JPS5859970A - Production of 2,2,4-trimethyl-1,2-dihydroquinoline - Google Patents

Production of 2,2,4-trimethyl-1,2-dihydroquinoline

Info

Publication number
JPS5859970A
JPS5859970A JP56159649A JP15964981A JPS5859970A JP S5859970 A JPS5859970 A JP S5859970A JP 56159649 A JP56159649 A JP 56159649A JP 15964981 A JP15964981 A JP 15964981A JP S5859970 A JPS5859970 A JP S5859970A
Authority
JP
Japan
Prior art keywords
aniline
sulfonic acid
acetone
reaction
acid resin
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.)
Granted
Application number
JP56159649A
Other languages
Japanese (ja)
Other versions
JPS6348868B2 (en
Inventor
Takashi Kojima
隆 小島
Masahisa Shiotani
塩谷 正久
Eizo Okino
沖野 栄三
Masahito Umehara
梅原 正仁
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.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo 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 Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP56159649A priority Critical patent/JPS5859970A/en
Publication of JPS5859970A publication Critical patent/JPS5859970A/en
Publication of JPS6348868B2 publication Critical patent/JPS6348868B2/ja
Granted 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

Abstract

PURPOSE:Polyfluorinated sulfonic acid resin is used as a catalyst to effect the reaction between aniline and acetone to produce the titled compound with increased yield, reduced residual amount of by-products, which is used as an antioxidant. CONSTITUTION:The reaction of aniline with acetone or diacetone alcohol or mesityl oxide is conducted in the presence of a polyfluorinated sulfonic acid resin catalyst to give 2,2,4-trimethyl-1,2-dihydroquinoline. As the polyfluorinated sulfonic acid resin, is preferably used a product by Dupont C. in USA, named Nafion H and the amount is 1-100g per mole of aniline.

Description

【発明の詳細な説明】 本発明は、! 、 2 、4−)ジメチル−1,2−ジ
ヒドロキノリンの製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides the following features: , 2,4-) It relates to a method for producing dimethyl-1,2-dihydroquinoline.

2.2.4−)ジメチル−1,2−ジヒドロキノリンは
高分子物質の老化防止剤として有用な化合物であり、こ
のものは通常−塩酸、ヨウ素などの酸性触媒の存在下、
アニリンにアセトンまたはジアセトンアルコールまたは
メシチルオキシドを加熱状層で作用させ、脱水縮合反応
によって製造されることが知られているが、上記酸性触
媒下の反応時には2,2.4−1−’Jメチルー1.2
−ジヒドロキノリン単量体(以下モノマーと呼ぶ)以外
に、その重合生成物(以下ポリマーと呼ぶ)およびその
他の不純物が種々副生することが知られている。
2.2.4-) Dimethyl-1,2-dihydroquinoline is a compound useful as an anti-aging agent for polymeric materials, which is usually treated in the presence of an acidic catalyst such as hydrochloric acid or iodine.
It is known that aniline is produced by a dehydration condensation reaction by reacting acetone, diacetone alcohol, or mesityl oxide in a heated layer, but when the reaction is carried out under the above acidic catalyst, 2,2.4-1-' J Methyl-1.2
-It is known that in addition to the dihydroquinoline monomer (hereinafter referred to as monomer), its polymerization product (hereinafter referred to as polymer) and other impurities are produced as various by-products.

たとえばアニリンに対してO,OSモル比の塩酸を触媒
として含むアニリンを100℃に保温しながら、5.5
時間にわたってアセトンを作用させる方法、あるいはア
ニリンに対して1/7.5モル比の塩酸を触媒としで含
むアニリンを180〜140℃に保温し、6時間にわた
ってアセトンを作用させる方法等が知られているが、前
者の方法では僅か約2896のそツマ−と約18%の残
液が得られるにすぎず、仕込んだアニリンの大半は未反
応のままであり、後者の方法ではポリマー等の残渣が約
64%であって、モノマーは収率的19%で得られるに
すぎない。
For example, while keeping aniline containing hydrochloric acid as a catalyst at a molar ratio of O and OS to aniline at 100°C,
There are two known methods: one in which acetone is allowed to act on the aniline for a period of time, and another method in which aniline containing hydrochloric acid at a molar ratio of 1/7.5 to aniline is kept at 180 to 140°C and acetone is made to act on it for 6 hours. However, in the former method, only about 2,896 particles and about 18% of the residual liquid are obtained, and most of the charged aniline remains unreacted, while in the latter method, residues such as polymers are obtained. About 64%, the monomer is obtained with a yield of only 19%.

