CN101417935B - Method for preparing oxo-isophorone by catalytic oxidation using metal free catalytic system - Google Patents

Method for preparing oxo-isophorone by catalytic oxidation using metal free catalytic system Download PDF

Info

Publication number
CN101417935B
CN101417935B CN2008101629956A CN200810162995A CN101417935B CN 101417935 B CN101417935 B CN 101417935B CN 2008101629956 A CN2008101629956 A CN 2008101629956A CN 200810162995 A CN200810162995 A CN 200810162995A CN 101417935 B CN101417935 B CN 101417935B
Authority
CN
China
Prior art keywords
isophorone
reaction
hydroxyphthalimide
ketoisophorone
catalyzer
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.)
Active
Application number
CN2008101629956A
Other languages
Chinese (zh)
Other versions
CN101417935A (en
Inventor
李浩然
陈志荣
毛建拥
王从敏
胡兴邦
胡柏剡
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.)
Zhejiang University ZJU
Zhejiang NHU Co Ltd
Original Assignee
Zhejiang University ZJU
Zhejiang NHU Co Ltd
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 Zhejiang University ZJU, Zhejiang NHU Co Ltd filed Critical Zhejiang University ZJU
Priority to CN2008101629956A priority Critical patent/CN101417935B/en
Publication of CN101417935A publication Critical patent/CN101417935A/en
Application granted granted Critical
Publication of CN101417935B publication Critical patent/CN101417935B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention relates to a new method for preparing keto-isophorone, which utilizes metal free co-catalyst system to catalyze and oxidize Beta-isophorone. Beta-isophorone is used as the raw material; in the presence of an organic solvent, molecular oxygen or an oxygen rich gas is used as an oxidant; under the effect of the co-catalyst system composed by the main catalyst N-hydroxyphthalimide and the analogues of N-hydroxyphthalimide, and organic cocatalyst, keto-isophorone is prepared by catalytic oxidation; reaction temperature ranges from 0 to 120 DEG C; reaction time ranges from 5 to 50 hours; keto-isophorone with high selectivity can be generated. The method has the advantages that, the catalyst is metal free, cheap and easy to be obtained; reaction conditions are mild; operation is simple; the product has high selectively; recycling is easy, and multiple usage can be realized.

