JP2002234886A - Method for producing acetal - Google Patents

Method for producing acetal

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Publication number
JP2002234886A
JP2002234886A JP2001282983A JP2001282983A JP2002234886A JP 2002234886 A JP2002234886 A JP 2002234886A JP 2001282983 A JP2001282983 A JP 2001282983A JP 2001282983 A JP2001282983 A JP 2001282983A JP 2002234886 A JP2002234886 A JP 2002234886A
Authority
JP
Japan
Prior art keywords
ketone
acetal
aldehyde
polyhydric alcohol
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
JP2001282983A
Other languages
Japanese (ja)
Inventor
Hideo Tawara
秀雄 田原
Toshinori Tanaka
俊伯 田中
Kaoru Omae
薫 大前
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.)
Kao Corp
Original Assignee
Kao Corp
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 Kao Corp filed Critical Kao Corp
Priority to JP2001282983A priority Critical patent/JP2002234886A/en
Publication of JP2002234886A publication Critical patent/JP2002234886A/en
Pending legal-status Critical Current

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for easily and efficiently producing a high-quality acetal in a short time. SOLUTION: This method for producing an acetal comprises reaction between a polyhydric alcohol and a ketone or aldehyde in the equivalent ratio of the ketone or aldehyde to the to-be-acetalized hydroxy groups in the polyhydric alcohol of (0.5-4):2 in the presence of a solid acid catalyst without conducting a substantial dehydration, and distillation of the resultant reaction liquid.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、化粧品等の乳化剤
や保湿剤、工業用乳化剤、界面活性剤及び食品添加物等
の製造原料、並びに各種有機合成における中間体として
有用な多価アルコールのケタール又はアセタール(以下
単にアセタールという)の製造法に関する。
The present invention relates to a raw material for producing emulsifiers and humectants for cosmetics, industrial emulsifiers, surfactants and food additives, and ketals of polyhydric alcohols useful as intermediates in various organic syntheses. Or, it relates to a method for producing acetal (hereinafter simply referred to as acetal).

【0002】[0002]

【従来の技術及び発明が解決しようとする課題】アセタ
ールの製造法としては、酸触媒存在下、多価アルコール
とケトン又はアルデヒドを、石油エーテル、ヘキサン等
の共沸脱水溶媒を用い脱水条件下で反応させる方法(例
えば特開昭60−87282号)や、捕水剤を用い反応
を行う方法(例えばUSP3,535,888号)が知
られている。しかしながら、これらの方法は脱水条件の
選定が必要であり、また、アセタール化の反応が脱水律
速であるため、高反応率を得るためには反応時間が長い
などの問題がある。
2. Description of the Related Art As a method for producing an acetal, a polyhydric alcohol and a ketone or an aldehyde are prepared under the conditions of dehydration using an azeotropic dehydration solvent such as petroleum ether or hexane in the presence of an acid catalyst. A method of reacting (for example, JP-A-60-87282) and a method of performing a reaction using a water catching agent (for example, US Pat. No. 3,535,888) are known. However, these methods require selection of dehydration conditions, and have a problem that the reaction for acetalization is rate-determined by dehydration, so that a long reaction time is required to obtain a high conversion.

【0003】また、共沸脱水溶媒や捕水剤等で脱水を行
わなくても、反応率を上げるために大過剰(多価アルコ
ールに対して15倍モル以上)のケトン又はアルデヒド
を加えて反応を行う方法は知られている(例えばWO9
811087)。しかしこの方法は、アセタールを得る
ために、中和後、多量に用いたケトン又はアルデヒドを
除去する必要があり、生産性が悪く、工業化に適した方
法とは言えない。
[0003] even without dehydration by azeotropic dehydration solvent and water-capturing agent, etc., in addition to a ketone or aldehyde of large excess in order to increase the reaction rate (15 times by mole or more based on the polyhydric alcohol) reaction Is known (for example, WO9
811087). However, this method requires a large amount of ketone or aldehyde to be removed after neutralization in order to obtain an acetal, so that the productivity is poor and cannot be said to be a method suitable for industrialization.

【0004】本発明の課題は、短時間に簡便に効率よく
アセタールを製造する方法を提供することにある。
An object of the present invention is to provide a method for efficiently and efficiently producing an acetal in a short time.

