JPH0125748B2 - - Google Patents

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Publication number
JPH0125748B2
JPH0125748B2 JP56070658A JP7065881A JPH0125748B2 JP H0125748 B2 JPH0125748 B2 JP H0125748B2 JP 56070658 A JP56070658 A JP 56070658A JP 7065881 A JP7065881 A JP 7065881A JP H0125748 B2 JPH0125748 B2 JP H0125748B2
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JP
Japan
Prior art keywords
formula
reaction
hydroxy
alkyl
represented
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
Application number
JP56070658A
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Japanese (ja)
Other versions
JPS57188584A (en
Inventor
Harue Ryo
Minoru Iwamoto
Kunio Kojo
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.)
T Hasegawa Co Ltd
Original Assignee
T Hasegawa Co Ltd
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Filing date
Publication date
Application filed by T Hasegawa Co Ltd filed Critical T Hasegawa Co Ltd
Priority to JP56070658A priority Critical patent/JPS57188584A/en
Publication of JPS57188584A publication Critical patent/JPS57188584A/en
Publication of JPH0125748B2 publication Critical patent/JPH0125748B2/ja
Granted legal-status Critical Current

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    • 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

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  • Pyrane Compounds (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、香料物質として極めて重要である
α,β−不飽和−δ−ラクトン類の新規な製法に
関する。 更に詳しくは、例えば、下記式(3) 但し式中、RはC1〜C12の直鎖および分枝状ア
ルキル基、C7〜C8のアラルキル基、C3〜C6のシ
クロアルキル基を示す、 で表わされる4−ヒドロキシ−2−アルキル−2
−シクロペンテン−1−オン類を、触媒の存在下
に接触還元せしめて得ることのできる前記式(2)で
表わされる4−ヒドロキシ−2−アルキル−1−
シクロペンタノン類を、過酸の存在下に酸化脱水
反応せしめることを特徴とする下記式(1) 但し式中、Rは上述したと同義、 で表わされるα,β−不飽和−δ−ラクトン類の
新規な製法に関する。 上記式(1)で表わされるα,β−不飽和ラクトン
類は、食品フレーバーとして極めて重要で広く使
用されている公知の香料物質である。例えば、上
記式(1)に包含される2−デセン−5−オリドは、
Cry−ptocaria massoiaの樹皮油の主成分であ
り、別名マソイヤ ラクトンとして知られてい
る。又砂糖キビ(Sacclarum officinarum var.
NC0310)中も見出され、更にバター中からもバ
ターの主要香気成分として見出され、該物質は食
品フレーバーとして広く利用されている重要な香
料物質である。 従来、前記2−デセン−5−オリドを包含する
前記式(1)で表わされるα,β−不飽和−δ−ラク
トン類の合成に関し、2,3の提案がなされてい
るが、いづれも原料面、操作、収率などの点で不
満足であつて、工業的に充分満足すべき提案は現
在まで知られていない。 従来提案として、例えば下記工程図に示す方法
(Agr.Biol.Chen.,32.1016(1968))が知られてい
る。 上記方法は、多工程且つ煩雑な操作が必要であ
り、又使用原料が高価であるうえに、更に、各工
程の収率が低く、工業的方法としては満足すべき
ものではない。 本発明者等は、上述の如き従来法の欠陥乃至不
利益を克服して、上記式(1)化合物の改善製法を提
供すべく研究を行つた。 その結果、従来提案の欠陥乃至不利益を克服し
て、上記(3)で表わされる4−ヒドロキシ−2−ア
ルキル−2−シクロペンテン−1−オンから2工
程で容易な操作で且つ安価に高収率をもつて工業
的に有利に式(1)化合物を製造できることを発見し
た。 従つて本発明の目的は、香気香味賦与乃至変調
剤として有用な前記式(1)で表わされるα,β−不
飽和ラクトンを工業的に有利に製造できる新規な
製造法を提供するにある。 本発明の目的および更に他の多くの目的ならび
に利点は以下の記載から一層明らかとなるであろ
う。 本発明の出発物質である前記式(2)化合物を製造
するのに有利に利用できる前記式(3)で表わされる
4−ヒドロキシ−2−アルキル−2−シクロペン
テン−1−オンは、同一出願人に係わる昭和54年
11月28日付出願の発明の名称;「2−置換−ヒド
ロキシシクロペンテノン類およびその製法」(出
願番号54−153004、特開昭56−77232号公報、54
−153005、特開昭56−77237号公報)に詳細に説
明されている方法により容易に製造できる。 本発明に於ける前記式(1)で表わされるα,β−
不飽和−δ−ラクトン類の製造工程図は、例えば
下記の様に示すことができる。 (式中、Rは前記したと同義) 上記式(2)で表わされる4−ヒドロキシ−2−ア
ルキル−1−シクロペンタノン類は、上記式(3)で
表わされる4−ヒドロキシ−2−アルキル−2−
シクロペンテン−1−オンを触媒の存在下に接触
水素還元することにより、容易に製造することが
できる。 上記反応は、所望により有機溶媒中で行つても
良い。 該反応に用いる触媒としては、例えば、パラジ
ウム黒、パラジウム炭素などの担体つきパラジウ
ム、コロイドパラジウムなどの如きパラジウム系
触媒;コロイドロジウム、ロジウムカーボンなど
の如きロジウム系触媒;ケイソウ土などの担体つ
きニツケル、ラネーニツケルなどの如きニツケル
系触媒などを例示することができる。 又、反応に用いる場合の有機溶媒としては、例
えばメタノール、エタノールなどの如きアルコー
ル類;ジオキサン、テトラヒドロフランなどの如
