Process for producing N-alkylimidazole

Abstract: Disclosed is a process for producing an N-alkylimidazole which comprises reacting an imidazole with an N-alkylating agent in an organic solvent in the presence of alkali particles having a specific surface area of 0.6 m 2 /g or larger.

Description: FIELD OF THE INVENTION The present invention relates to a process for industrially advantageously producing an N-alkylimidazole from an imidazole. BACKGROUND OF THE INVENTION N-Alkylimidazoles such as, e.g., 2-alkyl-4-halo-1-(4-halobenzyl)-5-formylimidazoles are useful as raw materials for medicines such as diuretics and hypotensive drugs. In J. Org. Chem., 59 , 6391-6394 (1994) is disclosed a method in which 2-n-butyl-4-chloro-5-formylimidazole is reacted with 4-bromobenzyl bromide together with powdery potassium carbonate at -10°C in N,N-dimethylacetamide to benzylate the imidazole. However, powdery potassium carbonate has drawbacks in that it is apt to fly off during handling and is highly hygroscopic, although the yield of the target compound in the above method is as high as 93%. Hence, the above method is not always advantageous when practiced on an industrial scale. JP-A-56-140972 discloses a process for producing alkylimidazoles comprising reacting imidazoles with an alkyl halide in acetone in the presence of potassium hydroxide particles or sodium hydroxide particles. SUMMARY OF THE INVENTION An object of the present invention is to provide an industrial process for the production of N-alkylimidazoles, in which an easily handleable chemical is used to smoothly conduct a reaction and to obtain the target compound in a high yield. The present inventors made intensive investigations on alkali particles with respect to their particle diameters and specific surface areas based on the finding that the shape, properties, etc. of alkali particles greatly influence the yield of an N-alkylimidazole. As a result, it has been found that when a reaction is conducted using a commercial particulate alkali, e.g., particulate potassium carbonate, the reaction comes not to proceed any more at the time when the yield has reached about 40 to 50%, and that the specific surface area of the powdery potassium carbonate mentioned above is about 0.5 m 2 /g at the most. It has been thus found that modifications or variations in the above point influence the yield of a target compound. The present invention provides a process for producing an N-alkylimidazole which comprises reacting a 2-alkyl-4-halo-5-formylimidazole with a benzyl halide in an organic solvent in the presence of alkali particles having a specific surface area of 0.6 m 2 /g or larger, the alkali particles being potassium carbonate particles, sodium carbonate particles, or potassium nitrate particles. According to a preferred embodiment of the invention, in the alkali particles, the content of particles each having a diameter of 74 µm or smaller is not higher than 50% by weight. DETAILED DESCRIPTION OF THE INVENTION The present invention will be explained below in detail. The imidazole as a starting material is a 2-alkyl-4-halo-5-formylimidazole. Preferred examples of alkyl include alkyl groups having 2 to 10 carbon atoms, among which n-butyl is especially important. Preferred examples of halo include chlorine and bromine, among which chlorine is especially preferred. Examples of the organic solvent include nonhalogenated solvents such as N,N-dimethylacetamide, N,N-dimethylformamide, hexamethylphosphoramide, acetonitrile, ethyl acetate, acetone, and methyl ethyl ketone and halogenated solvents such as ethane dichloride and chloroform. However, nonhalogenated solvents are preferably used. More preferred is N,N-dimethylacetamide. Specific examples of benzyl halides include benzyl halides, o-halobenzyl halides, m-halobenzyl halides, p-halobenzyl halides, o-alkylbenzyl halides, m-alkylbenzyl halides, p-alkylbenzyl halides, o-alkoxycarbonylbenzyl halides, p-alkoxycarbonylbenzyl halides, m-alkoxycarbonylbenzyl halides, o-arylbenzyl halides, m-arylbenzyl halides, p-arylbenzyl halides, o-cyanobenzyl halides, m-cyanobenzyl halides, p-cyanobenzyl halides, o-halomethylbenzoic acids, m-halomethylbenzoic