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JPS6019283B2 - Method for side chain chlorination of aromatic hydrocarbons having side chains - Google Patents
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JPS6019283B2 - Method for side chain chlorination of aromatic hydrocarbons having side chains - Google Patents

Method for side chain chlorination of aromatic hydrocarbons having side chains

Info

Publication number
JPS6019283B2
JPS6019283B2 JP51153088A JP15308876A JPS6019283B2 JP S6019283 B2 JPS6019283 B2 JP S6019283B2 JP 51153088 A JP51153088 A JP 51153088A JP 15308876 A JP15308876 A JP 15308876A JP S6019283 B2 JPS6019283 B2 JP S6019283B2
Authority
JP
Japan
Prior art keywords
reaction
side chain
aromatic hydrocarbons
side chains
chlorination
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
JP51153088A
Other languages
Japanese (ja)
Other versions
JPS5377022A (en
Inventor
仁一郎 長谷川
泰史 小林
孝明 清水
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.)
Shin Etsu Chemical Co Ltd
Original Assignee
Shin Etsu Chemical 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 Shin Etsu Chemical Co Ltd filed Critical Shin Etsu Chemical Co Ltd
Priority to JP51153088A priority Critical patent/JPS6019283B2/en
Publication of JPS5377022A publication Critical patent/JPS5377022A/en
Publication of JPS6019283B2 publication Critical patent/JPS6019283B2/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

  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

【発明の詳細な説明】 本発明は側鎖を有する芳香族炭化水素の側鎖塩素化方法
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for side chain chlorination of aromatic hydrocarbons having side chains.

従来、側鎖を有する芳香族炭化水素の側鎖塩素化方法と
しては、側鎖としてメチル基などのアルキル基を有する
芳香族炭化水素を四塩化炭素のような溶剤を溶解し、こ
れに紫外線を照射しながら塩素を導入する方法が公知と
されているが、この方法には生成物が融点が高いという
制約から反応温度を高くする必要があるほか、反応完了
に長時間を要する不利がある。
Conventionally, as a side chain chlorination method for aromatic hydrocarbons having side chains, aromatic hydrocarbons having alkyl groups such as methyl groups as side chains are dissolved in a solvent such as carbon tetrachloride, and then ultraviolet rays are irradiated. A method of introducing chlorine during irradiation is known, but this method requires a high reaction temperature due to the high melting point of the product and has the disadvantage of requiring a long time to complete the reaction.

しかもこのようにして塩素化反応を行わせると、塩素化
は側鎖のみならず芳香族炭化水素の核にも起こり、樹脂
状物も相当量副生するので、目的生成物の収率が低く、
また反応混合物は副生物により黒色になるので、精製に
困難をともなう不利がある。他方、上記のような欠点を
解決すべくその塩素化反応を行うにあたって、アルキレ
ンボリアミン、ベンツアミド、尿素、アセトアミド、ト
リアリールホスフェート、ソルビトールなどの触媒を使
用する方法が提案されているが、これらの場合にも反応
の進行にともなって創生枕でん物を生成するなどの不都
合があり、目的生成物の収率、純度等の点で必ずしも満
足すべき結果を与えない。
Moreover, when the chlorination reaction is carried out in this manner, chlorination occurs not only in the side chains but also in the nucleus of the aromatic hydrocarbon, and a considerable amount of resinous substances are produced as by-products, resulting in a low yield of the desired product. ,
Moreover, since the reaction mixture becomes black due to by-products, there is a disadvantage that purification is difficult. On the other hand, in order to solve the above-mentioned drawbacks, methods using catalysts such as alkylene polyamine, benzamide, urea, acetamide, triaryl phosphate, and sorbitol have been proposed in carrying out the chlorination reaction. In this case as well, there are inconveniences such as the production of synthetic polymers as the reaction progresses, and the results are not necessarily satisfactory in terms of yield, purity, etc. of the desired product.

