JPH0525080A - Production of cycloalkanone - Google Patents

Production of cycloalkanone

Info

Publication number
JPH0525080A
JPH0525080A JP3273011A JP27301191A JPH0525080A JP H0525080 A JPH0525080 A JP H0525080A JP 3273011 A JP3273011 A JP 3273011A JP 27301191 A JP27301191 A JP 27301191A JP H0525080 A JPH0525080 A JP H0525080A
Authority
JP
Japan
Prior art keywords
cycloalkanone
cycloalkanol
hydrogen peroxide
water
bromide
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
JP3273011A
Other languages
Japanese (ja)
Other versions
JP3069925B2 (en
Inventor
Mihoko Horibatake
美保子 堀畑
Hirohisa Nito
浩久 仁藤
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.)
TOKAI ELECTRO CHEMICAL CO
Tokai Denka Kogyo KK
Original Assignee
TOKAI ELECTRO CHEMICAL CO
Tokai Denka Kogyo KK
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 TOKAI ELECTRO CHEMICAL CO, Tokai Denka Kogyo KK filed Critical TOKAI ELECTRO CHEMICAL CO
Priority to JP3273011A priority Critical patent/JP3069925B2/en
Publication of JPH0525080A publication Critical patent/JPH0525080A/en
Application granted granted Critical
Publication of JP3069925B2 publication Critical patent/JP3069925B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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:To provide a method for producing a cycloalkanone by efficiently oxidizing a cycloalkanol with hydroperoxide. CONSTITUTION:A cycloalkanol is reacted with hydrogen peroxide in the presence of tungstenic acid and a quaternary ammonium salt, e.g. tetrabutylammonium bromide, in a homogeneous system to produce a cycloalkanone, e.g. 4-methylcyclohexanone.

Description

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

【0001】[0001]

【産業上の利用分野】本発明はシクロアルカノンの製造
方法に関し、特にシクロアルカノールを過酸化水素で酸
化し対応するシクロアルカノンを製造する方法に関す
る。
TECHNICAL FIELD The present invention relates to a method for producing cycloalkanone, and more particularly to a method for producing a corresponding cycloalkanone by oxidizing cycloalkanol with hydrogen peroxide.

【0002】[0002]

【従来の技術とその課題】シクロヘキサノールや4−メ
チルシクロヘキサノール等のシクロアルカノールを酸化
して対応するシクロアルカノンを製造する方法として
は、たとえばJ.Org. Chem., 52, 1
868(1987)やJ. Org. Chem.,
53, 3587(1988)に、触媒としてへテロポ
リ酸に塩化セチルピリジニウムを反応させて得られる化
合物等を用い過酸化水素で酸化する方法が開示されてい
る。この方法で用いる触媒は優れた触媒能は有している
が、触媒調製に別個の反応工程を要し、又過剰の過酸化
水素を要するという問題点を有する。Tetrahed
ron Lett., 25,173(1984)には
モリブデン酸アンモニウムと炭化カリウムと塩化テトラ
ブチルアンモニウムからなる触媒を用いて過酸化水素で
酸化する方法が開示されているが反応完結に長時間を要
するという問題点を有する。Chem. Lett.,
1984,1247には塩化ロジウムとトリフェニル
ホスフィンからなる触媒を用いて酸素で酸化する方法が
開示されているが、目的物の収率が低いと共に触媒の入
手が困難であるという問題点を有する。また特公昭44
−26657や特開昭50−149649等にはp−ク
レゾール等のフェノール類をパラジウム系触媒の存在下
に水素によって液相で酸化して対応するシクロアルカノ
ンを製造する方法が開示されている。この方法では触媒
の調製に別個の反応工程を要すると共に、シクロアルカ
ノールが副生する傾向にあり、これが副生すると別途の
酸化工程が必要となるという問題点を有する。
2. Description of the Related Art As a method for producing a corresponding cycloalkanone by oxidizing a cycloalkanol such as cyclohexanol or 4-methylcyclohexanol, the method described in J. Org. Chem. , 52, 1
868 (1987) and J. Org. Chem. ,
53, 3587 (1988) discloses a method of oxidizing with hydrogen peroxide using a compound obtained by reacting a heteropolyacid with cetylpyridinium chloride as a catalyst. Although the catalyst used in this method has an excellent catalytic ability, it has a problem that it requires a separate reaction step for preparing the catalyst and also requires an excess of hydrogen peroxide. Tetrahed
ron Lett. , 25, 173 (1984) discloses a method of oxidizing with hydrogen peroxide using a catalyst composed of ammonium molybdate, potassium carbide and tetrabutylammonium chloride, but the problem that it takes a long time to complete the reaction is disclosed. Have. Chem. Lett. ,
1984, 1247 discloses a method of oxidizing with oxygen using a catalyst composed of rhodium chloride and triphenylphosphine, but it has a problem that the yield of the desired product is low and the catalyst is difficult to obtain. See also
-26657 and Japanese Patent Laid-Open No. 50-149649 disclose a method for producing a corresponding cycloalkanone by oxidizing a phenol such as p-cresol in the liquid phase with hydrogen in the presence of a palladium catalyst. This method has a problem that a separate reaction step is required for the preparation of the catalyst and cycloalkanol tends to be produced as a by-product, and if this is produced as a by-product, a separate oxidation step is required.

