Process for producing amide by liquid phase rearrangement of oxime

Abstract: A process for producing an amide which comprises subjecting an oxime to liquid phase rearrangement in the presence of phosphorus pentoxide and at least one compound selected from the group consisting of N,N-dialkyl amides, N-alkyl cyclic amides and dialkyl sulfoxides and optionally a fluorine-containing strong said or its derivative. Said process can rearrange an oxime to a corresponding amide in a good yield under mild reaction conditions in the presence of a less stoichiometric amount of a catalyst.

Description: This invention relates to a process for producing an amide by liquid phase rearrangement of an oxime. Rearrangement of an oxime to an amide is known as Beckmann rearrangement. For example, in the production of ε-caprolactam by rearrangement of cyclohexanone oxime, fuming sulfuric acid is used as a catalyst in industry. However, in processes using fuming sulfuric acid, there is an essential problem that a large amount of ammonium sulfate is produced as a by-product, and there are many other problems such as corrosion of apparatus and the like. Thus, there has been desired a development of an efficient catalyst for the rearrangement. For example, a solid oxide catalyst in which boron oxide is supported on silica, alumina or titania and a zeolite catalyst have been proposed. However, when these solid catalysts are used in the rearrangement, it is necessary to adopt gas phase reaction at high temperatures, so that the reaction is accompanied by reduction of ε-caprolactam yield, deterioration of catalyst and an increase of energy cost. Thus, the use of the solid catalysts has a problem in commercial production. Some processes for producing ε-caprolactam by rearranging cyclohexanone oxime under such relatively mild reaction conditions that liquid phase reaction is effected are known. One of the processes uses as a catalyst an ion pair obtained by reacting N,N-dimethylformamide with chlorosulfonic acid (namely, Bilsmeyer complex) [see M.A. Kira and Y.M. Shaker, Egypt. J. Chem., 16 , 551 (1973)]. It is stated, however, that in this process, the lactam produced and the catalyst form a 1 : 1 complex, so that it is necessary to use the catalyst in an amount equimolar to the oxime. For this reason, said process cannot be said to be economical. One of the present inventors previously reported liquid phase Beckmann rearrangement using a catalyst consisting of an N,N-dialkylformamide and an alkylating agent obtained from an epoxy compound and a strong acid (boron trifluoride-etherate or the like) [see Y. Izumi, Chemistry Letters, pp. 2171 et seq. (1990)]. This process is a novel, excellent rearrangement process; however, it is not always satisfactory in respect of economy and workability in its commercial application because an epoxy compound and a strong acid are required for forming an alkylating agent which is one of the rearrangement catalyst components. Japanese Patent Application Kokai No. 62-149665 discloses a process for producing ε-caprolactam by rearranging cyclohexanone oxime with a phosphoric acid catalyst in a heptane solvent. In this process, however, the phosphoric acid is required to be used as a catalyst in an amount as large as about 2 moles per mole of the oxime. Hence, said Japanese publication describes that the reaction mixture is neutralized with ammonia after the reaction and the phosphoric acid catalyst is recovered through complex steps and then reused. The present inventors have made extensive research on catalysts for rearranging oximes to corresponding amides and consequently found that the oxime rearrangement is remarkably accelerated by effecting the reaction in the presence of phosphorus pentoxide and at least one compound selected from the group consisting of N,N-dialkyl amides, N-alkyl cyclic amides and dialkyl sulfoxides and optionally a fluorine-containing strong acid or its derivative. An object of this invention is to provide a process for producing an amide free from the above-mentioned problems. Another object of this invention is to provide a process for producing an amide by rearranging an oxime in a liquid phase at a mild reaction temperature in the presence of a catalyst in a less than stoichiometric amount. Other objects and advantages of this invention will become apparent from the following description. According to this invention, there is provided a process for producing an amide which comprises subjecting an oxime to liquid phase