CN115368226A - Hydroxy arone and preparation method thereof - Google Patents

Hydroxy arone and preparation method thereof Download PDF

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CN115368226A
CN115368226A CN202110547479.0A CN202110547479A CN115368226A CN 115368226 A CN115368226 A CN 115368226A CN 202110547479 A CN202110547479 A CN 202110547479A CN 115368226 A CN115368226 A CN 115368226A
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acetate
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CN115368226B (en
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刘旭
王艳红
刘仲能
涂云宝
白雪
徐晓清
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China Petroleum and Chemical Corp
Sinopec Shanghai Research Institute of Petrochemical Technology
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Sinopec Shanghai Research Institute of Petrochemical Technology
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/51Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by pyrolysis, rearrangement or decomposition
    • C07C45/54Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by pyrolysis, rearrangement or decomposition of compounds containing doubly bound oxygen atoms, e.g. esters
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C49/00Ketones; Ketenes; Dimeric ketenes; Ketonic chelates
    • C07C49/76Ketones containing a keto group bound to a six-membered aromatic ring
    • C07C49/82Ketones containing a keto group bound to a six-membered aromatic ring containing hydroxy groups
    • C07C49/825Ketones containing a keto group bound to a six-membered aromatic ring containing hydroxy groups all hydroxy groups bound to the ring
    • 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
    • Y02P20/54Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids

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Abstract

The invention discloses a hydroxyl arone and a preparation method thereof. The preparation method comprises the step of reacting alkylphenol ester and/or halogenated phenol ester under the action of a catalyst in a solvent or non-solvent state to obtain the hydroxy aryl ketone, wherein the catalyst comprises ionic liquid and organic metal framework material. The preparation method can effectively improve the conversion rate of the phenolic ester and the selectivity of the hydroxyl arone.