【0003】本発明の目的は上記した如き従来技術の問
題点を解決することにあり、特に簡単な操作により、不
均一系反応にみられるような過剰の過酸化水素を必要と
することなく、短時間に高収率で目的とするシクロアル
カノンを製造させることができ、且つ触媒の繰返し使用
が可能な、シクロアルカノールの過酸化水素酸化による
シクロアルカノンの製造方法を提供することにある。
An object of the present invention is to solve the above-mentioned problems of the prior art, and by a particularly simple operation, without the need for excess hydrogen peroxide as seen in a heterogeneous reaction, It is an object of the present invention to provide a method for producing a cycloalkanone by oxidizing a cycloalkanol with hydrogen peroxide, which makes it possible to produce a desired cycloalkanone in a short time in a high yield, and which allows repeated use of a catalyst.

【0004】[0004]

【課題を解決するための手段】本発明は、シクロアルカ
ノールと過酸化水素とを、タングステン酸と4級オニウ
ム塩の存在下、均一系で反応させることを特徴とするシ
クロアルカノンの製造方法である。
The present invention provides a method for producing cycloalkanone, which comprises reacting cycloalkanol and hydrogen peroxide in a homogeneous system in the presence of tungstic acid and a quaternary onium salt. is there.

【0005】本発明方法で用いるシクロアルカノールと
しては酸化により対応するシクロアルカノンとなりうる
化合物であれば置換、非置換いずれのシクロアルカノー
ルも用いうる。具体例としてはシクロヘキサノールや4
−メチルシクロヘキサノール等のアルキル置換シクロヘ
キサノール等がある。
As the cycloalkanol used in the method of the present invention, a substituted or unsubstituted cycloalkanol can be used as long as it is a compound which can be converted into a corresponding cycloalkanone by oxidation. Specific examples include cyclohexanol and 4
-Alkyl-substituted cyclohexanol such as methylcyclohexanol and the like.

【0006】過酸化水素は水溶液で用いられる。過酸化
水素の使用量は原料であるシクロアルカノールに対し過
剰量でも用いうるが、約1モル当量で十分である。用い
る過酸化水素水溶液の濃度は特に制限はなく、通常5〜
90重量%、特に35〜60重量%濃度のものが好まし
く用いられる。
Hydrogen peroxide is used in aqueous solution. The hydrogen peroxide can be used in an excess amount with respect to the starting material cycloalkanol, but about 1 molar equivalent is sufficient. The concentration of the aqueous hydrogen peroxide solution used is not particularly limited and is usually 5 to 5.
Those having a concentration of 90% by weight, particularly 35 to 60% by weight are preferably used.

【0007】触媒の一方の成分であるタングステン酸の
使用量は、過酸化水素に対して1/1,000〜1モル
当量の範囲が好ましく、特に1/100〜1/500モ
ル当量の範囲が好ましい。
The amount of tungstic acid used as one component of the catalyst is preferably in the range of 1 / 1,000 to 1 molar equivalent, particularly 1/100 to 1/500 molar equivalent with respect to hydrogen peroxide. preferable.

【0008】触媒の他方の成分である4級オニウム塩の
使用量は、タングステン酸に対して1/5〜10モル当
量の範囲が好ましく、特に1/2〜2モル当量の範囲が
好ましい。
The amount of the quaternary onium salt, which is the other component of the catalyst, is preferably in the range of 1/5 to 10 molar equivalents, particularly preferably in the range of 1/2 to 2 molar equivalents, with respect to tungstic acid.

