JPS6116252B2 - - Google Patents
Info
- Publication number
- JPS6116252B2 JPS6116252B2 JP13632978A JP13632978A JPS6116252B2 JP S6116252 B2 JPS6116252 B2 JP S6116252B2 JP 13632978 A JP13632978 A JP 13632978A JP 13632978 A JP13632978 A JP 13632978A JP S6116252 B2 JPS6116252 B2 JP S6116252B2
- Authority
- JP
- Japan
- Prior art keywords
- reaction
- bromine
- solvent
- dibromobiphenyl
- biphenyl
- 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
Links
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N diphenyl Chemical compound C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 claims description 42
- 239000002904 solvent Substances 0.000 claims description 25
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 claims description 24
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 claims description 24
- 229910052794 bromium Inorganic materials 0.000 claims description 24
- 239000004305 biphenyl Substances 0.000 claims description 21
- 235000010290 biphenyl Nutrition 0.000 claims description 21
- HQJQYILBCQPYBI-UHFFFAOYSA-N 1-bromo-4-(4-bromophenyl)benzene Chemical group C1=CC(Br)=CC=C1C1=CC=C(Br)C=C1 HQJQYILBCQPYBI-UHFFFAOYSA-N 0.000 claims description 18
- 238000006243 chemical reaction Methods 0.000 claims description 18
- LQNUZADURLCDLV-UHFFFAOYSA-N nitrobenzene Chemical compound [O-][N+](=O)C1=CC=CC=C1 LQNUZADURLCDLV-UHFFFAOYSA-N 0.000 claims description 8
- RFFLAFLAYFXFSW-UHFFFAOYSA-N 1,2-dichlorobenzene Chemical compound ClC1=CC=CC=C1Cl RFFLAFLAYFXFSW-UHFFFAOYSA-N 0.000 claims description 6
- 125000004432 carbon atom Chemical group C* 0.000 claims description 4
- 150000001875 compounds Chemical class 0.000 claims description 4
- 229920006395 saturated elastomer Polymers 0.000 claims description 4
- 125000001931 aliphatic group Chemical group 0.000 claims 2
- 229910052799 carbon Inorganic materials 0.000 claims 1
- 238000000034 method Methods 0.000 description 18
- CPELXLSAUQHCOX-UHFFFAOYSA-N Hydrogen bromide Chemical compound Br CPELXLSAUQHCOX-UHFFFAOYSA-N 0.000 description 10
- 239000013078 crystal Substances 0.000 description 10
- 239000000047 product Substances 0.000 description 8
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 5
- 239000006227 byproduct Substances 0.000 description 5
- 229910000042 hydrogen bromide Inorganic materials 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 4
- 238000005893 bromination reaction Methods 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 239000007795 chemical reaction product Substances 0.000 description 3
- 239000007810 chemical reaction solvent Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000004817 gas chromatography Methods 0.000 description 3
- 238000009776 industrial production Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 229960000583 acetic acid Drugs 0.000 description 2
