Process for producing 2-fluoro-4-(trifluoromethyl)acetanilide

Abstract: The process comprises reacting 3,4-difluorobenzotrifluoride with acetamide in the presence of a base in an aprotic polar solvent or in a mixture of an aprotic polar solvent and an aprotic non-polar solvent.

Description: This invention relates to an industrially advantageous process for producing 2-fluoro-4-(trifluoromethyl)acetanilide, which is useful as an intermediate for the production of insecticides. The so-far known processes for producing 2-fluoro-4-(trifluoromethyl)acetanilide as described in J. Org. Chem. , 50 , 4576 (1985) and EP-A-0246061 may be illustrated as follows: J. Org. Chem., 50 , 4576 (1985) EP-A-0246061 However, these processes are not necessarily satisfactory for the commercial production of 2-fluoro-4-(trifluoromethyl)acetanilide; That is to say, trifluoromethyl hypofluorite is hardly available because of the necessity of special fluorine-handling techniques, while xenon difluoride is an expensive reagent and the fluorination therewith is not very regioselective, hence the purity of the product is not good. Furthermore, these processes give only low yields and cannot be said to be advantageous from the commercial standpoint. Under the circumstances, we made intensive investigations in an attempt to develop a process for producing 2-fluoro-4-(trifluoromethyl)acetanilide which is much improved from the industrial viewpoint. As a result, we found that the object can be achieved when the method mentioned below is used. Based on this finding, we have completed the present invention. The invention thus provides a process for producing 2-fluoro-4-(trifluoromethyl)acetanilide which comprises reacting 3,4-difluorobenzotrifluoride with acetamide in the presence of a base in an aprotic polar solvent or in a mixture of an aprotic polar solvent and an aprotic non-polar solvent. As for the amounts of the reactants, acetamide and the base are each used generally in an amount of about 1 to about 10 moles, preferably (from the viewpoint of the reaction yield and the economics) about 1.8 to about 2.2 moles, per mole of 3,4-difluorobenzotrifluoride. The reaction is carried out at a temperature within the range of usually about 30 to about 160°C, preferably about 40 to about 100°C, usually for a period of about 0.5 to about 100 hours. The base includes a non-nucleophilic strong base, for example, an alkali metal hydride such as sodium hydride, or an alkali metal carbonate such as potassium carbonate. The aprotic polar solvent includes, among others, dimethylformamide, dimethyl sulfoxide, hexamethylphosphoric triamide, sulfolane, N-methylpyrrolidone, 1,3-dimethyl-2-imidazolidinone, 1,3-dimethyl-3,4,5,6-tetrahydro-2-(1H)-pyrimidone, acetonitrile, tetrahydrofuran and dioxane, and mixtures of these. Furthermore, as a solvent, a mixture of an aprotic polar solvent and an aprotic non-polar solvent may also be used. The aprotic non-polar solvent is preferably, for example, an aromatic hydrocarbon (e.g. C₆-C₈) such as benzene, toluene, etc., an aliphatic hydrocarbon (e.g. C₆-C₈) such as hexane, heptane etc., or a halogenated hydrocarbon (e.g. C₁-C₆) solvent such as chloroform, carbon tetrachloride, chlorobenzene, etc, and mixture of these. When such mixture of an aprotic polar solvent and an aprotic non-polar solvent is used as the reaction solvent, the amount of the aprotic polar solvent is preferably more than 50wt.% based on the weight of said mixture. In order to isolate the desired product, namely 2-fluoro-4-(trifluoromethyl)acetanilide, the reaction mixture is first treated with water or a diluted acid, such as aqueous hydrochloric acid, aqueous ammonium chloride, aqueous citric acid and then subjected to organic solvent extraction and concentration. Examples of organic solvent useful for the extraction is diethyl ether, diisopropyl ether, dichloromethane, chloroform, carbon tetrachloride, benzene, toluene, xylene, chlorobenzene, bromobenzene, ethyl acetate, n-hexane or n-heptane. If necessary, the desired product 2-fluoro-4-(trifluoromethyl) acetanilide can further be purified by recrystallization or chromatography, for instance. If desired, unreacted 3,4-difluorobenzotrifluoride can be recovered from the reaction mixture by distillation or by organic solvent extraction followed by distillation. If the reaction mentioned above is carried out in a reactor equipped with a distillation apparatus, the unreacted 3,4-difluorobenzotrifluoride can directly be recovered by distillation of the reaction mixture. For conducting the organic solvent extraction, the reaction mixture is treated with water or a diluted acid such as aqueous hydrochloric acid, and then subjected to extraction using a low-boiling organic solvent such as diethyl ether, dichloromethane, n-hexane etc. After separation of the aqueous layer, the organic layer is distilled, whereby the unreacted 3,4-difluorobenzotrifluoride is recovered. As a result, the desired product, 2-fluoro-4-(trifluoromethyl) acetoanilide is also obtained as a residue. The desired product 2-fluoro-4-(trifluoromethyl) acetanilide can be converted, upon hydrolysis (deacetylation), to 4-amino-3-fluorobenzotrifluoride, which in turn is converted to benzoylurea insecticides, as described, for instance, in EP-A-0246061. The conversion of 2-fluoro-4-(trifluoromethyl)acetanilide to 4-amino-3-fluorobenzotrifluoride by hydrolysis is also described in detail in Reference Example 1 to be set forth later. The starting material for carrying out the process of the invention, namely 3,4-difluorobenzotrifluoride, can be prepared, for instance, by the method described in U.S. Patent No. 4937396. The following working examples and reference example are further illustrative of the present invention but are by no means limitative of the scope thereof. Example 1 A reactor was charged with 13.6 g (0.231 mole) of acetamide, 9.23 g of sodium hydride (60% w/w dispersion in mineral oil, 0.23 mole) and 200 ml of dimethylformamide, and the mixture was heated to 60°C with stirring. At that temperature, a solution of 20 g (0.11 mole) of 3,4-difluorobenzotrifluoride in 20 ml of dimethylformamide was added dropwise gradually to the reactor contents. After completion of the dropwise addition, the reactor contents were heated to 100°C and further stirred for an hour. The reaction mixture was cooled to room temperature (about 20°C) and then poured slowly into 5% hydrochloric acid, and the resultant mixture was extracted with two 300-ml portions of ethyl acetate. The ethyl acetate layers were combined, washed with water, dried over anhydrous sodium sulfate and concentrated to give a crude product. This crude product was subjected to silica gel column chromatography (eluent: n-hexane/ethyl acetate = 1/1) to give 18.7 g of 2-fluoro-4-(trifluoromethyl) acetanilide. Yield 77%. Melting point 135.6°C. Example 2 A reactor was charged with 0.32 g (5.42 mmoles) of acetamide, 0.22 g of sodium hydride (60% w/w disperision in mineral oil, 5.5 mmoles), 0.5 g (2.75 mmoles) of 3,4-difluorobenzotrifluoride and 10 ml of dimethyl sulfoxide, and the mixture was heated to 60°C with gentle stirring. Then, after stirring at 60-65°C for 30 minutes, the reaction mixture was cooled to room temperature (about 20°C) and slowly poured into 5% hydrochloric acid. The resultant mixture was extracted with two 200-ml portions of ethyl acetate. The ethyl acetate layers were combined, washed with water, dried over anhydrous magnesium sulfate and concentrated to give a crude product. This crude product was subjected to silica gel column chromatography (eluent: n-hexane/ethyl acetate = 1/1) to give 0.45 g of 2-fluoro-4-(trifluoromethyl) acetanilide. Yield 95%. Melting point 135.4°C. Reference Example 1 A reactor was charged with 10.0 g of 2-fluoro-4-(trifluoromethyl) acetanilide, 50 ml of 20% aqueous sulfuric acid and 50 ml of methyl alcohol, and the mixture was stirred under reflux for 4 hours. The reaction mixture was cooled to room temperature (about 20°C) and then made weakly alkaline by slowly adding a 5% aqueous solution of sodium hydrogen carbonate. The resultant solution was then extracted with two 200-ml portions of diethyl ether. The diethyl ether layers were combined, washed with water, dried over anhydrous magnesium sulfate and concentrated to give a crude product. This crude product was subjected to silica gel column chromatography (eluent: n-hexane/ethyl acetate = 4/1) to give 7.29 g of 4-amino-3-fluorobenzotrifluoride. As a process for producing 2-fluoro-4-(trifluoromethyl)acetanilide, the process of the invention is advantageous over the prior art methods from the industrial standpoint since the desired product can be obtained with high selectivity and high yield by reacting 3,4-difluorobenzotrifluoride with acetamide which is inexpensive.

