METHOD OF MANUFACTURING AROMATIC URETHANE AND INTERMEDIATE PRODUCT THEREOF

Abstract: The present invention relates to a method of manufactur­ ing aromatic urethane, an aromatic mononitro-compound , an aromatic primary amine, and carbon oxide being reacted using a catalyst containing a platinum group metal-­ containing compound as a major constituent to prepare N,N′-­ di-substituted urea. The resultant N,N′-di-substituted urea is reacted with a hydroxyl group-containing organic compound to prepare an aromatic primary amine and aromatic urethane, and the aromatic primary amine is separated to obtain arom­ atic urethane.

Description: The present invention relates to a method of manufacturing aromatic urethane. Various conventional methods of manufacturing aromatic urethane have been proposed. These methods are classified into a method using an aromatic nitro-compound as a starting material and a method using an aromatic primary amine as a starting material. According to the conventional method using an aromatic nitro-compound as a starting material, an aromatic nitro-compound (e.g., nitrobenzene), an organic compound (e.g., an alcohol) containing a hydroxyl group, and carbon monoxide are allowed to react reductively with each other in the presence of a catalyst having a platinum group compound such as a palladium or rhodium compound as a major constituent to manufacture aromatic urethane. Examples of this method are described in Japanese Patent Disclosure (Kokai) Nos. 51-98240 and 54-22339 and Japanese Patent Publication No. 43-23939. According to the conventional method using an aromatic primary amine as a starting material, an aromatic primary amine (e.g., aniline), an organic compound (e.g., an alcohol) containing a hydroxyl group, and carbon monoxide are allowed to react oxidatively with each other in the presence of an oxidizer such as oxygen or an organic nitro-compound through a catalyst containing a platinum group metal compound such as a palladium or rhodium compound to prepare aromatic urethane. Examples of this method are described, e.g., in Japanese Patent Disclosure (Kokai) Nos. 55-124750, 55-120551, and 59-172451. In either method, since use of only a platinum group metal compound as the major constituent of the catalyst results in low synthetic activity of urethane, a halogen compound such as iron chloride, iron oxychloride, vanadium oxychloride, or potassium iodide is used as an assistant catalyst. A mixture of the platinum group metal compound and the assistant catalyst are dissolved in a reacting system. However, the halogen compound greatly corrodes a metal material such as a reaction chamber and piping valves. For this reason, an expensive metal material having a good anticorrosion property must be used. When a platinum group metal compound as a main catalyst is dissolved in a reaction solution or a solid platinum group metal compound is used, the platinum group metal partially contains a halogen compound and the halogen compound is eluted in the reaction solution. In order to recover the platinum group metal compound from the reaction solution at the end of reaction, cumbersome operations and high cost are required. In addition, an organic compound containing a hydroxyl group for a reaction material is used as a reaction solution, and aromatic urethane has high solubility in the organic compound containing a hydroxyl group. For this reason, in order to crystallize and separate aromatic urethane from the solution after reaction, the solution must be cooled to an extremely low temperature of several tens of minus degrees in centigrade. Alternatively, the solution must be condensed and cooled to allow precipitation of crystals. Even if such precipitation is performed, it is difficult to recover aromatic urethane dissolved in the solution separately from the catalyst. Another method of recovering aromatic urethane is a distillation method. In this case, however, since the dissolved catalyst must be recovered as a distillation residue, aromatic urethane must be distilled. However, aromatic urethane is a compound having a high boiling point and must be distilled at a temperature of 100 to 150°C under a high vacuum of about 1,3 · 10⁻³ bar (1mm Hg). Furthermore, if an aromatic nitro-compound is used as a starting material, a small amount of nonreacted aromatic nitro-compound is left in the reaction solution. If distillation is performed in this state, aromatic urethane is colored in brown by the aromatic nitro-compound. As described above, it is difficult to separate and recover aromatic urethane from the solution and further recover the catalyst for reuse regardless of a recovery method, i.e. crystallization or distillation. If an aromatic nitro-compound is used as a starting material an aromatic amine is by-produced, and if an aromatic primary amine is used as a starting material, N,N'-di-substituted urea is by-produced, thereby decreasing the yield of aromatic urethane. From Chemical Abstracts, 78 , No. 43087m (1973), N, N'-disubstituted ureas are known wherein a mixture of amide, Co, and an aromatic nitro compound is heated in the presence of a metal belonging to group VIII. According to this prior art, Rh chloride, Pd chloride, Fe chloride, Co carbonyl,Pd carbide and Ir chloride are used as metal catalysts, however, no rhodium compound is mentioned which does not contain a halide. Also, no ruthenium compound is mentioned in this document. Experiments have shown that the catalysts mentioned in this document are poor in yield and in selectivity so that the demands in practice are not always met. Document US-A-2,409,712 discloses a process for preparing isocyanates, in particular a process for preparing isocyanic esters from N-substituted carbamic esters. Also, a process is described how to prepare aliphatic and aromatic esters of isocyanic acid from N-substituted carbamic esters without using P₂O₅ or other such reagents. According to this document US-A-2,409,712 ureas are decomposed by using an alcohol so as to manufacture isocyanate. However, the carbamate is formed as an intermediate product in the manufacturing process leading to