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JPS606950B2 - Method for purifying coumarin and its derivatives - Google Patents
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JPS606950B2 - Method for purifying coumarin and its derivatives - Google Patents

Method for purifying coumarin and its derivatives

Info

Publication number
JPS606950B2
JPS606950B2 JP50010123A JP1012375A JPS606950B2 JP S606950 B2 JPS606950 B2 JP S606950B2 JP 50010123 A JP50010123 A JP 50010123A JP 1012375 A JP1012375 A JP 1012375A JP S606950 B2 JPS606950 B2 JP S606950B2
Authority
JP
Japan
Prior art keywords
coumarin
weight
layer
solution
purified
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
JP50010123A
Other languages
Japanese (ja)
Other versions
JPS50106967A (en
Inventor
アロイ ト−マ ヨセフ
アントニアス マリア ユリアナ ステイ−フス ペトラス
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.)
Stamicarbon BV
Original Assignee
Stamicarbon BV
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 Stamicarbon BV filed Critical Stamicarbon BV
Publication of JPS50106967A publication Critical patent/JPS50106967A/ja
Publication of JPS606950B2 publication Critical patent/JPS606950B2/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D311/00Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings
    • C07D311/02Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings ortho- or peri-condensed with carbocyclic rings or ring systems
    • C07D311/04Benzo[b]pyrans, not hydrogenated in the carbocyclic ring
    • C07D311/06Benzo[b]pyrans, not hydrogenated in the carbocyclic ring with oxygen or sulfur atoms directly attached in position 2
    • C07D311/08Benzo[b]pyrans, not hydrogenated in the carbocyclic ring with oxygen or sulfur atoms directly attached in position 2 not hydrogenated in the hetero ring
    • C07D311/10Benzo[b]pyrans, not hydrogenated in the carbocyclic ring with oxygen or sulfur atoms directly attached in position 2 not hydrogenated in the hetero ring unsubstituted

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Pyrane Compounds (AREA)
  • Plural Heterocyclic Compounds (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Fats And Perfumes (AREA)
  • Cosmetics (AREA)

Description

【発明の詳細な説明】 本発明は次式 (式中、各置換基R,〜R6は水素原子かC,〜C5の
アルキル基であればよい。
DETAILED DESCRIPTION OF THE INVENTION The present invention is based on the following formula (wherein each substituent R, ~R6 may be a hydrogen atom or a C, ~C5 alkyl group).

ただし、置換基炭素原子の総数は10以上ではない)で
示される、不純物含有クマリンまたはアルキル化クマリ
ンの精製方法に関する。この種の化合物の製法はイギリ
ス特許第1,368 941号公報及び椿願昭48−9
8166号明細書(特開昭49−62473号)に記載
されている。
However, the total number of substituent carbon atoms is not 10 or more). The method for producing this type of compound is described in British Patent No. 1,368 941 and Tsubaki Gansho 48-9.
It is described in the specification of No. 8166 (Japanese Unexamined Patent Publication No. 49-62473).