【0009】4級オニウム塩としては4級アンモニウム
塩又は4級ホスホニウム塩が用いられる。
As the quaternary onium salt, a quaternary ammonium salt or a quaternary phosphonium salt is used.

【0010】4級アンモニウム塩の具体例としては、臭
化テトラブチルアンモニウム、塩化テトラブチルアンモ
ニウム、テトラブチルアンモニウム硫酸水素塩、臭化テ
トラメチルアンモニウム、臭化テトラエチルアンモニウ
ム、臭化テトラプロピルアンモニウム、臭化テトラベン
チルアンモニウム、臭化テトラデシルアンモニウム、塩
化メチルトリオクチルアンモニウム、臭化へキシルトリ
メチルアンモニウム、臭化テトラデシルトリメチルアン
モニウム、塩化セチルトリメチルアンモニウム、臭化フ
ェニルトリメチルアンモニウム、臭化ベンジルテトラデ
シルジメチルアンモニウムがある。
Specific examples of the quaternary ammonium salt include tetrabutylammonium bromide, tetrabutylammonium chloride, tetrabutylammonium hydrogen sulfate, tetramethylammonium bromide, tetraethylammonium bromide, tetrapropylammonium bromide and bromide. Tetrabentyl ammonium, tetradecyl ammonium bromide, methyltrioctyl ammonium chloride, hexyl trimethyl ammonium bromide, tetradecyl trimethyl ammonium bromide, cetyl trimethyl ammonium chloride, phenyl trimethyl ammonium bromide, benzyl tetradecyl dimethyl ammonium bromide is there.

【0011】4級ホスホニウム塩の具体例としては、臭
化テトラブチルホスホニウム、臭化ヘキシルトリメチル
ホスホニウム、臭化テトラフェニルホスホニウム、臭化
ブチルトリフェニルホスホニウム、臭化ペンチルトリフ
ェニルホスホニウム、臭化へプチルトリフェニルホスホ
ニウム、塩化ベンジルトリフェニルホスホニウム、臭化
ブロモメチルトリフェニルホスホニウム、臭化ブロモプ
ロピルトリフェニルホスホニウムがある。
Specific examples of the quaternary phosphonium salt include tetrabutylphosphonium bromide, hexyltrimethylphosphonium bromide, tetraphenylphosphonium bromide, butyltriphenylphosphonium bromide, pentyltriphenylphosphonium bromide, and heptyltrinium bromide. There are phenylphosphonium, benzyltriphenylphosphonium chloride, bromomethyltriphenylphosphonium bromide, and bromopropyltriphenylphosphonium bromide.

【0012】上記のオニウム塩のうち、臭化テトラブチ
ルアンモニウム及び臭化テトラフェニルホスホニウムが
経済性と反応性の面に於て、最も適している。
Of the above-mentioned onium salts, tetrabutylammonium bromide and tetraphenylphosphonium bromide are most suitable in terms of economy and reactivity.

【0013】本発明では上記の反応を均一系で行うこと
を本質とする。均一系は過酸化水素を水溶液として用い
る結果、これに均一系を形成しうる水溶性有機溶媒を組
み合わせることによって形成される。水溶性有機溶媒と
しては目的生成物であるシクロアルカノンも含め反応系
全体を均一系に保持しうる水溶性有機溶媒であれば本質
的にはいずれでもよく、用いる原料化合物や目的生成物
等に応じ適宜選択しうるが、原料化合物がアルコール系
化合物であることもあり、アルコール系の水溶性有機溶
媒とはいえない。特に好ましい水溶性有機溶媒としては
アセトニトリルがある。水溶性有機溶媒の使用量は系を
均一系に保持しうる量であればいずれでもよく、たとえ
ばシクロアルカノールに対し5〜30重量倍程度用いら
れる。
The essence of the present invention is to carry out the above reaction in a homogeneous system. The homogeneous system is formed by using hydrogen peroxide as an aqueous solution and combining it with a water-soluble organic solvent capable of forming a homogeneous system. The water-soluble organic solvent may be essentially any water-soluble organic solvent as long as it can maintain the entire reaction system in a uniform system including the target product cycloalkanone, and may be used as a raw material compound or a target product to be used. Although it can be appropriately selected depending on the case, since the raw material compound may be an alcohol-based compound, it cannot be said to be an alcohol-based water-soluble organic solvent. A particularly preferred water-soluble organic solvent is acetonitrile. The water-soluble organic solvent may be used in any amount as long as it can maintain the system in a homogeneous system, and is used, for example, in an amount of about 5 to 30 times by weight based on the cycloalkanol.

