JPS61186353A - Production of ketone - Google Patents

Production of ketone

Info

Publication number
JPS61186353A
JPS61186353A JP2528985A JP2528985A JPS61186353A JP S61186353 A JPS61186353 A JP S61186353A JP 2528985 A JP2528985 A JP 2528985A JP 2528985 A JP2528985 A JP 2528985A JP S61186353 A JPS61186353 A JP S61186353A
Authority
JP
Japan
Prior art keywords
lower alcohol
formula
platinum
catalyst
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.)
Pending
Application number
JP2528985A
Other languages
Japanese (ja)
Inventor
Teruyuki Nagata
永田 輝幸
Nobuyuki Kajimoto
梶本 延之
Katsuji Watanabe
勝治 渡辺
Masatoshi Sakai
堺 正敏
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP2528985A priority Critical patent/JPS61186353A/en
Publication of JPS61186353A publication Critical patent/JPS61186353A/en
Pending legal-status Critical Current

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Pyridine Compounds (AREA)

Abstract

PURPOSE:To obtain the titled compound useful as an intermediate for pharmaceuticals and agricultural chemicals, in high yield, suppressing the dehalogenation reaction, by carrying out the catalytic hydrogenation of a specific anthranyl in the presence of a platinum catalyst and a lower alcohol or a hydrated lower alcohol solvent. CONSTITUTION:The objective aromatic ketone of formula II can be produced by the catalytic hydrogenation of the anthranyl of formula I [X is halogen except for F; A is pyridyl, phenyl or p-halogenophenyl (except for F)] in the presence of a platinum catalyst and a lower alcohol or a hydrated lower alcohol solvent. The catalyst is preferably a platinum-carbon catalyst, and the amount of the platinum metal is 0.01-2.0wt%, preferably 0.03-1.0wt% based on the anthranyl.

Description

【発明の詳細な説明】 産業上の利用分 本発明は芳香族ケトンの製造方法に関する。詳しくは下
記一般式α)のアンスラニルの、C式中Xはフッ素を除
くハロゲン原子を意味し、Aはピリジル、フェニルまた
は。−またはp−ハロゲノフェニル基(但しフッ素を除
く)を意味する。〕 接触水素化反応による下記一般i(m)の−11−鴬嘘
hトンの製造において、脱ハロゲン反応を抑制して高収
率で得る方法に関する。
DETAILED DESCRIPTION OF THE INVENTION Industrial Application The present invention relates to a process for producing aromatic ketones. Specifically, in the anthranyl of the following general formula α), in the formula C, X means a halogen atom excluding fluorine, and A is pyridyl, phenyl or. - or p-halogenophenyl group (excluding fluorine). ] The present invention relates to a method for suppressing the dehalogenation reaction and obtaining high yields in the production of the following general i(m) by catalytic hydrogenation reaction.

(式中X及びAは式(I)と同一) の極めて有用な中間体である。(In the formula, X and A are the same as in formula (I)) It is an extremely useful intermediate for

五速II■L 核にハロゲン基を含有した2−アミノフェニルアリール
ケトンまたは2−アミノフェニルピリジルケトンの製造
法には、安臭香酸クロリドとp −ハロゲノアニリンよ
りフリーデルざラフト反応により合成する方法〔ジャー
ナル、オプ、オルガニックケミストリ(J、O,C) 
 29巻、2856頁、(1962))、相当するアン
スラニルを鉄粉還元する方法〔有機化合物合成法、20
巻、4頁 〕、また本発明方法に類似の接触水素化する
方法において、触媒として10%pd−炭素を使用して
酢酸エチル溶媒中で反応させる方法〔ジャーナル、オブ
、オルガニックケミストリ(J、 O,C,)、27巻
、1929頁(1962))  や、鉄含有パラジウム
触媒使用下低級アルコール溶媒中で反応させる方法〔特
公昭41−223851などが知られている。
Five-speed II■L A method for producing 2-aminophenyl aryl ketone or 2-aminophenyl pyridyl ketone containing a halogen group in the nucleus is to synthesize it from benbrozoic acid chloride and p-halogenoaniline by Friedel-Zaraft reaction. Methods [Journal, Op, Organic Chemistry (J, O, C)
29, p. 2856, (1962)), a method for reducing the corresponding anthranil with iron powder [Organic Compound Synthesis Method, 20
Volume, page 4], and a catalytic hydrogenation method similar to the method of the present invention in which the reaction is carried out in an ethyl acetate solvent using 10% PD-carbon as a catalyst [Journal of Organic Chemistry (J, O, C, ), Vol. 27, p. 1929 (1962)) and a method of reacting in a lower alcohol solvent using an iron-containing palladium catalyst [Japanese Patent Publication No. 41-223851, etc. are known.

