CN114539041B - Preparation method of penconazole intermediate - Google Patents

Preparation method of penconazole intermediate Download PDF

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Publication number
CN114539041B
CN114539041B CN202011345578.2A CN202011345578A CN114539041B CN 114539041 B CN114539041 B CN 114539041B CN 202011345578 A CN202011345578 A CN 202011345578A CN 114539041 B CN114539041 B CN 114539041B
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formula
penconazole
catalyst
chlorine
reaction
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CN114539041A (en
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焦体
谭徐林
李生学
李星强
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Purpana Beijing Technologies Co Ltd
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Purpana Beijing Technologies Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C253/00Preparation of carboxylic acid nitriles
    • C07C253/30Preparation of carboxylic acid nitriles by reactions not involving the formation of cyano groups
    • 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
    • C07C45/44Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reduction and hydrolysis of nitriles
    • 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
    • Y02P20/584Recycling of catalysts

Abstract

The invention belongs to the technical field of intermediate compound preparation, and particularly relates to a preparation method of a penconazole intermediate. The preparation method of the penconazole intermediate is a one-pot synthesis process, and comprises the following steps: under the action of inorganic base and catalyst, taking the reagent with the formula (II) and chlorine as raw materials, and blowing air to react to obtain the target product. The invention provides a one-pot synthesis line, which utilizes oxygen in air to oxidize cyano in formula (II) while chlorine-containing reagent reacts with R group in formula (II), thus greatly shortening reaction process and improving production efficiency; moreover, the reaction condition is milder, the waste water is less and is easy to treat, the method is more suitable for industrialized mass production, and the problems of harsh conditions, large three wastes, bad production environment and the like of the existing intermediate synthesis line are solved. Meanwhile, the cost of raw materials for synthesizing the intermediate of the penconazole can be greatly reduced, and the method has practical economic benefit.

