媒を仕込んでおき、CDTと臭素を同時に滴下して反応
する方法が示されている。In addition, Japanese Patent Publication No. Sho 53-12510 discloses a method in which a solvent is charged in a reactor and CDT and bromine are simultaneously added dropwise to react.
(発明が解決しようとする課題)
CDTの臭素付加反応によって生成するHBCDには、
物理的性質の違う三種類の異性体が存在することが知ら
れている(E.R.Larsenand E.L.E
cker, J.FireSc i.,4,261
(1986)).すなわち高速液体クロマトグラフィ
ーでODS逆相カラムを用いて分析すると、カラムから
溶出する順番にa−HBCD,73−HBCD,7−H
BCDと命名された異性体が存在することが述べられて
いる。(Problem to be solved by the invention) HBCD produced by the bromine addition reaction of CDT includes:
It is known that there are three types of isomers with different physical properties (E.R. Larsenand and E.L.E.
Kerr, J. FireSc i. ,4,261
(1986)). That is, when analyzed using an ODS reverse phase column in high performance liquid chromatography, a-HBCD, 73-HBCD, and 7-H are eluted from the column in the order of
It has been stated that an isomer named BCD exists.
本発明者らが、各異性体を単離し、物性値を測3
定した結果では、α一,β−,γ一体のそれぞれの融点
は184〜186゜C,168〜1716C,196〜
198℃である。また熱重量分析(空気中、昇温速度1
0℃/min)では、5%加熱重量減温度はそれぞれ2
42°0.217℃,245℃で、50%加熱重量減温
度はそれぞれ255℃.232℃,258℃である。従
ってγ−HBCD,α−HBCD, β−HBCDの
順に熱安定性は高い。The present inventors isolated each isomer and measured their physical properties. According to the results, the respective melting points of α-, β-, and γ were 184-186°C, 168-1716°C, and 196-1716°C.
The temperature is 198°C. In addition, thermogravimetric analysis (in air, heating rate 1
0°C/min), the 5% heating weight loss temperature is 2
42°0.217°C and 245°C, the 50% weight loss temperature was 255°C, respectively. 232°C and 258°C. Therefore, the thermal stability is higher in the order of γ-HBCD, α-HBCD, and β-HBCD.
難燃剤として用いられるHBCDはγ一体が主体のもの
であるが、これらの異性体の存在比の違いにより、HB
CDの品質が大きく左右される。HBCD used as a flame retardant is mainly composed of gamma monomer, but due to the difference in the abundance ratio of these isomers, HBCD
The quality of the CD is greatly affected.
例えば、融点が低く、熱安定性が低いβ一HBCDの存
在比が高くなると、HBCDの融点は低くなり、高分子
の成型加工時にはHBCDの熱分解が低温で起こり始め
るために、成型加工機の腐蝕が起こったり、樹脂が着色
を起こす等の問題があった。For example, if the abundance ratio of β-HBCD, which has a low melting point and low thermal stability, increases, the melting point of HBCD will decrease, and during polymer molding, thermal decomposition of HBCD will begin to occur at low temperatures, so the molding machine will There were problems such as corrosion and discoloration of the resin.
また、ドイツ特許1147574号明細書に記載されて
いる方法では、反応途中で溶媒に不溶の4
樹脂状物が析出するため、攪拌が困難になり、スケール
アップが困難であった。さらにこのとき生成するHBC
Dは融点が低いため、耐熱性が劣るといった欠点があっ
た。Furthermore, in the method described in German Patent No. 1,147,574, a resin-like substance insoluble in the solvent precipitates during the reaction, making stirring difficult and making scale-up difficult. Furthermore, HBC generated at this time
Since D had a low melting point, it had the disadvantage of poor heat resistance.
これらの欠点を解決するために提案された前述の混合溶
媒系で反応を行うと、混合溶媒の溶解性の影響で反応途
中の樹脂状物の析出はなくなる。When the reaction is carried out using the above-mentioned mixed solvent system proposed to solve these drawbacks, precipitation of resinous substances during the reaction is eliminated due to the solubility of the mixed solvent.
しかし生成するHBCDの融点が低いため、やはり耐熱
性の点で問題が残っていた。However, since the melting point of the produced HBCD is low, there still remains a problem in terms of heat resistance.