発明が解決しようとする問題1、 しかしながら、前記従来法の、フリーデルクラフト反応
においては、収率が20チ前後と極めて低く、マた鉄粉
還元法においては、排水及び廃棄物処理に多大の費用を
要す等の欠点を有し、工業的製法とは言い難い。
Problem 1 to be solved by the invention: However, in the Friedel-Crafts reaction, which is the conventional method, the yield is extremely low at around 20 cm, and in the maize iron powder reduction method, a large amount of waste water and waste treatment is required. It has drawbacks such as being expensive and cannot be called an industrial manufacturing method.

これらの改良法として前記パラジウム系触媒使用下、対
応するアントラニルの接触水素化による芳香族ケトンの
製法が開発されたが、本発明者等が詳細に追試した所に
よれば、無視できない数チの脱ハロゲン化生成物が生じ
、目的生成物の収率低下が認められた。この点は前記特
公昭41−22385公報明細書及び実施例中に、理論
水素吸収量が吸収されるや否や反応を中止する必要があ
る旨の記載があ全点からも容易に予想される所であり、
事実本発明者等の追試でも水素吸収は理論量で停止する
ことなく持続する事が認められた。
As an improvement on these methods, a method for producing aromatic ketones by catalytic hydrogenation of the corresponding anthranils using the palladium-based catalyst was developed, but according to the inventors' detailed follow-up experiments, several molecules that cannot be ignored are present. A dehalogenated product was produced, and a decrease in the yield of the desired product was observed. This point can be easily expected from the fact that the specification and examples of the above-mentioned Japanese Patent Publication No. 41-22385 state that it is necessary to stop the reaction as soon as the theoretical amount of hydrogen is absorbed. and
In fact, in additional tests conducted by the present inventors, it was confirmed that hydrogen absorption continued at the theoretical amount without stopping.

また本発明者等の検討によれば、この脱クロル反応は水
の存在下においてさらに加速されるので、原料や溶媒か
ら持込む水分の管理、ひいては回収再使用される溶媒中
の水分の管理にも注意を要す事も判明した。
In addition, according to the studies conducted by the present inventors, this dechlorination reaction is further accelerated in the presence of water, so it is important to manage the moisture brought in from raw materials and solvents, and even the moisture in solvents that are recovered and reused. It has also become clear that caution is required.

。 を  するだ の手段 本発明者等は上記欠点の無い、工業的に極めて有利な、
前記一般式〇)で示されるアンスラニルの接触水素化に
よる、前記一般式(n)で示される芳香族ケトンの製造
方法につき鋭意検討した結果、低級アルコール溶媒の存
在下に、触媒として白金。
. The present inventors have developed an extremely industrially advantageous method that does not have the above disadvantages.
As a result of intensive studies on a method for producing an aromatic ketone represented by the general formula (n) by catalytic hydrogenation of anthranil represented by the general formula (0), platinum was used as a catalyst in the presence of a lower alcohol solvent.

触媒を使用することにより、脱ハロゲン生成物の抑制さ
れた高品質の芳香族ケトンを製造できる事を見い出した
We have discovered that by using a catalyst, it is possible to produce high-quality aromatic ketones with suppressed dehalogenation products.