rearrangement in the presence of phosphorus pentoxide and at least one compound selected from N,N-dialkyl amides, N-alkyl cyclic amides and dialkyl sulfoxides, with the exception of a process which comprises combining 30 cm³ of N,N-dimethylformamide, 21.4 mmoles of propylene oxide and 10.0 mmoles of phosphorus pentoxide; reacting the resulting mixture at 50°C for 1 hour to form a reaction accelerator; adding to the reaction accelerator 61cm³ of N,N-dimethylformamide and 70.7 mmoles of cyclohexanone oxime; and subjecting the resulting mixture to reaction at 66°C for 2 hours to form ε-caprolactam. The N,N-dialkyl amides to be used in this invention are formamides having two same or different alkyl groups having 1 to 6 carbon atoms on its nitrogen atom or C₁₋₆ carboxylic acid amides having two same or different alkyl groups having 1 to 6 carbon atoms on its nitrogen atom. Specific examples thereof include N,N-dimethylformamide, N,N-diethylformamide, N,N-diisopropylformamide, N,N-dibutylformamide, N,N-dihexylformamide, N,N-dimethylacetamide, N,N-diethylacetamide, N,N-diisopropylacetamide, N,N-dimethylpropionamide, N,N-dimethylbutyramide, N,N-dimethylcapronamide and the like. The N-alkyl cyclic amides to be used in this invention are cyclic amides having 4 to 6 carbon atoms having an alkyl group having 1 to 6 carbon atoms on its nitrogen atom, and specific examples thereof include N-methylpyrrolidone, N-methylpiperidone and the like. The dialkyl sulfoxides to be used in this invention are sulfoxides having two same or different alkyl groups having 1 to 6 carbon atoms, and specific examples thereof include dimethyl sulfoxide, diethyl sulfoxide, dipropyl sulfoxide, dihexyl sulfoxide and the like. The rearrangement reaction activity in this invention is inhibited by water, and therefore, the above-mentioned compounds are previously dried and then used. The fluorine-containing strong acid or its derivative includes trifluorosulfonic acids and their derivatives such as trifluoromethanesulfonic acid, trifluoromethanesulfonic acid anhydride, ethyl trifluoromethanesulfonate, trimethylsilyl trifluoromethanesulfonate, tin trifluoromethanesulfonate and the like; trifluoroacetic acid; trifluoroacetic acid anhydride; boron trifluoride; boron trifluoride-ether complex; antimony pentafluoride; and the like. The amount of the phosphorus pentoxide used is not critical; however, it is preferably about 0.1 to 50 mole %, more preferably 1 to 20 mole %, based on the molar amount of the oxime. The amount of the fluorine-containing strong acid or its derivative used is preferably 0.01 to 50, more preferably 0.1 to 10 moles per mole of the phosphorus pentoxide. In this invention, the catalyst has its activity even in the absence of the fluorine-containing strong acid or its derivative; however, when the fluorine-containing strong acid or its derivative is used together with the other catalyst components, the catalyst activity can be remarkably enhanced. On the other hand, when the fluorine-containing strong acid or its derivative is used alone, only a less than stoichiometric amount of oxime can be rearranged to a corresponding amide. The process of this invention can be preferably applied to rearrangement of a ketone oxime to a corresponding amide. Specific examples of the ketone oxime include cyclohexanone oxime, cyclopentanone oxime, cyclododecanone oxime, acetone oxime, 2-butanone oxime, acetophenone oxime, benzophenone oxime and the like. Of these, cyclohexanone oxime is particularly preferably used in the process of this invention. In this invention, the rearrangement reaction can proceed upon merely mixing phosphorus pentoxide and an oxime with at least one compound selected from the group consisting of N,N-dialkyl amides, N-alkyl cyclic amides and dialkyl sulfoxides alone or in combination with a fluorine-containing strong acid or its derivative, whereby a corresponding amide can be obtained. The process of this invention can be practised, for example, by adding phosphorus pentoxide alone or in combination with a fluorine-containing strong acid or its derivative to at least one compound selected from the group consisting of N,N-dialkyl amides, N-alkyl cyclic amides and dialkyl sulfoxides, thereafter heating the resulting mixture to the desired temperature and then dropwise adding thereto an oxime solution in an N,N-dialkyl amide or the like to subject the oxime to rearrangement. The reaction temperature in this invention is preferably about 20-200°C, more preferably about 30-150°C. After