また、特公昭53−12510号に記載の方法でも、生
成するHBCDの融点が低いため、やはり耐熱性の点で
問題が残っていた。Furthermore, even in the method described in Japanese Patent Publication No. 53-12510, there remained a problem in terms of heat resistance because the melting point of the produced HBCD was low.
更に、上述した従来の反応方法では、CDTの臭素化反
応の際、CDTの二重結合への臭素付加反応以外に、ア
リル位の臭素化、脱臭化水素、または溶媒の臭素化等の
ような副反応が起こり品く、収率が低下したり、不純物
がHBCDの結晶中に混入するなどの問題があった。こ
れらの不純物も、成型加工機の腐蝕や、樹脂の着色の原
因になっている。Furthermore, in the conventional reaction method described above, in the bromination reaction of CDT, in addition to the addition reaction of bromine to the double bond of CDT, bromination of the allylic position, dehydrobromination, or bromination of the solvent, etc. There were problems such as side reactions occurring, resulting in lower yields, and impurities being mixed into the HBCD crystals. These impurities also cause corrosion of molding machines and coloration of resin.
そこで、熱安定性の高いγ−HBCDの選択的な製造法
が求められていた。Therefore, a method for selectively producing γ-HBCD with high thermal stability has been desired.
(課題を解決するための手段)
本発明者らは、上記事情に鑑み、熱安定性が高いγ一H
BCDの高選択的な製造法について鋭意検討した結果、
有機溶媒の存在下、臭素を炭素数1〜4のアルコールま
たはそれを含有する有機溶媒に溶解させた中に、CDT
を滴下して反応させることで、従来一般的に行われてい
た、有機溶媒にCDTを溶解させた中に臭素を滴下して
反応させる方法や、反応容器に反応溶媒をあらかじめ仕
込んでおき、CDTと臭素を同時に反応器に滴下しなが
ら反応させていく反応方法に比べて、γ一HBCDの選
択率が著しく向上し、さらには臭素付加反応以外の副反
応で生じると考えられる同定出来ない不明物が極めて減
少することを見出だし、本発明に到達したのである。(Means for Solving the Problems) In view of the above circumstances, the present inventors have developed a method for γ-H which has high thermal stability.
As a result of intensive studies on highly selective manufacturing methods for BCD,
In the presence of an organic solvent, in which bromine is dissolved in an alcohol having 1 to 4 carbon atoms or an organic solvent containing it, CDT is added.
The conventional method of reacting by dropping bromine into a solution of CDT in an organic solvent, or the method of reacting by adding bromine dropwise to a reaction vessel in advance, or Compared to a reaction method in which bromine and bromine are simultaneously added dropwise into the reactor, the selectivity of γ-HBCD is significantly improved, and furthermore, unidentified unknown substances that are thought to be produced by side reactions other than the bromine addition reaction are eliminated. The present invention was achieved based on the discovery that the
すなわち本発明は、有機溶媒の存在下、臭素とCDTを
反応させ、HBCDを製造する方法において、臭素を炭
素数1〜4のアルコールまたはそれを含有する有機溶媒
に溶解させた中に、CDTを滴下して反応させることを
特徴とする、HBCDの製造方法に関する。That is, the present invention provides a method for producing HBCD by reacting bromine and CDT in the presence of an organic solvent, in which CDT is dissolved in an alcohol having 1 to 4 carbon atoms or an organic solvent containing it. The present invention relates to a method for producing HBCD, which is characterized in that it is reacted by dropping it.
以下、本発明を詳細に説明する。The present invention will be explained in detail below.
