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JPS6136239A - Production of dihydro-beta-ionone - Google Patents

Production of dihydro-beta-ionone

Info

Publication number
JPS6136239A
JPS6136239A JP59155438A JP15543884A JPS6136239A JP S6136239 A JPS6136239 A JP S6136239A JP 59155438 A JP59155438 A JP 59155438A JP 15543884 A JP15543884 A JP 15543884A JP S6136239 A JPS6136239 A JP S6136239A
Authority
JP
Japan
Prior art keywords
ionone
dihydro
raney nickel
nickel catalyst
beta
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
JP59155438A
Other languages
Japanese (ja)
Inventor
Hideki Masuda
秀樹 増田
Satoshi Mihara
智 三原
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.)
OGAWA KORYO KK
Original Assignee
OGAWA KORYO 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 OGAWA KORYO KK filed Critical OGAWA KORYO KK
Priority to JP59155438A priority Critical patent/JPS6136239A/en
Publication of JPS6136239A publication Critical patent/JPS6136239A/en
Pending 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

Landscapes

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

Abstract

PURPOSE:In producing dihydro-beta-ionone useful as perfume, etc. by reducing catalytically beta-ionone, to obtain the aimed compound advantageously, by reducing selectively the double bond of a side chain by the use of a specifically treated Raney nickel catalyst. CONSTITUTION:A Raney alloy (alloy of nickel and aluminum) is added to an aqueous solution of sodium hydroxide, heated at about 70-110 deg.C, aluminum is eluted from the alloy, the supernatant liquid is removed, the precipitate is heated in water or an organic solvent (preferably ethanol) at about 50-80 deg.C to give Raney nickel catalyst. beta-Ionone is catalytically reduced by the use of the Raney nickel catalyst, to give selectively dihydro-beta-ionone useful as an intermediate for ionone derivatives useful as perfume existing in yellow passion fruit, osmanthus, etc., further to be expected as theaspirane, theaspirone, etc.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はジヒドロ−β−ヨノンの改良された製造方法に
関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to an improved method for producing dihydro-β-ionone.

さらに詳しくは、本発明はβ−ヨノンを接触還元してジ
ヒドロ−β−ヨノンを製造する方法において特定の処理
を施したラネーニッケル触媒を使用することにより選択
的に側鎖の二重結合を還元する改良されたジヒドロ、−
β−ヨノンの製法ニ関するものである。
More specifically, the present invention selectively reduces double bonds in side chains by using a specially treated Raney nickel catalyst in a method for producing dihydro-β-ionone by catalytic reduction of β-ionone. Improved dihydro, -
This invention relates to a method for producing β-ionone.

ジヒドロ−β−ヨノンは、きいちご、イエローノ9 ツ
ションフルーツ、オスマンサス等中に存在りそれ自体香
料として有用であシ、さらにテアスピラン、テアスピラ
ン等香料として将来期待される数多くのヨノン系誘導体
の合成中間体としても有用である。
Dihydro-β-ionone is present in strawberry, yellow fruit, osmanthus, etc., and is useful as a flavoring agent in itself.It is also useful for the synthesis of numerous ionone derivatives that are expected to be used as flavoring agents in the future, such as theaspiran and theaspiran. It is also useful as an intermediate.

α−ヨノン、β−ヨノン、バニリデンアセトン等の側鎖
に2重結合を有する不飽和カルボニル化合物の側鎖の2
重結合のみを選択的に還元する方法として、特定の条件
でラネーニッケルの展開を行なっだラネー触媒を使用す
る方法が知られている(特公昭58−19656号)。
2 of the side chain of unsaturated carbonyl compounds having a double bond in the side chain such as α-ionone, β-ionone, vanylidene acetone, etc.
As a method for selectively reducing only heavy bonds, a method using a Raney catalyst prepared by developing Raney nickel under specific conditions is known (Japanese Patent Publication No. 58-19656).

この従来法では、水酸化ナトリウム水溶液にラネー合金
(Ni:AA=1:1)を添加し、系を90〜95℃で
約3時間加熱し、約24時間放冷した後水酸化す) I
Jウム水溶液を加え、さらに約90〜95℃で約2時間
加熱して得られるラネー触媒が使用される。
In this conventional method, Raney alloy (Ni:AA=1:1) is added to an aqueous sodium hydroxide solution, the system is heated at 90 to 95°C for about 3 hours, allowed to cool for about 24 hours, and then hydroxylated.
A Raney catalyst obtained by adding a Jium aqueous solution and further heating at about 90 to 95° C. for about 2 hours is used.