本発明はこのような欠点のない側鎖を有する芳香族炭化
水素の側頭塩素化方法を提供しようとするもので、これ
は脂肪族多ハロゲン化炭化水素を溶剤とする側鎖を有す
る芳香族炭化水素の溶液に、アルキルアミン類、含窒素
榎素環アミン類およびアルカノールアミソ類から選ばれ
るアミソ化合物の1種もしくは2種以上を含有させ、つ
いで夕これと塩素とを紫外線の照射下において接触させ
ることを特徴とする方法であり、これによれば比較的低
い反応温度(おおむね80〜15000)で側鎖の塩素
化反応が選択的にしかも容易に進行し、樹脂状物などの
創生物はほとんど生成されず、また0反応混合物は反応
の進行にともなって黒色になるなどの欠点がないので、
目的物が高収率、高純度で得られる。さらに、このよう
な塩素化反応においては、不純物として塩化第二鉄など
が存在すると、側鎖のタ塩素化反応とともに核にも塩素
化が起こるおそれがあるが、本発明の方法によれば反応
系内にそのような不純物が存在しても塩素化反応は側鎖
について選択的に進行し、核塩素化物の創生はきわめて
少ないという有利性が与えられる。
The present invention aims to provide a method for lateral chlorination of aromatic hydrocarbons having side chains that does not have such drawbacks. A hydrocarbon solution contains one or more amiso compounds selected from alkyl amines, nitrogen-containing enocyclic amines, and alkanol amiso compounds, and then is brought into contact with chlorine under ultraviolet irradiation. According to this method, the chlorination reaction of side chains proceeds selectively and easily at a relatively low reaction temperature (approximately 80 to 15,000 ℃), and created substances such as resinous substances are Almost no product is produced, and the 0 reaction mixture does not have any drawbacks such as turning black as the reaction progresses.
The target product can be obtained in high yield and purity. Furthermore, in such a chlorination reaction, if ferric chloride or the like is present as an impurity, there is a risk that the nucleus will be chlorinated along with the side chain chlorination reaction, but according to the method of the present invention, the reaction can be prevented. Even if such impurities are present in the system, the chlorination reaction proceeds selectively with respect to side chains, giving the advantage that the creation of nuclear chlorinated products is extremely small.

これを説明すると、本発明で始発原料として使用される
側鎖を有する芳香族炭化水素としては、トルエン、キシ
レン、トリメチルベンゼンなどの低級アルキル基を側鎖
として有する芳香族炭化水素が例示される。
To explain this, examples of the aromatic hydrocarbon having a side chain used as a starting material in the present invention include aromatic hydrocarbons having a lower alkyl group as a side chain such as toluene, xylene, and trimethylbenzene.

なお、本発明の方法は核にハロゲン原子、カルボキシル
基、ハロゲン化アシル基、水酸基、スルホン基などの原
子または基が導入された側鎖を有する芳香族化合物に対
しても良好に側鎖塩素化を行うことができる。塩素化反
応にあたって溶剤として使用される脂肪族多ハロゲン化
炭化水素としては、塩素化反応に対して安定なものとく
に四塩化炭素が好ましい。
The method of the present invention can also effectively chlorinate side chains of aromatic compounds having side chains in which atoms or groups such as halogen atoms, carboxyl groups, halogenated acyl groups, hydroxyl groups, and sulfone groups have been introduced. It can be performed. The aliphatic polyhalogenated hydrocarbon used as a solvent in the chlorination reaction is preferably one that is stable against the chlorination reaction, particularly carbon tetrachloride.

なお、この場合の溶液の濃度は10〜7の重量%の範囲
内とすればよい。本発明の方法に使用される触媒は、ト
リェチルアミン、ジイソプロピルアミンなどのアルキル
アミン類、ピベリジン、N−メチルピベリジン、ピロリ
ジン、ピベラジン、ピリジン、N−メチルピロール、2
−ピロリドン、モルホリンなどの含窒素複素環アミン類
、およびモノェタノールアミン、インプロパノールアミ
ンなどのアルカノールアミン類である。
Note that the concentration of the solution in this case may be within the range of 10 to 7% by weight. Catalysts used in the method of the present invention include alkyl amines such as triethylamine and diisopropylamine, piperidine, N-methylpiveridine, pyrrolidine, piperazine, pyridine, N-methylpyrrole,
- Nitrogen-containing heterocyclic amines such as pyrrolidone and morpholine, and alkanolamines such as monoethanolamine and inpropanolamine.

2上記した触媒の好適な使用
量は、それらの種類によって異なるが、一般には原料芳
香族炭化水素に対して0.01〜5重量%とされる。ま
た、紫外線照射下に塩素化反応を行わせる際の反応温度
はおおむね80〜150qoとすればよい。紫外線の光
源と3してはキセノンランプ、低圧あるいは高圧の水銀
灯等を使用することができる。反応は、紫外線を透過す
る反応容器に原料芳香族化合物、触媒および溶剤を仕込
み、反応容器内底部に塩素を吹込むとともに紫外線を照
射すると3いう方法によればよい。
2 The preferable amount of the above-mentioned catalyst to be used varies depending on the type thereof, but is generally 0.01 to 5% by weight based on the aromatic hydrocarbon raw material. Moreover, the reaction temperature when performing the chlorination reaction under ultraviolet irradiation may be approximately 80 to 150 qo. As the ultraviolet light source 3, a xenon lamp, a low-pressure or high-pressure mercury lamp, or the like can be used. The reaction may be carried out by method 3, in which a raw material aromatic compound, a catalyst, and a solvent are placed in a reaction vessel that transmits ultraviolet rays, and chlorine is blown into the bottom of the reaction vessel while irradiating ultraviolet rays.

つぎに、実施例をあげてさらに詳細に説明する。Next, the present invention will be explained in more detail by giving examples.