きエーテル類など、更にこれらの任意の混合物を
挙げることができる。 上記反応の水素圧力は広い範囲で行うことがで
きるが、例えば、ほぼ大気圧〜約100Kg/cm2程度
の範囲、より好ましくはほぼ大気圧〜約50Kg/cm2
程度の範囲を例示することができる。又反応温度
としては、約20゜〜約80℃程度の範囲を、好まし
く例示することができる。 上記反応終了後、例えば、触媒を別し、溶媒
を留去することにより、上記式(2)4−ヒドロキシ
−2−アルキル−1−シクロペンタノン類を高収
率、高純度で得ることができる。更に望むならば
例えば再結晶、減圧蒸留、カラムクロマトなどの
手段を採用して精製することができる。 本発明の上記式(1)で表わされるα,β−不飽和
−γ−ラクトン類を合成するには、上記式(2)で表
わされる4−ヒドロキシ−2−アルキル−1−シ
クロペンタノン類を、例えば、有機もしくは無機
の過酸を用い、バイヤ・ビリガー反応条件下で反
応すれば酸化によるラクトン化と脱水反応が同時
に進行することにより、容易に合成することがで
きる。 該反応は、例えば、不活性溶媒中、上記式(2)化
合物に過酸を作用せしめることにより好収率で且
つ優れた選択率をもつて行うことができる。反応
温度としては、例えば約0℃〜約80℃程度の如き
温度を例示でき、約20゜〜約45℃程度の範囲の温
度を一層好ましく例示できる。反応時間は、反応
温度や過酸の種類などによつても適宜に選択でき
るが、例えば、数時間から数週間の如き反応時間
を例示することができる。 反応に使用する過酸の例としては、例えば過酸
化水素、過硫酸などの無機系過酸;過酢酸、過安
息香酸、m−クロロ過安息香酸、モノ過フタル酸
などの如き有機系過酸を例示することができる。
これら過酸の使用量としては、上記式(2)化合物に
対して約1〜約20倍モルの如き使用量を例示で
き、一層好ましくは約2〜10倍モル程度の使用量
を例示することができる。又、過酸による過酸化
反応を促進するために、過酸の他に、微量の無機
または有機酸例えば硫酸、フツ化水素酸、過塩素
酸、p−トルエンスルホン酸などを触媒として加
えてもよい。 また上記不活性溶媒は、使用する過酸と生成物
の種類によつて適宜に選択できる。例えば、水、
アルカリ水溶液、エタノール、エーテル、クロロ
ホルム、塩化メチレン、ギ酸、酢酸、無水酢酸、
ピリジン及びこれらの適宜な混合物などを例示す
ることができる。その使用量には特別な制約はな
いが、上記式(2)化合物に対して約1〜約40重量倍
程度、一層好ましくは約5〜約30重量倍程度の使
用量を例示することができる。 上記反応終了後、例えば、反応生成物を水中に
注入し、中和し、適当な溶媒で抽出し、溶媒層を
水洗、乾燥、濃縮することにより、上記式(1)で表
わされるα,β−不飽和−δ−ラクトンを高収
率、高純度で得ることができる。更に望むなら
ば、例えば減圧蒸留、カラムクロマトなどの手段
を採用して精製することができる。 実施例 1 4−ヒドロキシ−2−ペンチル−1−シクロペ
ンタノンの合成。 接触還元装置つきの反応容器に式(3)の4−ヒド
ロキシ−2−ペンチル−2−シクロペンテン−1
−オン25.2g(0.15モル)、5%パラジウム炭素
1.2g、メタノール50mlを仕込み、水素を導入し
ながら振盪する。直ちに水素の吸収がはじまり、
約4時間で水素の理論吸収量に近づくにつれ、吸
収速度が低下したところで振盪を止める。パラジ
ウム炭素を別し、メタノールを留去し、減圧下
に蒸留し無色透明の4−ヒドロキシ−2−ペンチ
ル−1−シクロペンタノン23g(収率90%)を得
る。沸点130゜〜137℃/1mmHg。構造はIR,
NMR,MSより確認した。実施例 2 2−デセン−5−オリドの合成。 フラスコに式(2)の4−ヒドロキシ−2−ペンチ
ル−1−シクロペンタノン10.2g(10.06モル)、
40%過酢酸81g、酢酸360ml、p−トルエンスル
ホン酸1.5gを仕込み、35℃の暗室恒温槽に60時
間放置する。反応物を氷水に注入し、エーテルで
抽出する。乾燥後エーテルを留去し、減圧下に蒸
留して2−デセン−5−オリド8.7gを得る。沸
点130〜134℃/1mmHg収率87%。構造はIR,
NMR,MSより確認した。 実施例 3 4−ヒドロキシ−2−ブチル−1−シクロペン
タノンの合成。 接触還元装置つきの反応容器に4−ヒドロキシ
−2−ブチル−2−シクロペンテン−1−オン
153g(1モル)、ロジウムカーボン4.5g、ジオ
キサン150c.c.を仕込み、水素を導入しながら水素
圧5〜10Kg/cm2、反応温度15〜40℃で反応を行
い、理論量の水素吸収のあつた所で終了する。反
応後ロジウムカーボンを別し、ジオキサンを留
去し、減圧下に蒸留し4−ヒドロキシ−2−ブチ
ル−1−シクロペンタノン140g(収率90%)を
得る。沸点124゜〜128℃/1mmHg構造はIR,
NMR,MSより確認した。 実施例 4 2−ノネン−5−オリドの合成。 フラスコに4−ヒドロキシ−2−ブチル−1−
シクロペンタノン77.5g(0.5モル)、40%過酢酸
60g、酢酸400ml、硫酸3gを仕込み、30℃の暗
室恒温槽に50時間放置する。反応物を氷水に注入
し、エーテルで抽出する。乾燥後エーテルを留去
し、減圧下に蒸留して2−ノネン−5−オリド64
gを得る。沸点125゜〜129℃/1mmHg収率85%。
構造はIR,NMR,MSより確認した。 実施例 5 実施例1,2もしくは実施例3,4と同様の手
段を用いて、種々のR基について行つた実験結果
を下記の表に示す。
The present invention relates to a new method for producing α,β-unsaturated-δ-lactones, which are extremely important as fragrance substances. More specifically, for example, the following formula (3) However, in the formula, R represents a C 1 to C 12 linear or branched alkyl group, a C 7 to C 8 aralkyl group, or a C 3 to C 6 cycloalkyl group. -alkyl-2
- 4-hydroxy-2-alkyl-1- represented by the above formula (2), which can be obtained by catalytic reduction of cyclopenten-1-ones in the presence of a catalyst.
The following formula (1) is characterized by subjecting cyclopentanones to an oxidation and dehydration reaction in the presence of a peracid. However, in the formula, R has the same meaning as described above, and relates to a novel method for producing α,β-unsaturated-δ-lactones represented by: The α,β-unsaturated lactones represented by the above formula (1) are known flavor substances that are extremely important and widely used as food flavors. For example, 2-decene-5-olide included in the above formula (1) is