(発明が解決しようとする問題点) 上記従来法によれば、α−ヨノンは選択的にジヒドロ−
α−ヨノンに還元されるが、β−ヨノンは選択的にジヒ
ドロ−β−ヨノンに還元されず、相当量のテトラヒドロ
フランが生成する。
(Problems to be Solved by the Invention) According to the above conventional method, α-ionone is selectively dihydro-
Although it is reduced to α-ionone, β-ionone is not selectively reduced to dihydro-β-ionone, and considerable amounts of tetrahydrofuran are formed.

従って本発明はβ−ヨノンの側鎖の2重結合のみを選択
的に還元してジヒドロ−β−ヨノンを製造する方法を提
供することを目的とする。
Therefore, an object of the present invention is to provide a method for producing dihydro-β-ionone by selectively reducing only the double bond in the side chain of β-ionone.

(問題を解決するだめの手段) 本発明の上記目的は、β−ヨノンを接触還元してジヒド
ロ−β−ヨノンを製造する方法において、下記のラネー
ニッケル触媒を使用する本発明の方法によって達成され
る: (ラネーニッケル触媒) 水酸化ナトリウム水溶液にラネー合金にニッケルとアル
ミニウムの合金)を加え、約70〜110℃に加熱して
該合金からアルミニウムを溶出させ、上清液を除き、沈
殿物を水または有機溶媒中で約50〜80℃に加熱して
得られるラネーニッケル触媒。
(Means for Solving the Problem) The above object of the present invention is achieved by the method of the present invention which uses the Raney nickel catalyst described below in a method for producing dihydro-β-ionone by catalytic reduction of β-ionone. : (Raney nickel catalyst) Raney alloy (nickel and aluminum alloy) is added to an aqueous sodium hydroxide solution and heated to approximately 70 to 110°C to elute aluminum from the alloy. The supernatant is removed and the precipitate is dissolved in water or Raney nickel catalyst obtained by heating to about 50-80°C in an organic solvent.

本発明の方法で使用されるラネーニッケル触媒を調製す
るに際しては、先ずニッケルとアルミニウムからなるラ
ネー合金を常法に従って水酸化ナトリウム水溶液中で約
70〜110℃に加熱する。ラネー合金のニッケルとア
ルミニウムとの比(重量)には特に制限はないが普通1
:1である。加熱温度は上記の範囲が適当であり、これ
より高い温度では触媒活性が弱くなりすぎて収量が低下
し、上記よシ低い温度では逆に触媒活性が強すぎて還元
の選択性に乏しくなる。加熱時間は約3〜10時間であ
る。加熱終了後放冷し、上清液を除き、望ましくはPH
7になるまで水洗し、沈殿物に水または有機溶媒を加え
て約50〜80℃で加熱する。有機溶媒としてはメタノ
ール、エタノール、プロA?ノール、ブタノールのよう
なアルコール類、酢酸エチルのようなエステル類、ジオ
キサン、テトラヒドロフランのようなエーテル類または
トルエンのような芳香族炭化水素類等が使用される。特
に好ましい溶媒は酢酸エチルまたはエタノールである。
In preparing the Raney nickel catalyst used in the method of the present invention, first, a Raney alloy consisting of nickel and aluminum is heated to about 70 to 110 DEG C. in an aqueous sodium hydroxide solution according to a conventional method. There is no particular limit to the ratio (weight) of nickel to aluminum in Raney alloys, but it is usually 1
:1. The heating temperature is preferably within the above range; at temperatures higher than this, the catalytic activity becomes too weak and the yield decreases, and at lower temperatures, the catalytic activity becomes too strong and the selectivity of reduction becomes poor. Heating time is approximately 3 to 10 hours. After heating, let it cool, remove the supernatant, and preferably adjust the pH.
7, add water or an organic solvent to the precipitate, and heat at about 50 to 80°C. As an organic solvent, methanol, ethanol, ProA? Alcohols such as alcohol and butanol, esters such as ethyl acetate, ethers such as dioxane and tetrahydrofuran, or aromatic hydrocarbons such as toluene are used. Particularly preferred solvents are ethyl acetate or ethanol.

加熱温度の下限は臨界的ではないが加熱時間等操作上の
見地から約50℃以上が望ましい。加熱温度の上限は約
80℃であり、これより高い温度で加熱すると収量が低
下する。加熱時間は加熱温度に依存する。加熱温度が5
0℃の場合は2時間以上好ましくは5〜6時間であシ、
エタノールの還流温度(79℃)の場合は1〜2時間が
適当である。
Although the lower limit of the heating temperature is not critical, it is preferably about 50° C. or higher from the operational standpoint such as heating time. The upper limit of the heating temperature is about 80° C., and heating at a temperature higher than this lowers the yield. Heating time depends on heating temperature. Heating temperature is 5
In the case of 0°C, it is 2 hours or more, preferably 5 to 6 hours,
In the case of the reflux temperature of ethanol (79°C), 1 to 2 hours is appropriate.

