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JPH07247240A - Production of lactones and esters - Google Patents

Production of lactones and esters

Info

Publication number
JPH07247240A
JPH07247240A JP6805494A JP6805494A JPH07247240A JP H07247240 A JPH07247240 A JP H07247240A JP 6805494 A JP6805494 A JP 6805494A JP 6805494 A JP6805494 A JP 6805494A JP H07247240 A JPH07247240 A JP H07247240A
Authority
JP
Japan
Prior art keywords
reaction
aromatic ring
producing
ketone
lactone
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
JP6805494A
Other languages
Japanese (ja)
Other versions
JP3802087B2 (en
Inventor
Kiyoomi Kaneda
清臣 金田
Shinji Ueno
晋司 上野
Takuya Matsubara
拓也 松原
Toshinobu Imanaka
利信 今中
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.)
Arakawa Chemical Industries Ltd
Original Assignee
Arakawa Chemical Industries 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 Arakawa Chemical Industries Ltd filed Critical Arakawa Chemical Industries Ltd
Priority to JP06805494A priority Critical patent/JP3802087B2/en
Publication of JPH07247240A publication Critical patent/JPH07247240A/en
Application granted granted Critical
Publication of JP3802087B2 publication Critical patent/JP3802087B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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

Abstract

PURPOSE:To provide a method capable of producing a lactone or a noncyclic ester containing an aromatic ring from a raw material ketone in the absence of a catalyst and even under a mild condition in high yield. CONSTITUTION:In producing a lactone by oxidizing an alicyclic ketone in a liquid phase in the presence of both an aldehyde and oxygen or producing a noncyclic ester containing an aromatic ring by oxidizing a noncyclic ketone containing an aromatic ring in a liquid phase, 0.5-25wt.%, preferably 1-15wt.% based on the raw material ketone of an acid chloride, preferably an aromatic acid chloride (especially benzoyl chloride) is added to the reaction system and the reaction is carried out usually at 0-65 deg.C, preferably 10-40 deg.C. The reaction is preferably done in a solvent system selected from among an aromatic hydrocarbon, an alkyl halide, a halogenated hydrocarbon and an ester in terms of yield of the prepared lactone or ester. Since a metal catalyst is not used, side reactions of the formed product will not occur and after-treatment is simple.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ラクトン類の製造法お
よびエステル類の製造法に関する。詳しくは脂環族ケト
ン類を液相酸化してラクトン類を製造する方法および芳
香環を有する非環状ケトン類を液相酸化して芳香環を有
する非環状エステル類を製造する方法に関する。
TECHNICAL FIELD The present invention relates to a method for producing lactones and a method for producing esters. Specifically, it relates to a method for producing a lactone by liquid-phase oxidation of an alicyclic ketone and a method for producing an acyclic ester having an aromatic ring by liquid-phase oxidation of an acyclic ketone having an aromatic ring.

【0002】[0002]

【従来の技術】ラクトン類および非環状エステル類は、
溶剤、機能性樹脂、医薬品など種々の工業薬品やその合
成中間体などに利用される有用な物質である。かかるラ
クトン類、非環状エステル類の製造法としてはケトン類
のバイヤービリガー反応が一般的である。しかし、この
反応は均一系反応であるため生成物の分離が困難であ
り、また高価な過酸を用いるため経済的に不利である。
BACKGROUND OF THE INVENTION Lactones and acyclic esters are
It is a useful substance used for various industrial chemicals such as solvents, functional resins, and pharmaceuticals, and their synthetic intermediates. As a method for producing such lactones and acyclic esters, the Bayer-Villiger reaction of ketones is generally used. However, since this reaction is a homogeneous reaction, it is difficult to separate products, and an expensive peracid is used, which is economically disadvantageous.