なお、下記の実施例において塩化第二鉄を添加したのは
、この塩素化反応に対してもっとも有害な不純物である
とされる鉄化合物の存在下にお4し、ても本発明の目的
が十分に達成されることを示すためであって、このよう
な鉄化合物が存在しない場合にはごうに良好な結果が得
られることはいうまでもない。実施例 底部に塩素ガス吹込みノズルを設けてなる石英ガラス製
反応器に、パラキシレン35夕、四塩化炭素25夕、下
記に示す触媒0.1夕、および不純物として塩化第二鉄
6Mを仕込み、反応器の一方の側から高圧水銀灯を用い
て紫外線を照射し、反応器内底部に塩素ガスを州そ/時
間の割合で吹込みながら、6時間反応させた。
In addition, in the following examples, ferric chloride was added in the presence of iron compounds, which are considered to be the most harmful impurities to this chlorination reaction. This is to show that this can be achieved satisfactorily, and it goes without saying that much better results can be obtained in the absence of such iron compounds. Example A quartz glass reactor equipped with a chlorine gas blowing nozzle at the bottom was charged with 35 m of paraxylene, 25 m of carbon tetrachloride, 0.1 m of the catalyst shown below, and 6 M of ferric chloride as an impurity. Ultraviolet rays were irradiated from one side of the reactor using a high-pressure mercury lamp, and the reactor was reacted for 6 hours while blowing chlorine gas into the bottom of the reactor at a rate of 1 hour.

反応温度は反応スタート時には90『0とし徐々に昇温
して13000までとした。反応終了後、四塩化炭素を
完全に除去したところ、いずれの場合にも室温で固体を
呈する生成物が得られ、理論値に対する収率はいずれの
場合にも95%以上であった。
The reaction temperature was 90'0 at the start of the reaction and was gradually raised to 13,000. After the reaction was completed, carbon tetrachloride was completely removed, and in each case a product was obtained that was solid at room temperature, and the yield relative to the theoretical value was 95% or more in each case.

他方、生成物についてガスクロマトグラフィ−により分
析したところ、目的生成物である1・4−ビス(トリク
ロロメチル)ベンゼンの純度がいずれの場合にも99重
量%以上であり、創生物(主として核塩素化物)の量は
それぞれ下記に示すとおりであった。
On the other hand, when the products were analyzed by gas chromatography, the purity of the target product, 1,4-bis(trichloromethyl)benzene, was 99% by weight or higher in all cases, and it was found that the purity of the target product, 1,4-bis(trichloromethyl)benzene, was 99% by weight or more, and ) were as shown below.

なお、上記反応生成物の10%四塩化炭素溶液について
外観(色調)および厚さ1肌の透光率(紫、緑)を調べ
た結果についても下記に示した。
The results of examining the appearance (color tone) and light transmittance (purple, green) of one skin thickness for a 10% carbon tetrachloride solution of the above reaction product are also shown below.

ただし、実験No.1は比較例を示したものである。However, experiment no. 1 shows a comparative example.

Claims (1)

【特許請求の範囲】[Claims] 1 脂肪族多ハロゲン化炭化水素を溶剤とする側鎖を有
する芳香族炭化水素の溶液に、アルキルアミン類、含窒
素複素環アミン類およびアルカノールアミン類から選ば
れるアミン化合物の1種もしくは2種以上を含有させ、
ついでこれと塩素とを紫外線の照射下において接触させ
ることを特徴とする側鎖を有する芳香族炭化水素の側鎖
塩素化方法。
1. One or more amine compounds selected from alkylamines, nitrogen-containing heterocyclic amines, and alkanolamines are added to a solution of an aromatic hydrocarbon having a side chain using an aliphatic polyhalogenated hydrocarbon as a solvent. to contain,
A method for chlorinating an aromatic hydrocarbon having a side chain, the method comprising: then contacting the aromatic hydrocarbon with chlorine under irradiation with ultraviolet rays.
JP51153088A 1976-12-20 1976-12-20 Method for side chain chlorination of aromatic hydrocarbons having side chains Expired JPS6019283B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP51153088A JPS6019283B2 (en) 1976-12-20 1976-12-20 Method for side chain chlorination of aromatic hydrocarbons having side chains

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP51153088A JPS6019283B2 (en) 1976-12-20 1976-12-20 Method for side chain chlorination of aromatic hydrocarbons having side chains

Publications (2)

Publication Number Publication Date
JPS5377022A JPS5377022A (en) 1978-07-08
JPS6019283B2 true JPS6019283B2 (en) 1985-05-15

Family

ID=15554703

Family Applications (1)

Application Number Title Priority Date Filing Date
JP51153088A Expired JPS6019283B2 (en) 1976-12-20 1976-12-20 Method for side chain chlorination of aromatic hydrocarbons having side chains

Country Status (1)

Country Link
JP (1) JPS6019283B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3938691A1 (en) * 1989-11-22 1991-05-23 Bayer Ag METHOD FOR PRODUCING 3-METHYL-BENZYL CHLORIDE

Also Published As

Publication number Publication date
JPS5377022A (en) 1978-07-08

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