【0005】[0005]

【課題を解決するための手段】本発明は、多価アルコー
ルとケトン又はアルデヒドとを、多価アルコールのアセ
タール化される水酸基2当量に対し、ケトン又はアルデ
ヒドを0.5〜4当量の割合で用い、酸触媒存在下、実
質的な脱水を行わずに反応させ、反応液から蒸留により
アセタールを得る、アセタールの製造法である。
According to the present invention, a polyhydric alcohol and a ketone or an aldehyde are added at a ratio of 0.5 to 4 equivalents of the ketone or the aldehyde to 2 equivalents of the hydroxyl group to be acetalized of the polyhydric alcohol. This is a method for producing an acetal in which a reaction is carried out in the presence of an acid catalyst without substantial dehydration, and an acetal is obtained from the reaction solution by distillation.

【0006】[0006]

【発明の実施の形態】本発明で用いる多価アルコールは
水酸基を2個以上もつ化合物であり、エチレングリコー
ル、プロピレングリコール、ブチレングリコール、グリ
セリン、エリスリトール、ソルビトール、トリメチロー
ルプロパン、ペンタエリスリトール、アラビノース、キ
シロース、グルコース、マンノース、ガラクトース、フ
ラクトース、イノシトール、ショ糖、乳糖、麦芽糖、セ
ロピオース、デキストリン、デンプン、セルロース、グ
ルコサゾン、グルコサミン、グルコン酸、酒石酸、アデ
ノシン、アスコルビン酸、ウリジン、オーキシン、モノ
グリセリド、ジグリセリン、トリグリセリン、モノグリ
セリルエーテル等が挙げられ、グリセリンが好ましい。
また、これら多価アルコールは、含水品を脱水したもの
を用いてもよい。
DETAILED DESCRIPTION OF THE INVENTION The polyhydric alcohol used in the present invention is a compound having two or more hydroxyl groups, and is ethylene glycol, propylene glycol, butylene glycol, glycerin, erythritol, sorbitol, trimethylolpropane, pentaerythritol, arabinose, xylose. Glucose, mannose, galactose, fructose, inositol, sucrose, lactose, maltose, cellopose, dextrin, starch, cellulose, glucosazone, glucosamine, gluconic acid, tartaric acid, adenosine, ascorbic acid, uridine, auxin, monoglyceride, diglycerin, triglyceride Glycerin, monoglyceryl ether and the like can be mentioned, and glycerin is preferable.
These polyhydric alcohols may be obtained by dehydrating a water-containing product.

【0007】また、本発明で用いるケトンとしては、ア
セトン、メチルエチルケトン、メチルイソブチルケト
ン、シクロヘキサノン、メチル−n−プロピルケトン、
メチル−n−ブチルケトン、メチル−sec−ブチルケト
ン、メチル−t−ブチルケトン、メチル−n−ヘキシル
ケトン、メチル−2−フリルケトン、ジエチルケトン、
エチル−n−プロピルケトン、ジ−n−ヘキシルベンジ
ルケトン、アセトフェノン、n−ブチロフェノン、ベン
ゾイン等が挙げられ、アルデヒドとしては、ホルムアル
デヒド、アセトアルデヒド、プロピオンアルデヒド、ブ
チルアルデヒド等が挙げられる。これらのケトン又はア
ルデヒドの中では、アセトンが好ましい。
The ketone used in the present invention includes acetone, methyl ethyl ketone, methyl isobutyl ketone, cyclohexanone, methyl-n-propyl ketone,
Methyl-n-butyl ketone, methyl-sec-butyl ketone, methyl-t-butyl ketone, methyl-n-hexyl ketone, methyl-2-furyl ketone, diethyl ketone,
Ethyl-n-propyl ketone, di-n-hexylbenzyl ketone, acetophenone, n-butyrophenone, benzoin and the like are mentioned, and aldehydes are formaldehyde, acetaldehyde, propionaldehyde, butyraldehyde and the like. Of these ketones or aldehydes, acetone is preferred.

【0008】本発明においては、効率的にアセタールを
得る観点から、多価アルコールのアセタール化される水
酸基2当量に対し、ケトン又はアルデヒドを0.5〜4
当量、好ましくは0.5〜2当量の割合で用い、実質的
な脱水を行わずに反応させる。
In the present invention, from the viewpoint of efficiently obtaining an acetal, a ketone or aldehyde is added in an amount of 0.5 to 4 with respect to 2 equivalents of the hydroxyl group to be acetalized of the polyhydric alcohol.
The reaction is performed in an equivalent amount, preferably in a ratio of 0.5 to 2 equivalents, without causing substantial dehydration.