- 150000001338 aliphatic hydrocarbons Chemical group 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- -1 poly(oxyalkylene) Polymers 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- QVLAWKAXOMEXPM-UHFFFAOYSA-N 1,1,1,2-tetrachloroethane Chemical compound ClCC(Cl)(Cl)Cl QVLAWKAXOMEXPM-UHFFFAOYSA-N 0.000 description 1
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 1
- QPFMBZIOSGYJDE-UHFFFAOYSA-N 1,1,2,2-tetrachloroethane Chemical compound ClC(Cl)C(Cl)Cl QPFMBZIOSGYJDE-UHFFFAOYSA-N 0.000 description 1
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 description 1
- KNKRKFALVUDBJE-UHFFFAOYSA-N 1,2-dichloropropane Chemical compound CC(Cl)CCl KNKRKFALVUDBJE-UHFFFAOYSA-N 0.000 description 1
- ZPQOPVIELGIULI-UHFFFAOYSA-N 1,3-dichlorobenzene Chemical compound ClC1=CC=CC(Cl)=C1 ZPQOPVIELGIULI-UHFFFAOYSA-N 0.000 description 1
- KTADSLDAUJLZGL-UHFFFAOYSA-N 1-bromo-2-phenylbenzene Chemical group BrC1=CC=CC=C1C1=CC=CC=C1 KTADSLDAUJLZGL-UHFFFAOYSA-N 0.000 description 1
- JSZOAYXJRCEYSX-UHFFFAOYSA-N 1-nitropropane Chemical compound CCC[N+]([O-])=O JSZOAYXJRCEYSX-UHFFFAOYSA-N 0.000 description 1
- FECNOIODIVNEKI-UHFFFAOYSA-N 2-[(2-aminobenzoyl)amino]benzoic acid Chemical class NC1=CC=CC=C1C(=O)NC1=CC=CC=C1C(O)=O FECNOIODIVNEKI-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000031709 bromination Effects 0.000 description 1
- QGJOPFRUJISHPQ-NJFSPNSNSA-N carbon disulfide-14c Chemical compound S=[14C]=S QGJOPFRUJISHPQ-NJFSPNSNSA-N 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012362 glacial acetic acid Substances 0.000 description 1
- 229920006015 heat resistant resin Polymers 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- MCSAJNNLRCFZED-UHFFFAOYSA-N nitroethane Chemical compound CC[N+]([O-])=O MCSAJNNLRCFZED-UHFFFAOYSA-N 0.000 description 1
- BNIXVQGCZULYKV-UHFFFAOYSA-N pentachloroethane Chemical compound ClC(Cl)C(Cl)(Cl)Cl BNIXVQGCZULYKV-UHFFFAOYSA-N 0.000 description 1
- 229920005862 polyol Polymers 0.000 description 1
- 150000003077 polyols Chemical class 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
【発明の詳細な説明】
本発明は、4,4′−ジブロモビフエニルの製造
法に関するものである。
本発明に係る4,4′−ジブロモビフエニルは、
ポリ(オキシアルキレン)ポリオール、スルホン
化脂肪族アルコール等の安定剤、染料中間体、お
よび耐熱性樹脂製造用などの中間原料として極め
て有用なものである。
従来ビフエニルと臭素とを溶剤の存在下、また
は溶剤なしに反応させて、4,4′−ジブロモビフ
エニルをうる方法としては下記の諸法が知られて
いる。(1)純ビフエニルを二硫化炭素に溶解し、臭
素を添加して2日間加熱還流し、さらに若干の臭
素を補充して密閉管中90℃で2時間加熱処理し、
目的の4,4′−ジブロモビフエニルをうる方法
〔ジヤーナル・オブ・ザ・ケミカル・ソサイエテ
イ(JCS.)47,586(1885)〕。(2)ビフエニルを溶
解した氷酢酸溶液に、臭素を添加して3時間加熱
還流し、冷却後過をして、4,4′−ジブロモビ
フエニルをうる方法〔ヘミシエ・ベリヒテ
(Chem.Ber.)44,1087(1911)〕。(3)ビフエニル
を硫酸中で臭素と反応させる方法〔ジヤーナル・
オ・ザ・アメリカン・ケミカル・ソサイエテイ
(JACS.)43,3061(1921)〕。(4)ビフエニルと臭
素とを二酸化硫黄中−40〜−5℃で反応させ4,
4′−ジブロモビフエニルをうる方法〔ドイツ公開
公報、第1930594号(1970)〕。(5)ビフエニルの微
粉末に臭素蒸気で室温で接触させて反応させ、粗
反応物をベンゼンで再結晶して、4,4′−ジブロ
モビフエニルをうる方法〔オーガニツク・シンテ
イシス・コレクテイブ・ボリユーム(Org.Syn.
