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CN100519499C - Method for preparing aromatic ketone or aromatic aldehyde by selectively oxidizing alkyl arene - Google Patents

Method for preparing aromatic ketone or aromatic aldehyde by selectively oxidizing alkyl arene Download PDF

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CN100519499C
CN100519499C CNB2006100895892A CN200610089589A CN100519499C CN 100519499 C CN100519499 C CN 100519499C CN B2006100895892 A CNB2006100895892 A CN B2006100895892A CN 200610089589 A CN200610089589 A CN 200610089589A CN 100519499 C CN100519499 C CN 100519499C
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aromatic
reaction
catalytic system
acridine
hydroxyphthalimide
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CN101100418A (en
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徐杰
仝新利
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Dalian Institute of Chemical Physics of CAS
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Dalian Institute of Chemical Physics of CAS
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Abstract

一种由吖啶类化合物、分子溴和N-羟基邻苯二甲酰亚胺三种有机小分子组成的非金属催化体系,可以催化分子氧作氧源的芳香烃选择氧化反应;使用该催化体系可以于温和条件下催化氧气氧化芳香烃生成芳香酮或芳香醛,避免了使用金属催化剂带来的毒性大、污染严重及费用高等缺点。A non-metallic catalytic system composed of acridine compounds, molecular bromine and N-hydroxyphthalimide three organic small molecules, which can catalyze the selective oxidation of aromatic hydrocarbons with molecular oxygen as the oxygen source; using the catalyst The system can catalyze the oxygen oxidation of aromatic hydrocarbons under mild conditions to generate aromatic ketones or aromatic aldehydes, avoiding the disadvantages of high toxicity, serious pollution and high cost caused by the use of metal catalysts.

Description

A kind ofly be used for the method that the alkylaromatic hydrocarbon selective oxidation becomes aromatic ketone or aromatic aldehyde
Technical field
The present invention relates to the catalyst system that is used for the various aromatic hydrocarbon benzyl of catalysis position selective oxidation reaction, specifically provided and a kind ofly can be used for the nonmetal catalyst system that organic molecule that aromatic hydrocarbon directly is oxidized to aromatic ketone or aromatic aldehyde is efficiently formed, this catalyst system can produce c h bond and the oxygen molecule that the organic free radical with overactivity function comes activated aromatics, thereby realizes the efficient oxidation process of aromatic hydrocarbon.
Background technology
The benzyl position selective oxidation of aromatic hydrocarbon is the great shift process in the organic chemistry, and its products obtained therefrom aromatic ketone, aromatic aldehyde etc. are the purposes intermediates of fine chemical product and synthesis of natural product very widely; Traditional method for oxidation mainly is to adopt oxidant stoichiometry Manganse Dioxide, dichromic acid etc. that aromatic hydrocarbon is carried out oxidation, and this process is seriously polluted, and Atom economy is poor; In recent years, begin to be subjected to people's attention with the green catalysis process of hydrogen peroxide and molecular oxygen as oxidant, wherein doing oxygen source with oxygen is a most competitive route.In this research field, mostly the catalyzer that adopts is transition metal-type compound (J.Mol.Catal.A:Chemical, 2003,201,9-22 at present; Adv.Synth.Catal.2005,347,703-705), there are shortcomings such as temperature of reaction height, selectivity of product difference in this type of system more.
In make the research that oxygen source carries out the organic substrates oxidizing reaction of molecular oxygen, Japanese's Hirai Naruhisa etc. has been reported the catalyst system (U.S. Pat 5 that a class is made up of 3-12 family metallic compound and N-hydroxyphthalimide, 981,420, European patent EP 858835, world patent WO9728897, Chinese patent CN 1185757A and Japanese Patent JP 11279112), this system can contain the aromatic hydroxy compound of methyl or methylene radical as catalyzed oxidation, generates oxygenatedchemicalss such as alcohol, ketone, acid down in mild conditions.
In Chinese patent CN1670130A, invented the nonmetal catalyst system that a kind of quinones and N-hydroxyphthalimide are combined into, also can be used for the catalytic oxidation of aromatic hydrocarbon.
Summary of the invention
The objective of the invention is to propose a kind of under mild conditions the alkylaromatic hydrocarbon selective oxidation become the method for aromatic ketone or aromatic aldehyde.
For achieving the above object, provided by the inventionly be used for the method that aromatic hydrocarbon selective is oxidized to aromatic ketone or aromatic aldehyde, in the presence of oxygen source, form catalyst system with acridine compound, halogenic molecule and three kinds of organic molecules of N-hydroxyphthalimide, aromatic hydrocarbon is prepared into aromatic ketone or aromatic aldehyde; Wherein: the molar percentage of catalyst system and reaction substrate is 0.01-30mol%; The molar percentage of halogenic molecule and reaction substrate is 0.01-5.0mol% in the catalyst system; The mol ratio of acridine compound and N-hydroxyphthalimide is 0.1-7 in the catalyst system; Temperature of reaction is 0-200 ℃; Reaction pressure is 0.001MPa-10MPa; Reaction times is 2-30 hour.
Acridine compound of the present invention is meant the acridine derivatives that does not contain or contain different substituents.
The nonmetal catalyst system that the present invention adopts shows the characteristics of sparing phase catalyst fully in reaction process, the catalytic activity height, and selectivity is higher; And catalyst levels can be optimized to trace, helps the separation and the purifying of reaction product.Reaction system is simple, and aftertreatment is easy; Production cost is low, and the no hidden danger of safety is also friendly to environment.
Specifically, the nonmetal catalyst system that is used for the oxidize aromatic hydrocarbon provided by the invention is made up of three kinds of organic molecules of the adjacent benzene dihydroxyl imines of acridine compound, molecular bromine and N-hydroxyl; Under mild conditions, the effect by each other can produce highly active free radical, and then the c h bond of activation aromatic hydrocarbons and the O-O key of molecular oxygen, to realize the clean oxidation process of aromatic hydrocarbon.
Acridine compound in the catalyst system component of the present invention can be that acridine, trypaflavine and acridine orange etc. contain various substituent acridine derivatives.
Molecular bromine in the catalyst system component of the present invention also can be by other halogen such as replacements such as iodine, chlorine.
Middle acridine compound concentrations in the catalyst system component of the present invention is 0.01-20mol%, and optimum concn is 1-10mol%; The mol ratio of acridine compound and N-hydroxyphthalimide is generally 0.1-7, and best proportioning coefficient is 1-5; The concentration of halogenic molecule is 0.01-5.0mol% (with the molar percentage of reaction substrate) in the catalyst system, and optimum concn is 1.0-3.0mol%.
Oxygen source used in the present invention is oxygen or air, and oxygen can consume by catalytic cycle in reaction process, and byproduct of reaction is a water, pollutes little.
Reaction of the present invention can also be carried out in organic solvent, and employed organic solvent comprises: nitrile solvents such as acetonitrile, cyanobenzene; Alcoholic solvent such as ethanol, methyl alcohol; Esters solvent such as ethyl acetate, methyl acetate, halogenated hydrocarbon solvents such as chloroform, monochloro methane; Aromatic hydrocarbon solvent such as benzene, chlorobenzene; Dimethyl formamide (DMF) or dimethyl sulfoxide (DMSO) non-protonic solvents such as (DMSO).
The reaction conditions gentleness of the present invention in catalyzed reaction, temperature of reaction are between 0-200 ℃, and temperature of reaction is between 40-80 ℃ preferably.Pressure is at 0.01MPa-10MPa, and reaction pressure is 0.1-1.5MPa preferably.
The related substrate of this reaction is an aromatic hydrocarbon, can be to contain-CH 2,-CH 3Or-hydrocarbon compound such as the alkylaromatic hydrocarbon of CH group or fragrant alkene, wherein aromatic nucleus can be phenyl ring, naphthalene nucleus or anthracene nucleus etc., also can contain heteroatomic aromatic heterocycles such as N, S, O, as contains substituent pyridine, thiophene or furans etc.
Non-metallic catalyst is different organic molecule among the present invention, and raw material is cheap and easy to get, can high-level efficiency, highly selective catalysis aromatic oxidation prepares aromatic ketone etc., and environmental friendliness, product is handled well; Just alkyl aromatic hydrocarbon compound, oxygen that whole process consumed, with low cost, can satisfy the requirement of Technological Economy, good prospects for application is arranged, be a catalyst system that has wide application prospects.
Embodiment
Give further instruction below by example to the present invention.
Embodiment 1: the catalyzed oxidation of indane
1ml (8.1mmol) indane is dissolved in the 10ml acetonitrile, adds the 0.20mmol trypaflavine, 0.24mmol molecular bromine and 0.67mmol N-hydroxyphthalimide, at 75 ℃, the O of 0.3MPa 2Under the pressure, react after 5 hours, with gas chromatograph analytical reaction result; The transformation efficiency of indane can reach 92%, and the selectivity of indan-1-one can reach 79%; Can cool off this moment, and product is collected in distillation.
Embodiment 2: the catalyzed oxidation of indane
1ml (8.1mmol) indane is dissolved in the 10ml methyl alcohol, adds the 0.01mmol trypaflavine, 0.08mmol molecular bromine and 0.67mmol N-hydroxyphthalimide, at 50 ℃, the O of 0.3MPa 2Under the pressure, react after 25 hours, with gas chromatograph analytical reaction result; The transformation efficiency of indane can reach 73%, and the selectivity of indan-1-one can reach 54%; Can cool off this moment, and product is collected in distillation.
Embodiment 3: the catalyzed oxidation of indane
1ml (8.1mmol) indane is dissolved in the 10ml ethyl acetate, adds the 0.20mmol acridine, 0.24mmol molecular bromine and 0.08mmol N-hydroxyphthalimide, at 200 ℃, the O of 0.001MPa 2Under the pressure, react after 5 hours, with gas chromatograph analytical reaction result; The transformation efficiency of indane can reach 19%, and the selectivity of indan-1-one can reach 13%; Can cool off this moment, and product is collected in distillation.
Embodiment 4: the catalyzed oxidation of ethylbenzene:
1ml (8.3mmol) ethylbenzene is dissolved in the 10ml monochloro methane, adds the 0.21mmol trypaflavine, 0.25mmol molecular bromine and 1.47mmol N-hydroxyphthalimide, at 75 ℃, the O of 0.3MPa 2Under the pressure, react after 5 hours, with gas chromatograph analytical reaction result; The transformation efficiency of ethylbenzene can reach 67%, and the selectivity of methyl phenyl ketone is 94%; Can cool off this moment, and product is collected in distillation.
Embodiment 5: the catalyzed oxidation of naphthane:
1ml (7.4mmol) naphthane is dissolved in the 10ml chlorobenzene, adds the 0.19mmol trypaflavine, 0.22mmol molecular bromine and 0.56mmol N-hydroxyphthalimide, at 0 ℃, the O of 10MPa 2Under the pressure, react after 30 hours, with gas chromatograph analytical reaction result; The transformation efficiency of naphthane can reach 54%, and the selectivity of naphthane-1-ketone can reach 95%; Can cool off this moment, and product is collected in distillation.
Embodiment 6: the catalyzed oxidation of ditane
1ml (6.0mmol) ditane is dissolved among the 10mlDMF, adds the 0.15mmol trypaflavine, 0.18mmol molecular bromine and 0.45mmol N-hydroxyphthalimide, at 100 ℃, the O of 1.5MPa 2Under the pressure, react after 20 hours, with gas chromatograph analytical reaction result; The transformation efficiency of ditane can reach 65%, and the selectivity of benzophenone can reach 99%; Can cool off this moment, and product is collected in distillation.
Embodiment 7: the catalyzed oxidation of acenaphthene
0.77g (5.0mmol) acenaphthene is dissolved in the 10ml benzene, adds the 0.13mmol trypaflavine, 0.15mmol molecular bromine and 0.38mmol N-hydroxyphthalimide, at 40 ℃, the O of 1.0MPa 2Under the pressure, react after 24 hours, with gas chromatograph analytical reaction result; The transformation efficiency of acenaphthene can reach 70%, and the selectivity of acenaphthene-1-ketone can reach 88%; Can cool off this moment, and product is collected in distillation.
Embodiment 8: the catalyzed oxidation of parachlorotoluene:
1ml (9.3mmol) parachlorotoluene is dissolved in the 10ml dimethyl sulfoxide (DMSO), adds the 0.23mmol trypaflavine, 0.28mmol molecular bromine and 0.70mmol N-hydroxyphthalimide, at 100 ℃, the O of 0.3MPa 2Under the pressure, react after 3 hours, with gas chromatograph analytical reaction result; The transformation efficiency of parachlorotoluene can reach 13%, and the selectivity of 4-chloro-benzaldehyde is 45%, and can cool off this moment, and product is collected in distillation.
The catalyzed oxidation of embodiment 9:3-ethyl furan
1ml (8.1mmol) 3-ethyl furan is dissolved in the 10ml methyl acetate, adds the 0.21mmol trypaflavine, 0.45mmol molecular bromine and 0.61mmol N-hydroxyphthalimide, at 150 ℃, the O of 0.3MPa 2Under the pressure, react after 2 hours, with gas chromatograph analytical reaction result; The transformation efficiency of 3-ethyl furan can reach 51%, and the selectivity of 1-furans-3-ethyl ketone is 97%; Can cool off this moment, and product is collected in distillation.
Above-mentioned example shows, adopts novel metalloid catalyst system provided by the present invention, in suitable reaction medium, and according to the condition that provided of invention, can high-level efficiency, highly selective generates ketone or aldehyde material with the aromatic hydrocarbon catalyzed oxidation.Oxygen source can be oxygen or the air that directly feeds; Catalyst dissolution embodies the advantage and the effect of even phase catalyst fully in reaction system in reaction process, thereby the reaction conditions gentleness; After entire reaction, oxygen source all consumes, and catalyzer and substrate and product have than big difference, is easy to separate.In total reaction process, just organic substrates and the oxygen (air) that are consumed.Production cost, cheap, product mainly is an oxygenatedchemicals, and is relatively more friendly to environment.Reaction process is simple, can satisfy the requirement of Technological Economy, is the catalyst system with broad prospect of application.

Claims (10)

1、一种用于芳香烃选择性氧化成芳香酮或芳香醛的方法,在空气或氧气存在下,以吖啶类化合物、卤素分子和N-羟基邻苯二甲酰亚胺三种有机小分子组成催化体系,将烷基芳香烃制备成芳香酮或芳香醛;其中:1. A method for the selective oxidation of aromatic hydrocarbons into aromatic ketones or aromatic aldehydes. In the presence of air or oxygen, three organic small compounds, acridine compounds, halogen molecules and N-hydroxyphthalimide Molecular composition catalytic system to prepare alkyl aromatic hydrocarbons into aromatic ketones or aromatic aldehydes; where: 催化体系与反应底物的摩尔百分比为0.01-30mol%;The molar percentage of the catalytic system and the reaction substrate is 0.01-30 mol%; 催化体系中卤素分子与反应底物的摩尔百分比为0.01-5.0mol%;The molar percentage of the halogen molecule and the reaction substrate in the catalytic system is 0.01-5.0 mol%; 催化体系中吖啶类化合物与N-羟基邻苯二甲酰亚胺的摩尔比为0.1-7;The molar ratio of acridine compound to N-hydroxyphthalimide in the catalytic system is 0.1-7; 反应温度为0-200℃;The reaction temperature is 0-200°C; 反应压强为0.001MPa-10MPa;The reaction pressure is 0.001MPa-10MPa; 反应时间为2-30小时。The reaction time is 2-30 hours. 2.根据权利要求1所述的方法,其中反应是在腈类、醇类、酯类、卤代烃类或芳香烃类溶剂中进行。2. The method according to claim 1, wherein the reaction is carried out in nitriles, alcohols, esters, halogenated hydrocarbons or aromatic hydrocarbon solvents. 3.根据权利要求2所述的方法,其中溶剂为乙腈、苯腈、乙醇、甲醇、乙酸乙酯、乙酸甲酯、氯仿、一氯甲烷、苯或氯苯。3. The method according to claim 2, wherein the solvent is acetonitrile, benzonitrile, ethanol, methyl alcohol, ethyl acetate, methyl acetate, chloroform, methylene chloride, benzene or chlorobenzene. 4.根据权利要求1所述的方法,其中烷基芳香烃是指苄位含C-H键的芳烃化合物、烷基吡啶、烷基噻吩或烷基呋喃杂环芳烃。4. The method according to claim 1, wherein the alkyl aromatic hydrocarbon refers to an aromatic compound containing a C-H bond at the benzylic position, an alkylpyridine, an alkylthiophene or an alkylfuran heterocyclic aromatic hydrocarbon. 5.根据权利要求1所述的方法,其中催化体系中吖啶类化合物是指不含或含有不同取代基的吖啶衍生物。5. The method according to claim 1, wherein the acridine compound in the catalytic system refers to acridine derivatives that do not contain or contain different substituents. 6.根据权利要求1所述的方法,其中卤素分子为溴、碘或氯气。6. The method of claim 1, wherein the halogen molecule is bromine, iodine or chlorine. 7.根据权利要求1所述的方法,其中催化体系中吖啶衍生物与N-羟基邻苯二甲酰亚胺的摩尔比为1-5。7. The method according to claim 1, wherein the molar ratio of the acridine derivative to the N-hydroxyphthalimide in the catalytic system is 1-5. 8.根据权利要求1所述的方法,其中催化体系与反应底物的摩尔百分比为1.0-3.0mol%。8. The method according to claim 1, wherein the molar percentage of the catalytic system and the reaction substrate is 1.0-3.0 mol%. 9.根据权利要求1所述的方法,其中反应温度为40-80℃。9. The method according to claim 1, wherein the reaction temperature is 40-80°C. 10.根据权利要求1所述的方法,其中反应压力为0.1-1.5MPa。10. The method according to claim 1, wherein the reaction pressure is 0.1-1.5 MPa.
CNB2006100895892A 2006-07-05 2006-07-05 Method for preparing aromatic ketone or aromatic aldehyde by selectively oxidizing alkyl arene Expired - Fee Related CN100519499C (en)

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CN101830784A (en) * 2010-05-18 2010-09-15 华东理工大学 Method for preparing alpha-aryl ketones compounds
CN106032355B (en) * 2015-03-10 2019-01-04 中国科学院大连化学物理研究所 A kind of method that pyridine side chain c h bond is direct oxidation into ketone
CN112774662B (en) * 2019-11-04 2023-08-15 北京氦舶科技有限责任公司 Monoatomic catalyst and preparation method and application thereof
CN112159314B (en) * 2020-09-08 2023-12-15 苏州陶逆科技有限公司 Method for catalyzing oxidation of alpha-monosubstituted styrene to generate benzaldehyde by using N-hydroxyphthalimide

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Publication number Priority date Publication date Assignee Title
CN1185757A (en) * 1996-02-07 1998-06-24 大赛璐化学工业株式会社 Oxidation catalyst system and process for oxidation with the same
CN1670130A (en) * 2004-03-16 2005-09-21 中国科学院大连化学物理研究所 A non-metallic composite catalytic system for catalytic selective oxidation of hydrocarbons

Patent Citations (2)

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Publication number Priority date Publication date Assignee Title
CN1185757A (en) * 1996-02-07 1998-06-24 大赛璐化学工业株式会社 Oxidation catalyst system and process for oxidation with the same
CN1670130A (en) * 2004-03-16 2005-09-21 中国科学院大连化学物理研究所 A non-metallic composite catalytic system for catalytic selective oxidation of hydrocarbons

Non-Patent Citations (1)

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