Description

Hydroxy arone and preparation method thereof
Technical Field
The invention relates to hydroxyl arone and a preparation method thereof.
Background
The hydroxy arone molecule contains hydroxy and keto on benzene ring, is a very important fine chemical and synthetic intermediate, and has wide application in the fields of medicine, cosmetics, food, synthetic material, etc. Wherein, the p-hydroxyacetophenone is an example, which is a natural plant extract, and is naturally present in stems and leaves of Artemisia scoparia of Compositae, and roots of Artemisia capillaris Thunb, asclepiadaceae plant, heteropappus ginseng, 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 that phenyl acetate is rearranged in molecules to obtain hydroxyacetophenone, the atom utilization rate is very high, so the method is favored, and in the prior art, the effective catalytic system is Lewis acid,
Figure BDA0003074158440000011
Acids and ionic liquid based catalysts. However, lewis acid and ionic liquid catalysts have the defects of large dosage, low selectivity of the hydroxyl arone and the like.
Disclosure of Invention
Aiming at the problems of low conversion rate of phenolic ester and low selectivity of hydroxyl arone in the catalytic synthesis of hydroxyl arone by alkylphenol ester or halogenated phenol ester in the prior art, the invention provides a novel preparation method of hydroxyl arone, which can effectively improve the conversion rate of phenolic ester and the selectivity of hydroxyl arone.
The invention provides a preparation method of hydroxyaryl ketone, which comprises reacting alkylphenol ester and/or halogenated phenol ester under the action of a catalyst in a solvent or non-solvent state to obtain hydroxyaryl ketone, wherein the catalyst comprises ionic liquid and organic metal framework material.
In the above technical solution, preferably, the organometallic framework material is selected from one or more of IRMOF, ZIFs, PCP and MIL; more preferably MIL.
In the above technical solution, preferably, the MIL is selected from one or more of MIL-53, MIL-100 and MIL-101; preferably MIL-100; more preferably Fe (III) -MIL-100 and/or Al (III) -MIL-100.
In the present invention, the organometallic framework material is preferably an organometallic framework material subjected to drying treatment.
In the above technical solution, preferably, the ionic liquid is selected from one or more of imidazole ionic liquid, quaternary ammonium salt ionic liquid, quaternary phosphonium salt ionic liquid, sulfonic acid ionic liquid and pyridine ionic liquid; preferably imidazole ionic liquid and/or quaternary ammonium salt ionic liquid; more preferably from [ Et ] 3 NHCl]·2AlCl 3 、[BMim]·2AlCl 3 、[Et 3 NHCl]·2FelCl 3 、[BMim]·2FeCl 3 One or more of (a). Such as but not limited to: [ Bmim ]] + Fe 2 C1 7 - 、[Bmim] + Al 2 C1 7 - And so on.
In the above technical solution, preferably, the alkylphenol ester has a structural formula shown in chemical formula a,
Figure BDA0003074158440000021
wherein R is 2 、R 3 Independently selected from H, C1-C6 alkyl; r 1 Is selected from C1-C6 alkyl and C6-C9.
In the above technical solution, preferably, the alkylphenol ester is selected from one or more of phenyl acetate, phenyl propionate, 2, 6-dimethylphenol acetate and 3, 5-dimethylphenol acetate.
In the above technical solution, preferably, the halogenated phenol ester has a structural formula shown in chemical formula b,
Figure BDA0003074158440000022
wherein R is 4 Selected from C1-C6 alkyl and C6-C9 aryl; x is selected from one of-F, -Cl, -Br and-I.
In the above technical solution, preferably, the halogenated phenol ester is m-fluorophenol acetate and/or m-chlorophenol acetate.
In the above technical solution, preferably, the weight ratio of the alkylphenol ester and/or halogenated phenol ester, the ionic liquid and the organic metal framework material is 1 (0.01-20) to (0.01-30), and preferably 1 (1-5) to (0.01-8).
In the above technical solution, preferably, the solvent is selected from one or more of chlorobenzene, nitrobenzene, toluene, nitromethane, acetonitrile and dichloromethane. In the present invention, the amount of the solvent to be added is selected from a wide range and may be determined as necessary. For example, the weight ratio of the alkylphenol ester and/or halogenated phenol ester to the amount of the solvent added is 1.
In the above technical solution, preferably, the reaction conditions include: the temperature is 20-200 deg.C, preferably 20-100 deg.C.
In the above technical solution, preferably, the reaction conditions include: the pressure is 0.1MPa to 6MPa, preferably 0.1MPa to 2MPa.
In the above technical solution, preferably, the reaction conditions include: the time is 0.1-10h, preferably 0.5-5h.
In the above-mentioned embodiment, the term "in a non-solvent state" means a state where no solvent is used.
In the above technical scheme, preferably, the preparation method further comprises adding water, stirring, extracting with ethyl acetate, combining organic phases, and anhydrous Na 2 SO 4 After drying, the mixture was filtered and the solvent was evaporated under reduced pressure.
In a second aspect, the present invention provides a hydroxyaryl ketone prepared by the above-mentioned preparation method.
The invention has the beneficial effects that:
the preparation method has the advantages of simple and efficient process and capability of effectively improving the conversion rate of the phenolic ester (alkylphenol ester and/or halogenated phenol ester) and the selectivity of the hydroxyl arone.
Detailed Description
In order that the present invention may be more readily understood, the following detailed description of the invention is given by way of example only, and is not intended to limit the scope of the invention.
In the examples of the present invention and comparative examples, all the materials were commercially available.
A calculation formula of a conversion rate of a raw material (alkylphenol ester and/or halogenated phenol ester) = (moles of alkylphenol ester and/or halogenated phenol ester added-moles of alkylphenol ester and/or halogenated phenol ester remaining after the reaction)/moles of alkylphenol ester and/or halogenated phenol ester added × 100%.
The formula for the calculation of the selectivity of the product (hydroxyaryl ketone) = moles of hydroxyaryl ketone in the product/moles of total product x 100%.
