CN110963877B - Preparation method of 1-chloro-1-chloroacetyl cyclopropane - Google Patents

Preparation method of 1-chloro-1-chloroacetyl cyclopropane Download PDF

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CN110963877B
CN110963877B CN201911308799.XA CN201911308799A CN110963877B CN 110963877 B CN110963877 B CN 110963877B CN 201911308799 A CN201911308799 A CN 201911308799A CN 110963877 B CN110963877 B CN 110963877B
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cyclopropane
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CN110963877A (en
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张捷
杨学林
闫晶红
王耀红
党伟荣
陈西波
闫英然
何海娜
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Dingzhou Risun Technology Co ltd
Hebei Xuyang Energy Co ltd
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    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2/00Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
    • C07C2/86Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation between a hydrocarbon and a non-hydrocarbon
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    • 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
    • C07C45/27Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation
    • C07C45/32Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen
    • C07C45/33Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties
    • C07C45/34Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties in unsaturated compounds
    • C07C45/35Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties in unsaturated compounds in propene or isobutene
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    • 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
    • C07C45/61Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups
    • C07C45/63Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by introduction of halogen; by substitution of halogen atoms by other halogen atoms
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    • C07C2601/02Systems containing only non-condensed rings with a three-membered ring

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Abstract

The application provides a preparation method of 1-chloro-1-chloroacetyl cyclopropane. The preparation method comprises the following steps: 1) Reacting 1, 3-butadiene with diazomethane to produce vinylcyclopropane; 2) Reacting a vinylcyclopropane with an oxidizing reagent to produce an acetylcyclopropane; and 3) reacting the acetylcyclopropane with a chlorinating agent to produce the target product 1-chloro-1-chloroacetylcyclopropane. The method can reduce the use of strong acid, strong base and chlorinating agent in the preparation of 1-chloro-1-chloroacetyl cyclopropane, thereby reducing the discharge of three wastes and the safety risk, and simultaneously can improve the synthesis yield so as to be suitable for industrial production.