これら化合物は香料産業において特に重要であり、従っ
て純度が極めて高くなければならない。一般に要求され
る純度の主な基準はクマリンの色であって、100o
日未満、好適には70o 日未満でなければならない。
クマリンに通常含まれている不純物には、3,4ージヒ
ドロクマリン、エチルフェノール、ジヒドロケィヒ酸や
エチルフェノールとジヒドロケィヒ酸のェステルがある
。クマリンの精製方法はいくつか知られている。例示す
れば、黍蟹及び再結晶がある(例えば、Kirk−00
meで,Encycloped;aofChemica
lTechnology、第2版、第6巻をみられたい
)。ところが、このような方法で得られるクマリンは純
度が香料工業に適用するには十分でなく、例えば精製ク
マリンの色は125〜2500 日である。一方、別な
公知方法によれば、粗製クマリンから樹脂質成分を連続
的に分離し、残ったクマリンを濃硫酸に溶解し、生成し
た溶液に高温で空気を通し、この溶液を水で処理するこ
とによってクマリンを析出させ、析出物を洗浄かつ中和
してから、これを減圧蒸留することによって精製クマリ
ンを得ることができる。この方法は複雑で、得られる製
品の色が約2000 日である上に、出発物質のかなり
の部分が失なわれる。さらに別な方法が茂richte
、第70巻、1937、P237に記載されているが、
この方法ではジヒドロクマリンの脱水素によって反応混
合物を得てから、この反応混合物を蒸留し、蟹出物を水
酸化カリウム水溶液に溶解し、このようにして得られた
溶液を酸で処理し、そしてエーテル抽出を適用すること
によってクマリンを回収している。
These compounds are of particular importance in the perfume industry and therefore must be of extremely high purity. The main criterion of purity generally required is the color of the coumarin, which is
It should be less than 70 days, preferably less than 70 days.
Impurities commonly found in coumarin include 3,4-dihydrocoumarin, ethylphenol, dihydrocinnamic acid, and esters of ethylphenol and dihydroccinnamic acid. Several methods are known for purifying coumarin. Examples include millet crab and recrystallization (e.g. Kirk-00
Me, Encycloped; aofChemica
Technology, 2nd Edition, Volume 6). However, the purity of coumarin obtained by such a method is not sufficient for application to the fragrance industry, for example, the color of purified coumarin is 125 to 2500 days old. On the other hand, according to another known method, the resinous components are continuously separated from the crude coumarin, the remaining coumarin is dissolved in concentrated sulfuric acid, air is passed through the resulting solution at high temperature, and this solution is treated with water. Purified coumarin can be obtained by precipitating coumarin, washing and neutralizing the precipitate, and then distilling it under reduced pressure. This process is complex, the color of the resulting product is approximately 2000 days, and a significant portion of the starting material is lost. There is another method
, Volume 70, 1937, P237,
In this method, a reaction mixture is obtained by dehydrogenation of dihydrocoumarin, the reaction mixture is distilled, the canidate is dissolved in an aqueous potassium hydroxide solution, the solution thus obtained is treated with an acid, and Coumarins have been recovered by applying ether extraction.

この手間のかかる方法によっても「実際的な面からみれ
ば純度が十分でないクマリンしか得られず、しかも上記
反応混合物を水酸化カリウムに熔解するために、大量の
、即ち100夕の反応混合物に対して約2.5モルの水
酸化カリウムが必要である。本発明は、次の一般式(式
中、各置換基R,〜R6は水素原子または炭素原子1〜
5個を有するアルキル基であり、置換基の炭素原子全数
は10以上はない)で示される、不純物含有クマリンま
たはアルキル化クマリンの精製方法において、該クマリ
ンを温度20〜150℃の塩基性化合物の水溶液で処理
し、かくして形成された水性層をクマリン含有層から分
離し、クマリン含有層を温度20o 〜150q0の水
で洗浄し、生成する洗浄層から精製クマリン化合物を回
収することを特徴とする方法を提供するものである。
Even with this labor-intensive method, only a coumarin of insufficient purity was obtained from a practical point of view, and furthermore, in order to dissolve the reaction mixture in potassium hydroxide, a large amount of the reaction mixture, i.e., 100 days, was required. About 2.5 mol of potassium hydroxide is required.The present invention is based on the following general formula (wherein each substituent R, ~R6 is a hydrogen atom or a carbon atom 1~
In the method for purifying impure coumarin or alkylated coumarin, which is an alkyl group having 5 carbon atoms and the total number of carbon atoms in the substituents is not 10 or more, the coumarin is purified with a basic compound at a temperature of 20 to 150 °C. A method characterized by treating with an aqueous solution, separating the aqueous layer thus formed from the coumarin-containing layer, washing the coumarin-containing layer with water at a temperature of 20° to 150q0, and recovering purified coumarin compounds from the resulting washed layer. It provides:

使用する塩基性の水溶液は、たとえばアルカリ金属また
はアルカリ士類金属の水酸化物、たとえば、Na〇日,
K〇日,Li〇日,Mg(〇H)2,Ca(OH)2及
び軸(OH)2の水溶液であればよい。本発明に使用で
きる他の溶液は炭酸ナトリウム、またはカリウム、酢酸
ナトリウムまたはカリウム、および安息香酸ナトリウム
またはカリウムの溶液である。前記溶液中の塩基性化合
物の量は不純物含有クマリン100のこつき塩基性化合
物0.001〜1モル当量が好ましい。最適量は一部は
不純物の量と性質により決定される。多くの場合、不純
物含有クマリン100のこつき塩基性化合物0.005
〜0.1モル当量を含む溶液を使用すれば十分である。
溶液濃度はまた広い範囲内から選択でき、たとえば溶液
は塩基性化合物0.1〜1の重量%を含有すればよい。
不純物含有クマリンの処理及び水洗を行う温度は70o
〜100qoの温度が好ましい。圧力は臨界的ではな
く、従ってこの方法は大気圧で行うことも可能である。
精製クマリン化合物は水洗された層から各種の方法で、
好ましくは蒸留により回収できる。
The basic aqueous solution used is, for example, an alkali metal or alkali metal hydroxide, such as Na
Any aqueous solution of K〇day, Li〇day, Mg(〇H)2, Ca(OH)2 and axis (OH)2 may be used. Other solutions that can be used in the present invention are solutions of sodium or potassium carbonate, sodium or potassium acetate, and sodium or potassium benzoate. The amount of the basic compound in the solution is preferably 0.001 to 1 molar equivalent of coumarin 100 containing impurities. The optimum amount is determined in part by the amount and nature of the impurity. Often contains impurities coumarin 100% stiff basic compound 0.005
It is sufficient to use a solution containing ~0.1 molar equivalent.
The solution concentration can also be selected within a wide range; for example, the solution may contain from 0.1 to 1% by weight of the basic compound.
The temperature for processing and washing coumarin containing impurities is 70o.
A temperature of ~100 qo is preferred. Pressure is not critical, so the process can also be carried out at atmospheric pressure.
Purified coumarin compounds are extracted from the water-washed layer by various methods.
Preferably, it can be recovered by distillation.

本発明による方法で得たクマリンは極めて純度が高く「
そのまま香料工業において使用でき、生成物の色は70
o 日未満である。もし極度に純粋なクマリンを得たい
ならば、これは蒸留によって回収したクマリン生成物を
、たとえばエタノールから再結晶すると得ることができ
る。次に本発明の実施例を示す。
The coumarin obtained by the method of the present invention has extremely high purity.
Can be used as is in the perfume industry, the color of the product is 70
Less than o days. If extremely pure coumarin is desired, this can be obtained by recrystallizing the coumarin product recovered by distillation, for example from ethanol. Next, examples of the present invention will be shown.

実施例 1 不純物含有クマリン186夕、及び水酸化ナトリウム水
溶液(NaOHO.75重量%)186夕を、雛梓機及
び還流冷却器付の500似フラスコに導入した。
Example 1 186 ml of coumarin containing impurities and 186 ml of an aqueous sodium hydroxide solution (NaOHO.75% by weight) were introduced into a 500-sized flask equipped with a filter and a reflux condenser.

不純物含有クマリンは3,4ージヒドロクマリン2重量
%、エチルフェノール0.2重量%、ジヒドロケィヒ酸
0.箱重量%、及び主としてエチルフェノールとジヒド
ロケィヒ酸とのェステルからなる高沸点不純物0.5重
量%を含んでいた。
Impurity-containing coumarin includes 2% by weight of 3,4-dihydrocoumarin, 0.2% by weight of ethylphenol, and 0.2% by weight of dihydrocinnamic acid. % by weight of the box, and 0.5% by weight of high-boiling impurities consisting primarily of esters of ethylphenol and dihydrocinnamic acid.

フラスコ内の混合物を還流下燈拝しながら1時間100
午0で加熱した。次にクマリンを含む層を水性層から分
離し、有機層を合計で180羽の水で2回洗った。クマ
リン170夕を水洗した生成物から蒸留によって回収し
た。このようにして得た精製クマリン生成物は99.9
%以上のクマリンを、0.01重量%のエチルフェノー
ル、0.03重量%のジヒドロケィヒ酸および0.03
重量%の高沸点不純物とともに含んでいた。
Heat the mixture in the flask under reflux for 1 hour.
It was heated at midnight. The coumarin-containing layer was then separated from the aqueous layer and the organic layer was washed twice with a total of 180 portions of water. 170 ml of coumarin was recovered from the water-washed product by distillation. The purified coumarin product thus obtained is 99.9
% of coumarin, 0.01% by weight of ethylphenol, 0.03% by weight of dihydrocinnamic acid and 0.03% by weight of coumarin.
It contained % by weight of high-boiling impurities.

生成物の色は650 日であった。クマリン生成物70
夕を50%エタノール250の‘から再結晶した。
The color of the product was 650 days. Coumarin product 70
The solution was recrystallized from 250 ml of 50% ethanol.