It is the main component of the bark oil of Cry-ptocaria massoia and is also known as massoia lactone. Also sugar millet (Sacclarum officinarum var.
It is also found in butter (NC 0 310) and as the main flavor component of butter, and is an important flavor substance widely used as a food flavor. Conventionally, a few proposals have been made regarding the synthesis of α,β-unsaturated-δ-lactones represented by the above formula (1) including the above-mentioned 2-decene-5-olide, but none of them involve starting materials. The method is unsatisfactory in terms of performance, operation, yield, etc., and no proposal that is industrially fully satisfactory has been known to date. As a conventional proposal, for example, the method shown in the process diagram below (Agr.Biol.Chen., 32.1016 (1968)) is known. The above method requires multiple steps and complicated operations, the raw materials used are expensive, and the yield in each step is low, so it is not satisfactory as an industrial method. The present inventors conducted research in order to overcome the defects and disadvantages of the conventional methods as described above and provide an improved method for producing the compound of formula (1). As a result, the defects and disadvantages of the conventional proposals have been overcome, and 4-hydroxy-2-alkyl-2-cyclopenten-1-one represented by the above (3) can be easily produced in two steps at low cost and in high yield. It has been discovered that the compound of formula (1) can be produced industrially at a high rate. Accordingly, an object of the present invention is to provide a novel method for industrially advantageous production of the α,β-unsaturated lactone represented by the formula (1), which is useful as an aroma and flavor imparting or modulating agent. The objects and many other objects and advantages of the present invention will become more apparent from the following description. The 4-hydroxy-2-alkyl-2-cyclopenten-1-one represented by the formula (3), which can be advantageously used to produce the compound of the formula (2), which is the starting material of the present invention, is 1978 related to
Title of the invention filed on November 28th: "2-Substituted-hydroxycyclopentenones and their production method" (Application number 54-153004, Japanese Patent Application Laid-Open No. 1977-77232, 54
-153005, Japanese Unexamined Patent Publication No. 56-77237). α, β− represented by the above formula (1) in the present invention
A process diagram for producing unsaturated -δ-lactones can be shown, for example, as shown below. (In the formula, R has the same meaning as defined above.) The 4-hydroxy-2-alkyl-1-cyclopentanones represented by the above formula (2) are the 4-hydroxy-2-alkyl represented by the above formula (3). -2-