Description

The method of preparing oxo-isophorone by catalytic oxidation using metal free catalytic system
Technical field
The present invention relates to a kind of novel method of utilizing the common catalystsystem catalyzed oxidation β-isophorone of no metal to prepare ketoisophorone; Particularly relate to method with preparing oxo-isophorone by catalytic oxidation using metal free catalytic system; It is characterized in that: raw material β-isophorone, in the presence of solvent, with N-hydroxyphthalimide and analogue and the common catalystsystem of organic promoter composition; Use molecular oxygen or oxygen rich gas to be oxygenant, oxidation generates ketoisophorone.
Background technology
Ketoisophorone is called for short KIP, is a kind of important chemical medicine intermediate, can be used as seasonings or spices in the foodstuff additive, also can be used for synthetic makeup.Ketoisophorone still prepares the important intermediate of VITAMINs and carrotenoid.Be a kind of weak yellow liquid or solid under the normal temperature, its pure article fragrance is strong, and lasting is lasting, and fragrance is that the close sweet banksia rose of little acid, dry fruit are fragrant, and various cigarette are all had significant perfuming effect.
Because the importance of ketoisophorone in fields such as chemical and medicine industry for a long time, is oxidized to the focus that ketoisophorone is chemical field research with α-isophorone or β-isophorone always.Particularly for the oxidation of β-isophorone, patent and the document reported at present are many.Generally speaking, the oxidation of β-isophorone at present mainly is that the organic coordination compounds with transition metal is a homogeneous catalyst, carries out oxidation with molecular oxygen or air, many times can add some additives (such as solubility promoter etc.).Different-phase catalyst also has application in reaction.
Catalyzer patent from reaction is adopted mainly contains transition metal salt catalyst, transition metal acetyl acetone complex catalyzer; Transition metal schiff bases complex catalyzer; In addition transition metal porphyrin or phthalocyanine complex catalyzer, also have all metal catalyst etc.Can find out that from these patents adopting transition metal is the catalyzer at center,, under the conditions such as solubility promoter, can generate ketoisophorone by catalyzed oxidation β-isophorone at suitable organic bases and solvent, have in addition have very high transformation efficiency and a productive rate.
In US 4046813, described a kind of in the presence of the organic bases pyridine; Use the acetyl acetone complex of lead, vanadium, chromium, manganese, iron, cobalt etc. to be catalyzer; Catalyzed oxidation β-isophorone prepares the method for ketoisophorone, though this method has about 100% transformation efficiency, reaction simultaneously also makes β-isophorone to α-isophorone isomerizing easily; And form the high by product that gathers in the reaction again easily, institute is so that reaction preference descends.
In US6297404 and US6300521, described a kind ofly in the presence of DMF or DMA and tripropyl amine, use the catalysis system catalyzed oxidation β-isophorone of Schiff's base and lithium acetate or ammonium acetate to prepare the method for ketoisophorone; The shortcoming of a maximum of this method is that reaction is easy to generate 3,5,5-trimethyl-cyclohex-2-en-4-hydroxyl-1-ketone; 2; 2,6-trimethyl-cyclohexane-1, by products such as 4-diketone; Because each side such as these by product molecular weight and character are similar with product, thereby it is quite difficult with separating of ketoisophorone.
And in US4898985; Described a kind ofly in the presence of triethylamine and glycol dimethyl ether, used the porphyrin of iron, cobalt, ketone, manganese or phthalocyanine complex to be catalyzer, catalyzed oxidation β-isophorone prepares the method for ketoisophorone; Though this method has very high yield; But the transition-metal catalyst of porphyrin class is quite expensive, and in reaction, also is destroyed easily, makes that this technology cost is higher.The alkaline environment of glycol dimethyl ether combination triethylamine formation is abnormally dangerous on oxidation operation in addition; Because the burning-point of this mixture is very low; So for security reasons, although this method has very high yield, it must just can be implemented on technical scale under preventive measures as safe as a house.
Situation from the above-identified patent summary; Transition metal-organic coordination compound the catalyzer that adopts at present carries out the reaction that oxidation of beta-isophorone prepares ketoisophorone; The problem that exists is that reaction is slow under cryogenic condition; The easy isomery of β-isophorone turns to α-isophorone and other by product under the high temperature, greatly reduces the selectivity of reaction and the productive rate of ketoisophorone; Though and employing porphyrin class catalyzer can overcome above-mentioned shortcoming, it is high a lot of that the price of synthetic porphyrin catalyst is wanted, and destroy catalyzer in reacting again easily or cause poisoning of catalyst etc., makes the reaction unstable increase greatly.Simultaneously; Homogeneous catalyst as transition metal-type;, reaction can not directly from reaction system, separate after accomplishing, recovery and reuse, and its result not only makes reaction solvent, product etc. separate difficulty to be increased; Portion of product also can polymerization form by product in the presence of catalyzer simultaneously, and the final a large amount of pin material that forms has also increased the pressure of environment.
Summary of the invention
The purpose of this invention is to provide a kind of novel method for preparing ketoisophorone.Especially, it is to have adopted N-hydroxyphthalimide and analogue thereof to be total to catalystsystem with other organic promoter bonded than the characteristics of above-mentioned catalyzer.Reaction can be carried out under the condition of gentleness, and reaction pin material rate is low, has good transformation efficiency and selectivity, and catalyzer can also reclaim and reuse simultaneously.