次にクマリンを炉過し、合計で50の‘の20%エタノ
ールで2回洗浄した。生成物を乾燥して純度99.95
%以上の高度に精製されたクマリン62夕を、0.01
重量%未満のジヒドロケィヒ酸及び0.01重量%の高
沸点不純物とともに得た。色相は60o 日であった。
実施例 0 不純物含有クマリン40夕と、炭酸ナトリウム(Na2
C瓜0.塁重量%)の水溶液40夕とを蝿梓機及び還流
冷却器付の100の‘フラスコに導入した。
The coumarin was then filtered and washed twice with a total of 50' of 20% ethanol. Dry the product to a purity of 99.95
More than 0.01% of highly purified coumarin 62%
It was obtained with less than % by weight of dihydrocinnamic acid and 0.01% by weight of high boiling impurities. The hue was 60°.
Example 0 Impurity-containing coumarin 40mg and sodium carbonate (Na2
C melon 0. An aqueous solution of 40% (% by weight) was introduced into a 100ml flask equipped with a flask and a reflux condenser.

不純物含有クマリンは90重量%のクマリンを、2重量
%の3,4−ジヒドロクマリン、0.2重量%のエチル
フェノール、0.3重量%のジヒドロケィヒ酸及び0.
5重量%の高沸点不純物とともに含んでいた。フラスコ
内の混合物を還流下損拝しながら100午0において1
時間加熱した。次にクマリンを含有する層を塩基性化合
物の含有層から分離し、合計で40の‘の水で2回洗浄
した。有機層を蒸留し、クマリン99.虫重量%以上を
エチルフェノール0.01重量%、ジヒドロケイヒ酸0
.01重量%禾満及び高沸点不純物0.02重量%とと
もに含む精製クマリン36夕を得た。生成物の色は6が
日であった。
The impure coumarin contains 90% by weight of coumarin, 2% by weight of 3,4-dihydrocoumarin, 0.2% by weight of ethylphenol, 0.3% by weight of dihydroccinnamic acid, and 0.2% by weight of ethylphenol.
It contained 5% by weight of high boiling point impurities. 1 at 100 pm while refluxing the mixture in the flask.
heated for an hour. The coumarin-containing layer was then separated from the basic compound-containing layer and washed twice with a total of 40' of water. Distill the organic layer and extract coumarin 99. Contains 0.01% by weight of ethylphenol and 0% dihydrocinnamic acid by weight of insects.
.. A purified coumarin containing 0.01% by weight and 0.02% by weight of high-boiling impurities was obtained. The color of the product was 6 days.

比較実験 実施例1で用いた不純物含有クマリンと同一組成を有す
る不純物含有クマリン100夕と、硫酸(8増量量%の
QS04)100夕とを還流冷却器、灘伴機及びガス導
入貸付の250一肌【フラスコに導入した。
Comparative Experiment Example 1 100 tons of impurity-containing coumarin having the same composition as the impurity-containing coumarin used in Example 1 and 100 tons of sulfuric acid (QS04 with an increase of 8%) were added to a reflux condenser, a Nada combustor, and 250 tons of gas introduction loan. Skin [introduced into flask.

フラスコ内の混合物を燭拝しながら110qoで2時間
加熱し、内容物に毎時135その空気を通入した。次に
反応混合物を200泌の水中に注ぎ、これによってクマ
リンの析出物を得た。
The mixture in the flask was heated with a candle at 110 qo for 2 hours, passing air through the contents at 135 liters per hour. The reaction mixture was then poured into 200 g of water, thereby obtaining a coumarin precipitate.

析出物を炉別し、水洗してから減圧で蒸留した。得られ
たクマリン生成物は99.5重量%のクマリンを、0.
1重量%のエチルフェノール、0.を重量%の3,4ー
ジヒドロクマリン、0.02重量%のジヒドロケィヒ酸
と、及び0.018重量%の高沸点不純物とともに含ん
でいた。
The precipitate was separated in a furnace, washed with water, and then distilled under reduced pressure. The resulting coumarin product contains 99.5% by weight of coumarin and 0.9% by weight of coumarin.
1% by weight of ethylphenol, 0. along with 3,4-dihydrocoumarin, 0.02% dihydroccinnamic acid, and 0.018% high boiling impurities.

生成物の色は2000日であった。The color of the product was 2000 days.

本発明の実施の態様を説明すると次のようになる。The embodiments of the present invention will be explained as follows.

{1’ 塩基性化合物の溶液が不純物含有クマリン10
0外こつき0.001〜1モル当量の塩基性化合物を含
むようにした特許請求の範囲に記載の方法。
{1' The solution of basic compound contains impurity coumarin 10
The method according to claim 1, wherein the basic compound is contained in an amount of 0.001 to 1 molar equivalent.