completion of the reaction, a small amount of an alkali is added to the reaction mixture to deactivate the catalyst. The reaction product is separated from the reaction mixture by a conventional means such as distillation or the like and then purified in a conventional manner. According to the process of this invention, an oxime can be rearranged in a liquid phase under relatively mild conditions to obtain an amide in a good yield. This invention is explained in more detail below referring to Examples which are merely by way of illustration and not by way of limitation. In the Examples, the amide (or lactam) yield is indicated by a molar yield (%) based on the starting oxime and the selectivity is indicated by [(yield/conversion) x 100] (%). Example 1 A 200-ml, round-bottomed flask was purged with nitrogen and therein were placed 45 ml of dried N,N-dimethylformamide and 0.35 g (2.5 mM) of phosphorus pentoxide, after which the resulting mixture was heated to 60°C. Subsequently, a solution of 8.0 g (70.7 mM) of cyclohexanone oxime in 45 ml of N,N-dimethylformamide was dropwise added to the mixture at 60°C over 60 minutes to effect reaction. After completion of the reaction, the reaction mixture was subjected to analysis by a gas chromatography to find that the conversion of cyclohexanone oxime is 52.9%, the ε-caprolactam yield is 48.1% (selectivity: 91.0%). The catalyst turnover (TON) of the ε-caprolactam produced based on phosphorus pentoxide was 13.8 (mol/mol). Examples 2 to 4 The same procedure as in Example 1 was repeated, except that the reaction temperature was changed to 80°C, 100°C or 120°C, to obtain the results shown in Table 1 in which the results in Example 1 are also shown. Example No. Reaction temp. (°C) Lactam yield (%) Lactam selectivity (%) TON (mol/mol) 1 60 48.1 91.0 13.8 2 80 64.7 91.2 18.6 3 100 69.1 90.1 19.8 4 120 68.2 89.5 19.5 Example 5 In a 200-ml round-bottomed flask purged with nitrogen were placed 75 ml of dried N,N-dimethylformamide and 0.70 g (5.0 mM) of phosphorus pentoxide and the resulting mixture was heated to 95°C. Subsequently, a solution of 8.0 g (70.7 mM) of cyclohexanone oxime in 75 ml of N,N-dimethylformamide was dropwise added to the mixture at 95°C over 60 minutes, to effect reaction. After completion of the reaction, the reaction mixture was subjected to analysis by a gas chromatography to find that the conversion of cyclohexanone oxime was 100% and the ε-caprolactam yield was 92.1% (selectivity: 92.1%). The catalyst turnover of the ε-caprolactam produced based on phosphorus pentoxide was 13.0 (mol/mol). Examples 6 to 10 In a 200-ml round-bottomed flask purged with nitrogen were placed 23 ml of one of the N,N-dialkyl amide, N-alkyl cyclic amide and dialkyl sulfoxide shown in Table 2 and 0.35 g (2.5 mM) of phosphorus pentoxide, and the resulting mixture was heated to 95°C. Subsequently, a solution of 4.0 g (35.4 mM) of cyclohexanone oxime in 22 ml of an N,N-dialkyl amide solvent as shown in Table 2 was dropwise added to the mixture at 95°C over 60 minutes to effect reaction. After completion of the reaction, the reaction mixture was subjected to analysis by a gas chromatography to obtain the results shown in Table 2. Example No. Solvent Lactam yield (%) Lactam selectivity (%) TON (mol/mol) 6 N,N-diethylformamide 54.0 81.2 7.6 7 N,N-diisopropylformamide 32.8 64.4 4.6 8 N,N-dimethylacetamide 46.2 74.3 6.5 9 Dimethyl sulfoxide 37.7 61.5 2.7 10 N-methyl-2-pyrrolidone 27.1 57.1 3.8 Examples 11 to 13 In a 200-ml round-bottomed flask purged with nitrogen were placed 23 ml of dried N,N-dimethylformamide and 0.18 g (1.25 mM) of phosphorus pentoxide, and the resulting mixture was heated to 120°C. Subsequently, a solution of 35.5 mM of one of the ketone oximes shown in Table 3 in 22 ml of N,N-dimethylformamide was dropwise added to the mixture at 120°C over 30 minutes to effect reaction. After completion of the reaction, the reaction mixture was subjected to analysis by a gas chromatography to obtain the results shown in Table 3. Example No. Starting oxime Amide product Yield (%) 11 Acetone oxime N-methylacetamide 5.6 12 syn-Acetophenone oxime Acetanilide 12.6 13 Cyclopentanone oxime 2-Piperidone 10.9 Examples 14 to 22 A 200-ml, round-bottomed flask purged with nitrogen were placed 45 ml of dried N,N-dimethylformamide, 0.175 g (1.25 mM) of phosphorous pentoxide, and one of the fluorine-containing strong acids and derivatives thereof shown in Table 4, and the resulting mixture was heated to 120°C. Subsequently, a solution