またその際、水素吸収は理論量付近で完全に停止する為
極めて反応の終点が明確であり、この傾向は含水低級ア
ルコール溶媒を使用しても影響はV なく、そのためアンスラニブの洗浄に水を多量に使用す
ることを可能にし、アンスラニルの乾燥の必要がなくな
り、工程が簡略化され、また含水アルコールを使用して
もさしつかえなく極めて有利な方法である。
In addition, since hydrogen absorption completely stops near the theoretical amount, the end point of the reaction is extremely clear, and this trend has no effect even if a water-containing lower alcohol solvent is used, so a large amount of water is used to wash anthranib. It is an extremely advantageous method that eliminates the need for drying anthranil, simplifies the process, and allows use of hydrous alcohol without any problems.

本発明において使用される原料、即ち一般式(I)で示
されるアンスラニルは下記一般式(III)、(式中人
は前記と同一) の化合物とp−ニトロハロゲノベンゼンとを反応させる
公知の方法により製造される。(例えば前記「有機化合
物合成法」参照) この1反応は通常低級アルコール及
び水中で水酸化ナトリウム等塩基の存在下に実施されて
おり、本発明方法においては、得られた一般式(I)化
合物を必ずしも単離して用いる必要はない。
The raw material used in the present invention, that is, anthranyl represented by general formula (I), can be obtained by a known method of reacting a compound of the following general formula (III) (in which the characters are the same as above) with p-nitrohalogenobenzene. Manufactured by. (For example, see the above-mentioned "organic compound synthesis method.") This first reaction is usually carried out in a lower alcohol and water in the presence of a base such as sodium hydroxide, and in the method of the present invention, the obtained compound of general formula (I) It is not necessarily necessary to isolate and use.

本発明方法の接触水素化反応において使用される白金触
媒としては酸化白金、炭素もしくはアルミナ等に担持さ
れた白金触媒が挙げられるが、白金、炭素触媒が好まし
い。その使用量はアントラニルに対し、白金金属量で0
.01〜2.0重量%、好ましくは0.03〜1゜0重
量%で良い。
Examples of the platinum catalyst used in the catalytic hydrogenation reaction of the method of the present invention include platinum oxide, platinum catalysts supported on carbon, alumina, etc., and platinum and carbon catalysts are preferred. The amount used is 0 in terms of platinum metal amount compared to anthranyl.
.. The amount may be 0.01 to 2.0% by weight, preferably 0.03 to 1.0% by weight.

反応に使用される溶媒としてはメタノール、エタノール
、プロパツール等低級アルコールまたはこれらの含水ア
ルコールが挙げられる。特に、原料アンスラニル製造時
の溶媒と同一のものが好ましく、メタノールが最も適す
る0 反応温度は特に限定されないが、好ましくは30〜60
℃で良い。反応圧力は常圧付近が選ばれ、加圧にする必
要性は認められない。
Examples of the solvent used in the reaction include lower alcohols such as methanol, ethanol, and propatool, and water-containing alcohols thereof. In particular, the same solvent as the one used in producing the raw material anthranil is preferred, and methanol is most suitable.The reaction temperature is not particularly limited, but is preferably 30 to 60%.
℃ is fine. The reaction pressure is selected to be around normal pressure, and there is no need to increase the pressure.

以下に実施例を挙げてさらに詳細に説明する。A more detailed explanation will be given below with reference to Examples.

実施例1 撹拌器、温度計及び冷却器を備えた300mJガラス製
フラスコに3−フェニル−5−クロルアンスラニル15
.11(0,065モル)、メタノール90ゴ、及び5
チ白金−炭素(日本エンゲルハルト社品)0.31を仕
込んだ。系内を窒素、続いて水素で置換後、水柱200
〜300snに維持された微圧下に40〜45℃の温度
で反応した。反応は120分後、水素が146ONrn
l吸収された時点で停止した。20分間熟成(この間の
水素吸収は認めなかった)後、冷却し系内を窒素で置換
後触媒を濾過した。F液を濃縮後残渣2−アミノ−5−
クロルベンゾフェノン15.1!iを得た。このものを
液体クロマトグラフィーにより分析した新米反応アンス
ラニルは検出されず、目的生成物99.4%であり、(
理論収率99.7%)副生物の脱クロル体である2−ア
ミノベンゾフェノンは0.2チでありた◎ 実施例2 実施例1に用いたメタノール90m1に水10プを添加
した以外は実施例1と同様に仕込み反応処理した。反応
は水素146ON+a/を吸収されて停止した。分析の
結果、理論収率99.6%で2−アミノ−5−クロルベ
ンゾフェノンを得た。
Example 1 3-Phenyl-5-chloroanthranyl 15 was added to a 300 mJ glass flask equipped with a stirrer, thermometer and condenser.
.. 11 (0,065 mol), methanol 90 g, and 5
0.31 of platinum-carbon (Japan Engelhard Co., Ltd.) was charged. After replacing the system with nitrogen and then with hydrogen, the water column was 200
The reaction was carried out at a temperature of 40-45° C. under micropressure maintained at ˜300 sn. After 120 minutes of reaction, hydrogen was 146ONrn.
It stopped when 1 was absorbed. After aging for 20 minutes (no hydrogen absorption was observed during this period), the system was cooled, the system was purged with nitrogen, and the catalyst was filtered. After concentrating solution F, the residue 2-amino-5-
Chlorbenzophenone 15.1! I got i. When this product was analyzed by liquid chromatography, no anthranil was detected, and the target product was 99.4%.
(Theoretical yield: 99.7%) The amount of 2-aminobenzophenone, which is the dechlorinated by-product, was 0.2%. ◎ Example 2 The procedure was carried out except that 10ml of water was added to 90ml of methanol used in Example 1. The preparation and reaction treatment were carried out in the same manner as in Example 1. The reaction stopped when 146ON+a/ of hydrogen was absorbed. As a result of analysis, 2-amino-5-chlorobenzophenone was obtained with a theoretical yield of 99.6%.

比較例1 5チ白金−炭素が5%パラジウム−炭素である以外実施
例1と同様に仕込んだ。反応は水素146ONm/吸収
した時点で中止した。直ちに冷却後系内を窒素置換して
触媒を濾過した。p液を濃縮後残渣15.19を得た。
Comparative Example 1 A sample was prepared in the same manner as in Example 1 except that 5% palladium-carbon was used instead of 5% palladium-carbon. The reaction was stopped when 146 ONm/hydrogen was absorbed. Immediately after cooling, the system was purged with nitrogen and the catalyst was filtered. After concentrating the p solution, a residue of 15.19% was obtained.

このものを液体クロマトグラフィーにより分析した所、
未反応物15.1%、目的物60.2 %であり(理論
収率71、Oチ)、副生物として製品の脱クロル体であ
る2−アミノ−ベンゾフェノンが5.2%含すれていた
When this substance was analyzed by liquid chromatography,
The unreacted material was 15.1%, the target product was 60.2% (theoretical yield 71, Oti), and the by-product contained 5.2% 2-amino-benzophenone, which is the dechlorinated product. .

比較例2 5%白金−炭素が5%パラジウム−炭素である以益実施
例2と同様に仕込み、反応した。反応は水素吸収量14
6ON−の時点で中止し、実施例2と同様に処理、分析
した。その結果、残渣中目的生成物ss、7%で2−ア
ミノ−5−クロルベンゾフェノンが得られた(理論収率
65.8%)に過ぎず、2−アミノ−ベンゾフェノンが
11.2%含まれていた◎
Comparative Example 2 The preparation and reaction were carried out in the same manner as in Example 2 except that 5% platinum-carbon was replaced by 5% palladium-carbon. The reaction is hydrogen absorption amount 14
The test was stopped at 6ON- and treated and analyzed in the same manner as in Example 2. As a result, the desired product ss in the residue was only 2-amino-5-chlorobenzophenone at 7% (theoretical yield 65.8%), and 2-amino-benzophenone was contained at 11.2%. It was◎

Claims (3)