【0003】また、バイヤービリガー反応に類する反応
として、特公昭39−5921号公報には、シクロヘキ
サノンなどの環状ケトン類を触媒、酸素含有ガスおよび
アルデヒド類の存在下に反応させて、ε−カプロラクト
ンなどのラクトン類とカルボン酸類を同時に製造する方
法が開示されている。しかし該方法は、ラクトン類の収
率が低いこと、さらには触媒としてコバルト、マンガ
ン、白金、パラジウム、バナジウム、ルテニウム、ジル
コニウム、アルミニウム、アンチモン、ベリリウムまた
は銅等の重金属化合物を使用するため、触媒の毒性の問
題や、反応生成物と該触媒との分離の問題がある。ま
た、特開昭53−25516号公報では、触媒としてク
ロム化合物を反応系に溶存させることを特徴とするが、
上記と同様、ラクトン類の収率や毒性などの点で不満足
である。また、特公昭55−36667号公報では、環
状ケトン類をアルデヒド類および分子状酸素の存在下に
液相酸化するに際し、過酸を添加することを特徴とする
が、過酸を使用するため安全面および経済面で不利があ
る。また、特開平5−65245号では、無触媒系また
は特公昭39−5921号公報に記載の公知のコバルト
触媒を用いた製造条件を採用し、且つ環状ケトン類とア
ルデヒド類を限定条件下に反応させれば副生成物を抑制
しうることが記載されているが、無触媒系では収率が十
分ではない。
As a reaction similar to the Bayer-Villiger reaction, Japanese Patent Publication No. 39-5921 discloses that cyclic ketones such as cyclohexanone are reacted in the presence of a catalyst, an oxygen-containing gas and aldehydes to obtain ε-caprolactone. The method for simultaneously producing the lactones and the carboxylic acids is disclosed. However, the method has a low yield of lactones, and further uses a heavy metal compound such as cobalt, manganese, platinum, palladium, vanadium, ruthenium, zirconium, aluminum, antimony, beryllium or copper as a catalyst. There are problems of toxicity and separation of the reaction product and the catalyst. Further, in JP-A-53-25516, a chromium compound is dissolved in a reaction system as a catalyst,
Similar to the above, it is unsatisfactory in terms of yield and toxicity of lactones. Further, JP-B-55-36667 is characterized by adding a peracid when liquid-phase oxidizing cyclic ketones in the presence of aldehydes and molecular oxygen, but is safe because peracid is used. There are disadvantages both economically and economically. Further, in Japanese Unexamined Patent Publication (Kokai) No. 5-65245, manufacturing conditions using a catalyst-free system or a known cobalt catalyst described in JP-B-39-5921 are adopted, and a cyclic ketone and an aldehyde are reacted under limited conditions. Although it is described that by-products can be suppressed by doing so, the yield is not sufficient in the non-catalyst system.

【0004】また、前記公報はいずれも最終目的物をラ
クトン類に限定しており、芳香環を有する非環状ケトン
類からこれに対応するエステル類を合成する方法に関し
ては全く記載されていない。
Further, all of the above publications limit the final product to lactones, and do not describe any method for synthesizing corresponding esters from acyclic ketones having an aromatic ring.

【0005】[0005]

【発明が解決しようとする課題】本発明は、穏やかな反
応条件下に、しかも金属触媒の非存在下においても、ケ
トン類からラクトン類または芳香環を有する非環状エス
テル類を高収率で収得できる新規な製造法を提供するこ
とを目的とする。
DISCLOSURE OF THE INVENTION The present invention provides a high yield of a lactone or an acyclic ester having an aromatic ring from a ketone under a mild reaction condition and in the absence of a metal catalyst. The purpose of the present invention is to provide a new production method that can be used.

【0006】[0006]

【課題を解決するための手段】本発明者らは、前記従来
技術の課題を解決すべく、鋭意研究を重ねた結果、アル
デヒド類および酸素の共存下に原料ケトン類を液相酸化
させるにあたり、酸塩化物を反応系内に添加すれば前記
従来技術の課題を解決しうることを見出した。本発明は
かかる新たな知見に基づいて完成されたものである。
Means for Solving the Problems As a result of intensive studies to solve the above-mentioned problems of the prior art, the present inventors have found that in the liquid-phase oxidation of starting material ketones in the coexistence of aldehydes and oxygen, It has been found that the above-mentioned problems of the prior art can be solved by adding an acid chloride into the reaction system. The present invention has been completed based on this new finding.