Description

Preparation method of 1-chloro-1-chloroacetyl cyclopropane
Technical Field
The invention relates to the field of fine organic synthesis, in particular to a preparation method of prothioconazole intermediate 1-chloro-1-chloroacetyl cyclopropane.
Background
Prothioconazole is a broad-spectrum triazolethione bactericide which is widely applied, can be used for diseases of crops such as cereals, wheat and beans, and has the advantages of high efficiency, low toxicity, no three causes (carcinogenesis, teratogenesis and mutagenesis), little influence on human and livestock and environmental safety. At present, a plurality of enterprises at home and abroad are producing or preparing the pesticide variety.
The 1-chloro-1-chloroacetyl cyclopropane (CAS No: 120983-72-4) is a key intermediate in the prothioconazole production process, and the production technology mainly takes acetyl-gamma-butyrolactone as a starting material and obtains the product through four steps of chlorination, acidolysis, ring closure, secondary chlorination and the like. Such as US patent No. 4938791, chinese patent No. CN105384617, CN108586220, etc. As chlorine/sulfonyl chloride, caustic soda, concentrated hydrochloric acid and the like are required to be continuously used in the production process, a large amount of three wastes are generated, and the environmental damage is large. At present, various colleges and universities, enterprises and scientific research institutions have proposed related improvement schemes, such as the Chinese patent CN105384617 and the Chinese patent CN 107118090.
In view of the above problems faced in the preparation of prothioconazole intermediates, there is still a need to develop a new process that can synthesize prothioconazole intermediates in an environmentally friendly manner.
Disclosure of Invention
The invention aims to provide a novel preparation process of prothioconazole intermediate 1-chloro-1-chloroacetyl cyclopropane, which can reduce the use of strong acid, strong base and chlorinating agent, further reduce the discharge of three wastes and the safety risk, and simultaneously can improve the synthesis yield so as to adapt to industrial production.
The invention provides a preparation method of 1-chloro-1-chloroacetyl cyclopropane, which comprises the following steps:
Figure BDA0002323942950000021
(1) And (3) naphthenization reaction: reacting 1, 3-butadiene with diazomethane to produce a vinylcyclopropane;
(2) And (3) oxidation reaction: reacting a vinylcyclopropane with an oxidizing reagent to produce an acetylcyclopropane; and
(3) Chlorination reaction: reacting the acetyl cyclopropane with a chlorinating agent to generate the target product 1-chloro-1-chloroacetyl cyclopropane.
In a particular embodiment, in step (1), the catalyst used may be selected from palladium dichloride, palladium acetate or tris (dibenzylideneacetone) dipalladium, preferably palladium acetate, and is used in an amount of 1 to 20% by weight based on 1, 3-butadiene.
In a particular embodiment, in step (1), the solvent used may be selected from diethyl ether, dichloromethane, acetonitrile or chloroform, preferably diethyl ether or acetonitrile.
In a specific embodiment, in step (2), the oxidizing agent may be selected from oxygen, air or hydrogen peroxide, preferably oxygen.
In a specific embodiment, in step (2), the catalyst used may be selected from palladium chloride, palladium acetate, the cocatalyst may be selected from cuprous chloride, cuprous acetate or silver nitrate, preferably, palladium chloride and cuprous chloride are used as the catalytic system, and the amount of the catalytic system is 1-10% by weight of the vinylcyclopropane.
In a specific embodiment, the solvent used in step (2) is a water-organic solvent mixed system in which the organic solvent may be selected from N, N-Dimethylformamide (DMF), N-dimethylacetamide, dimethylsulfoxide (DMSO), acetonitrile, tetrahydrofuran, or 1, 4-dioxane, preferably, the organic solvent is DMF; in the water-organic solvent mixed system, the volume ratio of water to organic solvent is 1.
In a specific embodiment, in step (3), the chlorinating agent may be selected from chlorine gas, sulfuryl chloride, thionyl chloride, alkyl sulfuryl chloride or N-chlorosuccinimide (NCS), preferably NCS.
In a particular embodiment, the solvent used in step (3) may be selected from dichloromethane, chloroform, carbon tetrachloride, acetonitrile or N, N-Dimethylformamide (DMF), preferably dichloromethane.
In a specific embodiment, the reaction temperature of step (1) is 0 to 40 ℃, preferably 10 to 30 ℃;
the reaction temperature of the step (2) is 0-80 ℃, preferably 25-45 ℃, and more preferably 40 ℃; and
the reaction temperature in step (3) is 0 to 80 ℃, preferably 20 to 30 ℃, and more preferably 25 ℃.
In a specific embodiment, in step (3), the addition manner and amount of the chlorinating agent are as follows: 1.0 to 1.1 moles of a chlorinating agent is added to 1 mole of acetylcyclopropane at 0 ℃, and after the temperature is raised to room temperature, 1.0 to 1.1 moles of the chlorinating agent is added again to 1 mole of acetylcyclopropane.