【0009】本発明において、実質的な脱水を行わない
とは、脱水を行わないことのみならず、アセタール化率
を90%以上に行う場合を目的として脱水を行わないこ
とを意味する。よって、その目的を目指さない範囲での
少量脱水は行っても構わない。
In the present invention, not substantially performing dehydration means not only not performing dehydration but also not performing dehydration for the purpose of performing an acetalization ratio of 90% or more. Therefore, a small amount of dehydration may be performed within a range not aiming at the purpose.

【0010】また、原料である多価アルコール、ケト
ン、アルデヒドは、含水したものを用いてもよいが、本
反応は水が生成する平衡反応であるため、反応中の水分
が少ない方がアセタール化率が向上するため、予め脱水
し、水分を低減した原料を用いることが好ましい。
Further, the polyhydric alcohol which is the raw material, ketones, aldehydes, may be used after water, because the reaction is an equilibrium reaction which produces water, it is acetalization moisture is less in the reaction In order to improve the efficiency, it is preferable to use a raw material which has been previously dehydrated and reduced in water content.

【0011】本発明に用いられる酸触媒は、特に限定さ
れないが、塩酸、硫酸等の無機酸、パラトルエンスルホ
ン酸、ベンゼンスルホン酸等の有機酸等が挙げられる。
酸触媒は、多価アルコールに対して、好ましくは0.0
01〜50重量%、更に好ましくは0.05〜1.0重
量%用いる。
The acid catalyst used in the present invention is not particularly limited, and examples thereof include inorganic acids such as hydrochloric acid and sulfuric acid, and organic acids such as paratoluenesulfonic acid and benzenesulfonic acid.
Acid catalyst, relative to the polyhydric alcohol, preferably 0.0
It is used in an amount of from 0.01 to 50% by weight, more preferably from 0.05 to 1.0% by weight.

【0012】本発明においては、減圧又は常圧下、好ま
しくは10〜200℃、更に好ましくは20〜100℃
の反応温度で、脱水を行わずに、多価アルコールのアセ
タール化を行う。反応終了後、酸触媒を中和し、未反応
のケトン又はアルデヒドと生成した水を減圧留去等の方
法で除いた後、アセタールを蒸留により得る。
In the present invention, under reduced pressure or normal pressure, preferably 10 to 200 ° C., more preferably 20 to 100 ° C.
The acetalization of the polyhydric alcohol is carried out at the reaction temperature of 1 without dehydration. After completion of the reaction, the acid catalyst is neutralized, unreacted ketone or aldehyde and generated water are removed by a method such as distillation under reduced pressure, and the acetal is obtained by distillation.

【0013】更に、本発明においては、上記の蒸留前に
回収したケトン又はアルデヒドと、アセタール回収後の
多価アルコールを含んだ残液とを用いて、同様のアセタ
ール化を行うのが好ましい。
Further, in the present invention, it is preferable to perform the same acetalization using the ketone or aldehyde recovered before the above-mentioned distillation and the residual liquid containing the polyhydric alcohol after the recovery of the acetal.

【0014】[0014]

【発明の効果】本発明により、化粧品等の乳化剤や保湿
剤、工業用乳化剤、界面活性剤及び食品添加物等の製造
原料、並びに各種有機合成の中間体として有用な多価ア
ルコールのアセタールを短時間で簡便に効率よく合成す
ることが可能となる。
Industrial Applicability According to the present invention, raw materials for producing emulsifiers and humectants for cosmetics and the like, industrial emulsifiers, surfactants and food additives, and acetal of polyhydric alcohols useful as intermediates for various organic synthesis can be shortened. It is possible to simply and efficiently synthesize in a short time.

【0015】[0015]

【実施例】尚、例中の%は特記しない限り重量基準であ
る。
EXAMPLES The percentages in the examples are by weight unless otherwise specified.

【0016】実施例1 ケトンとしてアセトン、多価アルコールとしてグリセリ
ンを、表1に示す割合で用い、硫酸を多価アルコールに
対して0.1%仕込み、65℃の温度で1時間反応を行
った。次に触媒を水酸化ナトリウムで中和し、アセトン
を減圧留去した後、1.33kPaで80〜100℃で減
圧蒸留を行い、目的物である2,2−ジメチル−1,3
−ジオキソラン−4−メタノールを得た。仕込み重量収
率{[生成アセタールg/(グリセリンg+アセトン
g)]×100(wt%)}を表1に示す。
Example 1 Acetone was used as a ketone and glycerin was used as a polyhydric alcohol at the ratios shown in Table 1, and 0.1% of sulfuric acid was added to the polyhydric alcohol, followed by a reaction at a temperature of 65 ° C. for 1 hour. . Then neutralize the catalyst with sodium hydroxide, was distilled off under reduced pressure and acetone, subjected to vacuum distillation at 80 to 100 ° C. at 1.33 kPa, the desired product 2,2-dimethyl-1,3
-Dioxolane-4-methanol was obtained. Table 1 shows the charge weight yield {[acetal formed g / (glycerin g + acetone g)] × 100 (wt%)}.