Coll.Vol.)4,256〕などである。
しかし、これらの諸法は、いずれも下記のよう
な欠点を有し、到底工業的製法として採用できる
ものでない。すなわち、(1)の方法においては、反
応時間が2日間と非常に長く実用的でない。(2)の
方法では、収率71%と低く、さらに溶剤である酢
酸と臭素との反応が一部起り、臭素の損失が大と
なる。(3)の方法は、目的物の収率が13%と極めて
低い。(4)の方法では、反応時間、目的物選択率の
点においては好ましいが、極低温下多量の液化毒
性ガス中での反応を行うために、その反応装置や
安全対策などに多額の設備投資を要し、大規模の
生産でなければ、その工業化は困難である。(5)の
方法は、ビフエニルの微粉末と臭素蒸気との反応
であるため、粉体を取扱うための機械的困難さが
伴い、粉体の内部まで均一に反応することが困難
であり、また目的物以外のジブロム化合物が副生
し、さらに反応組成物が若干粘着性を持ち、製品
をうるために再結晶が必要であり工業的製造法と
しては不適当な方法である。
以上の理由から、本発明者らは、これらの従来
法における欠点を除去した新規で改良された工業
的製造法、すなわち常温ないし若干加熱温度にお
いて常圧で触媒を用いることなく、容易に臭素化
が進行し、目的物の4,4′−ジブロモビフエニル
を好収率で得られる方法を提供することを目的と
して、詳細な検討を行なつた結果特定の溶剤中で
反応を行なわせる本発明を完成した。
すなわち、本発明は、o−ジクロロベンゼン、
ニトロベンゼンならびに一般式R・Clo(式中R
は、炭素原子数2〜5の飽和脂肪族炭化水素残基
を、nは1〜5を示す。)および一般式R′・NO2
(式中R′は、炭素原子数1〜3の飽和脂肪族炭化
水素残基を示す。)で表わされ、かつ常温におけ
る誘電率が6.5以上の化合物の群から選ばれた1
種以上の溶剤中で、ビフエニルと臭素とを反応さ
せて4,4′−ジブロモビフエニルを製造する方法
である。
臭素化反応は、ビフエニルと溶剤との混合系
に、かきまぜ下に臭素を添加して行なうか、また
はビフエニルを完全に溶解させ溶剤系に、同種溶
剤で希釈した臭素を添加して行うことができる
が、後者がより好ましい。反応中は臭化水素ガス
が発生するので、これを水またはアルカリ水溶液
などに導き吸収させる。
生成した4,4′−ジブロモビフエニルの大部分
は結晶として析出するが、副生成物は溶剤層に溶
解している。次に反応系に残存した過剰の臭素と
溶存臭素化水素とを除くため、反応物系にアルカ
リ性物質たとえば水酸化ナトリウムなどの水溶液
を加えて中和し、過、水洗、乾燥することによ
り、目的の4,4′−ジブロモビフエニルをうるこ
とができる。さらに液の溶剤層を濃縮後冷却す
ることにより、溶存した少量の4,4′−ジブロモ
ビフエニルを結晶として回収できる。このときの
濃縮率は、約90%程度まで行なうことが好まし
い。
本発明に使用する溶剤は、原料であるビフエニ
ルの溶剤であり、前記のとおり、o−ジクロロベ
ンゼン、ニトロベンゼン又は一般式と誘電率εと
により特徴付けることができる。これは、多くの
溶剤と収率との相関を求めると、ほぼεが6.5以
下ではεが小さく成るほど急速に収率が低下し、
6.5以上では、80%以上ほぼ90%の収率を保つよ
うに整理される。前記定義の溶剤は、溶剤として
すぐれているばかりでなく、臭素および副生する
臭化水素に対し安定である。
前記一般式R・Cloに属する溶剤としては、た
とえば1,1−ジクロロエタン、1,2−ジクロ
ロエタン、1,1,1−トリクロロエタン、1,
1,2,2−テトラクロロエタン、1,2−ジク
ロロプロパンなどであり、又一般式R′・NO2に属
する溶剤としては、たとえばニトロエタン、ニト
ロプロパンなどである。ニトロベンゼンおよび前
記のうち1,2−ジクロロエタンなどは、工業的
に安定して入手できるので好ましい溶剤である。
四塩化炭素、クロロホルム、1,1,1,2−
テトラクロルエタン、ペンタクロロエタン、n−
ヘキサン、m−ジクロロベンゼンなどの誘電率の
小さい溶剤では、臭素化反応が遅く、また目的物
の選択率も悪い。
溶剤の使用量は、ビフエニルの溶解度によつて
異なるが、一般にはビフエニルの重量に対して
1.5〜3.5倍が好ましい。
本発明の実施に当つて、ビフエニルに対する臭
素の使用量は2.0〜2.4モル倍であるが好ましくは
2.1〜2.2モル倍である。
反応温度は、10〜60℃であるが、好ましくは30
〜50℃である。すなわち約30℃で臭素を添加し、
添加終了後45〜50℃まで昇温して反応を完結させ