It can be easily produced by catalytic hydrogen reduction of cyclopenten-1-one in the presence of a catalyst. The above reaction may be carried out in an organic solvent if desired. Catalysts used in the reaction include, for example, palladium-based catalysts such as palladium with a carrier such as palladium black and palladium-carbon, and colloidal palladium; rhodium-based catalysts such as colloidal rhodium and rhodium carbon; nickel with a carrier such as diatomaceous earth; Examples include nickel-based catalysts such as Raney nickel. Examples of the organic solvent used in the reaction include alcohols such as methanol and ethanol; ethers such as dioxane and tetrahydrofuran; and any mixtures thereof. The hydrogen pressure in the above reaction can be carried out in a wide range, but for example, from about atmospheric pressure to about 100 Kg/cm 2 , more preferably from about atmospheric pressure to about 50 Kg/cm 2
A range of degrees can be exemplified. The reaction temperature is preferably in the range of about 20°C to about 80°C. After the completion of the above reaction, the 4-hydroxy-2-alkyl-1-cyclopentanones of the above formula (2) can be obtained in high yield and purity by, for example, separating the catalyst and distilling off the solvent. can. If desired, further purification can be carried out by employing methods such as recrystallization, vacuum distillation, and column chromatography. In order to synthesize the α,β-unsaturated-γ-lactones represented by the above formula (1) of the present invention, 4-hydroxy-2-alkyl-1-cyclopentanones represented by the above formula (2) are synthesized. can be easily synthesized, for example, by using an organic or inorganic peracid and reacting under Bayer-Villiger reaction conditions, whereby lactonization by oxidation and dehydration reaction proceed simultaneously. The reaction can be carried out in good yield and with excellent selectivity, for example, by reacting the compound of formula (2) with a peracid in an inert solvent. The reaction temperature may be, for example, about 0°C to about 80°C, and more preferably about 20° to about 45°C. The reaction time can be appropriately selected depending on the reaction temperature, the type of peracid, etc., and can be, for example, a reaction time of several hours to several weeks. Examples of peracids used in the reaction include inorganic peracids such as hydrogen peroxide and persulfuric acid; organic peracids such as peracetic acid, perbenzoic acid, m-chloroperbenzoic acid, and monoperphthalic acid. can be exemplified.
Examples of the amount of these peracids to be used include about 1 to about 20 times the molar amount of the compound of formula (2), more preferably about 2 to 10 times the molar amount. Can be done. Furthermore, in order to promote the peroxidation reaction caused by peracid, in addition to peracid, a trace amount of an inorganic or organic acid such as sulfuric acid, hydrofluoric acid, perchloric acid, p-toluenesulfonic acid, etc. may be added as a catalyst. good. Further, the above-mentioned inert solvent can be appropriately selected depending on the peracid used and the type of product. For example, water,
Alkaline aqueous solution, ethanol, ether, chloroform, methylene chloride, formic acid, acetic acid, acetic anhydride,