【0007】すなわち本発明は、アルデヒド類および酸
素の共存下に脂環族ケトン類を液相酸化してラクトン類
を製造する方法において、反応系内に酸塩化物を添加す
ることを特徴とするラクトン類の製造法、ならびにアル
デヒド類および酸素の共存下に芳香環を有する非環状ケ
トン類を液相酸化して芳香環を有する非環状エステル類
を製造する方法において、反応系内に酸塩化物を添加す
ることを特徴とする芳香環を有する非環状エステル類の
製造法に関する。
That is, the present invention is characterized in that an acid chloride is added to the reaction system in a method for producing a lactone by liquid phase oxidation of an alicyclic ketone in the presence of aldehydes and oxygen. A method for producing a lactone and a method for producing an acyclic ester having an aromatic ring by subjecting an acyclic ketone having an aromatic ring to liquid phase oxidation in the coexistence of an aldehyde and oxygen to produce an acid chloride in the reaction system. And a method for producing an acyclic ester having an aromatic ring.

【0008】本発明における原料である脂環族ケトン類
としては、特に制限なく各種公知のものを使用できる。
その具体例としては、例えばシクロペンタノン、3−メ
チルシクロペンタノン、シクロヘキサノン、2−メチル
シクロヘキサノン、3−メチルシクロヘキサノン、4−
メチルシクロヘキサノン、2−エチルシクロヘキサノ
ン、2−イソプロピル−5−メチルシクロヘキサノン、
2−メトキシシクロヘキサノン、4−メトキシシクロヘ
キサノン、3,3,5−トリメチルシクロヘキサノン、
4−t−ブチルシクロヘキサノン、2,5−メタノシク
ロヘキサノン、シクロヘプタノン、2−アダマンタノン
などがあげられる。
As the alicyclic ketones used as the raw material in the present invention, various known ones can be used without particular limitation.
Specific examples thereof include cyclopentanone, 3-methylcyclopentanone, cyclohexanone, 2-methylcyclohexanone, 3-methylcyclohexanone, 4-
Methylcyclohexanone, 2-ethylcyclohexanone, 2-isopropyl-5-methylcyclohexanone,
2-methoxycyclohexanone, 4-methoxycyclohexanone, 3,3,5-trimethylcyclohexanone,
4-t-butylcyclohexanone, 2,5-methanocyclohexanone, cycloheptanone, 2-adamantanone and the like can be mentioned.

【0009】また、芳香環を有する非環状ケトン類とし
ては、特に制限なく各種公知のものを使用できる。その
具体例としては、例えば4−メトキシアセトフェノン、
4−メチルアセトフェノン、2−エトキシ−2−フェニ
ルアセトフェノン、ベンゾイルアセトン、o−ベンゾイ
ル安息香酸、2−ベンゾイルピリジン、ベンゾフェノ
ン、プロピオフェノン、ペンタノフェノン、4−メトキ
シフェニルシクロプロピルケトン、シクロペンチルフェ
ニルブタノン、ミリストフェノン、ブチロフェノン、ク
ロロフェニルエタノン、ブロモフェニルブタノン、1−
フェニルドデカフェノン、ヘプタノフェノンなどがあげ
られる。
As the acyclic ketone having an aromatic ring, various known ones can be used without particular limitation. Specific examples thereof include 4-methoxyacetophenone,
4-methylacetophenone, 2-ethoxy-2-phenylacetophenone, benzoylacetone, o-benzoylbenzoic acid, 2-benzoylpyridine, benzophenone, propiophenone, pentanophenone, 4-methoxyphenylcyclopropylketone, cyclopentylphenylbutanone, Myristophenone, butyrophenone, chlorophenylethanone, bromophenylbutanone, 1-
Examples include phenyl dodecaphenone and heptanophenone.

【0010】本発明で使用する酸塩化物は、特に制限な
く各種公知のものを使用できる。その具体例としては、
例えば塩化ベンゾイル、塩化プロピオニル、塩化ペンチ
リル、p−メトキシ塩化ベンゾイル、p−クロロ塩化ベ
ンゾイルなどがあげられる。これらのなかでも塩化ベン
ゾイルなどの芳香族酸塩化物が好ましい。
The acid chloride used in the present invention may be any known one without any particular limitation. As a concrete example,
Examples thereof include benzoyl chloride, propionyl chloride, pentylyl chloride, p-methoxybenzoyl chloride and p-chlorobenzoyl chloride. Among these, aromatic acid chlorides such as benzoyl chloride are preferable.