るのが好適である。普通数時間以内は反応は完結
する。
本発明の溶剤中では、臭素化反応は良好な転化
率をもつて進行し、また目的物の選択率も良い。
また本溶剤は、前記の通り目的物の4,4′−ジブ
ロモビフエニルの溶解性が悪く、また副生物の溶
解性は大きいので、過した結晶および液を濃
縮して得た結晶を合せて純度の高い目的物を良好
な収率で得ることができる。また副生物中の4−
ブロモビフエニルは、濃縮物中から回収し、次回
の反応に循環使用することができる。
本発明方法によれば、溶剤の化学的安定性が高
いため、溶剤を蒸留して循環使用する際損失が少
なく、また目的とする4,4′−ジブロモビフエニ
ルを従来法より著しく高収率で高収率良く得られ
るのでその経済的効果は著しいものである。
以下実施例をあげて本発明をさらに説明する。
実施例 1
23.1gのビフエニルと40gの1.2−ジクロロエ
タンとを、かきまぜ機のついた300ml四ツ口フラ
スコ中に仕込み、完全に溶解させる。
温度30〜35℃を保つて、52.7gの臭素と6gの
1.2−ジクロロエタンとの混合溶液を約1時間か
けて適下し、適下終了後50℃まで昇温し、同温度
を保持して5時間反応させた。この時一部をサン
プリングしてガスクロマトグラフ分析(以下GC
分析と略称)した結果を表−1に示した。反応中
発生した臭化水素は、水を入れたガス吸収びんに
導き吸収させた。次にこの反応系に50℃以下で10
%の水酸化ナトリウム水溶液を加え、過剰の臭素
と溶存臭化水素とを中和し、反応物を10〜15℃ま
で冷却し、過、水洗、乾燥して、4,4′−ジブ
ロモビフエニルの一次晶を得た。また液からそ
の90%の溶剤を留去濃縮し、同様に冷却、過、
水洗、乾燥して4,4′−ジブロモビフエニルの二
次晶を得た。一次晶とこれを合せ、合計42.8gを
得た。収率は90%(対仕込みビフエニル)であつ
た。GC分析による結晶純度は98.6%、融度は
165.5〜167℃であつた。
実施例 2,3,4,5,6,7
実施例1と反応溶剤のみを代えたほかは、同様
に処理した結果を表−1に示した。
比較例 1
23.1gの微粉砕したビフエニルと58.5gの臭素
とを別個の蒸発皿に入れ、この両者を陶製棚の入
つた直径35cmのガス抜き付きのデシケーター中に
入れ、棚の上部にビフエニルを、下部に臭素を置
き、室温で粉末ビフエニルと臭素蒸気とを12時間
接触反応させた。粗反応物の一部を試料採取し、
GC分析した結果を表−1に示した。この粗反応
物を、ベンゼン113mlで再結晶し、35.6gの白色
結晶を得た。4,4′−ジブロモビフエニルとして
収率75%(対仕込みビフエニル)であつた。GC
分析による結晶の純度は98.5%、融点は165.5〜
167℃であつた。
比較例 2
実施例1と反応溶剤、臭素適下後の反応温度お
よび時間を代えたほかは同様に処理した結果を表
−1に示した。
比較例 3,4,5,6
実施例1と反応溶剤を代えたほかは同様に処理
した結果を表−1に示した。
【表】DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing 4,4'-dibromobiphenyl. The 4,4′-dibromobiphenyl according to the present invention is
It is extremely useful as a stabilizer for poly(oxyalkylene) polyols, sulfonated aliphatic alcohols, dye intermediates, and intermediate raw materials for producing heat-resistant resins. Conventionally, the following methods are known for producing 4,4'-dibromobiphenyl by reacting biphenyl and bromine in the presence or absence of a solvent. (1) Pure biphenyl was dissolved in carbon disulfide, bromine was added, and the mixture was heated under reflux for 2 days.Additionally, some bromine was added and heat treated at 90°C for 2 hours in a sealed tube.