Advantageous effects
The preparation method of the prothioconazole intermediate has the following advantages:
1) 1, 3-butadiene which is a common product in the petrochemical industry is used as a raw material instead of acetyl-gamma-butyrolactone, so that the raw material source is wider and easily available, and the raw material cost is saved;
2) Diazomethane is used as a naphthenic reagent, a byproduct is only nitrogen, the treatment of waste gas is simplified, and a catalyst and a solvent can be recycled;
3) The preparation of the acetyl cyclopropane uses air and the like as oxidation reagents, the atom utilization rate is high, the discharge of three wastes is less, and the catalyst can be recycled for multiple times;
4) In the chlorination step, NCS is preferably used as a chlorination reagent, so that the selectivity is high, the by-product is succinimide, and the succinimide can be regenerated and recycled in combination with chlor-alkali enterprises after simple distillation and purification;
5) Compared with the traditional process, the method basically generates no wastewater, so the whole process is green and environment-friendly.
Drawings
FIG. 1 is a gas chromatogram of the product 1-chloro-1-chloroacetylcyclopropane obtained in the present invention.
FIG. 2 is a nuclear magnetic resonance spectrum of the product 1-chloro-1-chloroacetylcyclopropane obtained in the present invention.
Detailed Description
The process disclosed herein is described below with reference to specific embodiments. These descriptions are not intended to limit the scope of the invention.
Examples
Step 1: a stainless steel reaction kettle with a tetrafluoro lining is added with ethyl ether solution of diazomethane and a catalytic amount of palladium acetate, then the reaction kettle is closed and replaced by nitrogen, stirring is started, and 1, 3-butadiene is slowly introduced at room temperature, and the pressure is kept at 0.4MPa. As the reaction proceeded, the pressure began to decrease, and 1, 3-butadiene was continuously supplied until the pressure remained 0.4MPa and did not decrease, and the reaction was continued for 1 hour. After the reaction is finished, the reaction kettle is opened, the reaction solution is distilled, the ether and the product of the vinylcyclopropane are distilled out, and the catalyst palladium acetate is left at the bottom of the kettle and can be recycled along with the distilled ether. The boiling range of the product vinylcyclopropane is 40-42 ℃ under normal pressure. The reaction yield was > 90% calculated on diazomethane consumption.
1 H-NMR(400MH,CDCl 3 ):δ=5.44(1H,t),5.16(1H,m),4.94(1H,m),1.40(1H,m),0.72(2H,m),0.48(2H,m)。
And 2, step: in an oil bath, a 500mL three-necked flask was placed, a gas introduction-receiving device was installed, and a tetrafluoro stirrer was added, and then 200mL of a mixed solvent of water and DMF (volume ratio 1. The reaction time was 6 hours, during which the degree of reaction progress was checked by gas chromatography. After the reactant is completely converted, the device is changed into a fractionating device, samples at different stages are collected, and 19g of pale yellow oily liquid can be collected, wherein the yield is 80 percent, and the content is more than 98 percent.
1 H-NMR(400MH,CDCl 3 ):δ=2.20(3H,s),2.00(1H,m),0.92(2H,m),0.64(2H,m)。
And step 3: 10g of acetylcyclopropane (0.12 mol) and 30ml of methylene chloride were charged into a 250ml three-neck round-bottom flask, and the mixture was cooled down in a 0 ℃ cooling bath, followed by addition of 33.5g of NCS (0.25 mol), and the temperature was gradually raised to room temperature with stirring. Stirring for 2-3 hours. The reaction produced a large amount of precipitate. After the reaction was completed, the mixture was filtered in a fume hood. The filter cake was washed with a small amount of dichloromethane, the filtrates were combined, the solvent dichloromethane was distilled off from the filtrate, followed by distillation under reduced pressure to give the objective product as a pale yellow transparent oily liquid 16.8g, which was confirmed to be 1-chloro-1-chloroacetylcyclopropane with a purity of > 97% by GC-MS (FIG. 1) and H-NMR (FIG. 2). The yield thereof was found to be 92%. The recovered succinimide can be directly used for preparing NCS for recycling.
1 H-NMR(400MH,CDCl 3 ):δ=4.76(2H,s),1.76(2H,q),1.45(2H,q)。
The above examples show that the process flow of the invention is simple, the comprehensive yield is high, the invention can be used for preparing high-purity 1-chloro-1-chloroacetyl cyclopropane, and the invention is suitable for industrial scale production.
The above are only specific embodiments of the present invention, and any changes or modifications obvious to those skilled in the art using the method of the present invention are within the protection scope of the present patent.