Examples include pyridine and appropriate mixtures thereof. There is no particular restriction on the amount used, but the amount used may be about 1 to about 40 times, more preferably about 5 to about 30 times the weight of the compound of formula (2) above. . After the completion of the above reaction, for example, the reaction product is poured into water, neutralized, extracted with an appropriate solvent, and the solvent layer is washed with water, dried, and concentrated to obtain α, β expressed by the above formula (1). -Unsaturated-δ-lactone can be obtained in high yield and purity. If desired, further purification can be carried out by employing means such as vacuum distillation and column chromatography. Example 1 Synthesis of 4-hydroxy-2-pentyl-1-cyclopentanone. 4-hydroxy-2-pentyl-2-cyclopentene-1 of formula (3) was placed in a reaction vessel equipped with a catalytic reduction device.
-one 25.2g (0.15mol), 5% palladium on carbon
Add 1.2 g and 50 ml of methanol, and shake while introducing hydrogen. Hydrogen absorption begins immediately,
As the theoretical amount of hydrogen absorption is approached in about 4 hours, the shaking is stopped when the absorption rate decreases. The palladium on carbon is separated, methanol is distilled off, and the mixture is distilled under reduced pressure to obtain 23 g (yield: 90%) of colorless and transparent 4-hydroxy-2-pentyl-1-cyclopentanone. Boiling point 130°~137°C/1mmHg. The structure is IR,
Confirmed by NMR and MS. Example 2 Synthesis of 2-decene-5-olide. 10.2 g (10.06 mol) of 4-hydroxy-2-pentyl-1-cyclopentanone of formula (2) in the flask,
Add 81 g of 40% peracetic acid, 360 ml of acetic acid, and 1.5 g of p-toluenesulfonic acid, and leave in a thermostat in a dark room at 35°C for 60 hours. Pour the reaction into ice water and extract with ether. After drying, the ether was distilled off and distilled under reduced pressure to obtain 8.7 g of 2-decene-5-olide. Boiling point 130-134℃/1mmHg Yield 87%. The structure is IR,
Confirmed by NMR and MS. Example 3 Synthesis of 4-hydroxy-2-butyl-1-cyclopentanone. 4-hydroxy-2-butyl-2-cyclopenten-1-one in a reaction vessel equipped with a catalytic reduction device.
153 g (1 mole), rhodium carbon 4.5 g, and dioxane 150 c.c. were charged, and while introducing hydrogen, the reaction was carried out at a hydrogen pressure of 5 to 10 Kg/cm 2 and a reaction temperature of 15 to 40°C, until the theoretical amount of hydrogen was absorbed. It ends when it gets hot. After the reaction, the rhodium carbon is separated, the dioxane is distilled off, and the mixture is distilled under reduced pressure to obtain 140 g (yield: 90%) of 4-hydroxy-2-butyl-1-cyclopentanone. Boiling point 124°~128°C/1mmHg structure is IR,
Confirmed by NMR and MS. Example 4 Synthesis of 2-nonene-5-olide. 4-hydroxy-2-butyl-1- in the flask
Cyclopentanone 77.5g (0.5mol), 40% peracetic acid
60 g, acetic acid 400 ml, and sulfuric acid 3 g, and left in a dark room constant temperature bath at 30°C for 50 hours. Pour the reaction into ice water and extract with ether. After drying, remove the ether and distill under reduced pressure to obtain 2-nonene-5-olide64
get g. Boiling point 125°~129°C/1mmHg Yield 85%.
The structure was confirmed by IR, NMR, and MS. Example 5 Using the same procedure as in Examples 1 and 2 or Examples 3 and 4, the results of experiments conducted on various R groups are shown in the table below.