Method for obtaining the desired 4,4'-dibromobiphenyl [Journal of the Chemical Society (JCS.) 47 , 586 (1885)]. (2) A method for obtaining 4,4'-dibromobiphenyl by adding bromine to a glacial acetic acid solution in which biphenyl is dissolved, heating under reflux for 3 hours, cooling and filtering to obtain 4,4'-dibromobiphenyl [Chem. ) 44 , 1087 (1911)]. (3) Method of reacting biphenyl with bromine in sulfuric acid [Journal.
JACS. 43 , 3061 (1921)]. (4) Reacting biphenyl and bromine in sulfur dioxide at -40 to -5°C4,
Method for obtaining 4'-dibromobiphenyl [German Open Gazette, No. 1930594 (1970)]. (5) A method to obtain 4,4'-dibromobiphenyl by contacting fine biphenyl powder with bromine vapor at room temperature and recrystallizing the crude reaction product with benzene [Organic Synthesis Collective Volume ( Org.Syn.
Coll. Vol.) 4 , 256] etc. However, all of these methods have the following drawbacks and cannot be adopted as industrial production methods. That is, in method (1), the reaction time is extremely long, 2 days, and is not practical. Method (2) has a low yield of 71%, and furthermore, a portion of the reaction between the solvent acetic acid and bromine occurs, resulting in a large loss of bromine. In method (3), the yield of the target product is extremely low at 13%. Method (4) is preferable in terms of reaction time and target product selectivity, but requires a large investment in equipment and safety measures because the reaction is carried out in a large amount of liquefied toxic gas at extremely low temperatures. It is difficult to industrialize it unless it is produced on a large scale. Since method (5) involves the reaction of fine biphenyl powder with bromine vapor, it involves mechanical difficulties in handling the powder, making it difficult to react uniformly to the inside of the powder. Dibrome compounds other than the target compound are produced as by-products, the reaction composition is slightly sticky, and recrystallization is required to obtain the product, making this method unsuitable for industrial production. For the above reasons, the present inventors have developed a new and improved industrial production method that eliminates the drawbacks of these conventional methods, that is, a method that allows easy bromination at room temperature to slightly heated temperature and normal pressure without using a catalyst. With the aim of providing a method in which 4,4'-dibromobiphenyl, the target product, can be obtained in good yield, the present invention, in which the reaction is carried out in a specific solvent, was developed as a result of detailed studies. completed. That is, the present invention provides o-dichlorobenzene,
Nitrobenzene and the general formula R・Cl o (in the formula R
represents a saturated aliphatic hydrocarbon residue having 2 to 5 carbon atoms, and n represents 1 to 5. ) and the general formula R′・NO 2
(In the formula, R' represents a saturated aliphatic hydrocarbon residue having 1 to 3 carbon atoms.) 1 selected from the group of compounds having a dielectric constant of 6.5 or more at room temperature.
This is a method for producing 4,4'-dibromobiphenyl by reacting biphenyl with bromine in one or more solvents. The bromination reaction can be carried out by adding bromine to a mixed system of biphenyl and a solvent while stirring, or by completely dissolving the biphenyl and adding bromine diluted with a similar solvent to the solvent system. However, the latter is more preferred. During the reaction, hydrogen bromide gas is generated, which is introduced into water or an alkaline aqueous solution and absorbed. Most of the 4,4'-dibromobiphenyl produced is precipitated as crystals, but by-products are dissolved in the solvent layer. Next, in order to remove excess bromine and dissolved hydrogen bromide remaining in the reaction system, the reaction system is neutralized by adding an aqueous solution of an alkaline substance such as sodium hydroxide, filtered, washed with water, and dried. 4,4'-dibromobiphenyl can be obtained. Further, by concentrating and cooling the solvent layer of the liquid, a small amount of dissolved 4,4'-dibromobiphenyl can be recovered as crystals. The concentration ratio at this time is preferably about 90%. The solvent used in the present invention is a solvent for biphenyl, which is a raw material, and can be characterized by o-dichlorobenzene, nitrobenzene, or the general formula and dielectric constant ε, as described above. This is because when looking at the correlation between many solvents and yield, when ε is approximately 6.5 or less, the smaller ε becomes, the more rapidly the yield decreases.