【0017】[0017]

【表1】 [Table 1]

【0018】表1から明らかなように、グリセリンに対
して0.5〜4倍モルのアセトンを使用した場合に、仕
込み重量収率が高い。
As is evident from Table 1, when the acetone is used in an amount of 0.5 to 4 times mol of glycerin, the charged weight yield is high.

【0019】実施例2:2,2−ジメチル−1,3−ジ
オキソラン−4−メタノールの合成) 3L4ツ口フラスコに、グリセリン920.9g(1
0.0モル)とアセトン1162.0g(20.0モ
ル)と硫酸1.04gを仕込み、65℃の温度で1時間
反応を行った。次に触媒を水酸化ナトリウムで中和し、
アセトンを減圧留去した後、1.33kPaで80〜10
0℃で減圧蒸留を行い、目的物である2,2−ジメチル
−1,3−ジオキソラン−4−メタノールを留分として
528.6g得た。ガスクロ純度99.6area%、仕込
み重量収率25.4wt%。トータル合成時間5時間。
Example 2: Synthesis of 2,2-dimethyl-1,3-dioxolan-4-methanol In a 3L four-necked flask, 920.9 g of glycerin (1
(0.0 mol), 1162.0 g (20.0 mol) of acetone and 1.04 g of sulfuric acid, and reacted at a temperature of 65 ° C. for 1 hour. Then the catalyst is neutralized with sodium hydroxide,
After acetone was distilled off under reduced pressure, with 1.33 kPa 80 to 10
Vacuum distillation was carried out at 0 ° C. to obtain 528.6 g of 2,2-dimethyl-1,3-dioxolan-4-methanol as a fraction as a fraction. Gas chromatography purity: 99.6 area%, charge weight yield: 25.4 wt%. Total synthesis time 5 hours.

【0020】上記の減圧留去したアセトン(含水7%)
100gを、理論段数10段、還流比2の精留塔にて蒸
留を行い、回収アセトン(含水1%)を95g得た。上
記減圧蒸留の残液(グリセリンが主成分)46gに、こ
の回収アセトン(含水1%)58gと硫酸0.05gを
仕込み、65℃の温度で1時間反応を行った。次に触媒
を水酸化ナトリウムで中和し、アセトンを減圧留去した
後、1.33kPaで80〜100℃で減圧蒸留を行い、
目的物である2,2−ジメチル−1,3−ジオキソラン
−4−メタノールを留分として24.0g得た。ガスク
ロ純度99.2area%。
Acetone distilled off under reduced pressure (containing 7% of water)
100 g was distilled in a rectification column having 10 theoretical plates and a reflux ratio of 2 to obtain 95 g of recovered acetone (containing 1% of water). 58 g of the recovered acetone (containing 1% of water) and 0.05 g of sulfuric acid were charged into 46 g of the residual liquid (mainly composed of glycerin) from the above vacuum distillation, and a reaction was carried out at a temperature of 65 ° C. for 1 hour. Next, the catalyst was neutralized with sodium hydroxide, acetone was distilled off under reduced pressure, and then vacuum distillation was performed at 1.33 kPa at 80 to 100 ° C.
As a fraction, 24.0 g of 2,2-dimethyl-1,3-dioxolan-4-methanol, which was the target substance, was obtained. Gas chromatography purity 99.2 area%.