【0011】前記の酸塩化物の使用量は、脂環族ケトン
類または芳香環を有する非環状ケトン類などの原料ケト
ン類に対して通常は0.5〜25重量%程度、好ましく
は1〜15重量%である。0.5重量%より少ない場合
は、添加効果が低いため十分な反応速度が得られない。
また25重量%を越える場合は、費用や作業の点で不利
がある。なお、酸塩化物の添加によるその作用機構は明
らかにはなっていないが、ラジカル供与剤として発生す
る過酸ラジカルの発生を促進しているものと考えられ
る。
The acid chloride is used in an amount of usually about 0.5 to 25% by weight, preferably 1 to 25% by weight based on the starting ketones such as alicyclic ketones or acyclic ketones having an aromatic ring. It is 15% by weight. If it is less than 0.5% by weight, the effect of addition is low and a sufficient reaction rate cannot be obtained.
If it exceeds 25% by weight, it is disadvantageous in terms of cost and work. Although the mechanism of action by the addition of the acid chloride has not been clarified, it is considered that it promotes the generation of peroxy acid radicals generated as a radical donor.

【0012】また、アルデヒド類としては、各種の公知
のものを使用できるが、特に芳香族アルデヒド類が好ま
しい。芳香族アルデヒド類としては、ベンズアルデヒ
ド、ジメチルベンズアルデヒド、トリメチルベンズアル
デヒド、エチルベンズアルデヒド、ブチルベンズアルデ
ヒド、メトキシベンズアルデヒド、フェノキシベンズア
ルデヒド、ヒドロキシベンズアルデヒド、シクロヘキシ
ルベンズアルデヒド、ビフェニルベンズアルデヒドなど
があげられる。
Various known aldehydes can be used, but aromatic aldehydes are particularly preferable. Examples of aromatic aldehydes include benzaldehyde, dimethylbenzaldehyde, trimethylbenzaldehyde, ethylbenzaldehyde, butylbenzaldehyde, methoxybenzaldehyde, phenoxybenzaldehyde, hydroxybenzaldehyde, cyclohexylbenzaldehyde and biphenylbenzaldehyde.

【0013】本発明の製造法においては、必ずしも溶媒
の存在下に反応させる必要はないが、得られるラクトン
類または芳香環を有する非環状エステル類の収率の点か
ら以下のような溶媒系で行うのが好ましい。該溶媒とし
ては、芳香族炭化水素類、アルキルハライド類、ハロゲ
ン化炭素およびエステル類およびから選ばれる少なくと
も1種を使用できる。
In the production method of the present invention, it is not always necessary to carry out the reaction in the presence of a solvent, but from the viewpoint of the yield of the obtained lactone or acyclic ester having an aromatic ring, the following solvent system is used. It is preferable to carry out. As the solvent, at least one selected from aromatic hydrocarbons, alkyl halides, halogenated carbons and esters can be used.

【0014】上記溶媒のうち芳香族炭化水素類として
は、ベンゼン、トルエン、キシレン、エチルベンゼン、
プロピルベンゼン、イソブチルベンゼン、メチルエチル
ベンゼン、ジエチルベンゼン、テトラリン等の各種公知
のものが例示できるが、なかでもベンゼンが好ましい。
アルキルハライド類も公知のものを使用できるが、なか
でも炭素数1〜5程度のものが好ましく、ジクロロメタ
ン、トリクロロメタン、ジクロロエタン、トリクロロエ
タン、ジクロロプロパン、ジクロロブタン、トリクロロ
プロパン、トリクロロブタン、テトラクロロプロパン、
テトラクロロブタン等があげられる。ハロゲン化炭素と
しては、例えば四塩化炭素、ヘキサクロロエタン、オク
タクロロプロパン等があげられる。また、エステル類と
しては酢酸メチル、酢酸エチル、酢酸イソブチル、プロ
ピオン酸メチル、プロピオン酸エチル、プロピオン酸イ
ソブチル等があげられる。
Among the above solvents, aromatic hydrocarbons include benzene, toluene, xylene, ethylbenzene,
Various known compounds such as propylbenzene, isobutylbenzene, methylethylbenzene, diethylbenzene, and tetralin can be exemplified, but among them, benzene is preferable.
Known alkyl halides can be used, but those having about 1 to 5 carbon atoms are preferable, and dichloromethane, trichloromethane, dichloroethane, trichloroethane, dichloropropane, dichlorobutane, trichloropropane, trichlorobutane, tetrachloropropane,
Examples include tetrachlorobutane. Examples of the carbon halide include carbon tetrachloride, hexachloroethane, octachloropropane and the like. Examples of the esters include methyl acetate, ethyl acetate, isobutyl acetate, methyl propionate, ethyl propionate, isobutyl propionate and the like.