acids, and p-halomethylbenzoic acids. These halides are preferably bromides, chlorides, or iodides. The most characteristic feature of the present invention resides in that the reaction of the imidazole with the benzyl halide in an organic solvent is conducted in the presence of specific alkali particles having a specific surface area of 0.6 m 2 /g or larger. The alkali particles are particles of potassium carbonate, sodium carbonate, and potassium nitrate. However, potassium carbonate particles or sodium carbonate particles are preferably used. The preferred range of the specific surface area of the alkali particles is from 0.9 to 1.9 m 2 /g. The specific surface area was measured by the BET method. The alkali particles are not particularly limited in particle diameter. However, it is preferred to use alkali particles in which the proportion of fine particles is low, because such alkali particles are easy to handle. Specifically, the content of particles each having a size of 74 µm or smaller (particles passing through a standard 200-mesh sieve) is preferably 50% by weight or lower, more preferably 30% by weight or lower. Alkali particles in which the content of 74-µm and finer particles exceeds 50% by weight are undesirable in that they are apt to fly off during handling and are highly hygroscopic. Alkali particles having a surface area within the range specified above can be obtained, for example, by a method comprising melting ordinary alkali particles and drying the melt while foaming the same to obtain porous particles. Although the imidazole and the benzyl halide are used basically in an equimolar proportion, the reaction itself proceeds even when the latter reactant is used in excess. Consequently, the industrially acceptable range of the amount of the latter (benzyl halide) is from 0.8 to 5 mol, especially from 0.9 to 1.5 mol, per mol of the former (imidazole). The use amount of alkali particles is generally from 1 to 10 mol, preferably from 1.01 to 2 mol, per mol of the imidazole. The use amount of the organic solvent is suitably determined as long as the system can be stirred smoothly. In general, however, the use amount of the organic solvent is from 1 to 200 parts by weight, especially from 5 to 50 parts by weight, per part by weight of the sum of the imidazole, alkali particles, and benzyl halide. Methods for introducing these ingredients into a reactor are not particularly limited. In general, however, the imidazole and the benzyl halide are dissolved in the organic solvent in an inert gas atmosphere or air atmosphere, and alkali particles are then introduced into the solution in a period of from 5 minutes to 5 hours. The reactants are reacted for further 1 to 8 hours at -20 to 50°C. For isolating the target compound from the reaction mixture after the reaction, various techniques commonly used by persons skilled in the art can be employed. Examples thereof include a method comprising adding water to the reaction mixture and recovering the resultant crystals, and a method comprising concentrating the reaction mixture, adding water and an appropriate organic solvent to the concentrated reaction mixture to cause phase separation, separating the resultant organic layer therefrom, and washing the same with water. EXAMPLES The present invention will be explained below in more detail by reference to Examples. EXAMPLE 1 Production of 2-n-butyl-4-chloro-1-(4-bromobenzyl)-5 formylimidazole This Example is represented by the following reaction scheme. In 200 ml of N,N-dimethylacetamide (DMAC) were dissolved 31.0 g (0.166 mol) of 2-n-butyl-4-chloro-5-formylimidazole and 41.5 g (0.166 mol) of p-bromobenzyl bromide. After this solution was cooled to -10°C, 23.7 g (0.168 mol) of potassium carbonate particles which had a specific surface area of 1.5 m 2 /g and in which the content of particles each having a diameter of 74 µm or smaller was 30% by weight were added to the solution over 10 minutes while holding the solution at -10 to -5°C. The resultant mixture was stirred at -10°C for 2 hours, subsequently heated to room temperature, and then stirred for 2 hours to complete the reaction (which was conducted in an air