【表】 実施例 6 実施例1,2もしくは実施例3,4,5と同様
な手段を用いて、次のR基について行つた場合の
実験結果を下表に示す。
[Table] Example 6 Using the same method as in Examples 1 and 2 or Examples 3, 4, and 5, the experimental results for the following R groups are shown in the table below.

【表】【table】

Claims (1)

【特許請求の範囲】 1 下記式(2) 但し式中、RはC1〜C12の直鎖および分枝状ア
ルキル基、C7〜C8のアラルキル基、C3〜C6のシ
クロアルキル基を示す、 で表わされる4−ヒドロキシ−2−アルキル−1
−シクロペンタノン類を過酸の存在下に酸化脱水
反反応せしめることを特徴とする下記式(1) 但し式中、Rは上記したと同義、 で表わされるα,β−不飽和−δ−ラクトン類の
製法。 2 下記式(3) 但し式中、RはC1〜C12の直鎖および分枝状ア
ルキル基、C7〜C8のアラルキル基、C3〜C6のシ
クロアルキル基を示す、 で表わされる4−ヒドロキシ−2−アルキル−2
−シクロペンテン−1−オン類を、触媒の存在下
に接触水素還元せしめて、下記式(2) 但し式中、Rは上記したと同義、 で表わされる4−ヒドロキシ−2−アルキル−1
−シクロペンタノン類を形成し、該式(2)化合物を
過酸の存在下に酸化脱水反応せしめることを特徴
とする下記式(1) 但し式中、Rは上記したと同義 で表わされるα,β−不飽和−δ−ラクトン類の
製法。
[Claims] 1. The following formula (2) However, in the formula, R represents a C 1 to C 12 linear or branched alkyl group, a C 7 to C 8 aralkyl group, or a C 3 to C 6 cycloalkyl group. -alkyl-1
- The following formula (1) characterized by subjecting cyclopentanones to an oxidation-dehydration reaction in the presence of a peracid. However, in the formula, R has the same meaning as above. A method for producing α,β-unsaturated-δ-lactones represented by: 2 The following formula (3) However, in the formula, R represents a C 1 to C 12 linear or branched alkyl group, a C 7 to C 8 aralkyl group, or a C 3 to C 6 cycloalkyl group. -alkyl-2
-Cyclopenten-1-ones are subjected to catalytic hydrogen reduction in the presence of a catalyst to form the following formula (2): However, in the formula, R has the same meaning as above, and 4-hydroxy-2-alkyl-1 represented by
- The following formula (1) is characterized by forming cyclopentanones and subjecting the compound of formula (2) to an oxidation and dehydration reaction in the presence of a peracid. However, in the formula, R is a method for producing α,β-unsaturated-δ-lactones represented by the same meaning as above.
JP56070658A 1981-05-13 1981-05-13 Preparation of alpha,beta-unsaturated-delta-lactone Granted JPS57188584A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56070658A JPS57188584A (en) 1981-05-13 1981-05-13 Preparation of alpha,beta-unsaturated-delta-lactone

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56070658A JPS57188584A (en) 1981-05-13 1981-05-13 Preparation of alpha,beta-unsaturated-delta-lactone

Publications (2)

Publication Number Publication Date
JPS57188584A JPS57188584A (en) 1982-11-19
JPH0125748B2 true JPH0125748B2 (en) 1989-05-19

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP56070658A Granted JPS57188584A (en) 1981-05-13 1981-05-13 Preparation of alpha,beta-unsaturated-delta-lactone

Country Status (1)

Country Link
JP (1) JPS57188584A (en)

Also Published As

Publication number Publication date
JPS57188584A (en) 1982-11-19

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