本発明の方法において、β−ヨノンの還元工程は従来公
知の方法と同様にして実施される。すなわち、β−ヨノ
ンを酢酸エチル等の適当な不活性有機溶媒に溶解し、本
発明のラネーニッケル触媒を加え、反応系を水素ガスで
置換する。水素圧は常圧で十分である。
In the method of the present invention, the reduction step of β-ionone is carried out in the same manner as conventionally known methods. That is, β-ionone is dissolved in a suitable inert organic solvent such as ethyl acetate, the Raney nickel catalyst of the present invention is added, and the reaction system is replaced with hydrogen gas. Normal hydrogen pressure is sufficient.

反応温度は40〜60℃が好ましい。40℃以下の温度
では反応が遅く、60℃以上の温度では副生成物である
テトラヒドロフランの量が多くなる。
The reaction temperature is preferably 40 to 60°C. At temperatures below 40°C, the reaction is slow, and at temperatures above 60°C, the amount of by-product tetrahydrofuran increases.

反応時間はおよそ10〜40時間であシ、攪拌によって
反応時間は大きく短縮される。反応終了後、所望の生成
物は常法に従って反応混合物中から採取される。例えば
、反応混合液を濾過して触媒を除き、涙液を減圧濃縮す
る。残留物を減圧蒸留すると所望のジヒドロ−β−ヨノ
ンが得られる。
The reaction time is approximately 10 to 40 hours, and the reaction time is greatly shortened by stirring. After the reaction is complete, the desired product is recovered from the reaction mixture according to conventional methods. For example, the reaction mixture is filtered to remove the catalyst and the lachrymal fluid is concentrated under reduced pressure. Distillation of the residue under reduced pressure yields the desired dihydro-β-ionone.

次に実施例を示して本発明の方法をさらに具体的に説明
する。
Next, the method of the present invention will be explained in more detail with reference to Examples.

実施例1 水酸化ナトリウム12.6L?を水100m7!に溶解
し、氷水浴にて内温10℃以下に冷却する。これにラネ
ー合金(Ni :、AA=1:1,50%)2o1をよ
くかきまぜながら少しずつ加える。その間液温を25℃
以下に保つ。添加終了後、該混合物を油浴温度90〜9
5℃、内温的70〜75℃で7時間加熱、攪拌する。放
冷後、沈殿物を流水で洗浄し、PHが7に彦っだときに
95係エタノールで2回洗浄し、ついで99.5ヂエタ
ノールを加えて50℃で6時間加熱する。
Example 1 Sodium hydroxide 12.6L? 100m7 of water! and cooled to an internal temperature of 10°C or less in an ice water bath. Raney alloy (Ni:, AA=1:1, 50%) 2o1 is added little by little to this while stirring well. Meanwhile, keep the liquid temperature at 25℃.
Keep below. After the addition is complete, the mixture is heated to an oil bath temperature of 90-90.
Heat and stir at 5°C, internal temperature 70-75°C for 7 hours. After cooling, the precipitate was washed with running water, and when the pH reached 7, it was washed twice with 95% ethanol, and then 99.5% ethanol was added and heated at 50°C for 6 hours.

β−ヨノン(純度98%)72グを酢酸エチル108グ
に溶解する。上で調製したラネーニッケル触媒のエタノ
ール溶液からエタノールを傾斜法で除き、泥状のラネー
ニッケル触媒11グを上記溶液に加える。反応系内を水
素ガス置換し、内温50℃で29時間、激しく攪拌する
。反応液をろ過し、酢酸エチルで触媒を十分洗浄し、減
圧濃縮して溶媒を除く。粗油を減圧蒸留するとジヒドロ
−β−ヨノン64.91(純度93チ、bp105℃/
 :llmmI(g +収率89.3 w/w%、83
1モル1モル係)が得られる。
Dissolve 72 g of β-ionone (98% purity) in 108 g of ethyl acetate. Ethanol is removed from the ethanol solution of Raney nickel catalyst prepared above by decanting, and 11 g of Raney nickel catalyst in mud form is added to the solution. The inside of the reaction system was replaced with hydrogen gas, and the mixture was vigorously stirred at an internal temperature of 50° C. for 29 hours. The reaction solution is filtered, the catalyst is thoroughly washed with ethyl acetate, and the solvent is removed by concentration under reduced pressure. When the crude oil was distilled under reduced pressure, dihydro-β-ionone 64.91 (purity 93%, bp 105℃/
:llmmI(g + yield 89.3 w/w%, 83
1 mole) is obtained.