このようなことから本発明者らは2,2.4−トリメチ
ル−1,2−ジヒドロキノリンの製速決について研究を
行い、さきに触媒としてP−トルエンスルホン酸を用い
る方法を見出した(特1j@5$−115587%)が
、CCO方法によりても残渣が19%程度副生し、目的
とするモノマー収率は約60%であった。
For these reasons, the present inventors conducted research on the rapid production of 2,2,4-trimethyl-1,2-dihydroquinoline, and first discovered a method using P-toluenesulfonic acid as a catalyst (Special 1j @5$-115587%), but even with the CCO method, about 19% of the residue was produced as a by-product, and the desired monomer yield was about 60%.

その後、本発明者らはよりすぐれたモノマーの製造法を
開発すべく更に検討した結果、触媒としてポリフッ素化
スルホン酸樹脂を用いることにより、これらの方法によ
る場合よりもモノマーの収率が向上し、残渣量も減少す
ることを見い出し本発明に至った。
Subsequently, the present inventors conducted further studies to develop a better method for producing monomers, and found that by using a polyfluorinated sulfonic acid resin as a catalyst, the yield of monomers was improved compared to those using these methods. The inventors have discovered that the amount of residue is also reduced, leading to the present invention.

すなわち本発明は、アニリンとアセトン(またはジアセ
トンアルコールまたはメシチルオキシド)とを反応させ
て、2,2.4−トリメチル−1,2−ジヒドロキノリ
ン(モノマー)を製造する方法において、ポリフッ素化
スルホン酸樹脂を触媒として用いる仁とにより、モノマ
ーの収率を向上させ、副生残渣量の低減を可能ならしめ
たモノマーの改良製造法である。
That is, the present invention provides a method for producing 2,2,4-trimethyl-1,2-dihydroquinoline (monomer) by reacting aniline with acetone (or diacetone alcohol or mesityl oxide), in which a polyfluorinated This is an improved method for producing monomers that uses a sulfonic acid resin as a catalyst to improve the monomer yield and reduce the amount of by-product residue.

本発明において触媒として用いるポリフッ素化スルホン
酸樹脂(代表的なものとしては米国デュポン社の1品名
ナフィオンHがある)の使用量は特に制限されないが、
反応速度、経済性などの点からアニリン1モルに対して
1〜1001程度が好ましい。
The amount of polyfluorinated sulfonic acid resin used as a catalyst in the present invention (a typical example is Nafion H manufactured by DuPont in the United States) is not particularly limited, but
From the viewpoint of reaction rate, economy, etc., it is preferably about 1 to 1,001 moles of aniline.

その他の反応条件については、従来公知の方法が準用さ
れ、特に制限をうけるものではない。
Regarding other reaction conditions, conventionally known methods can be applied mutatis mutandis, and there are no particular restrictions.

次に本発明を実施例により説明する。Next, the present invention will be explained by examples.

実施例1 アセトン導入装置、温度計、攪拌機、コンデンサーを備
えた5 Q Omj! 4つロフラスコにアニリン12
1P(1,8モル)、ポリフッ素化スルホン酸樹脂57
.2F(スルホン酸基1あたりの分子量を1100とし
て0.052モル相当)を仕込み加熱する。
Example 1 5 Q Omj! equipped with acetone introduction device, thermometer, stirrer and condenser. Aniline 12 in 4 flasks
1P (1.8 mol), polyfluorinated sulfonic acid resin 57
.. 2F (equivalent to 0.052 mol based on the molecular weight of 1100 per sulfonic acid group) is charged and heated.

内温を95〜too’cに保ちながら756tのアセト
ンを8時間で導入する。 留出した未反応のアセトンは
脱水反応で生成した水を含んでいるので精留して回収し
、次回の反応に用いる。 アセトン導入装置後、グラス
フィルターでフラスコの内容物を一過してポリフッ素化
スルホン酸樹脂をF別する。 再び500 m14つ目
フラスコ内にF液を移し、内温を140〜146℃に保
ちながら徐々に減圧にし、未反応のアニリンを回収する
と、減圧度10鱈顯以上で2ipのアニリンが回収され
た。 その後内温を190℃まで上昇し、減圧度を8 
m Hg tでにすると純度96%のモノマー158.
ilが得られ、12.2tの残渣が副生した。
756 tons of acetone is introduced over 8 hours while maintaining the internal temperature at 95-too'c. The distilled unreacted acetone contains water produced by the dehydration reaction, so it is recovered by rectification and used for the next reaction. After the acetone introduction device, the contents of the flask are passed through a glass filter to separate the polyfluorinated sulfonic acid resin. Transfer the F solution into the 14th 500 m flask again and gradually reduce the pressure while keeping the internal temperature at 140-146°C to recover unreacted aniline. 2ip of aniline was recovered at a vacuum level of 10 or higher. . After that, the internal temperature was raised to 190℃, and the degree of vacuum was reduced to 8.
Monomer with a purity of 96% in m Hg t 158.
il was obtained, and 12.2 t of residue was produced as a by-product.