【0014】反応温度は通常40〜100℃、特に反応
系を還流するに充分な温度(80〜100℃)が好まし
い。
The reaction temperature is usually 40 to 100 ° C., and particularly preferably a temperature (80 to 100 ° C.) sufficient to reflux the reaction system.

【0015】反応終了後は適宜の手段で目的生成物を取
得しうる。たとえば蒸留により水溶性有機溶媒と水を留
去した後、減圧蒸留で目的生成物であるシクロアルカノ
ンを取得し、残された触媒は繰り返し酸化反応に使用さ
れる。
After completion of the reaction, the desired product can be obtained by an appropriate means. For example, after distilling off the water-soluble organic solvent and water by distillation, the desired product, cycloalkanone, is obtained by vacuum distillation, and the remaining catalyst is repeatedly used in the oxidation reaction.

【0016】かくして得られるシクロアルカノンは、た
とえば医薬中間体、ビスアジド型の光感光性樹脂原料等
種々の用途に用いうる有用な化合物である。
The cycloalkanone thus obtained is a useful compound which can be used for various purposes such as a pharmaceutical intermediate and a bisazide type photosensitive resin raw material.

【0017】[0017]

【実施例】【Example】

実施例1:容量500mlのセパラブルフラスコに、ア
セトニトリル150ml、4−メチルシクロヘキサノー
ル11.4g(0.1mol)、60%過酸化水素5.
67g(0.1mol)、タングステン酸50.0mg
(0.2mmol)及び臭化テトラブチルアンモニウム
129.0mg(0.4mmol)を加え、湯浴上で過
熱還流下、6時間撹拌した。
Example 1: In a separable flask having a capacity of 500 ml, 150 ml of acetonitrile, 11.4 g (0.1 mol) of 4-methylcyclohexanol, 60% hydrogen peroxide 5.
67 g (0.1 mol), tungstic acid 50.0 mg
(0.2 mmol) and 129.0 mg (0.4 mmol) of tetrabutylammonium bromide were added, and the mixture was stirred on a water bath under reflux with heating for 6 hours.

【0018】未反応4−メチルシクロヘキサノール及び
4−メチルシクロヘキサノンはガスクロマトグラフィー
により分析した。
Unreacted 4-methylcyclohexanol and 4-methylcyclohexanone were analyzed by gas chromatography.

【0019】結果は、表1に示した如く、4−メチルシ
クロヘキサノン収率100%であった。
As a result, as shown in Table 1, the yield of 4-methylcyclohexanone was 100%.

【0020】実施例2−8:タングステン酸及び臭化テ
トラブチルアンモニウムの使用量を変えた他は、実施例
1と同様に反応を行った。
Example 2-8: The reaction was performed in the same manner as in Example 1 except that the amounts of tungstic acid and tetrabutylammonium bromide used were changed.

【0021】結果は、表1の通りである。The results are shown in Table 1.

【0022】[0022]

【表1】 実施例9−12:4級オニウム塩を変えた以外は、実施
例1と同様に反応を行った。
[Table 1] Examples 9-12: The reaction was performed in the same manner as in Example 1 except that the quaternary onium salt was changed.

【0023】結果は、表2の通りである。The results are shown in Table 2.

【0024】[0024]

【表2】 実施例13−16:過酸化水素の濃度を変えた以外は、
実施例1と同様に反応を行った。
[Table 2] Examples 13-16: except that the concentration of hydrogen peroxide was changed.
The reaction was carried out in the same manner as in Example 1.

【0025】結果は、表3の通りである。The results are shown in Table 3.

【0026】[0026]

【表3】 実施例17:容量3lの三つ口フラスコに、アセトニト
リル1.50l、4−メチルシクロヘキサノール11
4.2g(1.0mol)、60%過酸化水素溶液5
6.7g(1.0mol)、タングステン酸0.50g
(2.0mmol)及び臭化テトラブチルアンモニウム
1.29g(4mmol)を加え、湯浴上で過熱還流
下、8時間撹拌した。
[Table 3] Example 17: 1.50 l of acetonitrile and 4-methylcyclohexanol 11 in a 3-necked flask with a volume of 3 l
4.2 g (1.0 mol), 60% hydrogen peroxide solution 5
6.7 g (1.0 mol), tungstic acid 0.50 g
(2.0 mmol) and 1.29 g (4 mmol) of tetrabutylammonium bromide were added, and the mixture was stirred on a hot water bath under reflux with heating for 8 hours.