比較のため実施例1において、ラネーニッケルの展開後
にエタノール中で加熱しない触媒を用いて上記と同様に
してβ−ヨノンを還元したところ、・ソヒドローβ−ヨ
ノンの収率は42.3 w/w%であり、副生物(テト
ラヒドロイオン)の収率は54.4. w/wチであっ
た。
For comparison, in Example 1, β-ionone was reduced in the same manner as above using a catalyst that was not heated in ethanol after development of Raney nickel, and the yield of sohydro β-ionone was 42.3 w/w%. The yield of the by-product (tetrahydro ion) is 54.4. It was w/w chi.

また前記特公昭58−19656号に記載のラネーニッ
ケル触媒を使用して上記と同様にしてβ−ヨノンを還元
したところ、ジヒドロ−β−ヨノンの収率は32.2%
であった。
Furthermore, when β-ionone was reduced in the same manner as above using the Raney nickel catalyst described in Japanese Patent Publication No. 58-19656, the yield of dihydro-β-ionone was 32.2%.
Met.

実施例2 ラネーニッケル触媒の調製 水酸化ナトリウム101を水40づに溶解し、氷水浴に
て内温2℃以下に冷却する。これにラネー合金(Ni:
AA=1:1.50チ)10tをよくかきまぜながら少
しずつ加える。その間液温を25℃以下に保つ。添加終
了後、該混合物を油浴温度130℃、内温110℃に4
時間加熱攪拌する。
Example 2 Preparation of Raney Nickel Catalyst 101 parts of sodium hydroxide was dissolved in 40 parts of water and cooled to an internal temperature of 2° C. or less in an ice water bath. This is combined with Raney alloy (Ni:
AA=1:1.50ch) Add 10t little by little while stirring well. During this time, keep the liquid temperature below 25°C. After the addition was completed, the mixture was heated to an oil bath temperature of 130°C and an internal temperature of 110°C.
Heat and stir for an hour.

次いで19係水酸化す) IJウム水溶液(NaOH2
,7グ、)I20137りを加え、内温110℃で3時
間加熱攪拌する(油浴温度130℃)。放冷後、沈殿物
を流水でPH7になるまで洗浄し、次いで95チエタノ
ールで2回洗浄し、99.5%エタノールを加えて2時
間加熱還流する。
Next, 19 hydroxide) IJium aqueous solution (NaOH2
, 7g, ) I20137 was added, and the mixture was heated and stirred at an internal temperature of 110°C for 3 hours (oil bath temperature: 130°C). After cooling, the precipitate was washed with running water until the pH reached 7, then washed twice with 95% ethanol, added with 99.5% ethanol, and heated under reflux for 2 hours.

β−ヨノン(純度98%)25ft’を酢酸エチル50
fIに溶解する。上で調製したラネーニッケル触媒のエ
タノール溶液からエタノールを傾斜法で除き、泥状のラ
ネーニッケル触媒3.51を上記溶液に加える。反応系
を水素ガス置換し、内温50℃で4時間激しく攪拌する
。反応液をろ過し、酢酸エチルで触媒を十分洗浄し、減
圧濃縮して溶媒を除く。粗油を減圧蒸留するとジヒドロ
−β−ヨノン21.7 f (純度86%、bp96℃
72mmEg、収率86.6 w/w % 、74.5
モル1モル%)が得られる。
25 ft' of β-ionone (98% purity) in 50 ml of ethyl acetate
Dissolve in fI. Ethanol is decanted from the ethanol solution of Raney nickel catalyst prepared above, and 3.5 liters of Raney nickel catalyst in slurry form is added to the solution. The reaction system was purged with hydrogen gas and stirred vigorously for 4 hours at an internal temperature of 50°C. The reaction solution is filtered, the catalyst is thoroughly washed with ethyl acetate, and the solvent is removed by concentration under reduced pressure. Dihydro-β-ionone 21.7 f (purity 86%, bp 96°C) was distilled under reduced pressure from the crude oil.
72 mmEg, yield 86.6 w/w%, 74.5
1 mol %) is obtained.