本発明の方法で用いられる溶媒は、炭素数1〜4のアル
コールまたはそれを含有する有機溶媒である。炭素数1
〜4のアルコールとしては、メタノール、エタノール、
n−プロパノール、インブロパノール、n−ブタノール
、see−ブタノール、インブタノール、tert−ブ
タノール、エチレングリコール、ジエチレングリコール
、プロピレングリコール等があげられる。これらの溶媒
の中ではエタノール、n−プロバノール、tert−ブ
タノールなどが特に好ましい。アルコールと混合する溶
媒としては、エーテル系の溶媒、ハロゲン系炭化水素溶
媒、エステル系の溶媒があげられる。それぞれの溶媒の
具体例としては、工一テル系の溶媒としてはジプロピル
エーテル、ジイソプ口ピルエーテル、テトラヒド口フラ
ン(THF)、ジオキサン、ジエチレングリコールジメ
チ7
ルエーテル、ジエチレングリコールジエチルエーテル等
が、ハロゲン系炭化水素溶媒としては、四塩化炭素、ク
ロロホルム、塩化メチレン、二塩化エチレン(EDC)
等が、エステル系の溶媒としては酢酸エチル、酢酸メチ
ル、2−メトキシエチルアセタート等があげられる。混
合溶媒としてはエタノールー酢酸エチル,エタノールー
THF,エタノールージオキサン,エタノールーEDC
,エタノールー塩化メチレン等が反応成績の面から特に
好ましいものである。The solvent used in the method of the present invention is an alcohol having 1 to 4 carbon atoms or an organic solvent containing it. Carbon number 1
~4 alcohols include methanol, ethanol,
Examples include n-propanol, imbropanol, n-butanol, see-butanol, inbutanol, tert-butanol, ethylene glycol, diethylene glycol, propylene glycol, and the like. Among these solvents, ethanol, n-probanol, tert-butanol and the like are particularly preferred. Examples of solvents that can be mixed with alcohol include ether solvents, halogenated hydrocarbon solvents, and ester solvents. Specific examples of each solvent include dipropyl ether, diisopropyl ether, tetrahydrofuran (THF), dioxane, diethylene glycol dimethyl ether, diethylene glycol diethyl ether, and halogen-based hydrocarbons. As a solvent, carbon tetrachloride, chloroform, methylene chloride, ethylene dichloride (EDC)
Examples of ester solvents include ethyl acetate, methyl acetate, and 2-methoxyethyl acetate. Mixed solvents include ethanol-ethyl acetate, ethanol-THF, ethanol-dioxane, and ethanol-EDC.
, ethanol-methylene chloride, etc. are particularly preferred from the viewpoint of reaction results.
本発明の方法を実施するにあたっての反応温度は格別の
限定はないが、高温で反応をおこなうと、臭素付加反応
以外の置換反応が起こりやすくなるため不純物が増加し
たり、反応溶媒と臭素の反応が起こりやすくなる為あま
り好ましくない。また極端な低温で反応を行った場合に
は、溶媒の変性はおさえられるが、反応速度がおそくな
るため反応が完結せず、反応中間体で止まるため好まし
くない。反応温度は通常約−20℃〜約50℃の範囲で
ある。There are no particular limitations on the reaction temperature when carrying out the method of the present invention, but if the reaction is carried out at a high temperature, substitution reactions other than bromine addition reaction will likely occur, resulting in an increase in impurities or a reaction between the reaction solvent and bromine. This is not very desirable as it can easily occur. Furthermore, when the reaction is carried out at an extremely low temperature, denaturation of the solvent can be suppressed, but the reaction rate is slow and the reaction is not completed and remains as a reaction intermediate, which is not preferable. The reaction temperature usually ranges from about -20°C to about 50°C.
8
本発明を実施するにあたっての反応時間は反応温度や仕
込み量等により変わりうるが、CDTの滴下時間は通常
約10分ないし10時間程度、さらにCDTの滴下が終
了してから約3時間程度反応させることでなしとげられ
る。8 The reaction time in carrying out the present invention may vary depending on the reaction temperature, amount of preparation, etc., but the dropwise addition time of CDT is usually about 10 minutes to 10 hours, and the reaction time is about 3 hours after the completion of dropping CDT. It can be achieved by letting it happen.
CDTに対する臭素の使用量は、B r 2 / C
DT(モル比)で3.0以上、好ましくは3.0〜10
.0である。3.0未満では、CDTに対して臭素が不
足しているため、反応が完結しない。The amount of bromine used for CDT is B r 2 / C
DT (molar ratio) is 3.0 or more, preferably 3.0 to 10
.. It is 0. If it is less than 3.0, the reaction will not be completed due to the lack of bromine relative to CDT.
10.0を越える場合では、過剰臭素による副反応が起
こりやすくなるため、好ましくない。If it exceeds 10.0, side reactions due to excess bromine tend to occur, which is not preferable.
反応溶媒に対するCDTの濃度は格別の限定はないが、
通常0.1〜4 0 w t / v o l%程度で
ある。0.1wt/vol%より基質濃度が低いときは
、経済的な見地から考えにくく、また40w t /
v o 1%以上では副反応が起こりやすくなる。There is no particular limitation on the concentration of CDT in the reaction solvent, but
It is usually about 0.1 to 40 wt/vol%. When the substrate concentration is lower than 0.1wt/vol%, it is difficult to consider from an economical point of view, and 40wt/vol%
If v o is 1% or more, side reactions are likely to occur.