of 8.0 g (70.7 mM) of cyclohexanone oxime in 45 ml of N,N-dimethylformamide was dropwise added to the mixture to effect reaction. After completion of the reaction, the reaction mixture was treated with an alkali and then subjected to analysis by a gas chromatography to obtain the results shown in Table 4. Example No. Fluorine-containing strong acid or its derivative ε-Caprolactam TON (mol/mol) Kind Amount (mM) Yield (%) Selectivity (%) 14 (CF₃SO₂)₂O 0.625 58.7 91.3 32.7 15 CF₃SO₃SiMe₃ 0.625 47.8 92.8 24.7 16 CF₃SO₃Et 0.625 39.4 92.4 22.0 17 (CF₃CO)₂O 0.625 40.2 85.7 22.4 18 (CF₃SO₂)₂O 1.25 72.1 87.5 41.0 19 (CF₃SO₂)₂Sn 1.25 41.4 92.6 23.1 20 CF₃SO₃H 1.25 54.0 92.8 30.1 21 (CF₃CO)₂O 1.25 48.0 90.8 26.8 22 BF₃-ether complex 1.25 55.4 90.2 30.9 Comparative Example 1 The same procedure as in Example 20 was repeated, except that the phosphorus pentoxide was not added. The results obtained were such that the yield of ε-caprolactam was 2.0% and the selectivity was 40.2%. Examples 23 to 26 A 200-ml, round-bottomed flask purged with nitrogen were placed 45 ml of dried N,N-dimethylformamide, 1.25 mM of trifluoromethanesulfonic acid anhydride and phosphorus pentoxide in an amount as shown in Table 5, and the resulting mixture was heated to 120°C. Subsequently, a solution of 8.0 g (70.7 mM) of cyclohexanone oxime in 45 ml of N,N-dimethylformamide was dropwise added to the mixture at 120°C over 30 minutes to effect reaction. After completion of the reaction, the reaction mixture was treated with an alkali and then subjected to analysis by a gas chromatography to obtain the results shown in Table 5. Comparative Example 2 The same procedure as in Example 23 was repeated, except that the phosphorus pentoxide was not added, to obtain the results shown in Table 5. Examples 27 to 30 In a 200-ml, round-bottomed flask purged with nitrogen were placed 45 ml of dried N,N-dimethylformamide, 0.175 g (1.25 mM) of phosphorus pentoxide and trifluoromethanesulfonic acid in an amount as shown in Table 6, and the resulting mixture was heated to 120°C. Subsequently, a solution of 8.0 g (70.7 mM) of cyclohexanone oxime in 45 ml of N,N-dimethylformamide was dropwise added to the mixture at 120°C over 30 minutes to effect reaction. After completion of the reaction, the reaction mixture was treated with an alkali and subjected to analysis by a gas chromatography to obtain the results shown in Table 6. Example No. Amount of CF₃SO₃H added (mM) ε-Caprolactam TON (mol/mol) Yield (%) Selectivity (%) 27 1.25 54.0 92.8 30.1 28 2.50 71.4 92.1 39.8 29 3.75 78.7 92.2 43.9 30 5.00 88.4 93.3 49.3 Examples 31 to 33 In a 200-ml, round-bottomed flask purged with nitrogen were placed 23 ml of dried N,N-dimethylformamide, 0.18 g (1.25 mM) of phosphorus pentoxide and 1.25 mM of trifluoromethanesulfonic acid anhydride, and the resulting mixture was heated to 120°C. Subsequently, a solution of 35.5 mM of one of the ketone oximes shown in Table 7 in 22 ml of N,N-dimethylformamide was dropwise added to the mixture at 120°C over 30 minutes to effect reaction. After completion of the reaction, the reaction mixture was treated with an alkali and subjected to analysis by a gas chromatography to obtain the results shown in Table 7. Example No. Starting oxime Product Amide Yield (%) 31 Acetone oxime N-methylacetamide 100 32 syn-Acetophenone oxime Acetanilide 22.4 33 Cyclopentanone oxime 2-Piperidone 59.5 Examples 34 to 37 In a 200-ml, round-bottomed flask purged with nitrogen were placed 90 ml of dried N,N-dimethylformamide, 0.36 g (2.50 mM) of phosphorus pentoxide and 2.50 mM of trifluoromethanesulfonic acid anhydride, and the resulting mixture was heated to a temperature as shown in Table 8. Subsequently, a solution of 16 g (141.4 mM) of cyclohexanone oxime in 90 ml of N,N-dimethylformamide was dropwise added to the mixture at a temperature as shown in Table 8 over 30 minutes to effect reaction. After completion of the reaction, the reaction mixture was treated with an alkali and subjected to analysis by a gas chromatography to obtain the results shown in Table 8. Example No. Reaction temperature (°C) ε-Caprolactam TON (mol/mol) Yield (%) selectivity (%) 34 60 53.5 94.4 30.7 35 80 77.4 93.2 44.4 36 100 75.2 91.8 43.1 37 120 71.5 89.0 40.1 Example 38 The same procedure as in Example 36 was repeated, except that the trifluoromethanesulfonic acid anhydride was replaced by antimony pentafluoride. As a result, the ε-caprolactam yield was 57.3%, the selectivity was 91.0% and the catalyst turnover (TON) was 32.9 mol/mol.