atmosphere). Thereafter, the reaction mixture was filtered and the filtrate was cooled to 0°C. Thereto was added 320 ml of 15°C water. The crystals thus precipitated were taken out by filtration to obtain 55.8 g of 2-n-butyl-4-chloro-1-(4-bromobenzyl)-5-formylimidazole having a purity of 99.8% (yield, 98.0%). EXAMPLE 2 The same procedure as in Example 1 was conducted, except that in place of the potassium carbonate particles used in Example 1, use was made of the same amount of potassium carbonate particles which had a specific surface area of 1.5 m 2 /g and in which the content of particles each having a diameter of 74 µm or smaller was 40% by weight. As a result, 55.8 g of 2-n-butyl-4-chloro-1-(4-bromobenzyl)-5-formylimidazole having a purity of 99.8% was obtained (yield, 98.0%). EXAMPLE 3 The same procedure as in Example 1 was conducted, except that in place of the potassium carbonate particles used in Example 1, use was made of the same amount of potassium carbonate particles which had a specific surface area of 1.5 m 2 /g and in which the content of particles each having a diameter of 74 µm or smaller was 60% by weight. As a result, 54.1 g of 2-n-butyl-4-chloro-1-(4-bromobenzyl)-5-formylimidazole having a purity of 99.8% was obtained (yield, 95.0%). EXAMPLE 4 The same procedure as in Example 1 was conducted, except that in place of the potassium carbonate particles used in Example 1, use was made of the same molar amount of sodium carbonate particles which had a specific surface area of 1.5 m 2 /g and in which the content of particles each having a diameter of 74 µm or smaller was 30% by weight. As a result, 55.8 g of 2-n-butyl-4-chloro-1-(4-bromobenzyl)-5-formylimidazole having a purity of 99.8% was obtained (yield, 98.0%). EXAMPLE 5 The same procedure as in Example 1 was conducted, except that in place of the potassium carbonate particles used in Example 1, use was made of the same molar amount of potassium nitrate particles which had a specific surface area of 1.5 m 2 /g and in which the content of particles each having a diameter of 74 µm or smaller was 30% by weight. As a result, 54.1 g of 2-n-butyl-4-chloro-1-(4-bromobenzyl)-5-formylimidazole having a purity of 99.8% was obtained (yield, 95.0%). COMPARATIVE EXAMPLE 1 The same procedure as in Example 1 was conducted, except that in place of the potassium carbonate particles used in Example 1, use was made of the same amount of potassium carbonate particles which had a specific surface area of 0.56 m 2 /g and in which the content of particles each having a diameter of 74 µm or smaller was 60% by weight. The potassium carbonate particles showed poor handleability because the particles caused dusting during the feeding thereof. As a result, 52.6 g of 2-n-butyl-4-chloro-1- (4-bromobenzyl) -5-formylimidazole having a purity of 99.8% was obtained (yield, 92.5%). COMPARATIVE EXAMPLE 2 The same procedure as in Example 1 was conducted, except that in place of the potassium carbonate used in Example 1, use was made of the same amount of potassium carbonate particles which had a specific surface area of 0.22 m 2 /g and in which the content of particles each having a diameter of 74 µm or smaller was 30% by weight. As a result, 26.7 g of 2-n-butyl-4-chloro-1-(4-bromobenzyl)-5-formylimidazole having a purity of 99.8% was obtained (yield, 47.0%).

Claims: A process for producing an N-alkylimidazole which comprises reacting a 2-alkyl-4-halo-5-formylimidazole with a benzyl halide in an organic solvent in the presence of alkali particles having a specific surface area of 0.6 m 2 /g or larger, the alkali particles being potassium carbonate particles, sodium carbonate particles, or potassium nitrate particles. The process of claim 1, wherein in the alkali particles, the content of particles each having a diameter of 74 µm or smaller is not higher than 50% by weight.

Inventors: HIRATA KAZUMASA, KAWATA NARITOSHI, HIRATA, KAZUMASA, KAWATA, NARITOSHI, Hirata, Kazumasa The Nippon Syn.Chem.Ind.Co.,Ltd., Kawata, Naritoshi The Nippon Syn.Chem.Ind.Co.,Ltd.
Applicants: NIPPON SYNTHETIC CHEM IND, THE NIPPON SYNTHETIC CHEMICAL INDUSTRY CO., LTD.
Application year: 1998
Main classification: C07D233
IPC codes: C07D233