JPS609739B2 - Method for producing diarylamine - Google Patents
Method for producing diarylamineInfo
- Publication number
- JPS609739B2 JPS609739B2 JP55125163A JP12516380A JPS609739B2 JP S609739 B2 JPS609739 B2 JP S609739B2 JP 55125163 A JP55125163 A JP 55125163A JP 12516380 A JP12516380 A JP 12516380A JP S609739 B2 JPS609739 B2 JP S609739B2
- Authority
- JP
- Japan
- Prior art keywords
- moles
- phenol
- aniline
- diarylamine
- reaction
- 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
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Description
【発明の詳細な説明】
従来ジアリールァミンの合成法としては、加圧下にァリ
ールアミンの塩酸塩としてアリールアミンを反応させる
方法、加圧下にPC13、CuC12、N比C1、BF
3等を触媒として用い反応させる方法等が知られている
。Detailed Description of the Invention Conventional methods for synthesizing diarylamines include a method in which arylamine is reacted as a hydrochloride of arylamine under pressure, PC13, CuC12, N ratio C1, BF
A method of reacting using No. 3 or the like as a catalyst is known.
しかし、アニリンがフェノールを原料として工業的に製
造されている今日、より安価なフェノールとアニリンと
から脱水縮合反応でジフェニルアミンの合成が出来れば
、原料費面で有利になる事は明らかである。従来からも
、アリールアミンとフェノール類とから脱水縮合反応で
ジアリールアミンを合成する方法がなかった訳ではなく
、塩化亜鉛等を触媒とする方法があるが、収率の低いの
が欠点となっている。本発明者等はアリールアミンとフ
ェノール類の縮合触媒についているいる検討した結果、
リン酸系統の化合物、即ちオルトリン酸、ピロリン酸、
メタリン酸、五酸化リン、ポリリン酸、亜リン酸等が有
効である事を知ったが、上記の脱水縮合反応が高温下で
の反応であることを考慮して装置の腐食を伴わない触媒
について更に検討を重ねた結果、亜リン酸のフェニル及
びアルキルフェニルェステル類を用いると腐食が殆んど
ないばかりでなく、得られるジアリールアミンの収率及
び品質が特に良くなる事を見出し本発明をなすに致つた
。However, today, when aniline is industrially produced from phenol as a raw material, it is clear that it would be advantageous in terms of raw material costs if diphenylamine could be synthesized from cheaper phenol and aniline through a dehydration condensation reaction. This does not mean that there has not been a conventional method of synthesizing diarylamine from arylamine and phenols through a dehydration condensation reaction, and there is a method using zinc chloride as a catalyst, but the disadvantage is that the yield is low. There is. As a result of the present inventors' study on the condensation catalyst of arylamine and phenols,
Compounds of the phosphoric acid family, i.e. orthophosphoric acid, pyrophosphoric acid,
I learned that metaphosphoric acid, phosphorus pentoxide, polyphosphoric acid, phosphorous acid, etc. are effective, but considering that the above dehydration condensation reaction is a reaction at high temperatures, I am looking for a catalyst that does not cause corrosion of the equipment. As a result of further studies, we discovered that when phenyl and alkylphenyl esters of phosphorous acid are used, not only is there almost no corrosion, but the yield and quality of the diarylamine obtained is particularly good. I ended up with eggplant.