Claims: A process for producing an amide which comprises subjecting an oxime to liquid phase rearrangement in the presence of phosphorus pentoxide and at least one compound selected from N,N-dialkyl amides, N-alkyl cyclic amides and dialkyl sulfoxides, with the exception of a process which comprises combining 30 cm³ of N,N-dimethylformamide, 21.4 mmoles of propylene oxide and 10.0 mmoles of phosphorus pentoxide; reacting the resulting mixture at 50°C for 1 hour to form a reaction accelerator; adding to the reaction accelerator 61cm³ of N,N-dimethylformamide and 70.7 mmoles of cyclohexanone oxime; and subjecting the resulting mixture to reaction at 66°C for 2 hours to form ε-caprolactam. A process for producing an amide which comprises subjecting an oxime to liquid phase rearrangement in the presence of a fluorine-containing strong acid or a derivative thereof, phosphorus pentoxide and at least one compound selected from N,N-dialkyl amides, N-alkyl cyclic amides and dialkyl sulfoxides. A process according to claim 2 wherein the fluorine-containing strong acid or derivative is selected from trifluoromethanesulfonic acid, trifluoromethanesulfonic acid anhydride, ethyl trifluoromethanesulfonate, trimethylsilyl trifluoromethanesulfonate, tin trifluoromethanesulfonate, trifluoroacetic acid, trifluoroacetic acid anhydride, boron trifluoride, boron trifluoride-ether complex and antimony pentafluoride. A process according to any one of claims 1 to 3 conducted in the presence of a N,N-dialkyl C₁₋₆ carboxylic acid amide in which the two alkyl groups are the same or different and each alkyl group has 1 to 6 carbon atoms. A process according to claim 4, wherein the N,N-dialkyl amide is N,N-dimethylformamide, N,N-diethylformamide, N,N-diisopropylformamide, N,N-dibutylformamide, N,N-dihexylformamide, N,N-dimethylacetamide, N,N-diethylacetamide, N,N-diisopropylacetamide, N,N-dimethylpropionamide, N,N-dimethylbutyramide or N,N-dimethylcaproamide. A process according to any one of claims 1 to 5 conducted in the presence of an N-alkyl cyclic amide having 4 to 6 carbon atoms in the cyclic amide group and 1 to 6 carbon atoms in the N-alkyl group. A process according to claim 6 wherein the N-alkyl cyclic amide is N-methylpyrrolidone or N-methylpiperidone. A process according to any one of claims 1 to 7 conduced in the presence of a dialkyl sulfoxide in which the two alkyl groups are the same or different and each has 1 to 6 carbon atoms. A process according to claim 8 wherein the dialkyl sulfoxide is dimethylsulfoxide, diethylsulfoxide, dipropylsulfoxide or dihexylsulfoxide. A process according to any one of claims 1 to 9 wherein the oxime is cyclohexanone oxime, cyclopentanone oxime, cyclododecanone oxime, acetone oxime, 2-butanone oxime, acetophenone oxime or benzophenone oxime. A process according to claim 11 wherein the oxime is cyclohexanone oxime. A process according to any one of claims 1 to 11 wherein the rearrangement is effected at a temperature of 20 to 200°C. A process according to any one of claims 1 to 13 conducted in the presence of 0.1 to 50 mole %, based on the molar amount of the oxime, of phosphorus pentoxide. The process according to claim 13 conducted in the presence of 0.01 to 50 moles, per mole of the phosphorus pentoxide, of a fluorine - containing strong acid or a derivative thereof.

Inventors: IZUMI YUSUKE, NOMURA YOSHISABUROU, SATO HIROSHI, YOSHIOKA HIROSHI, IZUMI, YUSUKE, NOMURA, YOSHISABUROU, SATO, HIROSHI, YOSHIOKA, HIROSHI
Applicants: IZUMI YUSUKE, SUMITOMO CHEMICAL CO, IZUMI, YUSUKE, SUMITOMO CHEMICAL COMPANY LIMITED
Application year: 1992
Main classification: C07C231
IPC codes: C07D201, C07C231