At 6.5 or higher, the yield is maintained at 80% or more and almost 90%. The above-defined solvent is not only excellent as a solvent, but also stable against bromine and by-product hydrogen bromide. Examples of solvents belonging to the general formula R.Cl o include 1,1-dichloroethane, 1,2-dichloroethane, 1,1,1-trichloroethane, 1,
These include 1,2,2-tetrachloroethane and 1,2-dichloropropane, and examples of solvents belonging to the general formula R'.NO 2 include nitroethane and nitropropane. Nitrobenzene and 1,2-dichloroethane among the above are preferred solvents because they are industrially stably available. Carbon tetrachloride, chloroform, 1,1,1,2-
Tetrachloroethane, pentachloroethane, n-
When using a solvent with a small dielectric constant such as hexane or m-dichlorobenzene, the bromination reaction is slow and the selectivity of the target product is also poor. The amount of solvent used varies depending on the solubility of biphenyl, but is generally based on the weight of biphenyl.
1.5 to 3.5 times is preferable. In carrying out the present invention, the amount of bromine used is 2.0 to 2.4 times the mole of biphenyl, but preferably
It is 2.1 to 2.2 times the mole. The reaction temperature is 10 to 60°C, preferably 30°C.
~50℃. That is, add bromine at about 30℃,
After the addition is completed, it is preferable to raise the temperature to 45 to 50°C to complete the reaction. The reaction is usually complete within several hours. In the solvent of the present invention, the bromination reaction proceeds with a good conversion rate and also has a good selectivity of the target product.
In addition, as mentioned above, this solvent has poor solubility for the target product, 4,4'-dibromobiphenyl, and the solubility of by-products is high, so the filtered crystals and the crystals obtained by concentrating the liquid are combined. A highly pure target product can be obtained in good yield. Also, 4- in the by-product
Bromobiphenyl can be recovered from the concentrate and recycled for the next reaction. According to the method of the present invention, since the solvent has high chemical stability, there is little loss when the solvent is distilled and recycled, and the target 4,4'-dibromobiphenyl can be produced in a significantly higher yield than the conventional method. Since it can be obtained in high yield, its economic effect is significant. The present invention will be further explained below with reference to Examples. Example 1 23.1 g of biphenyl and 40 g of 1,2-dichloroethane are placed in a 300 ml four-necked flask equipped with a stirrer and completely dissolved. Keeping the temperature at 30~35℃, 52.7g of bromine and 6g of
A mixed solution with 1,2-dichloroethane was dropped over about 1 hour, and after the dropping was completed, the temperature was raised to 50°C, and the same temperature was maintained for 5 hours of reaction. At this time, a portion is sampled and analyzed by gas chromatography (hereinafter referred to as GC).
The results are shown in Table 1. Hydrogen bromide generated during the reaction was introduced into a gas absorption bottle containing water and absorbed. Next, add 10% to this reaction system at below 50°C.