実施例3 ラネーニッケル触媒の調製 実施例2のラネーニッケル触媒の調製において、ラネー
展開後の触媒をエタノール中で加熱する代りに水媒体中
、50℃で6時間加熱する以外は実施例1と同様の操作
によシラネーニッ久ル触媒を調製した。
Example 3 Preparation of Raney nickel catalyst In preparing the Raney nickel catalyst of Example 2, the same procedure as in Example 1 was performed except that instead of heating the Raney developed catalyst in ethanol, the catalyst was heated at 50° C. for 6 hours in an aqueous medium. A silane nickel catalyst was prepared.

β−ヨノン(純度98%)2Ofをエタノール40′?
に溶解する。上で調製したラネーニッケルの水溶液から
水を傾斜法で除き、泥状のラネーニッケル触媒31を上
記溶液に加える。反応系を水素ガス置換し、内温50℃
で4時間激しく攪拌する。反応液を濾過し、エタノール
で触媒を十分洗浄し、減圧濃縮して溶媒を除く。粗油を
減圧蒸留するとジヒドロ−β−ヨノン17f(純度88
%。
β-ionone (98% purity) 2Of ethanol 40'?
dissolve in Water is removed from the Raney nickel aqueous solution prepared above by decanting, and muddy Raney nickel catalyst 31 is added to the solution. The reaction system was replaced with hydrogen gas, and the internal temperature was 50℃.
Stir vigorously for 4 hours. The reaction solution is filtered, the catalyst is thoroughly washed with ethanol, and the solvent is removed by concentration under reduced pressure. Dihydro-β-ionone 17f (purity 88
%.

bp 96℃/ 2 mmHg + 収率85 w/w
%、75.5モル1壬ルチ)が得られる。
bp 96℃/2 mmHg + Yield 85 w/w
%, 75.5 mol 1 ruti) is obtained.

Claims (2)

【特許請求の範囲】[Claims] (1)β−ヨノンを接触還元してジヒドロ−β−ヨノン
を製造する方法において下記のラネーニッケル触媒を使
用することを特徴とするジヒドロ−β−ヨノンの製法。 (ラネーニッケル触媒) 水酸化ナトリウム水溶液にラネー合金(ニ ッケルとアルミニウムの合金)を加え、約 70〜110℃に加熱して該合金からアルミニウムを溶
出させ、上清液を除き、沈殿物を水または有機溶媒中で
約50〜80℃に加熱して得られるラネーニッケル触媒
(1) A method for producing dihydro-β-ionone, which comprises using the following Raney nickel catalyst in the method for producing dihydro-β-ionone by catalytic reduction of β-ionone. (Raney nickel catalyst) Raney alloy (nickel and aluminum alloy) is added to an aqueous sodium hydroxide solution, heated to approximately 70 to 110°C to elute aluminum from the alloy, the supernatant liquid is removed, and the precipitate is washed with water or organic Raney nickel catalyst obtained by heating to about 50-80°C in a solvent.
(2)有機溶媒がエタノールである特許請求の範囲第1
項記載のジヒドロ−β−ヨノンの製法。
(2) Claim 1 in which the organic solvent is ethanol
Method for producing dihydro-β-ionone as described in Section 1.
JP59155438A 1984-07-27 1984-07-27 Production of dihydro-beta-ionone Pending JPS6136239A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59155438A JPS6136239A (en) 1984-07-27 1984-07-27 Production of dihydro-beta-ionone

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59155438A JPS6136239A (en) 1984-07-27 1984-07-27 Production of dihydro-beta-ionone

Publications (1)

Publication Number Publication Date
JPS6136239A true JPS6136239A (en) 1986-02-20

Family

ID=15606030

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59155438A Pending JPS6136239A (en) 1984-07-27 1984-07-27 Production of dihydro-beta-ionone

Country Status (1)

Country Link
JP (1) JPS6136239A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1081950C (en) * 1998-09-14 2002-04-03 中国科学院广州化学研究所 Method preparation of compound catalyst with selective preparation of dihydro-beta-irisone
CN111871429A (en) * 2020-08-28 2020-11-03 万华化学集团股份有限公司 Raney catalyst and preparation method thereof, and method for preparing gamma-ketene from alpha, gamma-dienone

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1081950C (en) * 1998-09-14 2002-04-03 中国科学院广州化学研究所 Method preparation of compound catalyst with selective preparation of dihydro-beta-irisone
CN111871429A (en) * 2020-08-28 2020-11-03 万华化学集团股份有限公司 Raney catalyst and preparation method thereof, and method for preparing gamma-ketene from alpha, gamma-dienone
CN111871429B (en) * 2020-08-28 2022-07-12 万华化学集团股份有限公司 Raney catalyst and preparation method thereof, and method for preparing gamma-ketene from alpha, gamma-dienone

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