Claims (17)

1. A method for preparing 1-chloro-1-chloroacetyl cyclopropane, which comprises the following steps:
Figure FDA0003594700490000011
(1) And (3) performing a naphthenic reaction: reacting 1, 3-butadiene with diazomethane to produce a vinylcyclopropane;
(2) And (3) oxidation reaction: reacting a vinylcyclopropane with an oxidizing reagent to produce an acetylcyclopropane; and
(3) Chlorination reaction: reacting acetyl cyclopropane with a chlorinating agent to generate the target product 1-chloro-1-chloroacetyl cyclopropane
Wherein, in the step (3), the chlorinating reagent is N-chlorosuccinimide.
2. The process according to claim 1, wherein in step (1), the catalyst used is selected from palladium dichloride, palladium acetate and tris (dibenzylideneacetone) dipalladium and is used in an amount of 1 to 20% by weight based on 1, 3-butadiene.
3. The process according to claim 1, wherein in step (1), the catalyst used is palladium acetate and the amount of the catalyst is 1 to 20% by weight based on 1, 3-butadiene.
4. The method according to claim 1, wherein, in step (1), the solvent used is selected from the group consisting of diethyl ether, dichloromethane, acetonitrile and chloroform.
5. The process according to claim 1, wherein in step (1), the solvent used is diethyl ether or acetonitrile.
6. The process of claim 1, wherein in step (2), the oxidizing agent is selected from the group consisting of oxygen, air, and hydrogen peroxide.
7. The method of claim 1, wherein in step (2), the oxidizing agent is oxygen.
8. The process according to claim 1, wherein in step (2), the catalyst used is selected from palladium chloride and palladium acetate, the promoter is selected from cuprous chloride, cuprous acetate and silver nitrate, and the catalyst system is used in an amount of 1-10% by weight of vinylcyclopropane.
9. The process according to claim 1, wherein in step (2), palladium chloride and cuprous chloride are used as catalytic system and the amount of said catalytic system is 1-10% by weight of vinylcyclopropane.
10. The method according to claim 1, wherein, in step (2), the solvent used is a water-organic solvent mixed system in which the organic solvent is selected from the group consisting of N, N-dimethylformamide, N-dimethylacetamide, dimethylsulfoxide, acetonitrile, tetrahydrofuran and 1, 4-dioxane, and the volume ratio of water to organic solvent is 1.
11. The method according to claim 1, wherein, in step (2), the solvent used is a water-organic solvent mixed system in which the organic solvent is N, N-dimethylformamide, and the volume ratio of water to organic solvent is 1.
12. The method according to claim 1, wherein, in step (3), the solvent used is selected from the group consisting of dichloromethane, chloroform, carbon tetrachloride, acetonitrile and N, N-dimethylformamide.
13. The process according to claim 1, wherein in step (3), the solvent used is dichloromethane.
14. The method of claim 1, wherein,
the reaction temperature of the step (1) is 0-40 ℃;
the reaction temperature of the step (2) is 0-80 ℃; and
the reaction temperature in the step (3) is 0-80 ℃.
15. The method of claim 1, wherein,
the reaction temperature of the step (1) is 10-30 ℃;
the reaction temperature of the step (2) is 25-45 ℃; and
the reaction temperature of the step (3) is 20-30 ℃.
16. The method of claim 1, wherein,
the reaction temperature of the step (2) is 40 ℃; and
the reaction temperature in step (3) was 25 ℃.
17. The method according to claim 1, wherein in step (3), the chlorinating agent is added in the following manner and in the following amount: 1.0 to 1.1 moles of chlorinating agent are added to 1 mole of acetylcyclopropane at 0 ℃, and after the temperature is raised to room temperature, 1.0 to 1.1 moles of chlorinating agent to 1 mole of acetylcyclopropane are added again.
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1054586A (en) * 1990-03-08 1991-09-18 藤泽药品工业株式会社 New substituted amine compound and preparation method thereof
CN105683146A (en) * 2013-10-25 2016-06-15 奇华顿股份有限公司 Preparation of homoallylic compounds by reaction of cyclopropylvinyl precursors with bronstedt acids
CN109748783A (en) * 2019-01-31 2019-05-14 河北诚信集团有限公司 A kind of preparation method of the chloro- 1- of 2- (1- chlorine cyclopropyl) ethyl ketone
CN110577484A (en) * 2019-07-02 2019-12-17 凯莱英医药集团(天津)股份有限公司 Method and device for continuously synthesizing cyclopropane compound

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1054586A (en) * 1990-03-08 1991-09-18 藤泽药品工业株式会社 New substituted amine compound and preparation method thereof
CN105683146A (en) * 2013-10-25 2016-06-15 奇华顿股份有限公司 Preparation of homoallylic compounds by reaction of cyclopropylvinyl precursors with bronstedt acids
CN109748783A (en) * 2019-01-31 2019-05-14 河北诚信集团有限公司 A kind of preparation method of the chloro- 1- of 2- (1- chlorine cyclopropyl) ethyl ketone
CN110577484A (en) * 2019-07-02 2019-12-17 凯莱英医药集团(天津)股份有限公司 Method and device for continuously synthesizing cyclopropane compound

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
Reaction of diazoalkanes with unsaturated compounds. 6. Catalytic cyclopropanation of various unsaturated hydrocarbons and their derivatives by diazomethane;Dzhemilev, U. M. et al.;《Izvestiya Akademii Nauk SSSR, Seriya Khimicheskaya》;19891231;第8卷;1861-1869 *

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