The method of preparing oxo-isophorone by catalytic oxidation using metal free catalytic system provided by the invention, reaction formula is:
Figure G2008101629956D00021
β-IP is oxidized to KIP
The present invention is that (β-IP) is a raw material with β-isophorone; In the presence of organic solvent; Common catalystsystem with N-hydroxyphthalimide and analogue and organic promoter composition uses molecular oxygen or oxygen rich gas oxygenant, and catalyzed oxidation prepares ketoisophorone (KIP).Temperature of reaction is 0 ℃~120 ℃, and the reaction times is 5~50 hours, generates the high ketoisophorone of selectivity.
In the altogether catalystsystem of the present invention, Primary Catalysts is a N-hydroxyphthalimide, 3,4, a kind of in 5,6 tetrachloros-N-hydroxyphthalimide, the 4-alkoxyl formyl-N-hydroxyphthalimide; And preferred N-hydroxyphthalimide.
In the altogether catalystsystem of the present invention, promotor is Lucidol, anthraquinone and 1,4-diamino--2, and 3-dichloroanthraquinone, Tetrabutyl amonium bromide, 2,2 '-a kind of in Diisopropyl azodicarboxylate, phenanthrolene and the bromine; And preferred Lucidol, anthraquinone.
In the catalystsystem altogether of the present invention, the scope of the mol ratio of Primary Catalysts and promotor is between 200: 1 to 10: 1, and preferably between 80: 1 to 40: 1.
The mol ratio of β-isophorone of the present invention and Primary Catalysts can be in the variation range of a broad, usually between 100: 1 to 1: 5, and preferably between 25: 1 to 1: 2.
Oxygenant of the present invention can be pure oxygen, be rich in the gas of oxygen, air.In 1 kilogram of β-isophorone, oxygen-supply quantity hourly is 50~1000L normally, and preferably at 100~500L.Oxygenous for other, its air flow can be converted according to oxygen level accordingly.
Temperature of reaction of the present invention is between 0 ℃~120 ℃, and preferably between 20 ℃~80 ℃.
Reaction solvent of the present invention can be one or both in acetone, benzyl cyanide, ETHYLE ACETATE, acetate, acetonitrile, DMSO 99.8MIN., phenyl trichloromethane, N, toluene, THF, the pyridine, and ethyl acetate, acetone, acetonitrile.
The scope of β-isophorone of the present invention and reaction solvent mol ratio is between 5: 1 to 1: 50, and preferably between 2: 1 to 1: 10.
Reaction times of the present invention is between 5~50 hours, and preferably between 10~30 hours.
The N-hydroxyphthalimide of use of the present invention and analogue catalyzer thereof make catalyzer separate with solvent and ketoisophorone through recrystallization after reaction finishes, and the catalyzer that obtains is used for the oxidizing reaction of β-isophorone once more.
Compare with traditional method, the used catalyzer of the present invention is very novel, and this N-hydroxyphthalimide catalyst system has following characteristic: 1) it is the organic catalytic system that cheap no metal is participated in; 2) the reaction conditions needed is gentle; 3) product selectivity is high.Than the transition metal-type homogeneous catalyst, it can utilize through simple recovery again.Simultaneously, the by product like two clusters in the reaction significantly reduces, and reaction conditions is gentle, separate easily and control, and preparing ketoisophorone for catalyzed oxidation β-isophorone is a kind of good method and catalyzer separate easily and control, is easy to utilize again.
Embodiment:
Following embodiment will more comprehensively describe the present invention.
Embodiment 1
The N-hydroxyphthalimide catalyzer that in the 50ml flask with four necks,round bottom, adds 0.82g, the acetone of 40ml is put into 60 ℃ water-bath; β-the isophorone that adds 6.9g after 20 minutes again, the Lucidol of 0.02g, aerating oxygen reacts then; Reaction process is monitored with gc; With ethyl benzoate is that interior mark is demarcated, and the transformation efficiency of measuring β-isophorone behind the 20h is 93%, and the selectivity of ketoisophorone is 88.5%.
Embodiment 2
4-alkoxyl formyl-N-hydroxyphthalimide the catalyzer that in the 50ml flask with four necks,round bottom, adds 1.46g, the acetone of 40ml is put into 60 ℃ water-bath; β-the isophorone that adds 6.9g after 20 minutes again, the phenanthrolene of 0.02g, aerating oxygen reacts then; Reaction process is monitored with gc; With ethyl benzoate is that interior mark is demarcated, and the transformation efficiency of measuring β-isophorone behind the 20h is 97%, and the selectivity of ketoisophorone is 78.5%.
Embodiment 3-5
Be similar to embodiment 1, temperature of reaction is to carry out under 60 ℃ the condition, and the reaction times is 20h; Change the molar ratio of β-isophorone and N-hydroxyphthalimide, must be like following table after the reaction end:
Figure G2008101629956D00041
Embodiment 6-8
Be similar to embodiment 1, temperature of reaction is to carry out under 60 ℃ the condition, and the reaction times is 20h; Select different solvents, must be like following table after reaction finishes:
Figure G2008101629956D00042
Embodiment 9-12
Be similar to embodiment 1, temperature of reaction is to carry out under 60 ℃ the condition, and the reaction times is 20h; Select different common catalystsystem, must be like following table after reaction finishes:
Figure G2008101629956D00043
Figure G2008101629956D00051
Embodiment 13
Reaction conditions according to embodiment 1 reacts.Reaction is removed most of solvent through underpressure distillation after accomplishing, and puts into refrigerator and cooled then and freezes, and has the NHPI crystal to separate out, and filters washing, the NHPI catalyzer that drying obtains reclaiming.The catalyzer that reclaims is reused for β-isophorone oxidation, and oxidizing condition is according to embodiment 1, and measuring β-isophorone transformation efficiency behind the reaction 20h is 88%, and the ketoisophorone selectivity is 86%.