[ PREPARATION EXAMPLE 1 ]
The Fe (III) -MIL-100 was dried overnight in an oven at 150 ℃.
[ PREPARATION EXAMPLE 2 ]
1-butyl-3-methylimidazole chloride salt ([ Bmim ]] + C1 - ) With anhydrous FeCl 3 Mixing the components according to the mass ratio of 1] + Fe 2 C1 7 -
[ PREPARATION EXAMPLES 3 to 8 ]
Respectively placing Al (III) -MIL-100, MIL-53, MIL-101, IRMOF, ZIFs and PCP in an oven at 150 ℃ for drying overnight.
[ PREPARATION EXAMPLES 9 to 10 ]
Respectively adding Et 3 NHCl, BMimCl and anhydrous AlCl 3 The substances are mixed according to the mass ratio of 1 3 NHCl]·2AlCl 3 、[BMim]·2AlCl 3
[ PREPARATION EXAMPLE 11 ]
Adding Et 3 NHCl and anhydrous FeCl 3 The materials are mixed according to the mass ratio of 1 3 NHCl]·2FelCl 3
[ example 1 ]
A50 mL flask was charged with 2.5g of phenyl acetate, 0.2g of dried Fe (III) -MIL-100 (obtained in preparation example 1) and 1g of [ Bmim ]] + Fe 2 C1 7 - (obtained in preparation example 2), the system was heated to 80 ℃ under normal pressure 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 (Agilent model 7890). The results of the conversion of the starting material (phenyl acetate) and the selectivity of the product (hydroxyacetophenone) are shown in Table 1.
[ examples 2 to 7 ]
Following the procedure of example 1, except that Fe (III) -MIL-100 was replaced with Al (III) -MIL-100, MIL-53, MIL-101, IRMOF, ZIFs, PCP, which were obtained after drying in preparation examples 3-8, respectively. The results of conversion of the starting material (phenyl acetate) and selectivity of the product (hydroxyacetophenone) are shown in Table 1.
[ examples 8 to 10 ]
Following the procedure of example 1, except that [ Bmim ] is] + Fe 2 C1 7 - Respective substitutions were made with [ Et ] obtained in production examples 9 to 11 3 NHCl]·2AlCl 3 、[BMim]·2AlCl 3 、[Et 3 NHCl]·2FelCl 3 . The results of conversion of the starting material (phenyl acetate) and selectivity of the product (hydroxyacetophenone) are shown in Table 1.
[ example 11 ]
A50 mL flask was charged with 2.5g of phenyl acetate, 0.025g of dried Fe (III) -MIL-100 (obtained in preparation example 1) and 2.5g of [ Bmim ]] + Fe 2 C1 7 - (obtained in preparation example 2), the system was heated to 80 ℃ under normal pressure 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 results of conversion of the starting material (phenyl acetate) and selectivity of the product (hydroxyacetophenone) are shown in Table 1.
[ example 12 ] A method for producing a polycarbonate
A50 mL flask was charged with2.5g of phenyl acetate, 20g of dried Fe (III) -MIL-100 (obtained in preparation example 1) and 12.5g of [ Bmim ]] + Fe 2 C1 7 - (obtained in production example 2), the system was heated to 80 ℃ for 4 hours under normal pressure, 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 results of conversion of the starting material (phenyl acetate) and selectivity of the product (hydroxyacetophenone) are shown in Table 1.
[ example 13 ]
A50 mL flask was charged with 2.5g of phenyl acetate, 75g of dried Fe (III) -MIL-100 (obtained in preparation example 1) and 50g of [ Bmim ]] + Fe 2 C1 7 - (obtained in production example 2), the system was heated to 80 ℃ for 4 hours under normal pressure, 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 results of conversion of the starting material (phenyl acetate) and selectivity of the product (hydroxyacetophenone) are shown in Table 1.
[ example 14 ] A method for producing a polycarbonate
A50 mL flask was charged with 2.5g of phenyl acetate, 0.2g of dried Fe (III) -MIL-100 (obtained in preparation example 1), and 1g of [ Bmim ]] + Fe 2 C1 7 - (obtained in preparation example 2) and 20ml of acetonitrile, and the system was heated to 80 ℃ under normal pressure 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 results of conversion of the starting material (phenyl acetate) and selectivity of the product (hydroxyacetophenone) are shown in Table 1.
[ example 15 ]
A50 mL flask was charged with 2.5g of phenyl acetate, 0.2g of dried Fe (III) -MIL-100 (obtained in preparation example 1), and 1g of [ Bmim ]] + Fe 2 C1 7 - (obtained in preparation example 2) and 20ml of nitrobenzene were heated to 80 ℃ under normal pressure for 4 hours and cooled to room temperature. 50mL of water was addedStirring thoroughly, extracting with ethyl acetate for three times, mixing 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 results of conversion of the starting material (phenyl acetate) and selectivity of the product (hydroxyacetophenone) are shown in Table 1.
[ examples 16 to 19 ]
The procedure of example 1 was followed except that 80 ℃ was replaced with 20 ℃, 40 ℃, 60 ℃ and 100 ℃, respectively. The results of conversion of the starting material (phenyl acetate) and selectivity of the product (hydroxyacetophenone) are shown in Table 1.
[ examples 20 to 23 ]
The procedure of example 1 was repeated except that phenyl acetate was replaced with 2, 6-dimethylphenol acetate, 3, 5-dimethylphenol acetate, m-fluorophenol acetate, and m-chlorophenol acetate, respectively. The results of conversion of the starting material and selectivity of the product (substituted hydroxyacetophenone) are shown in Table 1.
Comparative example 1
A50 mL flask was charged with 2.5g of phenyl acetate and 0.2g of dried Fe (III) -MIL-100 (obtained in preparation example 1), and the system was heated to 80 ℃ under normal pressure 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 results of conversion of the starting material (phenyl acetate) and selectivity of the product (hydroxyacetophenone) are shown in Table 1.
Comparative example 2
A50 mL flask was charged with 2.5g of phenyl acetate and 1g of [ Bmim ]] + Fe 2 C1 7 - (obtained in preparation example 2), the system was heated to 80 ℃ under normal pressure 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 results of conversion of the starting material (phenyl acetate) and selectivity of the product (hydroxyacetophenone) are shown in Table 1.
TABLE 1
Figure BDA0003074158440000071
Figure BDA0003074158440000081
What has been described above is merely a preferred example of the present invention. It should be noted that other equivalent variations and modifications can be made by those skilled in the art based on the technical teaching provided by the present invention, and the protection scope of the present invention should be considered.