本発明の更なる特徴は、出発原料を選べば、非対称のジ
アリールアミンの合成も可能な事にある。即ち、アニリ
ンとアルキルアニリンの如き、アリールアミン同志から
出発して脱アンモニア縮合すると、生成物はジフェニル
アミン、モノアルキルジフェニルアミン及びジアルキル
ジフェニルアミンの混合物となるが、フェノール又はア
ルキルフェノールとアニリン又はアルキルアニリンから
出発して脱水縮合を行うと、任意の位置にアルキル置換
基を有するモノアルキルジフェニルアミン及びジアルキ
ルジフェニルアミンの合成が可能な事にある。更に又本
発明の特徴とするところは、通常予想されるフェノール
類同志の縮合によるジフェニルェーテル類の副生が全く
なく、目的とするジアリールアミンのみが選択的に高収
率、高純度で得られる点にある。本発明を実施するに当
り、フェノール類としては、フェノール、クレゾール、
エチルフヱノ−ル、キシレノール等が使用可能であり、
アリールアミンとしてはアニリン、エチルアニリン、ジ
メチルアニリン、トリメチルアニリン、トルイジンなど
が使用可能である。A further feature of the present invention is that it is possible to synthesize asymmetric diarylamines by selecting starting materials. That is, when deammoniated condensation starts from an arylamine such as aniline and an alkylaniline, the product is a mixture of diphenylamine, monoalkyldiphenylamine and dialkyldiphenylamine, whereas starting from phenol or alkylphenol and aniline or alkylaniline, By performing dehydration condensation, it is possible to synthesize monoalkyldiphenylamines and dialkyldiphenylamines having an alkyl substituent at any position. Furthermore, the present invention is characterized in that there is no by-product of diphenyl ethers due to the condensation of phenols, which is normally expected, and only the target diarylamine is selectively produced in high yield and purity. It's in the point where you can get it. In carrying out the present invention, phenols include phenol, cresol,
Ethylphenol, xylenol, etc. can be used,
As the arylamine, aniline, ethylaniline, dimethylaniline, trimethylaniline, toluidine, etc. can be used.
原料であるフェノール類とアリールアミンの仕込みモル
比は、フェノール類の方を1〜10モル倍過剰に用いる
のが好ましい。特に好ましくは2〜3モル倍である。触
媒濃度は仕込原料混合液に対し、0.5〜1の重量%が
好ましく、反応時間を考慮すると2〜5重量%が特に好
ましい。反応温度は200〜450q0、特に好ましく
は300〜350oCの範囲である。反応は生成水を逐
次系外に蟹出させながら行う。反応液は禾反応原料、目
的物以外は極〈小量のタール化物を含むだけなので、単
純な蒸留で容易に高純度のジアリールアミンを得ること
が出来る。以下実施例をもって本発明を更に具体的に説
明するが、本発明はこれ等の実施例に限定されるもので
はない。Regarding the molar ratio of the raw materials phenols and arylamines, it is preferable to use 1 to 10 times the molar excess of the phenols. Particularly preferably, it is 2 to 3 times the mole amount. The catalyst concentration is preferably 0.5 to 1% by weight, and particularly preferably 2 to 5% by weight, based on the raw material mixture. The reaction temperature ranges from 200 to 450 qO, particularly preferably from 300 to 350 oC. The reaction is carried out while the produced water is successively removed from the system. Since the reaction solution contains only a very small amount of tar compound other than the reaction raw materials and the target product, a highly pure diarylamine can be easily obtained by simple distillation. The present invention will be explained in more detail below with reference to Examples, but the present invention is not limited to these Examples.
実施例 1
鷹梓機、温度計、圧力計、生成水蟹出ライン及び冷却器
を備えたオートクレープにフェノール376.4夕(4
モル)、アニリン186.2夕(2モル)、トリフェニ
ルフオスフアイト17夕(3%対仕込フェノール、アニ
リン)を仕込み「密閉後、蝿梓昇温し、33000とす
る。Example 1 Phenol 376.4 hours (4 hours
After charging, 186.2 moles of aniline (2 moles) and 17 moles of triphenyl phosphorite (3% to phenol and aniline) were sealed, and the temperature was raised to 33,000 mol.
その時の圧力は約17k9/地。以後33〜34000
を保って2時間毎に圧を抜いて(約20→16k9/地
)水を蟹出させながら、1加持間反応を行なった。得ら
れた反応液を蒸留すると、禾反応フェノール278.3
夕(2.957モル)、未反応アニリン63.9夕(0
.686モル)が回収され、ジフェニルアミン191.
