Preparation of thioamides

Abstract: A process for preparing an aliphatic thioamide comprises reacting a nitrile compound of the general formula R₁R₂R₃C-CN, wherein R₁ denotes a hydrogen atom, an alkyl radical containing from 1 to 5 carbon atoms or an aryl radical and R₂ and R₃ each denotes a hydrogen atom or an alkyl radical containing from 1 to 5 carbon atoms, with hydrogen sulphide, in the presence as catalyst of an aliphatic amine of the general formula R₄R₅R₆N, wherein R₄ denotes an alkyl radical containing 1 to 5 carbon atoms and R₅ and R₆ each denotes a hydrogen atom or an alkyl radical containing 1 to 5 carbon atoms, in a water-miscible polar solvent.

Description: The present invention is concerned with the preparation of thioamides, that is amides in which the oxygen atom is notionally replaced by a sulphur atom. Thioamides, and in particular aliphatic thioamides, are of value as intermediates in the preparation of various products having a wide range of applications. By way of example, thioamides are useful in the preparation of thiazoles, many of which find application as pharmaceuticals. For these reasons, many different processes have been proposed for the preparation of thioamides. The most widely practised process for this purpose entails reacting the corresponding amide with a suitable thiation agent, such as phosphorus pentasulphide or an aromatic derivative thereof known as Lawesson's Reagent. However phosphorus pentasulphide is a very difficult reagent to handle and the effluent obtained in the reaction is expensive to treat and dispose of. Lawesson's reagent is very expensive and also gives an effluent which entails disposal problems. With a view to avoiding these foregoing difficulties, an alternative process has been proposed involving reacting a nitrile with hydrogen sulphide, to form the desired thioamide by direct addition of the hydrogen sulphide across the cyanide group. 'The reaction may be catalysed by amines. However, while this addition reaction gives good yields when applied to aromatic nitriles, aliphatic nitriles undergo reaction very slowly and give poor yields unless the reaction is carried out at elevated temperatures and pressures. See, for example, US-A-3274243, which proposes to improve the reaction rate of alkanoic nitriles by including a strongly basic amine in the reaction mixture and carrying out the reaction at temperatures up to reflux temperatures. Against this background, it is an object of the present invention to provide a process for converting aliphatic nitriles to thioamides, by which improved reaction rates and/or improved yields of the desired product may be obtained even at ambient temperatures. The process according to the present invention, for the preparation of aliphatic thioamides, comprises reacting a nitrile compound of the general formula R 1 R 2 R 3 C -CN wherein the symbol R 1 denotes a hydrogen atom, an alkyl radical containing from 1 to 5 carbon atoms or an aryl radical and the symbols R 2 and R 3 each denotes a hydrogen atom or an alkyl radical containing from 1 to 5 carbon atoms, with hydrogen sulphide, in the presence of an aliphatic amine of the general formula R 4 R 5 R 6 N wherein the symbol R 4 denotes an alkyl radical containing from 1 to 5 carbon atoms and the symbols R 5 and R 6 each denotes a hydrogen atom, in a water-miscible polar solvent. The nitrile compound which is reacted in the process according to the invention is an aliphatic nitrile of the formula R 1 R 2 R 3 C-CN, wherein the symbols R 1 , R 2 and R 3 have the meanings given above. The alkyl groups may have straight or branched chains. Typical nitriles to which the reaction may be applied include acetonitrile, propionitrile, n- and isobutyronitrile and phenylacetonitrile and homologues of these foregoing compounds within the specified limits. Reaction of isobutyronitrile to yield thio-isobutyramide is of particular interest. The reaction is catalysed by an aliphatic amine of the formula R 4 R 5 R 6 N, wherein the symbols R 4 , R 5 and R 6 have meanings given above. By way of example, the catalyst may be methylamine, ethylamine or n- or isopropylamine. Of these, isopropylamine is particularly preferred. The quantity of the catalyst used is not critical but typically will be in the range of 10 to 100 mole per cent in relation to the quantity of the nitrile. The preferred amount is in the range from 20 to 40 mole per cent. The reaction is carried out in a water-miscible polar solvent, preferably an aprotic polar solvent, and such solvents are important in achieving acceptably high reaction rates. Suitable solvents for this purpose include dimethylacetamide, sulpholane, N-methylpyrrolidinone,1,3-dimethylimidazolidinone and dimethyl sulphoxide. The particularly preferred solvent is dimethylformamide. The quantity of solvent is preferably in the range from 100 to 500g per mole of the nitrile, more preferably in the range from 120 to 300g per mole of the nitrile. The molar quantity of hydrogen sulphide preferably exceeds that of the nitrile and more preferably amounts to 110 to 300 mole per cent of the quantity of the nitrile. Typically, it amounts to 160 to 250 mole per cent based on the nitrile. The process according to the invention may be carried out under ambient conditions of temperature and pressure and makes possible good yields of the desired thioamide. However the reaction may, if desired, be accelerated and the yield enhanced by heating the reaction mixture to a temperature a little above the ambient temperature, for example to a temperature lying in the range from 30°C to 50°C, preferably from 30°C to 40°C. The thioamide produced by the process may readily be separated from the reaction mixture by quenching with water and solvent extraction, for example using a solvent such as dichloromethane. The invention will be further described and illustrated by means of the following examples. Example 1 To a stirred flask fitted with a condenser attached to a caustic scrubber were charged isobutyronitrile (100g), isopropylamine (30g), and dimethylformamide (400 ml). Hydrogen sulphide gas was charged to the vessel over a period of 24 hours and the reaction mixture stirred until the consumption of the nitrile became very slow. The reaction mixture was quenched into water (900 ml) and extracted into dichloromethane (3 x 250 ml). The combined organic phases were dried with magnesium sulphate and then concentrated on a rotary evaporator, thereby yielding an oil which, apart from residual solvent, was essentially pure thioisobutyramide (127g, 85 per cent yield). Example 2 A solution of isobutyronitrile (80g) and isopropylamine (27.0g) in dimethyl sulphoxide (125 ml) in a stirred reaction vessel fitted with a condenser was cooled to 0-5°C and connected to a caustic scrubber. A total of 85g of hydrogen sulphide gas was added over 6 hours and the reaction mixture stirred until the reaction became very slow. Quenching into water (500 ml), extraction into dichloromethane (3 x 250 ml), followed by a small water backwash, yielded, on concentration, an oil which apart from residual solvent was essentially pure thioisobutyramide (yield 85g, 71%). Example 3 Isopropylamine (54g), propionitrile (128g) and dimethylformamide (300 ml) were charged to a stirred reaction vessel fitted with a condenser attached to a caustic scrubber. The mixture was cooled to 0-5°C and hydrogen sulphide gas charged over 24 hours, during which time the termperature was slowly allowed to rise to ambient temperature. After standing for a further 12 hours, the solution was concentrated under vacuum to 75% of its original volume,quenched into water (1600 ml) and then extracted with dichloromethane (3 x 250 ml). The combined organic phases were dried with magnesium sulphate and concentrated on a rotary evaporator to an oil which apart from residual solvent was essentially pure thiopropionamide (145g, 70% yield). Examples 4 to 9 Using the reaction methods and separation techniques described in Examples 1 to 3, the nitriles set forth in the following table were reacted with hydrogen sulphide gas in the solvents shown, in the presence of the catalysts specified in the table. The yields of the corresponding thioamides are shown.