Claims (10)

1. A preparation method of hydroxyaryl ketone comprises the step of reacting alkylphenol ester and/or halogenated phenol ester under the action of a catalyst in a solvent or non-solvent state to obtain hydroxyaryl ketone, wherein the catalyst comprises an ionic liquid and an organic metal framework material.
2. The preparation method according to claim 1, wherein the organometallic framework material is selected from one or more of IRMOF, ZIFs, PCP and MIL; more preferably MIL.
3. The method of claim 2, wherein the MIL is selected from one or more of MIL-53, MIL-100, and MIL-101; preferably MIL-100; more preferably Fe (III) -MIL-100 and/or Al (III) -MIL-100.
4. The preparation method of claim 1, wherein the ionic liquid is selected from one or more of imidazole ionic liquids, quaternary ammonium salt ionic liquids, quaternary phosphonium salt ionic liquids, sulfonic acid ionic liquids and pyridine ionic liquids; preferably imidazole ionic liquid and/or quaternary ammonium salt ionic liquid; more preferably from [ Et ] 3 NHCl]·2AlCl 3 、[BMim]·2AlCl 3 、[Et 3 NHCl]·2FelCl 3 、[BMim]·2FeCl 3 One or more of (a).
5. The method according to any one of claims 1 to 4, wherein the alkylphenol ester has a structural formula shown by the chemical formula a,
Figure FDA0003074158430000011
wherein R is 2 、R 3 Independently selected from H, C1-C6 alkyl; r 1 Selected from C1-C6 alkyl and C6-C9 aryl;
more preferably, the alkylphenol ester is selected from one or more of phenyl acetate, phenyl propionate, (2, 6-dimethylphenol) acetate and (3, 5-dimethylphenol) acetate.
6. The method according to any one of claims 1 to 4, wherein the halogenated phenol ester has a structural formula shown by the chemical formula b,
Figure FDA0003074158430000021
wherein R is 4 Selected from C1-C6 alkyl and C6-C9 aryl; x is selected from one of-F, -Cl, -Br and-I;
more preferably, the halogenated phenol ester is m-fluorophenol acetate and/or m-chlorophenol acetate.
7. The method according to any one of claims 1 to 4, wherein the weight ratio of the alkylphenol ester and/or halogenated phenol ester, the ionic liquid and the organometallic framework material is 1 (0.01-20) to (0.01-30), preferably 1 (1-5) to (0.01-8).
8. The method according to any one of claims 1 to 4, wherein the solvent is one or more selected from chlorobenzene, nitrobenzene, toluene, nitromethane, acetonitrile and dichloromethane.
9. The production method according to any one of claims 1 to 4, wherein the reaction conditions include: the temperature is 20-200 ℃, preferably 20-100 ℃; and/or the pressure is 0.1MPa to 6MPa, preferably 0.1MPa to 2MPa; the time is 0.1-10h, preferably 0.5-5h.
10. A hydroxyaryl ketone produced by the production method according to any one of claims 1 to 9.
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19624292A1 (en) * 1996-06-18 1998-01-02 Merckle Gmbh Preparation of optically pure 1'-hydroxy-benz-bromoarone
CN103360225A (en) * 2013-06-28 2013-10-23 大连大学 Method for preparing p-hydroxy phenyl ethyl ketone compound through rearrangement reaction under catalysis of acidic ionic liquid
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
CN105130781A (en) * 2015-08-20 2015-12-09 上海应用技术学院 Preparation method of 2-hydroxyacetophenone
CN111514939A (en) * 2020-06-16 2020-08-11 太原理工大学 Preparation method and application of ionic liquid/MOF composite catalyst

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19624292A1 (en) * 1996-06-18 1998-01-02 Merckle Gmbh Preparation of optically pure 1'-hydroxy-benz-bromoarone
CN103360225A (en) * 2013-06-28 2013-10-23 大连大学 Method for preparing p-hydroxy phenyl ethyl ketone compound through rearrangement reaction under catalysis of acidic ionic liquid
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
CN105130781A (en) * 2015-08-20 2015-12-09 上海应用技术学院 Preparation method of 2-hydroxyacetophenone
CN111514939A (en) * 2020-06-16 2020-08-11 太原理工大学 Preparation method and application of ionic liquid/MOF composite catalyst

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
姜红波: "咪唑类离子液体及其催化有机重排反应", 《化工时刊》, vol. 24, no. 11, 30 November 2010 (2010-11-30), pages 57 - 59 *

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