■ 前記塩基性化合物がアルカリ金属水酸化物またはア
ルカリ金属炭酸塩である特許請求の範囲または実施の態
様mに記載の方法。
(2) The method according to claim or embodiment m, wherein the basic compound is an alkali metal hydroxide or an alkali metal carbonate.

【3} 水洗工程後、クマリン化合物を蒸留により回収
するようにした特許請求の範囲並に実施の態様1},■
のいずれかに記載の方法。
[3} Claims and embodiment 1 in which the coumarin compound is recovered by distillation after the water washing process}, ■
The method described in any of the above.

{4} 前記蒸留で得たクマリン化合物を再結晶するよ
うにした前項‘3’1こ記載の方法。
{4} The method described in the preceding item '3'1, wherein the coumarin compound obtained by the distillation is recrystallized.

‘51 特に実施例を引用して実質的にここに記載した
特許請求の範囲に記載の方法。
'51 A method as claimed substantially herein with particular reference to the Examples.

Claims (1)

【特許請求の範囲】 1 次の一般式 ▲数式、化学式、表等があります▼ (式中、各置換基R_1〜R_6は水素原子または炭素
原子1〜5個を有するアルキル基であり、置換基の炭素
原子全数は10以上はない)で示される、不純物含有ク
マリンまたはアルキル化クマリンの精製方法において、
該クマリンを温度20〜150℃の塩基性化合物の水溶
液で処理し、かくして形成された水性層をクマリン含有
層から分離し、クマリン含有層を温度20°〜150℃
の水で洗浄し、生成する洗浄層から精製クマリン化合物
を回収することを特徴とする方法。
[Claims] 1. The following general formula ▲ Numerical formula, chemical formula, table, etc. ▼ (In the formula, each substituent R_1 to R_6 is a hydrogen atom or an alkyl group having 1 to 5 carbon atoms, The total number of carbon atoms is not more than 10), in a method for purifying impure coumarin or alkylated coumarin,
The coumarin is treated with an aqueous solution of a basic compound at a temperature of 20° to 150°C, the aqueous layer thus formed is separated from the coumarin-containing layer, and the coumarin-containing layer is heated to a temperature of 20° to 150°C.
A method characterized by washing with water and recovering a purified coumarin compound from the resulting washing layer.
JP50010123A 1974-01-25 1975-01-23 Method for purifying coumarin and its derivatives Expired JPS606950B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NL7401012A NL7401012A (en) 1974-01-25 1974-01-25 PURIFICATION OF CUMARIN AND ITS ALKYLATED DERIVATIVES.
NL7401012 1974-01-25

Publications (2)

Publication Number Publication Date
JPS50106967A JPS50106967A (en) 1975-08-22
JPS606950B2 true JPS606950B2 (en) 1985-02-21

Family

ID=19820611

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50010123A Expired JPS606950B2 (en) 1974-01-25 1975-01-23 Method for purifying coumarin and its derivatives

Country Status (11)

Country Link
JP (1) JPS606950B2 (en)
BE (1) BE824780A (en)
CA (1) CA1053687A (en)
CH (1) CH593276A5 (en)
DE (1) DE2502690C2 (en)
ES (1) ES434112A1 (en)
FR (1) FR2259101B1 (en)
GB (1) GB1443406A (en)
IT (1) IT1026457B (en)
NL (1) NL7401012A (en)
SE (1) SE417609B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018110059A1 (en) 2016-12-16 2018-06-21 株式会社ダイセル Paper sheet and method for manufacturing paper sheet

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3191333B2 (en) * 1990-12-19 2001-07-23 住友化学工業株式会社 Method for producing 3,4-dihydrocoumarin
HRP960308A2 (en) * 1996-07-02 1998-08-31 Ljerka Poljak New coumarine derivatives, process for the preparation thereof and their use

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018110059A1 (en) 2016-12-16 2018-06-21 株式会社ダイセル Paper sheet and method for manufacturing paper sheet

Also Published As

Publication number Publication date
DE2502690C2 (en) 1984-05-10
CA1053687A (en) 1979-05-01
DE2502690A1 (en) 1975-07-31
SE7500786L (en) 1975-07-28
SE417609B (en) 1981-03-30
CH593276A5 (en) 1977-11-30
JPS50106967A (en) 1975-08-22
ES434112A1 (en) 1976-12-16
BE824780A (en) 1975-07-24
NL7401012A (en) 1975-07-29
GB1443406A (en) 1976-07-21
IT1026457B (en) 1978-09-20
FR2259101B1 (en) 1978-02-24
FR2259101A1 (en) 1975-08-22

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