Claims (3)

1. the method for a preparing oxo-isophorone by catalytic oxidation using metal free catalytic system; It is characterized in that: with β-isophorone is raw material; In the presence of organic solvent; Use molecular oxygen or oxygen rich gas to be oxygenant, catalyzed oxidation prepares ketoisophorone under the common catalystsystem effect of being made up of the Primary Catalysts and the organic promoter of N-hydroxyphthalimide and analogue thereof; Described Primary Catalysts is: N-hydroxyphthalimide, 3,4, a kind of in 5,6 tetrachloros-N-hydroxyphthalimide, the 4-alkoxyl formyl-N-hydroxyphthalimide; Said organic promoter is: Lucidol, anthraquinone, 1, and 4-diamino--2,3-dichloroanthraquinone, Tetrabutyl amonium bromide, 2,2 '-a kind of in the Diisopropyl azodicarboxylate, phenanthrolene; The mol ratio of Primary Catalysts and promotor is between 200: 1 to 10: 1 in the said catalystsystem altogether; The mol ratio of said β-isophorone and Primary Catalysts is between 100: 1 to 1: 5; Said molecular oxygen or oxygen rich gas, in 1 kilogram of β-isophorone, oxygen-supply quantity hourly is 50~1000L; Temperature of reaction is 0 ℃~120 ℃, and the reaction times is 5~50 hours, generates the high ketoisophorone of selectivity.
2. according to the said method for preparing ketoisophorone of claim 1, it is characterized in that: organic solvent is one or both in acetone, benzyl cyanide, ETHYLE ACETATE, acetate, acetonitrile, DMSO 99.8MIN., phenyl trichloromethane, N, toluene, THF, the pyridine.
3. according to the said method for preparing ketoisophorone of claim 1; It is characterized in that: N-hydroxyphthalimide and analogue catalyzer thereof are after reaction finishes; Through recrystallization catalyzer is separated with solvent and ketoisophorone, the catalyzer that obtains is used for the oxidizing reaction of β-isophorone once more.
CN2008101629956A 2008-12-11 2008-12-11 Method for preparing oxo-isophorone by catalytic oxidation using metal free catalytic system Active CN101417935B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2008101629956A CN101417935B (en) 2008-12-11 2008-12-11 Method for preparing oxo-isophorone by catalytic oxidation using metal free catalytic system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2008101629956A CN101417935B (en) 2008-12-11 2008-12-11 Method for preparing oxo-isophorone by catalytic oxidation using metal free catalytic system

Publications (2)

Publication Number Publication Date
CN101417935A CN101417935A (en) 2009-04-29
CN101417935B true CN101417935B (en) 2012-05-09

Family

ID=40628957

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2008101629956A Active CN101417935B (en) 2008-12-11 2008-12-11 Method for preparing oxo-isophorone by catalytic oxidation using metal free catalytic system

Country Status (1)