純度換算したときのモノマーの収量は147.8?であ
り、収率は65.6%である。 また副生じた残液12
.2Fは仕込アニリンに対して6.4%に相当する。
The yield of monomer when converted to purity is 147.8? The yield is 65.6%. In addition, residual liquid 12 produced as a by-product
.. 2F corresponds to 6.4% of the charged aniline.

実施例2 ポリフッ素化スルホン酸樹脂を28.6F使用し、反応
温度を105〜110℃とし、アセトンの導入時間を1
2時間とする以外は実施例1と同様にして脱水縮合反応
、後処理を行い、14111(純度95%)のモノマー
と15.6Fの残渣を櫓た。
Example 2 Polyfluorinated sulfonic acid resin was used at 28.6F, the reaction temperature was 105-110℃, and the introduction time of acetone was 1
The dehydration condensation reaction and post-treatment were carried out in the same manner as in Example 1, except that the reaction time was 2 hours, and a monomer of 14111 (purity 95%) and a residue of 15.6F were obtained.

アニリンに対するモノマーの収率4! 6 L、6%、
残渣は6.9%である。
Yield of monomer based on aniline: 4! 6 L, 6%,
The residue is 6.9%.

比較例1 実施例1の方法において、ポリフッ素化スルホン酸II
I 脂のかわりにパラトルエンスルホンII−水jJ[
12,4F(パラトルエンスルホン酸として0.065
モル)を用いる以外は全く同様にして脱水縮合反応を行
い1反応終了後、反応物はトルエン100 malで希
釈し、75〜85°Cに保ちすからNaOH2、6F及
び60峨の水で中和し、静置後分液して水層を除去する
。 油層は100 mlの水で数回洗浄する。 溶液が
中性になったら油層を分取し、トルエンを蒸留によって
除いた後、実施例1の場合と同様4ζ後処理を行い、1
42.4f(純度97%)のモノマーと42.1y−の
残渣を得た・ アニリンに対するモノマーの収率は61.8%、残渣は
18.7影である。
Comparative Example 1 In the method of Example 1, polyfluorinated sulfonic acid II
I Instead of fat, paratoluenesulfone II - water jJ [
12,4F (0.065 as para-toluenesulfonic acid
The dehydration condensation reaction was carried out in exactly the same manner except that 1 mol) was used. After one reaction was completed, the reaction product was diluted with 100 mol of toluene, kept at 75-85°C, and neutralized with NaOH2, 6F and 60 mol of water. After standing still, separate the layers and remove the aqueous layer. The oil layer is washed several times with 100 ml of water. When the solution became neutral, the oil layer was separated, toluene was removed by distillation, and 4ζ post-treatment was performed in the same manner as in Example 1.
A monomer of 42.4f (purity 97%) and a residue of 42.1y- were obtained. The yield of monomer based on aniline was 61.8%, and the residue was 18.7mm.

Claims (1)

【特許請求の範囲】[Claims] アニリンとアセトン(またはジアセトンアルコールまた
はメシチルオキシド)とを反応させるにあたり、触媒と
してlリッツ素化スルホン
When reacting aniline with acetone (or diacetone alcohol or mesityl oxide), a lithium-hydrogenated sulfone is used as a catalyst.
JP56159649A 1981-10-06 1981-10-06 Production of 2,2,4-trimethyl-1,2-dihydroquinoline Granted JPS5859970A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56159649A JPS5859970A (en) 1981-10-06 1981-10-06 Production of 2,2,4-trimethyl-1,2-dihydroquinoline

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56159649A JPS5859970A (en) 1981-10-06 1981-10-06 Production of 2,2,4-trimethyl-1,2-dihydroquinoline

Publications (2)

Publication Number Publication Date
JPS5859970A true JPS5859970A (en) 1983-04-09
JPS6348868B2 JPS6348868B2 (en) 1988-09-30

Family

ID=15698319

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56159649A Granted JPS5859970A (en) 1981-10-06 1981-10-06 Production of 2,2,4-trimethyl-1,2-dihydroquinoline

Country Status (1)

Country Link
JP (1) JPS5859970A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011136330A (en) * 2009-12-30 2011-07-14 Jiangsu Sinorgchem Technology Co Ltd Solid acid catalyst, method for preparing the same and method for synthesizing rubber antioxidant rd

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011136330A (en) * 2009-12-30 2011-07-14 Jiangsu Sinorgchem Technology Co Ltd Solid acid catalyst, method for preparing the same and method for synthesizing rubber antioxidant rd

Also Published As

Publication number Publication date
JPS6348868B2 (en) 1988-09-30

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