【0015】上記溶媒はいずれも1種を単独でまたは2
種以上を組み合わせて使用できる。また、ラクトン類ま
たは芳香環を有する非環状エステル類の収率の点からす
れば、上記溶媒のなかでも芳香族炭化水素類およびアル
キイルハライド類が好ましく、特にベンゼン、ジクロロ
エタンが好適である。
Each of the above solvents may be used alone or in combination.
A combination of two or more species can be used. From the viewpoint of the yield of lactones or acyclic esters having an aromatic ring, aromatic hydrocarbons and alkyl halides are preferable among the above solvents, and benzene and dichloroethane are particularly preferable.

【0016】原料ケトン類に対する、アルデヒド類およ
び任意に用いられる溶媒の使用量は、原料ケトン類の種
類に応じて適宜に決定すればよい。通常は原料ケトン類
1モル部に対し、アルデヒド類が1モル部以上、好まし
くは1〜50モル部である。アルデヒド類が1モル部未
満では該反応が十分に進行し難い。溶媒の使用量は、ア
ルデヒド類1重量部に対し、通常1重量部以上、好まし
くは2〜125重量部である。溶媒使用量が1重量部未
満では反応速度が低下する。
The amounts of the aldehydes and the optionally used solvent used with respect to the raw material ketones may be appropriately determined according to the type of the raw material ketones. Usually, the amount of aldehydes is 1 part by mole or more, preferably 1 to 50 parts by mole, relative to 1 part by weight of the starting ketones. When the amount of aldehydes is less than 1 part by mole, the reaction is difficult to proceed sufficiently. The amount of the solvent used is usually 1 part by weight or more, preferably 2 to 125 parts by weight, relative to 1 part by weight of the aldehyde. If the amount of solvent used is less than 1 part by weight, the reaction rate will decrease.

【0017】本発明の製造法としては、前記溶媒に所定
量のアルデヒド類および酸塩化物を溶解し、酸素雰囲気
下に該アルデヒド類を自動酸化して過酸化物を発生させ
たのち、前記原料ケトン類を所定量添加してこれをラク
トン化(またはエステル化)する2段階法、または中間
体としての過酸化物の発生と同時に所定量の原料ケトン
類をラクトン化(またはエステル化)する1段階法が採
用できる。反応効率の点から1段階法が好ましい。
In the production method of the present invention, a predetermined amount of an aldehyde and an acid chloride are dissolved in the solvent, and the aldehyde is automatically oxidized in an oxygen atmosphere to generate a peroxide. A two-step method in which a predetermined amount of ketones is added and lactonized (or esterified), or a predetermined amount of raw material ketones is lactonized (or esterified) simultaneously with the generation of a peroxide as an intermediate 1. A step method can be adopted. From the viewpoint of reaction efficiency, the one-step method is preferable.

【0018】本発明の製造法では、酸素雰囲気を形成さ
せる方法についての制限は特になく、例えば反応系の気
相に酸素流を供給したり、液相に直接酸素をバブリング
すれば容易に酸素雰囲気を調製できる。酸素供給量は、
反応系内の過酸の発生量と相関するため慎重に決定され
ねばならず、通常は反応液の単位容積単位時間あたりの
供給量が0.1〜1200リットル・hr-1・リットル
-1程度、好ましくは25〜200リットル・hr-1・リ
ットル-1とされる。
In the production method of the present invention, there is no particular limitation on the method of forming an oxygen atmosphere, and for example, if an oxygen stream is supplied to the gas phase of the reaction system or oxygen is bubbled directly into the liquid phase, the oxygen atmosphere can be easily obtained. Can be prepared. Oxygen supply is
It must be carefully determined because it correlates with the amount of peracid generated in the reaction system. Normally, the supply amount of the reaction solution per unit volume per unit time is 0.1 to 1200 liters hr -1 liters.
−1 , preferably 25 to 200 liters · hr −1 · liter −1 .