3夕(1.130モル)を得た。消費フェノール及びア
ニリンに対するジフェニルアミン収率は95.3%(対
理論)。得られたジフェニルアミンは極めて品質良好で
APHA70、F.P.529ooであった。実施例
2
フェノール376.4夕(4モル)、p−トルイジン2
14.3夕(2モル)、トリフエニルフオスフアイト1
7夕を実施例1と同様に反応させた。The pressure at that time was approximately 17k9/earth. From then on 33-34000
The reaction was carried out for one holding while maintaining the pressure and releasing the pressure every 2 hours (approximately 20 to 16 k9/kg) to allow water to come out. When the resulting reaction solution was distilled, the resulting reaction phenol was 278.3
(2.957 mol), unreacted aniline 63.9 mol (0
.. 686 moles) were recovered and 191.6 moles of diphenylamine were recovered.
3 (1.130 mol) was obtained. Diphenylamine yield based on consumed phenol and aniline is 95.3% (vs. theory). The obtained diphenylamine was of very good quality and had an APHA70, F. P. It was 529oo. Example
2 Phenol 376.4 moles (4 mol), p-toluidine 2
14.3 (2 moles), triphenylphosphite 1
7 days were reacted in the same manner as in Example 1.
生成物は4−メチルジフェニルアミンと極く少量の4・
4−ジメチルジフエニルアミンであり、ジフエニルエー
テルは認められなかった。反応液を蒸留すると未反応フ
ェノール283.4夕(3.015モル)、未反応Pー
トルィジン78.9夕(0.737モル)が回収され、
4ーメチルジフェニルアミン164.6(0.899モ
ル)が得られた。消費フェノール及びpートルィジンに
対する理論収率は80%であった。実施例 3
pークレゾール432.5夕(4モル)、アニリン18
6.2夕(2モル)、トリフエニルフオスフアイト17
夕を実施例1と同様に反応させると、生成物は4ーメチ
ルジフェニルアミンと少量のジフェニルアミンであり、
4−メチルジフェニルアミンの収率は消費pークレゾー
ル及びアニリンに対し理論の76%、M円は89o○で
あった。The product is 4-methyldiphenylamine and a very small amount of 4.
It was 4-dimethyldiphenylamine, and no diphenyl ether was observed. When the reaction solution was distilled, 283.4 moles (3.015 moles) of unreacted phenol and 78.9 moles (0.737 moles) of unreacted P-toluidine were recovered.
164.6 (0.899 mol) of 4-methyldiphenylamine were obtained. The theoretical yield based on consumed phenol and p-toluidine was 80%. Example 3 p-cresol 432.5 moles (4 moles), aniline 18
6.2 (2 moles), triphenylphosphite 17
When the mixture is reacted in the same manner as in Example 1, the products are 4-methyldiphenylamine and a small amount of diphenylamine,
The yield of 4-methyldiphenylamine was 76% of theory based on the consumed p-cresol and aniline, and the M circle was 89 o.
Claims (1)
類を触媒として、加圧下に200〜450℃の温度範囲
でアリールアミンとフエノール類を脱水縮合させる事を
特徴とするジアリールアミンの製造方法。1. A method for producing a diarylamine, which comprises dehydrating and condensing an arylamine and a phenol under pressure in a temperature range of 200 to 450°C using a phenyl or alkyl phenyl ester of phosphorous acid as a catalyst.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP55125163A JPS609739B2 (en) | 1980-09-09 | 1980-09-09 | Method for producing diarylamine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP55125163A JPS609739B2 (en) | 1980-09-09 | 1980-09-09 | Method for producing diarylamine |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5748946A JPS5748946A (en) | 1982-03-20 |
JPS609739B2 true JPS609739B2 (en) | 1985-03-12 |
Family
ID=14903431
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP55125163A Expired JPS609739B2 (en) | 1980-09-09 | 1980-09-09 | Method for producing diarylamine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS609739B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4684527A (en) * | 1984-10-04 | 1987-08-04 | Kikkoman Corporation | Process for producing seasoning |
JPS6251953A (en) * | 1985-08-29 | 1987-03-06 | Fuji Oil Co Ltd | Production of ungelatinized soybean protein |
JPH0697971B2 (en) * | 1986-04-09 | 1994-12-07 | 正田醤油株式会社 | Seasoning manufacturing method |
-
1980
- 1980-09-09 JP JP55125163A patent/JPS609739B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5748946A (en) | 1982-03-20 |
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