HK1034064B - Process for the production of formylimidazoles - Google Patents

Description

This invention concerns a new procedure for producing formyl imidazoles of the general formula in which R¹ is C_1-6alkyl, by catalytic oxidation of hydroxy methyl imidazoles of the general formula in which R¹ has the meaning given above.

Formyl imidazoles are important intermediate products, for example, for the production of pharmaceutical substances such as diuretics or antihypertensives ( WO-A 92/20651 ). Several procedures have previously been known for producing formyl imidazoles. In CH-A 685496 , a procedure is described in which the catalytic oxidation of hydroxy methyl imidazoles to formyl imidazoles is performed in the presence of noble metal catalysts such as platinum bismuth, platinum black, platinum or palladium on activated charcoal with oxygen insufflation.

The task of the invention was therefore to make available an economical, improved procedure for producing formyl imidazoles.

In this invention, this task is solved by the procedure defined in Claim 1. Accordingly, the present invention provides a process for producing formyl imidazoles of the formula (I): in which R¹ is C_1-6 alkyl, which comprises catalytic oxidation of hydroxymethyl imidazoles of the general formula (II): in which R¹ is as defined above, in the presence of a noble metal catalyst selected from a platinum/bismuth catalyst or a platinum/lead catalyst, wherein that the catalytic oxidation takes place in the presence of a peroxide selected from hydrogen peroxide and in presence of water, a water-miscible solvent or mixtures thereof, in an alkaline medium, wherein the alkaline medium is obtained by adding an alkali hydroxide, an alkali carbonate or an alkali acetate to the reaction mixture; and wherein the reaction is performed at a temperature of 20° to 120°C.

R¹ is a straight-chained or ramified alkyl group with 1 to 6 C atoms. Specifically, this may be methyl, ethyl, propyl, isopropyl, butyl, isobutyl, tert-butyl, pentyl and its isomers as well as hexyl and its isomers. The preferred meaning R¹ is butyl.

Hydroxy methyl imidazoles can be readily produced as starting compounds as specified, for example, in WO-A 92/20651 or in E.F. Godefroi et al., Trav. Chim. Receuil Pays-Bas, 91, 1383 (1972).

The noble metal catalyst is used by itself or bound to a vehicle such as, for example, activated charcoal, silicon dioxide, aluminum dioxide, silicon-aluminum dioxide, zirconium oxide or titanium oxide. It is preferably bound to activated charcoal.

Noble metal catalysts bound to activated charcoal can be commercially obtained, for example, from Degussa.

The appropriate percentage of the noble metal bound to a vehicle is between 0.1 and 15% by weight, and preferably between 0.5 and 7% by weight, relative to the vehicle material.

The noble metal catalyst is preferably used in an amount of 0.05 to 1.0 mol % noble metal base relative to hydroxy methyl imidazole, and an amount of 0.1 to 0.4 mol % noble metal base relative to hydroxy methyl imidazole is especially preferred. Hydrogen peroxide used in a 10% to 30% aqueous solution is particularly suitable.

The catalytic oxidation takes place appropriately in the presence of water, a water-miscible solvent or mixtures thereof, in an alkaline milieu.

Particularly suitable water-miscible solvents are, for example, alcohols or carboxylic acids with 1 to 6 C atoms or ketones such as, for example, acetone or methyl ethyl ketone.

Mixtures of water and water-miscible solvents are preferably used. It has proven to be advantageous if the water used is adjusted to be alkaline, by the appropriate addition of an alkali hydroxide, an alkali carbonate or an alkali acetate. Alkali hydroxide is preferably used in the ratio 1: 0.05 to 5, and preferably 1: 1 to 3, relative to the mol amount used of the hydroxy methyl imidazole of general formula II.

The catalytic oxidation is appropriately performed at a temperature of 20° to 120°C, preferably at 50° - 80°C.

After the standard peroxide dosing time of 2 -3 hours, the compound of general formula I can be isolated in the standard manner after a sufficient secondary reaction time.

The product is isolated by appropriate crystallization and filtration. The catalyst used can be used several times with no loss of activity.

Examples Example 1 Production of 4-[(2-butyl-5-formyl- 1H-imidazo-1-yl)methyl]benzoic acid

9.5 g (33 mmol) 4-[(2-butyl-5-hydroxymethyl-1H-imidazo-1-yl)methyl]benzoic acid, 40 ml water, 10 ml methanol, 4.2 g (105 mmol) NaOH and 0.92 g 5% platinum and 5% bismuth on activated charcoal (containing 60% water) are placed in a 100-ml flask at room temperature and heated to 60°C. 6.6 g (39 mmol) 20% aqueous H₂O₂ solution were added to this suspension at 60°C over 60 minutes and the mixture was then converted with HPLC. 6.6 g (39 mmol) 20% aqueous H₂O₂ solution were again added over 60 minutes. 1.7 g (10 mmol) 20% aqueous H₂O₂ solution were then added over 20 minutes (conversion > 90%). The mixture was cooled to room temperature. After acidification to pH 6.0 with 17.6 ml HCl (15%), the product was preciptated. It was cooled to 2°C, filtered, washed with 2 x 20 ml water, and dried at room temperature at 15 mbar. 7.2 g (70%) of yellow 4-[(2-butyl-5-formyl-1H-imidazo-1-yl)methyl]benzoic acid (HPLC content 95%) were obtained. Melting point: 144 - 146°C.

12.9 (1H, s);

9.65 (1H, s);

7.94 (1H, s);

7.90 (2H, d);

7.11 (2H, d);

5.65 (2H, s);

2.63 (2H, t);

1.54 (2H, pent);

1.36 (2H, hex);

0.79 (3 H, t).

Claims (2)

1. A process for producing formyl imidazoles of the formula (I): in which R¹ is C_1-6 alkyl, which comprises catalytic oxidation of hydroxymethyl imidazoles of the general formula (II): in which R¹ is as defined above, in the presence of a noble metal catalyst selected from a platinum/bismuth catalyst or a platinum/lead catalyst, wherein that the catalytic oxidation takes place in the presence of a peroxide selected from hydrogen peroxide and in presence of water, a water-miscible solvent or mixtures thereof, in an alkaline medium, wherein the alkaline medium is obtained by adding an alkali hydroxide, an alkali carbonate or an alkali acetate to the reaction mixture; and wherein the reaction is performed at a temperature of 20° to 120°C.
2. Process as in Claim 1, wherein R¹ is butyl.