Claims: A process for the preparation of an aliphatic thioamide, characterised in that it comprises reacting a nitrile compound of the general formula R 1 R 2 R 3 C-CN, wherein the symbol R 1 denotes a hydrogen atom, an alkyl radical containing from 1 to 5 carbon atoms or an aryl radical and the symbols R 2 and R 3 each denotes a hydrogen atom or an alkyl radical containing from 1 to 5 carbon atoms, with hydrogen sulphide, in the presence of an aliphatic amine of the general formula R 4 R 5 R 6 N, wherein the symbol R 4 denotes an alkyl radical containing from 1 to 5 carbon atoms and the symbols R 5 and R 6 each denotes a hydrogen atom, in a water-miscible polar solvent. A process according to Claim 1, characterised in that the nitrile compound is acetonitrile, propionitrile, n- or isobutyronitrile or phenylacetonitrile. A process according to Claim 1 or Claim 2, characterised in that the aliphatic amine is methylamine, ethylamine, n-propylamine or isopropylamine. A process according to any of the preceding claims, characterised in that the water-miscible polar solvent is dimethylformamide, dimethylacetamide, sulpholane, N-methylpyrrolidinone, 1,3-dimethylimazolidinone, or dimethyl sulphoxide. A process for the preparation of thioisobutyramide characterised in that it comprises reacting isobutyronitrile with hydogen sulphide in the presence of isopropylamine, in solution in dimethylformamide. A process according to any of the preceding claims, characterised in that the quantity of the aliphatic amine lies within the range of 10 to 100 mole per cent, based on the quantity of the nitrile compound. A process according to any of the preceding claims, characterised in that the quantity of hydrogen suphide lies within the range of 110 to 300 mole per cent, based on the quantity of the nitrile compound. A process according to any of the preceding claims, characterised in that the quantity of solvent lies within the range from 100 to 500g per mole of the nitrile. A process according to any of the preceding claims, characterised in that the reaction is carried out at a temperature lying in the range from 30°C to 50°C.

Inventors: HEYES GRAHAM, HOLMES DAVID, JACKSON ARTHUR, MORGAN CRAIG, HEYES, GRAHAM, HOLMES, DAVID, JACKSON, ARTHUR, MORGAN, CRAIG
Applicants: FINE ORGANICS LTD, FINE ORGANICS LIMITED
Application year: 1995
Main classification: C07C327
IPC codes: C07B61, C07C327, B01J31