% aqueous sodium hydroxide solution to neutralize excess bromine and dissolved hydrogen bromide, the reaction mixture was cooled to 10-15°C, filtered, washed with water, and dried to produce 4,4'-dibromobiphenyl. The primary crystal of was obtained. In addition, 90% of the solvent is distilled off and concentrated from the liquid, cooled, filtered,
After washing with water and drying, secondary crystals of 4,4'-dibromobiphenyl were obtained. A total of 42.8 g was obtained by combining this with the primary crystal. The yield was 90% (based on biphenyl charged). Crystal purity by GC analysis is 98.6%, melting point is
The temperature was 165.5-167℃. Examples 2, 3, 4, 5, 6, 7 Table 1 shows the results of the same treatment as in Example 1, except that only the reaction solvent was changed. Comparative Example 1 23.1 g of finely ground biphenyl and 58.5 g of bromine were placed in separate evaporation dishes, both were placed in a dessicator with a diameter of 35 cm and a gas vent equipped with a ceramic shelf, and the biphenyl was placed on the top of the shelf. , bromine was placed at the bottom, and powdered biphenyl and bromine vapor were allowed to contact react at room temperature for 12 hours. Collect a sample of a portion of the crude reaction product,
The results of GC analysis are shown in Table 1. This crude reaction product was recrystallized with 113 ml of benzene to obtain 35.6 g of white crystals. The yield of 4,4'-dibromobiphenyl was 75% (based on the charged biphenyl). G.C.
The purity of the crystal by analysis is 98.5%, the melting point is 165.5~
It was 167℃. Comparative Example 2 Table 1 shows the results of the same treatment as in Example 1, except that the reaction solvent, the reaction temperature after dropping bromine, and the time were changed. Comparative Examples 3, 4, 5, 6 Table 1 shows the results of the same treatment as in Example 1 except that the reaction solvent was changed. 【table】
Claims (1)
ジブロモビフエニルを製造するに際し、o−ジク
ロロベンゼン、ニトロベンゼンならびに一般式
R・Clo(式中Rは、炭素原子数2〜5の飽和脂
肪族炭化水素残基を、nは1〜5を示す。)およ
び一般式R′・NO2(式中R′は、炭素原子数1〜3
の飽和脂肪族炭化水素残基を示す。)で表わさ
れ、かつ常温における誘電率が6.5以上の化合物
の群から選ばれた1種以上の溶剤中で反応を行な
わせることを特徴とする4,4′−ジブロモビフエ
ニルの製造法。1 By reacting biphenyl with bromine, 4,4'-
When producing dibromobiphenyl, o-dichlorobenzene, nitrobenzene, and the general formula R・Cl o (wherein R represents a saturated aliphatic hydrocarbon residue having 2 to 5 carbon atoms, and n represents 1 to 5) ) and the general formula R′・NO 2 (in the formula, R′ is a carbon atom number of 1 to 3
represents a saturated aliphatic hydrocarbon residue. ), and the reaction is carried out in one or more solvents selected from the group of compounds having a dielectric constant of 6.5 or more at room temperature.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13632978A JPS5564532A (en) | 1978-11-07 | 1978-11-07 | Preparation of 4,4'-dibromobiphenyl |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13632978A JPS5564532A (en) | 1978-11-07 | 1978-11-07 | Preparation of 4,4'-dibromobiphenyl |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5564532A JPS5564532A (en) | 1980-05-15 |
JPS6116252B2 true JPS6116252B2 (en) | 1986-04-28 |
Family
ID=15172669
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13632978A Granted JPS5564532A (en) | 1978-11-07 | 1978-11-07 | Preparation of 4,4'-dibromobiphenyl |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5564532A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6362638A (en) * | 1986-09-01 | 1988-03-18 | Makino Milling Mach Co Ltd | Lubricating device for vertical spindle of machine tool |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2628100B1 (en) * | 1988-03-02 | 1990-11-30 | Rhone Poulenc Chimie | PROCESS FOR THE PREPARATION OF DIBROMO-4,4 (PRIME) BIPHENYL IN A SOLVENT MEDIUM AND WITH A CATALYST |
JPH05204870A (en) * | 1992-01-29 | 1993-08-13 | Sumitomo Metal Ind Ltd | Parallel calculation device |
JP4803911B2 (en) * | 2001-07-05 | 2011-10-26 | 日宝化学株式会社 | Method for producing 4,4'-dibromobiphenyl |
-
1978
- 1978-11-07 JP JP13632978A patent/JPS5564532A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6362638A (en) * | 1986-09-01 | 1988-03-18 | Makino Milling Mach Co Ltd | Lubricating device for vertical spindle of machine tool |
Also Published As
Publication number | Publication date |
---|---|
JPS5564532A (en) | 1980-05-15 |
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