Claims: A process for producing 2-fluoro-4-(trifluoromethyl) acetanilide which comprises reacting 3,4-difluorobenzotrifluoride with acetamide in the presence of a base in an aprotic polar solvent or in a mixture of an aprotic polar solvent and an aprotic non-polar solvent. A process as claimed in claim 1 wherein the base is a non-nucleophilic strong base. A process as claimed in claim 2, wherein the base is an alkali metal hydride or an alkali metal carbonate. A process as claimed in claim 3, wherein the base is an alkali metal hydride. A process as claimed in claim 4 wherein the base is sodium hydride. A process as claimed in any one of claims 1 to 4 conducted in at least one aprotic polar solvent selected from dimethylformamide, dimethyl sulphoxide, hexamethylphosphoric triamide, sulpholane, N-methylpyrrolidone, 1,3-dimethyl-2-imidazolidinone, 1,3-dimethyl-3,4,5,6-tetrahydro-2-(1H)-pyrimidone, acetonitrile, tetrahydrofuran and dioxane. A process as claimed in claim 6 wherein the aprotic polar solvent is dimethylformamide or dimethyl sulphoxide. A process as claimed in claim 7 wherein the aprotic polar solvent is dimethyl sulphoxide. A process as claimed in any one of claims 1 to 8 wherein acetamide and the base are each used in an amount of 1 to 10 moles per mole of 3,4-difluorobenzotrifluoride. A process as claimed in any one of claims 1 to 9 wherein the reaction is carried out at a temperature of 40 to 100°C.

Inventors: MATSUO NORITADA, SAKAMOTO NORIYASU, TAKI TOSHIAKI, MATSUO, NORITADA, SAKAMOTO, NORIYASU, TAKI, TOSHIAKI
Applicants: SUMITOMO CHEMICAL CO, SUMITOMO CHEMICAL COMPANY, LIMITED
Application year: 1992
Main classification: C07C231
IPC codes: C07C231