Country Link
CN (1) CN101417935B (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105601490B (en) * 2014-11-13 2017-10-17 四川大学 Efficiently catalyzing and oxidizing α isophorones prepare ketoisophorone
CN109456153B (en) * 2018-11-26 2020-04-28 上虞新和成生物化工有限公司 Synthesis method of oxoisophorone
CN115703702B (en) * 2021-08-16 2024-05-28 安徽圣诺贝化学科技有限公司 Method for preparing tea-flavored ketone by oxidizing alpha-isophorone
CN114797988B (en) * 2022-05-16 2023-08-11 万华化学(四川)有限公司 Synthesis of composite catalyst and method for preparing beta-isophorone
CN115677461A (en) * 2022-10-27 2023-02-03 万华化学集团股份有限公司 Method for continuously producing 4-oxoisophorone by using tower reactor

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1660753A (en) * 2004-12-10 2005-08-31 浙江大学 Method for preparing 3,5,5-trimethyl-hexamethylene-2-olefin-1,4 diketone

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1660753A (en) * 2004-12-10 2005-08-31 浙江大学 Method for preparing 3,5,5-trimethyl-hexamethylene-2-olefin-1,4 diketone

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
Xinli Tong et al..Highly efficient and metal-free oxidation of olefins by molecular oxygen under mild conditions.《Tetrahedron》.2007,第63卷第7634–7639页. *

Also Published As

Publication number Publication date
CN101417935A (en) 2009-04-29

Similar Documents

Publication Publication Date Title
CN101417935B (en) Method for preparing oxo-isophorone by catalytic oxidation using metal free catalytic system
CN107445827B (en) Method for preparing glyoxylic ester by oxidative dehydrogenation of glycolic ester
Zeng et al. One-pot three-component Mannich-type reactions using Sulfamic acid catalyst under ultrasound irradiation
Zhu et al. Study on guanidine-based task-specific ionic liquids as catalysts for direct aldol reactions without solvent
CN103539665B (en) A kind of method of preparing succinate
Chavan et al. Formation and role of cobalt and manganese cluster complexes in the oxidation of p-xylene
CN104592192A (en) Method for preparing epsilon-caprolactone
DE502007003524D1 (en) PREPARATION OF PHTHALIC ACID ANHYDRIDE BY GAS PHASE OXIDATION OF O-XYLENE IN A MAIN AND NIGHT REACTOR
US4581469A (en) Method for producing biphenyltetracarboxylic esters
Hu et al. Efficient and selective palladium-catalyzed direct oxidative esterification of benzylic alcohols under aerobic conditions
CN104292106B (en) A kind of one kettle way prepares the method for organic carboxylic ester
CN101182288A (en) Method for oxo isophorone by heterogeneous oxidization
KR100965633B1 (en) A process for the preparation of p-toluic acid by liquid phase oxidation of p-xylene in water
CN109574814A (en) A kind of method that toluene liquid phase catalytic oxidation prepares benzaldehyde and benzyl alcohol
WO2021047292A1 (en) NOVEL METHOD FOR CO-PRODUCTION OF CARBOXYLIC ACID BASED ON OXYGEN OXIDATION AND ε-CAPROLACTONE
CN107311890A (en) A kind of method of synthesis of carboxylic acid cyanomethyl ester
CN100497282C (en) Preparation method of oxoisophorone
CN109876849B (en) 1, 4-naphthoquinone catalyst prepared by liquid-phase oxidation of naphthalene and preparation method and application thereof
US4346230A (en) Process for the preparation of dimethyl terephthalate
CN101100418A (en) Method for preparing aromatic ketone or aromatic aldehyde by selectively oxidizing alkyl arene
JPS63130556A (en) Production of pyromellitic acid
US3564018A (en) Production of lactones having from six to thirteen ring members and isobutyric acid
CN1923783A (en) Method of preparing 3,5,5-trimethyl-cyclohex-2-en-1,4-dione by heterophase oxidation
CN1271031C (en) Method for preparing 3,5,5-trimethyl-hexamethylene-2-olefin-1,4 diketone
CN107619400B (en) Preparation method of maleic anhydride

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant