CN115805101A - Catalyst for preparing hydroxy arone and preparation method and application thereof - Google Patents

Catalyst for preparing hydroxy arone and preparation method and application thereof Download PDF

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CN115805101A
CN115805101A CN202111067853.3A CN202111067853A CN115805101A CN 115805101 A CN115805101 A CN 115805101A CN 202111067853 A CN202111067853 A CN 202111067853A CN 115805101 A CN115805101 A CN 115805101A
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catalyst
mil
benzyl
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chloride
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刘旭
王艳红
徐晓清
付伟
刘晓曦
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China Petroleum and Chemical Corp
Sinopec Shanghai Research Institute of Petrochemical Technology
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China Petroleum and Chemical Corp
Sinopec Shanghai Research Institute of Petrochemical Technology
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Abstract

The invention relates to a catalyst for preparing hydroxyl arone and a preparation method and application thereof. The catalyst comprises an organic metal framework material and benzyl functionalized ionic liquid; and the catalyst has a unique X-ray diffraction pattern. The benzyl functionalized ionic liquid in the catalyst is in a pore channel of the in-situ limited organic metal framework material, so that the performance of the benzyl functionalized ionic liquid is improved. The catalyst prepared by the method is applied to the preparation of the hydroxyl arone, and has the characteristics of improving the conversion rate of the phenolic ester and the selectivity of the hydroxyl arone.

Description

Catalyst for preparing hydroxyl arone and preparation method and application thereof
Technical Field
The invention belongs to the field of preparation of hydroxyaryl ketone, and particularly relates to a catalyst for preparing hydroxyaryl ketone, and a preparation method and application thereof.
Background
The hydroxyl arone molecule contains hydroxyl and ketone groups on benzene rings, is a very important fine chemical and synthetic intermediate, and has wide application in the fields of medicines, cosmetics, foods, synthetic materials and the like. Wherein, the p-hydroxyacetophenone is an example, which is a natural plant extract, and is naturally present in stems and leaves of artemisia scoparia belonging to the family Compositae, roots of artemisia capillaris, plants belonging to the family Asclepiadaceae, and tylophora floribunda, etc. It has important application value in the fields of medicine, dye, cosmetics, liquid crystal material, synthetic resin, etc. O-hydroxyacetophenone is mainly used as a pharmaceutical intermediate and a perfume, and is an important intermediate for, for example, propafenone Hydrochloride (IA) which is an antiarrhythmic drug, and chlorokanava Hydrochloride (Croconazol Hydrochloride) which is an antifungal drug.
The hydroxyacetophenone is synthesized mainly by phenyl acetate method, p-aminophenyl ketone method, photocatalytic method, etc. Wherein, the phenyl acetate method is to obtain the hydroxyacetophenone by intramolecular rearrangement of phenyl acetate, has high atom utilization rate, is favored, and the effective catalytic system is Lewis acid,
Figure BDA0003259237550000011
Acid and ionic liquid catalysts, but has the defect of low selectivity of para-hydroxy arone.
The metal organic framework material is a polymer crystal material with an intrinsic amphiphilic structure. Polar nodes in the MOFs structure can strongly interact with molecules through various acting forces such as coordination, ion exchange, electrostatic action and the like; in addition, MOFs have the characteristic of abundant pore structures, and are favorable for preparing composite materials in various modes such as in-situ embedding, late-stage modification and the like so as to improve the application performance of the composite materials.
Disclosure of Invention
The invention provides a novel catalyst for preparing hydroxyl arone, aiming at the problems of low conversion rate of phenolic ester and low selectivity of hydroxyl arone in the process of catalytically synthesizing hydroxyl arone by substituted alkylphenol ester or halogenated phenol ester in the prior art. The catalyst has the characteristics of improving the conversion rate of the phenolic ester and the selectivity of the hydroxyl arone.
To this end, the present invention provides in a first aspect a catalyst for the preparation of a hydroxyaryl ketone comprising an organometallic framework material and a benzyl-functionalized ionic liquid; and the catalyst has an X-ray diffraction pattern substantially as follows;
Figure BDA0003259237550000021
wherein (a) = ± 0.3 °.
The contents of the organometallic framework material and the benzyl functionalized ionic liquid in the catalyst are the actual amounts of the organometallic framework material and the benzyl functionalized ionic liquid used in the synthesis of the catalyst. Because the benzyl functionalized ionic liquid in the catalyst is confined in the pore channels of the organometallic framework material, and the excess benzyl functionalized ionic liquid which does not react in the pore channels can be washed away by the solvent, the content of the organometallic framework material and the benzyl functionalized ionic liquid in the catalyst is not specifically limited, and can be adjusted by a person skilled in the art according to actual needs.
In some embodiments of the invention, the organometallic framework material is selected from one or more of IRMOFs, ZIFs, PCPs, and MILs, preferably MILs.
In the invention, PCPs (porous coordination polymers) are a class of high-crystalline porous hybrid materials which connect metal clusters (or ions) and organic ligands through coordination bonds.
In some preferred embodiments of the invention, the MILs are selected from one or more of MIL-53, MIL-100 and MIL-101, preferably MIL-101, more preferably MIL-101 (Cr).
In some embodiments of the present invention, the benzyl functionalized ionic liquid has a structure containing a cation formed by a nitrogen heterocyclic organic compound and a benzyl halide compound, and a metal halide.
In some embodiments of the invention, the azacyclic organic compound is selected from one or more of imidazole, alkyl imidazole, pyridine, alkyl pyridine, pyrimidine, alkyl pyrimidine, pyrrole, and alkyl pyrrole; preferably, the alkyl group is selected from C 1 ~C 5 At least one of alkyl groups of (a); further preferably, the nitrogen heterocyclic organic compound is selected from one or more of pyridine, 4-methylpyridine, 3-methylpyridine and 3, 5-dimethylpyridine.
In a second aspect, the present invention provides a method for preparing a catalyst according to the first aspect of the present invention, comprising the steps of:
s1, mixing a solvent A, an organic metal framework material, a nitrogen heterocyclic organic compound and a benzyl halide compound, reacting, cooling, filtering, washing and drying to obtain a solid product;
and S2, mixing the solvent B, the solid product and Lewis acid, reacting, cooling, filtering, washing and drying to obtain the catalyst.
In some embodiments of the invention, the molar ratio of the azacyclic organic compound, the benzyl halide compound and the Lewis acid is (0.5-1.5): 1.5-2.5); preferably (0.8-1.2), (0.8-1.2) and (1.8-2.2); further preferably 1.
The amount of the organometallic framework material used in the above reaction is not specifically limited, and can be adjusted by those skilled in the art according to actual needs.
In some embodiments of the invention, the azacyclic organic compound is selected from one or more of imidazole, alkyl imidazole, pyridine, alkyl pyridine, pyrimidine, alkyl pyrimidine, pyrrole, and alkyl pyrrole; preferably, the alkane isRadical selected from C 1 ~C 5 At least one of alkyl groups of (a); further preferably, the nitrogen heterocyclic organic compound is selected from one or more of pyridine, 4-methylpyridine, 3-methylpyridine and 3, 5-dimethylpyridine.
In other embodiments of the present invention, the benzylic halide compound is selected from one or more of benzyl chloride, 2,4, 6-trimethylbenzyl chloride, p-trifluoromethylbenzyl chloride, benzyl bromide and 4-isopropylbenzyl bromide.
In some embodiments of the invention, the Lewis acid is selected from one or more of aluminum trichloride, aluminum tribromide, ferric trichloride, zinc chloride, boron trifluoride, gallium chloride, indium chloride, cuprous chloride; preferably one or more selected from the group consisting of aluminum trichloride and iron trichloride.
In other embodiments of the present invention, the solvent a and the solvent B are independently selected from any one of chlorobenzene, nitrobenzene, toluene, nitromethane, acetonitrile, dichloromethane.
The amounts of the solvent A and the solvent B used in the present invention are not specifically limited. Generally, it is sufficient if the corresponding solute can be dissolved. In some embodiments of the present invention, the solvent is used in an amount such that the concentration of the corresponding solute (solute desired to be dissolved by the solvent) is from 0.001mol/L to the saturation solubility.
In the present invention, the organometallic framework material may be pre-dried before use.
In other embodiments of the present invention, the temperature of the reaction in step S1 is 0 to 100 ℃, preferably 30 to 40 ℃; and/or the reaction time is 2 to 72 hours, preferably 12 to 15 hours.
In some embodiments of the invention, in step S2, the temperature of the reaction is between 0 and 100 ℃, preferably between 25 and 35 ℃; and/or the reaction time is 2-20 h, preferably 8-15 h.
The method limits the in-situ confinement of the benzyl functionalized ionic liquid in the pore canal of MIL-101 (Cr), thereby improving the performance of the benzyl functionalized ionic liquid. The catalyst prepared by the method has the characteristics of improving the conversion rate of the phenolic ester and the selectivity of the hydroxyl arone.
In a third aspect, the invention provides a method for preparing a hydroxy aromatic ketone from an alkylphenol ester or a halogenated phenol ester, which comprises catalyzing the alkylphenol ester or the halogenated phenol ester to carry out intramolecular rearrangement by using the catalyst according to the first aspect or the catalyst prepared by the method according to the second aspect of the invention in a solvent C or a non-solvent state, so as to synthesize the hydroxy aromatic ketone.
In some embodiments of the present invention, the alkylphenol or halophenol has a structural formula shown in formula a or formula b;
Figure BDA0003259237550000041
a chemical formula a;
Figure BDA0003259237550000051
a chemical formula b;
wherein, R is 2 And R 3 Each independently selected from H or C 1 ~C 6 Alkyl groups of (a); the R is 1 And R 4 Each independently is selected from C 1 ~C 6 Alkyl or C 6 ~C 9 Aryl of (a); and X is selected from any one of F, cl, br and I.
In other embodiments of the present invention, the weight ratio of the alkylphenol ester or halogenated phenol ester to the catalyst is 1 (0.001 to 20); preferably 1 (0.01 to 5).
In some embodiments of the present invention, the solvent C is selected from any one of chlorobenzene, nitrobenzene, toluene, nitromethane, acetonitrile and dichloromethane.
In other embodiments of the invention, the conditions of catalysis include: the temperature is 20-200 ℃, and preferably 20-100 ℃; and/or the pressure is normal pressure to 6MPa, preferably normal pressure to 2MPa; the time is 0.1 to 10 hours, preferably 0.5 to 5 hours.
The beneficial effects of the invention are as follows: the benzyl functionalized ionic liquid in the catalyst is confined in the pore channel of an organic metal framework material (such as MIL-101 (Cr)) in situ, so that the performance of the benzyl functionalized ionic liquid is improved. The catalyst prepared by the method is applied to the preparation of the hydroxyl arone, and has the characteristics of improving the conversion rate of the phenolic ester and the selectivity of the hydroxyl arone.
Drawings
The invention will be further explained with reference to the drawings.
FIG. 1 is an XRD spectrum of an organometallic framework material MIL-101 (Cr) used in example 1 of the present invention.
FIG. 2 is an XRD spectrum of catalyst MIL-101 (Cr) -Fe-1 prepared in example 1 of the present invention.
FIG. 3 is an IR spectrum of an organometallic framework material MIL-101 (Cr) used in example 1 of the present invention, and the main peak positions are: 3441cm -1 、1653cm -1 、1617cm -1 、1505cm -1 、1384cm -1 、1106cm -1 、749cm -1
FIG. 4 is an IR spectrum of an organometallic catalyst MIL-101 (Cr) -Fe-1 prepared in example 1 of the present invention, in which the main peak positions are: 3407cm -1 、3053cm -1 、1702cm -1 、1651cm -1 、1622cm -1 、1486cm -1 、1398cm -1 、1300cm -1 、1157cm -1 、1105cm -1 、1016cm -1 、749cm -1 、680cm -1 (ii) a Wherein the thickness is 3053cm -1 Peak for benzyl, 1702cm -1 1398cm as the peak of benzene ring -1 、1157cm -1 、680cm -1 Is peak of pyridine ring, 1300cm -1 、1016cm -1 The peak is the benzyl benzene ring.
Detailed Description
In order that the present invention may be more readily understood, the following detailed description will proceed with reference being made to examples, which are intended to be illustrative only and are not intended to limit the scope of the invention. The starting materials or components used in the present invention may be commercially or conventionally prepared unless otherwise specified.
[ PREPARATION EXAMPLE 1 ]
MIL-101 (Cr) (XRD spectrum shown in FIG. 1 and IR spectrum shown in FIG. 3) was dried overnight in an oven at 150 ℃.
To a dried 100mL three-necked flask, 25mL of anhydrous acetonitrile, 2g of dried MIL-101 (Cr), and 0.25mL of pyridine were added, and 0.32mL of benzyl chloride was added dropwise with stirring, followed by reaction at room temperature for 12 hours. And filtering the system, fully washing a filter cake by using anhydrous acetonitrile, and drying in vacuum to obtain a solid product.
Adding the solid product into a dried 100mL three-neck flask, adding 25mL anhydrous acetonitrile, adding 1g anhydrous ferric trichloride under stirring, and reacting at room temperature for 12 hours. Separating out acetonitrile layer, washing with anhydrous acetonitrile, and vacuum drying to obtain catalyst MIL-101 (Cr) -Fe-1 (XRD spectrogram is shown in figure 2, and IR spectrogram is shown in figure 4).
[ PREPARATION EXAMPLE 2 ]
MIL-101 (Cr) was dried overnight in an oven at 150 ℃.
To a dried 100mL three-necked flask, 25mL of anhydrous acetonitrile, 2g of dried MIL-101 (Cr), and 0.25mL of pyridine were added, and 0.32mL of benzyl chloride was added dropwise with stirring, followed by reaction at room temperature for 12 hours. And filtering the system, fully washing a filter cake by using anhydrous acetonitrile, and drying in vacuum to obtain a solid product.
The solid product was charged into a dried 100mL three-necked flask, 25mL of anhydrous acetonitrile was added, and 0.82g of aluminum chloride was added with stirring to conduct a reaction at room temperature for 12 hours. Separating out an acetonitrile layer, fully washing with anhydrous acetonitrile, and drying in vacuum to obtain the catalyst MIL-101 (Cr) -Al-1.
[ PREPARATION EXAMPLE 3 ]
MIL-101 (Cr) was dried overnight in an oven at 150 ℃.
In a dried 100mL three-necked flask, 25mL of anhydrous acetonitrile, 2g of dried MIL-101 (Cr), and 0.25mL of pyridine were added, and 0.32mL of benzyl chloride was added dropwise with stirring, followed by reaction at room temperature for 12 hours. And (3) filtering the system, fully washing a filter cake by using anhydrous acetonitrile, and drying in vacuum to obtain a solid product.
The solid product was charged into a dried 100mL three-necked flask, 25mL of anhydrous acetonitrile was added, and 0.84g of zinc chloride was added with stirring to react at room temperature for 12 hours. Separating out an acetonitrile layer, fully washing with anhydrous acetonitrile, and drying in vacuum to obtain the catalyst MIL-101 (Cr) -Zn-1.
[ PREPARATION EXAMPLE 4 ]
MIL-101 (Cr) was dried overnight in an oven at 150 ℃.
In a dried 100mL three-necked flask, 25mL of anhydrous acetonitrile, 2g of dried MIL-101 (Cr), and 0.25mL of pyridine were added, and 0.41mL of p-trifluoromethylbenzyl chloride was added dropwise with stirring, and the mixture was reacted at room temperature for 12 hours. And (3) filtering the system, fully washing a filter cake by using anhydrous acetonitrile, and drying in vacuum to obtain a solid product.
Adding the solid product into a dried 100mL three-neck flask, adding 25mL anhydrous acetonitrile, adding 1g anhydrous ferric trichloride under stirring, and reacting at room temperature for 12 hours. Separating out an acetonitrile layer, fully washing with anhydrous acetonitrile, and drying in vacuum to obtain the catalyst MIL-101 (Cr) -Fe-2.
[ PREPARATION EXAMPLE 5 ]
MIL-101 (Cr) was dried overnight in an oven at 150 ℃.
In a dried 100mL three-necked flask, 25mL of anhydrous acetonitrile, 2g of dried MIL-101 (Cr), and 0.25mL of pyridine were added, and 0.47mL of p-isopropylbenzyl chloride was added dropwise with stirring, followed by reaction at room temperature for 12 hours. And filtering the system, fully washing a filter cake by using anhydrous acetonitrile, and drying in vacuum to obtain a solid product.
Adding the solid product into a dried 100mL three-neck flask, adding 25mL anhydrous acetonitrile, adding 1g anhydrous ferric trichloride under stirring, and reacting at room temperature for 12 hours. Separating out an acetonitrile layer, fully washing with anhydrous acetonitrile, and drying in vacuum to obtain the catalyst MIL-101 (Cr) -Fe-3.
[ PREPARATION 6 ]
After drying, 100mL of anhydrous acetonitrile and 2.5mL of pyridine were added to a 200mL three-necked flask, and 3.2mL of benzyl chloride was added dropwise with stirring to react at room temperature for 12 hours. 10g of anhydrous ferric chloride was added thereto with stirring, and the mixture was reacted at room temperature for 12 hours. And separating an acetonitrile layer, fully washing with anhydrous acetonitrile, and drying in vacuum to obtain the catalyst PyBn-Fe.
Comparative example 1
A50 mL flask was charged with 2.5mL of phenyl acetate and 0.4g of the dried PyBn-Fe prepared in preparation example 6, and the system was heated to 80 ℃ for 4 hours and cooled to room temperature. Adding 50mL of water, stirring thoroughly, and usingExtracting with ethyl acetate for three times, mixing organic phases, and extracting with anhydrous Na 2 SO 4 After drying, filtration and evaporation of the solvent under reduced pressure, the residue was analyzed by GC. The conversion of phenyl acetate was 67.8% and the selectivity of hydroxyacetophenone was 59.4%.
[ example 1 ]
A50 mL flask was charged with 2.5g of phenyl acetate and 1g of dried MIL-101 (Cr) -Fe-1 prepared in preparation example 1, and the system was heated to 80 ℃ for 4 hours and cooled to room temperature. Adding 50mL of water, fully stirring, extracting with ethyl acetate for three times, combining organic phases, and adding anhydrous Na 2 SO 4 After drying, filtration and evaporation of the solvent under reduced pressure, the residue was analyzed by GC. The conversion of phenyl acetate was 99.2% and the selectivity of hydroxyacetophenone was 91.6%.
[ example 2 ] A method for producing a polycarbonate
A50 mL flask was charged with 2.5g of phenyl acetate and 1g of dried MIL-101 (Cr) -Al-1 prepared in preparation example 2, and the system was heated to 80 ℃ for 4 hours and cooled to room temperature. Adding 50mL of water, fully stirring, extracting with ethyl acetate for three times, combining organic phases, and adding anhydrous Na 2 SO 4 After drying, filtration and evaporation of the solvent under reduced pressure, the residue was analyzed by GC. The conversion of phenyl acetate was 99.9% and the selectivity of hydroxyacetophenone was 90.2%.
[ example 3 ] A method for producing a polycarbonate
A50 mL flask was charged with 2.5g of phenyl acetate, and 1g of the dried MIL-101 (Cr) -Zn-1 system prepared in preparation example 3 was heated to 80 ℃ for 4 hours, and cooled to room temperature. Adding 50mL of water, fully stirring, extracting with ethyl acetate for three times, combining organic phases, and adding anhydrous Na 2 SO 4 After drying, filtration was carried out, the solvent was distilled off under reduced pressure and the residue was analyzed by GC. The conversion of phenyl acetate was 97.3% and the selectivity of hydroxyacetophenone was 90.4%.
[ example 4 ]
A50 mL flask was charged with 2.5g of phenyl acetate and 1g of dried MIL-101 (Cr) -Fe-2 prepared in preparation example 4, and the system was heated to 80 ℃ for 4 hours and cooled to room temperature. Adding 50mL of water, fully stirring, extracting with ethyl acetate for three times, combining organic phases, and adding anhydrous Na 2 SO 4 Drying, filtering, reducingThe solvent was autoclaved and the residue was analyzed by GC. The conversion rate of phenyl acetate was 99.3%, and the selectivity of hydroxyacetophenone was 94.3%.
[ example 5 ]
A50 mL flask was charged with 2.5g of phenyl acetate and 1g of dried MIL-101 (Cr) -Fe-1 prepared in preparation example 5, and the system was heated to 80 ℃ for 4 hours and cooled to room temperature. Adding 50mL of water, fully stirring, extracting with ethyl acetate for three times, combining organic phases, and adding anhydrous Na 2 SO 4 After drying, filtration and evaporation of the solvent under reduced pressure, the residue was analyzed by GC. The conversion rate of phenyl acetate was 98.5%, and the selectivity of hydroxyacetophenone was 90.3%.
It should be noted that the above-mentioned embodiments are only for explaining the present invention, and do not constitute any limitation to the present invention. The present invention has been described with reference to exemplary embodiments, but the words which have been used herein are words of description and illustration, rather than words of limitation. The invention can be modified, as prescribed, within the scope of the claims and without departing from the scope and spirit of the invention. Although the invention has been described herein with reference to particular means, materials and embodiments, the invention is not intended to be limited to the particulars disclosed herein, but rather extends to all other methods and applications having the same functionality.

Claims (10)

1. A catalyst for the preparation of a hydroxyaryl ketone comprising an organometallic framework material and a benzyl-functionalized ionic liquid; and the catalyst has the following X-ray diffraction pattern;
Figure FDA0003259237540000011
wherein (a) = ± 0.3 °.
2. The catalyst according to claim 1, wherein the organometallic framework material is selected from one or more of IRMOF, ZIFs, PCPs and MIL, preferably MIL; further preferably, the MIL is selected from one or more of MIL-53, MIL-100 and MIL-101, more preferably MIL-101, even more preferably MIL-101 (Cr).
3. The catalyst according to claim 1 or 2, wherein the structure of the benzyl functionalized ionic liquid contains cations formed by nitrogen heterocyclic organic compounds and benzyl halogen compounds and metal halides.
4. A method for preparing a catalyst according to any one of claims 1 to 3, comprising the steps of:
s1, mixing a solvent A, an organic metal framework material, a nitrogen heterocyclic organic compound and a benzyl halide compound, reacting, cooling, filtering, washing and drying to obtain a solid product;
and S2, mixing the solvent B, the solid product and Lewis acid, reacting, cooling, filtering, washing and drying to obtain the catalyst.
5. The method as claimed in claim 4, wherein the molar ratio of the azacyclic organic compound, the benzyl halide compound and the Lewis acid is (0.5-1.5): 1.5-2.5); preferably (0.8-1.2): 1.8-2.2).
6. The process according to claim 4 or 5, wherein the azacyclic organic compound is selected from one or more of imidazole, alkyl imidazole, pyridine, alkyl pyridine, pyrimidine, alkyl pyrimidine, pyrrole and alkyl pyrrole; preferably, the alkyl group is selected from C 1 ~C 5 At least one of alkyl groups of (a); further preferably, the nitrogen heterocyclic organic compound is selected from one or more of pyridine, 4-methylpyridine, 3-methylpyridine and 3, 5-dimethylpyridine; and/or
The benzyl halide compound is selected from one or more of benzyl chloride, 2,4, 6-trimethylbenzyl chloride, p-trifluoromethylbenzyl chloride, benzyl bromide and 4-isopropylbenzyl bromide; and/or
The Lewis acid is selected from one or more of aluminum trichloride, aluminum tribromide, ferric trichloride, zinc chloride, boron trifluoride, gallium chloride, indium chloride and cuprous chloride; preferably one or more selected from the group consisting of aluminum trichloride and iron trichloride; and/or
The solvent A and the solvent B are respectively and independently selected from any one of chlorobenzene, nitrobenzene, toluene, nitromethane, acetonitrile and dichloromethane.
7. The process according to claim 4 or 5, wherein in step S1, the temperature of the reaction is between 0 and 100 ℃, preferably between 30 and 40 ℃; and/or the reaction time is 2-72 h, preferably 12-15 h; and/or
In the step S2, the reaction temperature is 0-100 ℃, and preferably 25-35 ℃; and/or the reaction time is 2 to 20 hours, preferably 8 to 15 hours.
8. A method for preparing a hydroxyaryl ketone from an alkylphenol ester or a halogenated phenol ester, which comprises catalyzing the intramolecular rearrangement of the alkylphenol ester or the halogenated phenol ester with the catalyst of any one of claims 1 to 3 or the catalyst prepared by the method of any one of claims 4 to 7 in the state of a solvent C or a non-solvent, thereby synthesizing the hydroxyaryl ketone.
9. The method of claim 8, wherein the alkylphenol or halophenol has a formula of formula a or b;
Figure FDA0003259237540000031
wherein, R is 2 And R 3 Each independently is selected from H or C 1 ~C 6 Alkyl groups of (a); the R is 1 And R 4 Each independently is selected from C 1 ~C 6 Alkyl or C 6 ~C 9 Aryl of (a); x is selected from any one of F, cl, br and ISeed growing;
preferably, the weight ratio of the alkylphenol ester or the halogenated phenol ester to the catalyst is 1 (0.001-20); preferably 1 (0.01 to 5).
10. The method according to claim 8 or 9, wherein the solvent C is selected from any one of chlorobenzene, nitrobenzene, toluene, nitromethane, acetonitrile and dichloromethane; and/or
The catalytic conditions include: the temperature is 20-200 ℃, and preferably 20-100 ℃; and/or the pressure is normal pressure to 6MPa, preferably normal pressure to 2MPa; the time is 0.1 to 10 hours, preferably 0.5 to 5 hours.
CN202111067853.3A 2021-09-13 2021-09-13 Catalyst for preparing hydroxy arone and preparation method and application thereof Pending CN115805101A (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103408414A (en) * 2013-07-19 2013-11-27 北京格林凯默科技有限公司 Preparation method of 2-hydroxyl-4-substituted arone compound
CN107626349A (en) * 2017-09-27 2018-01-26 三峡大学 A kind of catalyst for preparing phenmethylol, benzaldehyde and benzoic acid and the method for preparing phenmethylol, benzaldehyde and benzoic acid
CN110918124A (en) * 2019-12-12 2020-03-27 福建师范大学福清分校 Preparation method and application of iron-based MOFs immobilized ionic liquid
CN112521567A (en) * 2020-12-02 2021-03-19 新乡学院 Temperature-controlled ionic liquid functionalized temperature response covalent organic framework material and preparation method thereof

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103408414A (en) * 2013-07-19 2013-11-27 北京格林凯默科技有限公司 Preparation method of 2-hydroxyl-4-substituted arone compound
CN107626349A (en) * 2017-09-27 2018-01-26 三峡大学 A kind of catalyst for preparing phenmethylol, benzaldehyde and benzoic acid and the method for preparing phenmethylol, benzaldehyde and benzoic acid
CN110918124A (en) * 2019-12-12 2020-03-27 福建师范大学福清分校 Preparation method and application of iron-based MOFs immobilized ionic liquid
CN112521567A (en) * 2020-12-02 2021-03-19 新乡学院 Temperature-controlled ionic liquid functionalized temperature response covalent organic framework material and preparation method thereof

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