JPH0747553B2 - Process for producing dichloro- (2,2) -paracyclophane - Google Patents

Process for producing dichloro- (2,2) -paracyclophane

Info

Publication number
JPH0747553B2
JPH0747553B2 JP34223089A JP34223089A JPH0747553B2 JP H0747553 B2 JPH0747553 B2 JP H0747553B2 JP 34223089 A JP34223089 A JP 34223089A JP 34223089 A JP34223089 A JP 34223089A JP H0747553 B2 JPH0747553 B2 JP H0747553B2
Authority
JP
Japan
Prior art keywords
paracyclophane
reaction
dichloro
yield
solution
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 - Lifetime
Application number
JP34223089A
Other languages
Japanese (ja)
Other versions
JPH03206056A (en
Inventor
宏 丸山
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.)
Daisan Kasei Co Ltd
Original Assignee
Daisan Kasei 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 Daisan Kasei Co Ltd filed Critical Daisan Kasei Co Ltd
Priority to JP34223089A priority Critical patent/JPH0747553B2/en
Priority to CA002032714A priority patent/CA2032714C/en
Priority to DE90125764T priority patent/DE69005092T2/en
Priority to EP93106300A priority patent/EP0558096B1/en
Priority to DE69026119T priority patent/DE69026119T2/en
Priority to EP90125764A priority patent/EP0436957B1/en
Publication of JPH03206056A publication Critical patent/JPH03206056A/en
Priority to US07/913,742 priority patent/US5679874A/en
Publication of JPH0747553B2 publication Critical patent/JPH0747553B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 産業上の利用分野 本発明は下記構造式 で表されるジクロロ−(2,2)−パラシクロファンの製
造方法に関するものである。本化合物はポリジクロロパ
ラキシリレン樹脂製造の際の中間化合物として既知の物
質で、この樹脂は真空蒸着により材料表面に膜として形
成され、電気特性、高温特性等に優れた性能を有し、半
導体等電子部品や宇宙機器用部品等の被覆に広く用いら
れる。
DETAILED DESCRIPTION OF THE INVENTION Industrial Field of the Invention The present invention relates to a method for producing dichloro- (2,2) -paracyclophane represented by This compound is a substance known as an intermediate compound in the production of polydichloroparaxylylene resin, and this resin is formed as a film on the material surface by vacuum deposition and has excellent performance in electrical characteristics, high temperature characteristics, etc. Widely used for coating electronic components and parts for space equipment.

従来の技術 このジクロロ−(2,2)−パラシクロファンは(2,2)パ
ラシクロファンの直接塩素化により造られるか、又は、
2又は3(以下2(3)で表示)−クロロ−p−メチル
ベンジルクロライドより、(2,2)−パラシクロファン
と同様、第四級アンモニウム塩、第四級アンモニウムヒ
ドロキシドを経てホフマン脱離反応により造られる(特
開昭63−93740号公報、特開昭64−45322号公報等)。そ
して、この後者の製造方法の出発物質である2(3)−
クロロ−p−メチルベンジルクロライドあるいは2−ク
ロロ−p−キシレンを塩素化して造られる。
PRIOR ART This dichloro- (2,2) -paracyclophane is made by direct chlorination of (2,2) paracyclophane, or
From 2 or 3 (hereinafter referred to as 2 (3))-chloro-p-methylbenzyl chloride, Hofmann desorption is carried out via a quaternary ammonium salt and a quaternary ammonium hydroxide, similarly to (2,2) -paracyclophane. It is produced by a separation reaction (JP-A-63-93740, JP-A-64-45322, etc.). 2 (3)-which is the starting material of this latter production method
It is produced by chlorinating chloro-p-methylbenzyl chloride or 2-chloro-p-xylene.

発明が解決しようとする問題点 (2,2)パラシクロファンの直接塩素化法は収率はよい
が、その重合生成物であるポリモノクロロパラキシリレ
ン樹脂の性能を劣化させるアルファ塩素置換体の副生を
なくすることも、又、その除去も困難である。
Problems to be Solved by the Invention (2,2) Although the yield of the direct chlorination method of paracyclophane is good, the alpha chlorinated compound which deteriorates the performance of the polymerization product polymonochloroparaxylylene resin It is difficult to eliminate by-products and remove them.

ホフマン脱離反応を経由する後者の方法の問題点の一つ
は、2(3)−クロロ−p−メチルベンジルクロライド
の製造である。この製造方法としては、前述のように (A)、(B)二つのルートがあるがいずれの方法も製
造は煩雑で、しかも、反応で選択的にベンゼン核の一塩
素置換体のみを得ることはできず、出発物質や多塩素置
換体の混合物からの分離が必要となるが、これらの分離
精製はかなり困難であり、結果として、安価な、純度の
よいジクロロ−(2,2)−パラシクロファンが市場に存
在しない原因の一つとなっている。
One of the problems with the latter method via the Hoffmann elimination reaction is the production of 2 (3) -chloro-p-methylbenzyl chloride. As this manufacturing method, as described above Although there are two routes (A) and (B), the production is complicated in both methods, and furthermore, it is not possible to selectively obtain only the monochlorinated benzene nucleus by the reaction, and the starting material and polychlorinated substitution are not possible. Separation from the body mixture is required, but these separations and purifications are rather difficult, resulting in one of the reasons why cheap, pure dichloro- (2,2) -paracyclophane does not exist in the market. It has become one.

他の問題点としてはホフマンン脱離反応における収率の
問題があり、この問題点の解決のために種々の提案がな
されている(前記公開特許公報)。
Another problem is the problem of yield in the Hoffmann elimination reaction, and various proposals have been made to solve this problem (the above-mentioned Japanese Patent Laid-Open Publication).

本発明の目的は第1の問題点の解決にある。即ち、より
容易に、かつ、選択的に一塩素置換体を得る方法を提供
し、結果として、安価で純度のよいジクロロ−(2,2)
−パラシクロファンの製造を可能ならしめようとするも
のである。
An object of the present invention is to solve the first problem. That is, a method for more easily and selectively obtaining a monochlorinated product is provided, and as a result, dichloro- (2,2), which is inexpensive and has high purity,
-The aim is to make the production of paracyclophane possible.

問題点を解決するための手段 本発明者は、この問題解決のため研究を続けた結果、い
ままでの反応ルートとは異なり下記反応式 に示すように第四級アンモニウム塩を塩素化することに
より選択的にベンゼン核の一塩素置換体が生成すること
を見出した。この第四級アンモニウム塩の塩素化ではp
−メチルベンジルクロライドあるいは2−クロロ−pキ
シレンの塩素化とは異なり、その水溶液に塩素ガスを吹
込むだけで選択的にそのベンゼン核の一塩素置換体だけ
が生成することは驚くべき発見であった。
Means for Solving the Problems As a result of continuing the research for solving the problem, the present inventor was different from the conventional reaction route and the following reaction formula It was found that the chlorination of the quaternary ammonium salt selectively produces monochlorinated benzene nuclei as shown in FIG. In chlorination of this quaternary ammonium salt, p
It is a surprising finding that, unlike the chlorination of -methylbenzyl chloride or 2-chloro-p-xylene, only the monochlorinated form of the benzene nucleus is selectively formed by blowing chlorine gas into the aqueous solution. It was

この第四級アンモニウム塩、即ち、p−メチルベンジル
トリメチルアンモニウムクロライドは、p−メチルベン
ジルクロライドのエーテル等の溶液中にトリメチルアミ
ンを吹込み反応させて造ることが一般的であるが、トリ
メチルアミン水溶液を使用して造る方法が操作上簡単で
ある。両者は混合して撹拌するだけで反応し、反応が終
わると均一な液体となる。発熱があるから状況に応じて
冷却する。反応は室温でも進行する。次に、この反応溶
液に、撹拌しながら塩素ガスを導入する。反応熱により
内温が上昇するから適宜冷却する。反応温度は特に限定
しないが高すぎると以下に述べる分解反応等が起き収率
が低下し、低すぎると沈澱が生成するため撹拌に支障が
生じるため60〜0℃の範囲が望ましい。
This quaternary ammonium salt, that is, p-methylbenzyltrimethylammonium chloride is generally produced by blowing trimethylamine into a solution of p-methylbenzyl chloride ether or the like, but an aqueous trimethylamine solution is used. Is easy to operate. Both react by simply mixing and stirring, and when the reaction ends, a uniform liquid is formed. There is fever, so cool it depending on the situation. The reaction proceeds even at room temperature. Next, chlorine gas is introduced into this reaction solution while stirring. Since the internal temperature rises due to the heat of reaction, it is appropriately cooled. The reaction temperature is not particularly limited, but if it is too high, the decomposition reaction and the like described below will occur and the yield will decrease, and if it is too low, precipitation will occur and stirring will be hindered.

反応の進行状態はガスクロマトグラフィー(以下、GC)
分析等で追跡できる。この第四級アンモニウム塩は温度
が高いと下式 のように分解するから、これを利用し反応進行状況を知
ることができる。GC分析上のp−メチル−ベンジルクロ
ライドが検出されなくなったら塩素の吹込みを中止す
る。過剰の塩素は窒素等の不活性ガスを吹込み、できる
だけ追出しておく。
The progress of the reaction is gas chromatography (GC)
It can be traced by analysis etc. This quaternary ammonium salt has the following formula when the temperature is high. Since it decomposes like this, it is possible to know the progress of the reaction by utilizing this. When no p-methyl-benzyl chloride is detected by GC analysis, stop blowing chlorine. Excess chlorine is blown out as much as possible by blowing an inert gas such as nitrogen.

次に、この溶液にジオキサンと苛性アルカリを加え、加
熱しホフマン脱離反応を行う。このホフマン脱離反応前
に水素化ほう素ナトリウム(以下、SBH)等の還元剤を
加えると生成物の着色を減ずることができる。
Next, dioxane and caustic are added to this solution and heated to carry out the Hoffman elimination reaction. Coloring of the product can be reduced by adding a reducing agent such as sodium borohydride (hereinafter, SBH) before the Hoffmann elimination reaction.

実施例 以下に本発明の実施例を示すがこれは単に本発明の具体
例を示すためのものであってこれによって本発明が限定
されるものではないことは当然である。
Examples Examples of the present invention will be shown below, but it should be understood that the present invention is not intended to limit the present invention, which is merely for showing specific examples of the present invention.

実施例1 p−メチルベンジルクロライド14gと30%トリメチルア
ミン水溶液24gを水冷しつつ撹拌した。溶液が均一透明
になったら、この溶液に塩素ガスを吹込み反応を行っ
た。発熱により内温が上昇するが20℃以上にならないよ
うにした。
Example 1 14 g of p-methylbenzyl chloride and 24 g of a 30% trimethylamine aqueous solution were stirred while cooling with water. When the solution became uniform and transparent, chlorine gas was blown into the solution to carry out the reaction. The internal temperature rose due to heat generation, but it was controlled so that it did not rise above 20 ° C.

GC分析でp−メチルベンジルクロライドのピークが検出
されなくなった時点を反応の終点とした。後、窒素を吹
込み過剰の塩素を追出し、これに160mlのジオキサンを
加えた。これに85%水酸化カリウム38g/水34ml溶液を内
温40℃以下に保つようにして撹拌しつつ滴下、更にSBH
(水素化ほう素ナトリウム12%、水酸化ナトリウム40%
水溶液、以下同じ)2ml加えた。以後、約2時間30分を
かけ80℃まで昇温し、その温度で40時間反応をつづけ
た。反応物を水にあけ、沈澱物を取、洗浄、乾燥し
た。沈澱物はトルエン70mlに加温溶解、不溶物を除去、
トルエンを留去しジクロロ−(2,2)−パラシクロファ
ンを得た。
The end point of the reaction was the time when the peak of p-methylbenzyl chloride was not detected by GC analysis. After that, nitrogen was blown in to drive off excess chlorine, and 160 ml of dioxane was added thereto. 85% potassium hydroxide 38g / water 34ml solution was added dropwise to this while stirring while keeping the internal temperature below 40 ℃.
(Sodium borohydride 12%, sodium hydroxide 40%
2 ml of an aqueous solution, the same applies hereinafter) was added. Thereafter, the temperature was raised to 80 ° C. over about 2 hours and 30 minutes, and the reaction was continued at that temperature for 40 hours. The reaction product was poured into water, and the precipitate was collected, washed and dried. The precipitate was dissolved in 70 ml of toluene under heating to remove insoluble matter,
Toluene was distilled off to obtain dichloro- (2,2) -paracyclophane.

なお、(2,2)−パラシクロファン及び三塩素置換体以
上のものはGC分析で検出されないか、又は、無視できる
程度であった(以下の実施例においても同じ)。
In addition, (2,2) -paracyclophane and trichlorinated compounds or more were not detected by GC analysis or were negligible (the same applies to the following examples).

粗製品収量 12.3g 収率 89.1% 不溶物 1.7g 製品収量 10.2g 収率 73.9% 実施例2 p−メチルベンジルクロライド14gと15%トリメチルア
ミン水溶液48gを撹拌混合した。溶液が均一透明になっ
たとき、この溶液に内温5℃以下に保つように冷却しな
がら塩素ガスを吹込み反応を行った。途中、沈澱が析出
し撹拌状態が悪くなったので更に10mlの水を加えた。GC
分析で反応の終了を確認した後、窒素を吹込み過剰の塩
素を追出した。この溶液にジオキサン160mlを加え、撹
拌冷却し、内温20℃以下に保つように粒状85%水酸化カ
リウム及びSBH2mlを加えた。以後約3時間をかけ80℃ま
で昇温し、その温度で40時間反応を続けた。反応終了後
の処理は実施例1と同じ。
Crude product yield 12.3 g Yield 89.1% Insoluble matter 1.7 g Product yield 10.2 g Yield 73.9% Example 2 14 g of p-methylbenzyl chloride and 48 g of 15% aqueous trimethylamine solution were mixed with stirring. When the solution became uniform and transparent, chlorine gas was blown into the solution to carry out the reaction while cooling so that the internal temperature was kept at 5 ° C or lower. During the process, a precipitate was formed and the stirring condition deteriorated, so an additional 10 ml of water was added. GC
After confirming the completion of the reaction by analysis, nitrogen was blown in to drive off excess chlorine. Dioxane (160 ml) was added to this solution, and the mixture was stirred and cooled, and granular 85% potassium hydroxide and SBH (2 ml) were added so that the internal temperature was kept at 20 ° C or lower. Thereafter, the temperature was raised to 80 ° C. over about 3 hours, and the reaction was continued at that temperature for 40 hours. The treatment after the reaction is the same as in Example 1.