反応終了後生成したHBCDは公知の手段で分体として
単離できる。例えば、析出した結晶を濾過することで、
HBCDの結晶を得ることができる。さらに濾液として
回収された溶媒は、これに新しい溶媒を補充することで
繰返し反応溶媒として使用することができる。また、反
応終了時の反応液を貧溶媒に投入することで結晶を取り
上げてもよい。After completion of the reaction, the produced HBCD can be isolated as a fraction by known means. For example, by filtering the precipitated crystals,
Crystals of HBCD can be obtained. Furthermore, the solvent recovered as a filtrate can be repeatedly used as a reaction solvent by replenishing it with fresh solvent. Alternatively, the crystals may be taken up by pouring the reaction solution at the end of the reaction into a poor solvent.
(発明の効果)
本発明の方法を実施することにより、HBCDのγ一体
を高選択率,高収率で製造出来る様になった。また、通
常の、臭素を添加する反応方法に比べて、CDT由来の
不純物の生成が著しく減少する様になった。従って、色
相、熱安定性に優れたHBCDを選択的に製造できるよ
うになった。(Effects of the Invention) By carrying out the method of the present invention, it has become possible to produce γ-integrated HBCD with high selectivity and high yield. Furthermore, compared to the usual reaction method in which bromine is added, the production of impurities derived from CDT was significantly reduced. Therefore, it has become possible to selectively produce HBCD with excellent hue and thermal stability.
(実施例)
以下実施例に従って本発明を更に詳しく説明するが、本
発明はこれらにより限定されるものではない。(Examples) The present invention will be explained in more detail below according to Examples, but the present invention is not limited thereto.
実施例1〜9
還流冷却器、攪拌羽根を装備した丸底フラスコに、表1
及び2に示す組成の反応溶媒と臭素を仕込んだ。その中
に、表1及び2に示す量のCDTを30℃で2時間かけ
て滴下することで反応させた。CDTの仕込みの終了後
、さらに30℃で2時間熟成した。 反応終了後の反応
液を高速液体クロマトグラフィ−(カラム: TSKゲ
ルーODS−80T,東ソー側製、溶離液:アセトニト
リル/水−8 0 / 2 0 v o 1 %、検出
器:UV215nm)で解析し、その結果をまとめて表
1及び2に示した。なお同定出来ない成分については、
不明分とした。表中のDBCD (ジブロモシク口ドデ
カジエン)およびTBCD (テトラブ口モシク口ドデ
カエン)は、HBCD製造時の反応中間体である。なお
TBCDについては、異性体が存在するので、高速液体
クロマトグラフィーでODS逆相カラムを用いて分析し
、カラムから溶出する順番にα−TBCD,β一TBC
Dと命名した。Examples 1 to 9 Table 1 was added to a round bottom flask equipped with a reflux condenser and a stirring blade.
A reaction solvent having the composition shown in 2 and bromine were charged. The amount of CDT shown in Tables 1 and 2 was added dropwise into the mixture at 30° C. over 2 hours to cause a reaction. After the addition of CDT, the mixture was further aged at 30° C. for 2 hours. After the completion of the reaction, the reaction solution was analyzed by high performance liquid chromatography (column: TSK gel-ODS-80T, manufactured by Tosoh, eluent: acetonitrile/water-80/20 vol. 1%, detector: UV 215 nm), The results are summarized in Tables 1 and 2. For components that cannot be identified,
It was marked as unknown. DBCD (dibromosic dodecadiene) and TBCD (tetrabu-dodecadiene) in the table are reaction intermediates during the production of HBCD. Regarding TBCD, since isomers exist, it was analyzed using an ODS reverse phase column in high performance liquid chromatography, and α-TBCD, β-TBCD were eluted from the column in the order of
It was named D.
HBCDの収率および収量は、HBCDの異性体を合計
したもので計算した。またγ一HBCDの選択率は、γ
一HBCDの生成量をHBCD異性体の合計量で割った
値で示した(γ一HBCD11
/ (α
HBCD+β−HBCD+γ一HBCD))。The yield and yield of HBCD were calculated by summing the isomers of HBCD. In addition, the selectivity of γ-HBCD is γ
The amount of HBCD produced was divided by the total amount of HBCD isomers (γ-HBCD11/(αHBCD+β-HBCD+γ-HBCD)).