【0019】本発明の製造法における反応は常圧におい
ても収率よくラクトン類または芳香環を有する非環状エ
ステル類を収得できるが、加圧条件を排除するものでは
ない。反応温度は、アルデヒド類から生じた過酸が分解
しない程度の温度とするのがよく、通常は0〜65℃程
度、好ましくは10〜40℃であり、前記の酸塩化物を
使用することにより室温においても十分に反応を行うこ
とができる。また最適な反応温度は、溶媒の種類に応じ
て異なるため、適宜に最適な温度を選択して行うのがよ
い。なお、65℃を越える場合にはラクトン類または芳
香環を有する非環状エステル類の収率が低下する傾向が
ある。また、溶媒を使用し常圧で反応させる場合には、
上記温度範囲内でしかも溶媒の沸点以下の温度とするの
がよい。また、反応時間は原料ケトン類の種類や反応温
度などにより異なるが、通常2〜36時間程度とされ
る。
The reaction in the production method of the present invention can yield lactones or acyclic esters having an aromatic ring in good yield even at atmospheric pressure, but it does not exclude pressurized conditions. The reaction temperature is preferably such that the peracid generated from the aldehydes is not decomposed, usually about 0 to 65 ° C, preferably 10 to 40 ° C. The reaction can be sufficiently performed even at room temperature. Since the optimum reaction temperature varies depending on the type of solvent, it is preferable to select the optimum temperature as appropriate. If the temperature exceeds 65 ° C, the yield of lactones or acyclic esters having an aromatic ring tends to decrease. When using a solvent and reacting under normal pressure,
It is preferable that the temperature is within the above temperature range and not higher than the boiling point of the solvent. The reaction time varies depending on the kind of the starting ketones, the reaction temperature, etc., but is usually about 2 to 36 hours.

【0020】[0020]

【発明の効果】本発明によれば、無触媒でしかも温和な
条件下に、原料ケトン類からラクトン類または芳香環を
有する非環状エステル類を高収率で製造できる。かかる
本発明では金属触媒を使用していないため、生成物の副
反応が起こらず、後処理が簡単であり、触媒の毒性の問
題もない。また、室温で十分に反応が進行するため、安
全性がよく、経済性な効果も奏する。
EFFECTS OF THE INVENTION According to the present invention, lactones or acyclic esters having an aromatic ring can be produced in high yield from raw material ketones under mild conditions without catalyst. In the present invention, since no metal catalyst is used, side reaction of the product does not occur, post-treatment is easy, and there is no problem of catalyst toxicity. In addition, since the reaction proceeds sufficiently at room temperature, the safety is good and the economical effect is achieved.

【0021】[0021]

【実施例】以下に実施例および比較例をあげて本発明を
さらに具体的に説明するが、本発明はこれら実施例に限
定されるものではない。
The present invention will be described in more detail with reference to the following examples and comparative examples, but the present invention is not limited to these examples.

【0022】実施例1 還流管を備えた100mlの三ツ口フラスコに、溶媒と
してベンゼン15ml、アルデヒド化合物としてベンズ
アルデヒド1.27ml(12ミリモル)および塩化ベ
ンゾイル68mg(0.484ミリモル)を加えた後、
室温(18〜22℃)にて、45〜55ml/分の供給
量で酸素を30分間バブリングさせた。次いで、予めジ
クロロエタン5mlに原料ケトン類としてシクロヘキサ
ノン393mg(4ミリモル)を溶解した溶液を、10
分間かけて滴下し、さらに4.5時間反応させて目的生
成物であるラクトンを得た。該ラクトンの分析はガスク
ロマトグラフ法によった。転化率、選択率を表1に示
す。なお、選択率とは原料が転化したもののうちで、目
的生成物の占める割合をいう。
Example 1 To a 100 ml three-necked flask equipped with a reflux tube, 15 ml of benzene as a solvent, 1.27 ml (12 mmol) of benzaldehyde as an aldehyde compound and 68 mg (0.484 mmol) of benzoyl chloride were added.
Oxygen was bubbled for 30 minutes at room temperature (18-22 ° C.) with a supply rate of 45-55 ml / min. Then, a solution prepared by dissolving 393 mg (4 mmol) of cyclohexanone as a raw material ketone in 5 ml of dichloroethane in advance was used.
The mixture was added dropwise over 1 minute, and the reaction was continued for 4.5 hours to obtain the desired product, lactone. The lactone was analyzed by gas chromatography. Table 1 shows the conversion rate and the selectivity. The selectivity refers to the ratio of the target product in the converted raw materials.