粗製品収量 11.9g 収率 86.2% 不溶物 1.9g 製品収量 9.8g 収率 71.0% 実施例3 塩素化温度が50℃以下である以外は実施例1と同じで、
次の結果を得た。
Crude product yield 11.9 g Yield 86.2% Insoluble matter 1.9 g Product yield 9.8 g Yield 71.0% Example 3 Same as Example 1 except that the chlorination temperature was 50 ° C. or lower,
The following results were obtained.

粗製品収量 11.6g 収率 84.1% 不溶物 0.9g 製品収量 10.3g 収率 74.6% 発明の効果 本発明によれば塩素化工程が著しく簡素化され経済的で
あるばかりでなく、容易に純度の高いジクロロ−(2,
2)−パラシクロファンを得ることができる。
Crude product yield 11.6g Yield 84.1% Insoluble matter 0.9g Product yield 10.3g Yield 74.6% Effect of the Invention According to the present invention, not only is the chlorination process significantly simplified and economical, but also the purity is easily high. Dichloro- (2,
2) -Paracyclophane can be obtained.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】下記構造式 を有するジクロロ−(2,2)−パラシクロファンの製造
方法において、p−メチルベンジルトリメチルアンモニ
ウムクロライドを塩素化してモノ−クロロ−p−メチル
ベンジルトリメチルアンモニウムクロライドを合成し、
後、第四級アンモニウムヒドロキシド、ホフマン脱離反
応経由で製造することを特徴とするジクロロ−(2,2)
−パラシクロファンの製造方法。
1. The following structural formula In the method for producing dichloro- (2,2) -paracyclophane having, p-methylbenzyltrimethylammonium chloride is chlorinated to synthesize mono-chloro-p-methylbenzyltrimethylammonium chloride,
After that, dichloro- (2,2), characterized by being produced via a quaternary ammonium hydroxide and Hoffmann elimination reaction
-A method for producing paracyclophane.
【請求項2】塩素化剤が塩素ガスである特許請求の範囲
第1項記載の製造方法。
2. The production method according to claim 1, wherein the chlorinating agent is chlorine gas.
JP34223089A 1989-12-29 1989-12-29 Process for producing dichloro- (2,2) -paracyclophane Expired - Lifetime JPH0747553B2 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP34223089A JPH0747553B2 (en) 1989-12-29 1989-12-29 Process for producing dichloro- (2,2) -paracyclophane
CA002032714A CA2032714C (en) 1989-12-29 1990-12-19 Process for the preparation of dichloro-(2,2)-paracyclophane
DE90125764T DE69005092T2 (en) 1989-12-29 1990-12-28 Process for the preparation of dichloro (2,2) paracyclophane.
EP93106300A EP0558096B1 (en) 1989-12-29 1990-12-28 Process for the preparation of dichloro-(2,2)-paracyclophane
DE69026119T DE69026119T2 (en) 1989-12-29 1990-12-28 Process for the preparation of dichloro (2,2) -paracyclophanes
EP90125764A EP0436957B1 (en) 1989-12-29 1990-12-28 Process for the preparation of dichloro-(2,2)-paracyclophane
US07/913,742 US5679874A (en) 1989-12-29 1992-07-14 Process for the preparation of dichloro-(2,2)-paracyclophane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34223089A JPH0747553B2 (en) 1989-12-29 1989-12-29 Process for producing dichloro- (2,2) -paracyclophane

Publications (2)

Publication Number Publication Date
JPH03206056A JPH03206056A (en) 1991-09-09
JPH0747553B2 true JPH0747553B2 (en) 1995-05-24

Family

ID=18352123

Family Applications (1)

Application Number Title Priority Date Filing Date
JP34223089A Expired - Lifetime JPH0747553B2 (en) 1989-12-29 1989-12-29 Process for producing dichloro- (2,2) -paracyclophane

Country Status (1)

Country Link
JP (1) JPH0747553B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4554110B2 (en) * 2001-05-16 2010-09-29 Kisco株式会社 Binder for DNA chip, DNA chip, and method for producing DNA chip

Also Published As

Publication number Publication date
JPH03206056A (en) 1991-09-09

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