Description

Preparation method of penconazole intermediate
Technical Field
The invention belongs to the technical field of intermediate compound preparation, and particularly relates to a preparation method of a penconazole intermediate.
Background
The penoxsulam (common name: mefenobuconazole) is a triazole bactericide which is newly developed by Basoff company and has epoch-making significance, and is formally marketed in 2019, and the future market is expected to exceed 10 hundred million dollars per year.
The penconazole has the functions of broad spectrum, high efficiency, systemic, eradication, protection and the like, has outstanding biological activity especially on a plurality of fungal diseases which are difficult to control, can obviously strengthen the control of more than 60 crop diseases, such as field crops like corns, grains, soybeans and the like, economic crops like green peppers, grapes and the like, and can also be used for lawn and seed treatment and the like. It has higher bioactivity, good environmental characteristics, low toxicity to mammals, bees and the like, and high safety.
The 4- (4-chlorophenoxy) -2-trifluoromethyl acetophenone is a key intermediate for synthesizing the penconazole, and the penconazole is prepared through epoxidation and ring-opening substitution reaction, so that the process is simple and the yield is higher. The structure is as follows:
the technology currently used for producing 4- (4-chlorophenoxy) -2-trifluoromethyl acetophenone is mostly referred to the technology disclosed in the prior art CN103649057 a. 2-bromo-4-fluoro-benzotrifluoride is taken as a raw material, grignard reagent is prepared in tetrahydrofuran solution, acetyl chloride is added dropwise, after the reaction is finished, 4-fluoro-2-benzotrifluoride is prepared through processes such as extraction, water washing and the like, and then 4- (4-chlorophenoxy) -2-benzotrifluoride is synthesized by reacting with 4-chlorophenol. The specific reaction route is as follows:
however, the process route needs to use a format reaction, the condition is severe, and a large amount of magnesium-containing wastewater is generated after the reaction, so that the magnesium-containing wastewater is difficult to treat.
In conclusion, the existing method has the defects of large three wastes, high cost, bad production environment and the like when preparing the 4-p-chlorophenoxy acetophenone compounds.
Disclosure of Invention
The invention aims to provide a novel preparation method of a penconazole intermediate (4- (4-chlorophenoxy) -2-trifluoromethyl acetophenone).
The preparation method of the penconazole intermediate adopts a one-pot synthesis process; comprising the following steps: under the action of inorganic base and catalyst, the catalyst is represented by formula (II)The chlorine-containing reagent is used as a raw material, and a target product is obtained through air blowing and reaction;
in the formula (II), R is F, cl, br, I, NO 2 OH; preferably F, NO 2 、OH。
The chlorine-containing reagent is p-chlorophenol or p-dichlorobenzene.
Aiming at the defects of the existing synthesis process of the penconazole intermediate, the invention provides a one-pot synthesis line, and when a chlorine-containing reagent reacts with an R group in a formula (II), the cyano group in the formula (II) is oxidized by oxygen in the air, so that the reaction process can be greatly shortened, and the production efficiency is improved; moreover, the reaction condition is milder, the waste water is less and is easy to treat, the method is more suitable for industrialized mass production, and the problems of harsh conditions, large three wastes, bad production environment and the like of the existing intermediate synthesis line are solved.
Furthermore, screening is carried out according to formula (II)As a raw material, the cost of the raw material for synthesizing the intermediate of the penconazole can be greatly reduced, and the method has practical economic benefit.
The air intake is required to meet the actual production requirement, and can be adjusted by combining experience according to actual conditions by a person skilled in the art.
The process route of the invention is as follows:
as one of the specific embodiments of the present invention, R in the formula (II) is selected to be NO 2 The chlorine-containing reagent is parachlorophenol. Under the combined condition, the reaction is more fully carried out, and the yield is higher.
The inorganic base is any one of sodium hydroxide, potassium carbonate or sodium carbonate, preferably sodium carbonate or potassium carbonate. The inorganic base acts as an acid-fuelling agent. Compared with other inorganic bases, the sodium carbonate or the potassium carbonate is more beneficial to promoting the reaction and improving the yield.
The catalyst is any one of copper ions such as cuprous chloride, cuprous iodide, cuprous oxide, cupric acetate and the like, and preferably cupric acetate. Compared with other catalysts, the copper acetate can promote the reaction to be more fully carried out, and the reaction yield is higher.
As another embodiment of the present invention, the inorganic base is selected to be sodium carbonate or potassium carbonate; the catalyst is copper acetate. The catalytic effect of the copper acetate is better under the alkali system, which is more beneficial to the reaction and improves the yield.
The formula (II) described above relative to 1mol of formula (II): inorganic base: chlorine-containing reagent: the molar ratio of the catalyst to the use amount is 1:0.8-2:0.8-2:0.01-0.1; preferably, the molar ratio of the amount used is 1:0.9 to 1.2:0.9-1.1:0.02-0.05; the preferable dosage mole ratio has the advantages of high reaction yield, low cost and less three wastes.
The temperature of the reaction is 80-150 ℃, preferably 110-130 ℃; the time is 2-8 hours, preferably 3-5 hours.
The reaction is carried out in a polar solvent; the polar solvent is one of acetonitrile, dioxane, N-dimethylformamide, N-dimethylacetamide, dimethyl sulfoxide or N-methylpyrrolidone.
As one of specific embodiments of the invention, the preparation method of the penconazole intermediate comprises the following steps:
under the action of inorganic base and catalyst, the catalyst is represented by formula (II)The chlorine-containing reagent is used as a raw material, and a target product is obtained through air blowing and reaction;
wherein R in the formula (II) is NO 2
The chlorine-containing reagent is parachlorophenol;
the inorganic base is potassium carbonate;
the catalyst is copper acetate;
the polar solvent is DMF;
the formula (II): inorganic base: chlorine-containing reagent: the molar ratio of the catalyst to the use amount is 1:0.9 to 1.2:0.9-1.1:0.02-0.05;
the temperature of the reaction is 120-125 ℃.
The beneficial effects of the invention are as follows:
aiming at the defects of the prior art of the intermediate of the penconazole, the invention provides a new synthetic route. By selecting a specific formula (II) as a raw material, the synthesis of a target product is realized by adopting a one-pot method. The method can omit Grignard reaction and avoid harsh reaction conditions; meanwhile, the production cost is greatly reduced, the yield and purity are improved, and the method has industrial application value.
Detailed Description
The following examples are illustrative of the invention and are not intended to limit the scope of the invention.
The amounts of reactants and products were determined by liquid chromatography (Agilent HPLC 1260).
The conversion and selectivity of the reaction were calculated by the following formula:
conversion= (molar amount of raw material charged-molar amount of raw material remaining in product)/molar amount of raw material charged x 100%.
Selectivity = actual molar amount of target product/theoretical molar amount of target product x 100%
Unless otherwise specified, all materials used are commercially available products.
Example 1
Preparation of 4- (4-chlorophenoxy) -2-trifluoromethyl acetophenone
Into a four-necked flask equipped with a mechanical stirrer, a thermometer and a condenser, 25.7g (0.1 mol, 95%) of formula (II) and 150 mM LDMF were added, followed by 15.4g (0.12 mol, 99%) of p-chlorophenol, 16.8g (0.12 mol, 99%) of potassium carbonate and 0.4g of copper acetate, and the temperature was raised to 120-125℃and air was blown for stirring reaction for 5 hours;
HPLC detection of the raw materials is complete, toluene is added to the recovered solvent, acid water is added to adjust the pH to be 7, the water phase is separated, toluene is removed from the organic layer, 29.8g of 4- (4-chlorophenoxy) -2-trifluoromethyl acetophenone is obtained, the content is 98%, and the yield is 95%.
Example 2
Unlike example 1, the nitro group of formula (II) was replaced by fluoro group, the other conditions were unchanged, the content was 98%, and the yield was 89%.
Example 3
Unlike example 1, the nitro group of formula (II) was replaced with hydroxy group, p-chlorophenol was replaced with p-dichlorobenzene, the other conditions were unchanged, the content was 97%, and the yield was 85%.
While the invention has been described in detail in the foregoing general description and with reference to specific embodiments thereof, it will be apparent to one skilled in the art that modifications and improvements can be made thereto. Accordingly, such modifications or improvements may be made without departing from the spirit of the invention and are intended to be within the scope of the invention as claimed.