【0023】実施例2〜15 原料ケトン類の種類、塩化ベンゾイル量の添加率(原料
ケトン類に対する重量%)、溶媒の種類および反応温度
のうち少なくとも1種を表1に示すように代えた他は実
施例1と同様に行った。転化率、選択率を表1に示す。
Examples 2 to 15 At least one of the raw material ketones, the addition ratio of the amount of benzoyl chloride (% by weight relative to the raw material ketones), the type of solvent and the reaction temperature was changed as shown in Table 1. Was performed in the same manner as in Example 1. Table 1 shows the conversion rate and the selectivity.

【0024】比較例 各実施例において、塩化ベンゾイルを添加しなかった他
は、各実施例と同様に行った。転化率、選択率を表1に
示す。
Comparative Example In each example, the same procedure as in each example was performed except that benzoyl chloride was not added. Table 1 shows the conversion rate and the selectivity.

【0025】[0025]

【表1】 [Table 1]

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 アルデヒド類および酸素の共存下に脂環
族ケトン類を液相酸化してラクトン類を製造する方法に
おいて、反応系内に酸塩化物を添加することを特徴とす
るラクトン類の製造法。
1. A method for producing a lactone by subjecting an alicyclic ketone to liquid phase oxidation in the presence of an aldehyde and oxygen to produce a lactone, wherein an acid chloride is added to the reaction system. Manufacturing method.
【請求項2】 アルデヒド類および酸素の共存下に芳香
環を有する非環状ケトン類を液相酸化して芳香環を有す
る非環状エステル類を製造する方法において、反応系内
に酸塩化物を添加することを特徴とする非環状エステル
類の製造法。
2. A method for producing an acyclic ester having an aromatic ring by subjecting an acyclic ketone having an aromatic ring to liquid phase oxidation in the presence of aldehydes and oxygen to produce an acyclic ester having an aromatic ring, and adding an acid chloride to the reaction system. A method for producing an acyclic ester, comprising:
【請求項3】 有機溶媒を反応系に存在させる請求項1
または2記載の製造法。
3. An organic solvent is present in the reaction system.
Or the production method described in 2.
【請求項4】 有機溶媒が芳香族炭化水素、アルキルハ
ライド類、ハロゲン化炭素およびエステル類から選ばれ
る少なくとも1種である請求項3記載の製造法。
4. The method according to claim 3, wherein the organic solvent is at least one selected from aromatic hydrocarbons, alkyl halides, halogenated carbons and esters.
【請求項5】 アルデヒド類が、芳香族アルデヒド類で
ある請求項1または2記載の製造法。
5. The method according to claim 1 or 2, wherein the aldehydes are aromatic aldehydes.
JP06805494A 1994-03-10 1994-03-10 Process for producing lactones and process for producing esters Expired - Fee Related JP3802087B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06805494A JP3802087B2 (en) 1994-03-10 1994-03-10 Process for producing lactones and process for producing esters

Publications (2)

Publication Number Publication Date
JPH07247240A true JPH07247240A (en) 1995-09-26
JP3802087B2 JP3802087B2 (en) 2006-07-26

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Country Status (1)

Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5543280A (en) * 1994-11-24 1996-08-06 Agfa-Gevaert Ag Colour photographic recording material

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5543280A (en) * 1994-11-24 1996-08-06 Agfa-Gevaert Ag Colour photographic recording material

Also Published As

Publication number Publication date
JP3802087B2 (en) 2006-07-26

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