【0021】比較例1:2,2−ジメチル−1,3−ジ
オキソラン−4−メタノールの合成 1L4ツ口フラスコに、グリセリン50g(0.54モ
ル)とアセトン630.7g(10.86モル)と硫酸
3.4gを仕込み、還流下4時間反応を行った。次に触
媒を水酸化ナトリウムで中和し、アセトンを減圧留去し
た後、目的物である2,2−ジメチル−1,3−ジオキ
ソラン−4−メタノールを留分として71g得た。ガス
クロ純度95area%、仕込み重量収率10.4wt%。ト
ータル合成時間6時間。
Comparative Example 1: Synthesis of 2,2-dimethyl-1,3-dioxolan-4-methanol In a 1-L four-necked flask, 50 g (0.54 mol) of glycerin and 630.7 g (10.86 mol) of acetone were added. 3.4 g of sulfuric acid was charged and reacted for 4 hours under reflux. Next, the catalyst was neutralized with sodium hydroxide, and acetone was distilled off under reduced pressure. Thus, 71 g of 2,2-dimethyl-1,3-dioxolan-4-methanol, which was a target substance, was obtained as a fraction. Gas chromatography purity: 95area%, charge weight yield: 10.4wt%. 6 hours total synthesis time.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 多価アルコールとケトン又はアルデヒド
とを、多価アルコールのケタール又はアセタール(以下
単にアセタールという)化される水酸基2当量に対し、
ケトン又はアルデヒドを0.5〜4当量の割合で用い、
酸触媒存在下、実質的な脱水を行わずに反応させ、反応
液から蒸留によりアセタールを得る、アセタールの製造
法。
Claims: 1. A polyhydric alcohol and a ketone or aldehyde are converted to 2 equivalents of a hydroxyl group to be converted into a ketal or an acetal (hereinafter simply referred to as an acetal) of the polyhydric alcohol.
Using a ketone or aldehyde in a ratio of 0.5 to 4 equivalents,
A method for producing an acetal, comprising reacting in the presence of an acid catalyst without substantial dehydration to obtain an acetal by distillation from the reaction solution.
【請求項2】 ケトン又はアルデヒドが、蒸留前に回収
したケトン又はアルデヒドである請求項1記載の製造
法。
2. The method according to claim 1, wherein the ketone or aldehyde is a ketone or aldehyde recovered before distillation.
【請求項3】 多価アルコールが、アセタール回収後の
残液中に含まれるものである請求項1又は2記載の製造
法。
3. The method according to claim 1, wherein the polyhydric alcohol is contained in a residual liquid after the acetal is recovered.
JP2001282983A 2000-12-04 2001-09-18 Method for producing acetal Pending JP2002234886A (en)

Priority Applications (1)

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Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP2000367932 2000-12-04
JP2000-367932 2000-12-04
JP2001282983A JP2002234886A (en) 2000-12-04 2001-09-18 Method for producing acetal

Publications (1)

Publication Number Publication Date
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Family

ID=26605135

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Country Link
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002234885A (en) * 2000-12-04 2002-08-23 Kao Corp Method for producing acetal
JP2006273750A (en) * 2005-03-29 2006-10-12 Nof Corp Method for production of 1, 3-dioxolan compound
JP2009196917A (en) * 2008-02-20 2009-09-03 Kao Corp Method for producing 1,3-dioxane
WO2014156858A1 (en) * 2013-03-26 2014-10-02 花王株式会社 Method for improving strength of hydraulic composition hardened product

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6087282A (en) * 1983-10-20 1985-05-16 Nippon Oil & Fats Co Ltd Preparation of ketal
DD238232A1 (en) * 1985-06-11 1986-08-13 Univ Schiller Jena PROCESS FOR PREPARING 2,2-DIMETHYL-4-METHYLOL-1,3-DIOXOLANE
JPH0413643A (en) * 1990-05-07 1992-01-17 Kureha Chem Ind Co Ltd Production of chloroacetals
WO1998011087A1 (en) * 1996-09-10 1998-03-19 Daiso Co., Ltd. Process for preparing 1,3-dioxolane-4-methanol compounds
JP2000514302A (en) * 1996-07-16 2000-10-31 ペルノ、リカール Process for producing natural 1,3-diol derivatives and corresponding natural 1,3-dioxane derivatives

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6087282A (en) * 1983-10-20 1985-05-16 Nippon Oil & Fats Co Ltd Preparation of ketal
DD238232A1 (en) * 1985-06-11 1986-08-13 Univ Schiller Jena PROCESS FOR PREPARING 2,2-DIMETHYL-4-METHYLOL-1,3-DIOXOLANE
JPH0413643A (en) * 1990-05-07 1992-01-17 Kureha Chem Ind Co Ltd Production of chloroacetals
JP2000514302A (en) * 1996-07-16 2000-10-31 ペルノ、リカール Process for producing natural 1,3-diol derivatives and corresponding natural 1,3-dioxane derivatives
WO1998011087A1 (en) * 1996-09-10 1998-03-19 Daiso Co., Ltd. Process for preparing 1,3-dioxolane-4-methanol compounds

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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JP2009196917A (en) * 2008-02-20 2009-09-03 Kao Corp Method for producing 1,3-dioxane
WO2014156858A1 (en) * 2013-03-26 2014-10-02 花王株式会社 Method for improving strength of hydraulic composition hardened product
JP2014189417A (en) * 2013-03-26 2014-10-06 Kao Corp Strength improver composition for hydraulic powder

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