【特許請求の範囲】[Claims] (1)下記一般式( I )で示されるアンスラニルを、
▲数式、化学式、表等があります▼(I) 〔式中Xはフッ素を除くハロゲン原子を意味し、Aはピ
リジル、フェニルまたはo−もしくはp−ハロゲンフェ
ニル基(但しフッ素は除く)を意味する。〕 白金触媒及び低級アルコールまたは含水低級アルコール
溶媒存在下に接触水素化させることを特徴とする、一般
式(II) ▲数式、化学式、表等があります▼(II) (式中X及びAは、前記式( I )と同じ意味を有する
) で示される芳香族ケトンの製造方法。
(1) Anthranil represented by the following general formula (I),
▲There are mathematical formulas, chemical formulas, tables, etc.▼(I) [In the formula, X means a halogen atom excluding fluorine, and A means pyridyl, phenyl, or o- or p-halogen phenyl group (excluding fluorine) . ] General formula (II) characterized by catalytic hydrogenation in the presence of a platinum catalyst and a lower alcohol or a hydrous lower alcohol solvent ▲There are mathematical formulas, chemical formulas, tables, etc.▼(II) (In the formula, X and A are A method for producing an aromatic ketone represented by the formula (I).
(2)低級アルコールがメタノールである特許請求の範
囲第( I )項記載の方法。
(2) The method according to claim (I), wherein the lower alcohol is methanol.
(3)一般式(II)の化合物が2−アミノ−5−クロル
ベンゾフェノンである特許請求の範囲第(1)項記載の
方法。
(3) The method according to claim (1), wherein the compound of general formula (II) is 2-amino-5-chlorobenzophenone.
JP2528985A 1985-02-14 1985-02-14 Production of ketone Pending JPS61186353A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2528985A JPS61186353A (en) 1985-02-14 1985-02-14 Production of ketone

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2528985A JPS61186353A (en) 1985-02-14 1985-02-14 Production of ketone

Publications (1)

Publication Number Publication Date
JPS61186353A true JPS61186353A (en) 1986-08-20

Family

ID=12161855

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2528985A Pending JPS61186353A (en) 1985-02-14 1985-02-14 Production of ketone

Country Status (1)

Country Link
JP (1) JPS61186353A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104230727A (en) * 2014-08-28 2014-12-24 武汉怡兴化工有限公司 Synthesis technology for producing 2-amino-5-chlorobenzophenone by reducing isoxazole through iron powder
CN106083621A (en) * 2016-05-31 2016-11-09 成都切斯特科技有限公司 A kind of synthetic method of Amiprol pharmaceutical intermediate 2 amino 5 chloro benzophenone
CN106366007A (en) * 2016-08-30 2017-02-01 枣阳市福星化工有限公司 Method for producing 2-amino-5-chlorobenzophenone
CN106380411A (en) * 2016-08-30 2017-02-08 枣阳凤泽精细化工有限公司 Production method of 2-amino-5-chlorobenzophenone
CN106496050A (en) * 2016-08-30 2017-03-15 枣阳市福星化工有限公司 A kind of method of production 2 amino, 5 chlorobenzophenone
CN113861052A (en) * 2021-10-27 2021-12-31 枣阳市福星化工有限公司 Preparation method of 2-amino-5-chlorobenzophenone
CN114957021A (en) * 2022-06-28 2022-08-30 枣阳市福星化工有限公司 Preparation method of medicine intermediate 2-amino-5-chlorobenzophenone

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104230727A (en) * 2014-08-28 2014-12-24 武汉怡兴化工有限公司 Synthesis technology for producing 2-amino-5-chlorobenzophenone by reducing isoxazole through iron powder
CN106083621A (en) * 2016-05-31 2016-11-09 成都切斯特科技有限公司 A kind of synthetic method of Amiprol pharmaceutical intermediate 2 amino 5 chloro benzophenone
CN106366007A (en) * 2016-08-30 2017-02-01 枣阳市福星化工有限公司 Method for producing 2-amino-5-chlorobenzophenone
CN106380411A (en) * 2016-08-30 2017-02-08 枣阳凤泽精细化工有限公司 Production method of 2-amino-5-chlorobenzophenone
CN106496050A (en) * 2016-08-30 2017-03-15 枣阳市福星化工有限公司 A kind of method of production 2 amino, 5 chlorobenzophenone
CN113861052A (en) * 2021-10-27 2021-12-31 枣阳市福星化工有限公司 Preparation method of 2-amino-5-chlorobenzophenone
CN114957021A (en) * 2022-06-28 2022-08-30 枣阳市福星化工有限公司 Preparation method of medicine intermediate 2-amino-5-chlorobenzophenone

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