【0027】反応終了後、溶媒及び水を留去し、減圧蒸
留によって、目的物の4−メチルシクロヘキサノンを得
た。
After the reaction was completed, the solvent and water were distilled off, and the target substance, 4-methylcyclohexanone, was obtained by distillation under reduced pressure.

【0028】反応残渣の酸化触媒を回収し、これを再度
酸化反応に利用した。
The oxidation catalyst in the reaction residue was recovered and reused in the oxidation reaction.

【0029】結果は、表4に示した。The results are shown in Table 4.

【0030】[0030]

【表4】 比較例1−3:溶媒を変えた他は、実施例1と同様に反
応を行った。
[Table 4] Comparative Example 1-3: The reaction was performed in the same manner as in Example 1 except that the solvent was changed.

【0031】結果は、表5に示した。The results are shown in Table 5.

【0032】[0032]

【表5】 比較例4:4級オニウム塩を用いなかった他は、実施例
1と同様に反応を行った。
[Table 5] Comparative Example 4: The reaction was performed in the same manner as in Example 1 except that the quaternary onium salt was not used.

【0033】反応24時間後の4−メチルシクロヘキサ
ノンの収率は、47%であった。
The yield of 4-methylcyclohexanone after 24 hours of the reaction was 47%.

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 シクロアルカノールと過酸化水素とを、
タングステン酸と4級オニウム塩の存在下、均一系で反
応させることを特徴とするシクロアルカノンの製造方
法。
1. A cycloalkanol and hydrogen peroxide,
A method for producing cycloalkanone, which comprises reacting tungstic acid with a quaternary onium salt in a homogeneous system.
【請求項2】 シクロアルカノールがアルキル置換又は
非置換シクロヘキサノールである請求項1記載の方法。
2. The method according to claim 1, wherein the cycloalkanol is an alkyl-substituted or unsubstituted cyclohexanol.
【請求項3】 4級オニウム塩が4級アンモニウム塩又
は4級ホスホニウム塩である請求項1記載の方法。
3. The method according to claim 1, wherein the quaternary onium salt is a quaternary ammonium salt or a quaternary phosphonium salt.
【請求項4】 均一系を構成する媒体が水と水溶性有機
溶媒との混合系からなり、シクロアルカノール、シクロ
アルカノン、過酸化水素及び4級オニウム塩と均一系を
形成するものである請求項1記載の方法。
4. The medium constituting the homogeneous system comprises a mixed system of water and a water-soluble organic solvent, and forms a homogeneous system with cycloalkanol, cycloalkanone, hydrogen peroxide and quaternary onium salt. The method according to item 1.
【請求項5】 水溶性有機溶媒が非アルコール系溶媒で
ある請求項4記載の方法。
5. The method according to claim 4, wherein the water-soluble organic solvent is a non-alcoholic solvent.
【請求項6】 水溶性有機溶媒がアセトニトリルである
請求項4記載の方法。
6. The method according to claim 4, wherein the water-soluble organic solvent is acetonitrile.
JP3273011A 1991-07-23 1991-07-23 Method for producing cycloalkanone Expired - Fee Related JP3069925B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3273011A JP3069925B2 (en) 1991-07-23 1991-07-23 Method for producing cycloalkanone

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3273011A JP3069925B2 (en) 1991-07-23 1991-07-23 Method for producing cycloalkanone

Publications (2)

Publication Number Publication Date
JPH0525080A true JPH0525080A (en) 1993-02-02
JP3069925B2 JP3069925B2 (en) 2000-07-24

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Country Link
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ITMI20110666A1 (en) * 2011-04-19 2012-10-20 Dipharma Francis Srl PROCEDURE FOR THE PREPARATION OF (R) AND (S) PRAMIPEXOLO AND ITS INTERMEDIATES

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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JP2010235521A (en) * 2009-03-31 2010-10-21 Nagase Chemtex Corp Method for producing alcohol oxide
ITMI20110666A1 (en) * 2011-04-19 2012-10-20 Dipharma Francis Srl PROCEDURE FOR THE PREPARATION OF (R) AND (S) PRAMIPEXOLO AND ITS INTERMEDIATES

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