Claims (8)

1. A preparation method of a penconazole intermediate is characterized in that a one-pot synthesis process is adopted; comprising the following steps: under the action of inorganic base and catalyst, the catalyst is represented by formula (II)The chlorine-containing reagent is used as a raw material, and a target product is obtained through bubbling air for reaction;
in the formula (II), R is F, cl, br, I, NO 2 、OH;
The chlorine-containing reagent is p-chlorophenol or p-dichlorobenzene;
the reaction route is as follows:
the inorganic base is any one of sodium hydroxide, potassium carbonate or sodium carbonate;
the catalyst is any one of cuprous chloride, cuprous iodide, cuprous oxide and cupric acetate;
the reaction is carried out in a polar solvent; the polar solvent is one of acetonitrile, dioxane, N-dimethylformamide, N-dimethylacetamide, dimethyl sulfoxide or N-methylpyrrolidone.
2. The method for preparing a penconazole intermediate according to claim 1, wherein R in formula (II) is NO 2 The chlorine-containing reagent is parachlorophenol.
3. The method for preparing a penconazole intermediate according to claim 1, wherein said inorganic base is sodium carbonate or potassium carbonate; the catalyst is copper acetate.
4. The process for preparing a difenoconazole intermediate according to claim 3, wherein the molar ratio of inorganic base to chlorine-containing agent to catalyst is 1:0.8-2:0.8-2:0.01-0.1 with respect to 1mol of formula (II).
5. The process for preparing a difenoconazole intermediate according to claim 4, wherein the molar ratio of said formula (II) to inorganic base to chlorine-containing agent to catalyst is 1:0.9-1.2:0.9-1.1:0.02-0.05 with respect to 1mol of formula (II).
6. The method for preparing a penconazole intermediate according to claim 5, wherein the temperature of said reaction is 80-150 ℃.
7. The method for preparing a penconazole intermediate according to claim 6, wherein the temperature of said reaction is 110-130 ℃.
8. The method for preparing the intermediate of the penconazole according to any one of claims 1 to 7, wherein said method for preparing the intermediate of the penconazole is as follows:
under the action of inorganic base and catalyst, the catalyst is represented by formula (II)The chlorine-containing reagent is used as a raw material, and a target product is obtained through air blowing and reaction;
wherein R in the formula (II) is NO 2
The chlorine-containing reagent is parachlorophenol;
the inorganic base is potassium carbonate;
the catalyst is copper acetate;
the polar solvent is DMF;
the molar ratio of the inorganic base to the chlorine-containing reagent to the catalyst in the formula (II) is 1:0.9-1.2:0.9-1.1:0.02-0.05;
the temperature of the reaction is 120-125 ℃.
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Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1552696A (en) * 2003-05-30 2004-12-08 中国科学院大连化学物理研究所 Synthesis of p-cyanoacetophenone by direct catalyst selective oxidation
CN101786948A (en) * 2010-01-25 2010-07-28 江苏省农用激素工程技术研究中心有限公司 Method for preparing 1-(4-chlorphenyl)-2-cyclopropyl-1-acetone
CN102675074A (en) * 2012-05-25 2012-09-19 江西华士药业有限公司 Preparation method of cyproconazole key intermediate 1-(4-chlorphenyl)-2-cyclopropyl-1-acetone
CN103044230A (en) * 2012-12-26 2013-04-17 湖南化工研究院 Preparation method of 1-(4-chlorphenyl)-2-cyclopropyl-1-acetone
CN103649057A (en) * 2011-07-13 2014-03-19 巴斯夫欧洲公司 Fungicidal substituted 2-[2-halogenalkyl-4-(phenoxy)-phenyl]-1-[1,2,4]triazol-1-yl-ethanol compounds
CN105777508A (en) * 2014-12-22 2016-07-20 上海泰禾国际贸易有限公司 Synthesis method of 1-(4-chlorphenyl)-2-cyclopropyl-1-acetone
CN105829274A (en) * 2013-12-18 2016-08-03 巴斯夫农业公司 Process for the Preparation of Substituted Phenoxyphenyl Ketones
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CN103044230A (en) * 2012-12-26 2013-04-17 湖南化工研究院 Preparation method of 1-(4-chlorphenyl)-2-cyclopropyl-1-acetone
CN105829274A (en) * 2013-12-18 2016-08-03 巴斯夫农业公司 Process for the Preparation of Substituted Phenoxyphenyl Ketones
CN105777508A (en) * 2014-12-22 2016-07-20 上海泰禾国际贸易有限公司 Synthesis method of 1-(4-chlorphenyl)-2-cyclopropyl-1-acetone
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