反応終了時の反応液を濾過し、得られた結晶を乾燥させ
融点を測定し、その結果をまとめて表1及び2に示した
。At the end of the reaction, the reaction solution was filtered, the obtained crystals were dried, and the melting point was measured. The results are summarized in Tables 1 and 2.
比較例1〜3
還流冷却器、攪拌羽根を装備した丸底フラスコに、表3
に示す組成の反応溶媒とCDTを仕込んだ。その中に表
3に示す量の臭素を30℃で2時間かけて滴下させるこ
とで反応した。臭素の仕込みの終了後、さらに30℃で
2時間熟成した。反応終了後、実施例と同様な方法で後
処理と分析を行い、その結果をまとめて表3に示した。Comparative Examples 1 to 3 Table 3 was added to a round bottom flask equipped with a reflux condenser and a stirring blade.
A reaction solvent having the composition shown below and CDT were charged. The amount of bromine shown in Table 3 was added dropwise into the solution at 30° C. over 2 hours to cause a reaction. After the addition of bromine, the mixture was further aged at 30° C. for 2 hours. After the reaction was completed, post-treatment and analysis were performed in the same manner as in Examples, and the results are summarized in Table 3.
比較例4
還流冷却器、攪拌羽根を装備した丸底フラスコに、表3
に示す組成の反応溶媒を仕込んだ。その中に表3に示す
量の臭素とCDTを30℃で2時間かけて同時に滴下さ
せることで反応した。臭素1 2
とCDTの仕込みの終了後、さらに30℃で2時間熟成
した。反応終了後、実施例と同様な方法で後処理と分析
を行い、その結果をまとめて表3に示した。Comparative Example 4 Table 3 was added to a round bottom flask equipped with a reflux condenser and a stirring blade.
A reaction solvent having the composition shown in was charged. Bromine and CDT in the amounts shown in Table 3 were simultaneously dropped into the solution at 30° C. over 2 hours to cause a reaction. After the addition of bromine 1 2 and CDT, the mixture was further aged at 30° C. for 2 hours. After the reaction was completed, post-treatment and analysis were performed in the same manner as in Examples, and the results are summarized in Table 3.
Claims (1)
、トランス−シクロドデカトリエンを反応させ、1,2
,5,6,9,10−ヘキサブロモシクロドデカンを製
造する方法において、臭素を炭素数1〜4のアルコール
またはそれを含有する有機溶媒に溶解させた中に、1,
5,9−シス、トランス、トランス−シクロドデカトリ
エンを滴下して反応させることを特徴とする、1,2,
5,6,9,10−ヘキサブロモシクロドデカンの製造
方法。In the presence of an organic solvent, bromine and 1,5,9-cis, trans, trans-cyclododecatriene are reacted to form 1,2
, 5,6,9,10-hexabromocyclododecane, in which bromine is dissolved in an alcohol having 1 to 4 carbon atoms or an organic solvent containing it, 1,
1,2, characterized by reacting by dropping 5,9-cis, trans, trans-cyclododecatriene;
A method for producing 5,6,9,10-hexabromocyclododecane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP19900122178 EP0429059A3 (en) | 1989-11-21 | 1990-11-20 | Process for producing hexabromocyclododecane |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP30081889 | 1989-11-21 | ||
| JP1-300818 | 1989-11-21 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03218330A true JPH03218330A (en) | 1991-09-25 |
| JP2844899B2 JP2844899B2 (en) | 1999-01-13 |
Family
ID=17889477
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP28845290A Expired - Lifetime JP2844899B2 (en) | 1989-11-21 | 1990-10-29 | Method for producing hexabromocyclododecane |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2844899B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100407857B1 (en) * | 2000-12-22 | 2003-12-01 | 주식회사 상화 | Preparation Method Of Hexabromocyclododecane |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101012482B1 (en) * | 2008-09-26 | 2011-02-08 | 김평재 | Method for preparing hexabromocyclododecane |
-
1990
- 1990-10-29 JP JP28845290A patent/JP2844899B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100407857B1 (en) * | 2000-12-22 | 2003-12-01 | 주식회사 상화 | Preparation Method Of Hexabromocyclododecane |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2844899B2 (en) | 1999-01-13 |
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