isocyanate. Therefore, the carbamate yield is not mentioned in this document and it is to be expected that the respective yield is rather low. Also, nothing can be found in this document as to specific catalysts to be used for manufacturing ureas and aromatic urethane which have been found as particularly useful by the present inventor. It is an object of the present invention to provide a method of manufacturing aromatic urethane to solve various conventional problems without using a halogen compound as an assistant catalyst, to prepare aromatic urethane according to a two-step reaction, to increase the yield of intermediate product and aromatic urethane and to easily recover the catalyst and the resultant aromatic urethane. In order to solve the above object underlying the present invention there is provided a method of manufacturing aromatic urethane, comprising the following steps: an urea producing step of reaction an aromatic mononitro-compound, an aromatic primary amine, and carbon monoxide by using a catalyst having a platinum group metal-containing compound as a major constituent to prepare N,N'-di-substituted urea and of separating and recovering the resultant N, N'-di-substituted urea from a reaction solution, the aromatic primary amine being in an excessive amount to function as a solvent, the reaction being carried out in the absence of halogen or a halogen compound, and the catalyst being selected from the group consisting of Ru₃(CO)₁₂ , H₄Ru₄(CO)₁₂ , Ru(CO)₃(PPh₃)₂ , Ru(CO)₃(dppe) , Ru(CO)₂(HCO)₂P(C-C₆H₁₁)₃)₂ , Ru(acac)₃ , Rh₆(CO)₁₆ , RhH(CO)(PPh₃)₃ , Rh(acac)(CO)(PPh₃) , Rh(acac)(CO)₂ , and Rh(acac)₃ , wherein "dppe" represents diphenylphosphinoethane and "acac" represents acetylacetonato; a step of reacting the N,N'-di-substituted urea as an intermediate product prepared in the urea producing step with an organic compound containing a hydroxyl group to prepare an aromatic primary amine and aromatic urethane, and of separating the aromatic primary amine from the aromatic urethane, thereby obtaining the aromatic urethane; and a step of recirculating the separated aromatic primary amine to the urea producing step. According to a further development of the method according to the invention, the N, N'-di-substitued urea reacts with the hydroxyl group-containing organic compound without using a catalyst. According to a further aspect of the present invention, a method of manufacturing ureas is provided, comprising the following steps: reacting an aromatic mononitro-compound, an aromatic primary amine, and carbon monoxide by using a catalyst having a platinum group metal-containing compound as a major constituent to prepare N,N'-di-substituted urea and of separating and recovering the resultant N,N'-di-substituted urea from a reaction solution, the aromatic primary amine being in an excessive amount to function as a solvent, the reaction being carried out in the absence of halogen or a halogen compound, and the catalyst being selected from the group consisting of Ru₃(CO)₁₂ , H₄Ru₄(CO)₁₂ , Ru(CO)₃(PPh₃)₂ , Ru(CO)₃(dppe) , Ru(CO)₂(HCO)₂P(C-C₆H₁₁)₃)₂ , Ru(acac)₃ , Rh₆(CO)₁₆ , RhH(CO)(PPh₃)₃ , Rh(acac)(CO)(PPh₃) , Rh(acac)(CO)₂ , and Rh(acac)₃ , wherein "dppe" represents diphenylphosphinoethane and "acac" represents acetylacetonato. An aromatic mononitro-compound, aromatic primary amine, and carbon monoxide are reacted using a catalyst using a ruthenium complex compound as a major constituent. This reaction progresses according to the following general formula: The aromatic primary amine comprises anilines, aminonaphthalenes, aminoanthracenes, aminobiphenyls, and the like. Examples of these aromatic primary amine are aniline, o-, m- and p-toluidine, o-, m-and p-chloroaniline, α-and β-naphthylamine, 2-methyl-1-aminonaphthalene, diaminobenzene, triaminobenzene, aminotoluene, diaminotoluene, aminopyridine, diaminopyridine, aminonaphthalene, diaminonaphthalene, an isomer thereof, and a mixture thereof. An aromatic mononitro-compound comprises nitrobenzenes, nitronaphthalenes, nitroanthracenes, nitrobiphenyls, and a nitro-compound wherein at least one hydrogen atom is substituted with another substituent (e.g., a halogen atom, a cyano group, an alicyclic group, an aromatic group, an alkyl group, an alkoxy group, a sulfoxide group, a sulfone group, a carbonyl group, an ester group, and an amide group). Examples of these aromatic mononitro-compound are nitrobenzene, o-, m-, and p-nitrotoluene, o-nitro-p-xylene, 2-methyl-1-nitronaphthalene, o-, m- and p-chloronitrobenzene, 1-bromo-4-nitrobenzene, an isomer thereof, and a mixture thereof. It should be noted that a nitro-compound corresponding to the selected aromatic primary amine is preferable. Carbon monoxide may be pure carbon monoxide, or may be mixed with nitrogen, argon, helium, carbon dioxide gas, hydrocarbon, or halogenated hydrocarbon. Cobalt, iron, rhodium, palladium, or the like is combined with a platinum group metal compound. When a ruthenium complex compound is used as a major constituent of a catalyst, a reaction temperature generally falls within the range of 30 to 300°C and preferably 120 to 200°C. A reaction pressure generally falls within the range of 1 to 500 kg/cm² and preferably 10 to 300 kg/cm². When a rhodium complex compound is used as a major constituent of a catalyst, a reaction temperature generally falls within the range of 80 to 300°C and preferably 120 to 200°C. A reaction pressure generally falls with the range of 1 to 500 kg/cm² and preferably 20 to 300 kg/cm². The reaction time varies according to other conditions but generally falls within the range of 0.5 to 24 hours. The reaction can be achieved without using a solvent. However, a proper solvent such as an aromatic hydrocarbon (e.g., benzene, toluene, xylene, and cyclohexane) may be used. When the concentration of aromatic primary amine as a starting material is increased, the reaction rate is increased. Therefore, an aromatic primary amine is used in an excessive amount and can be substantially used as a solvent, thereby achieving the reaction at a maximum rate. The resultant N,N'-di-substituted urea has low solubility with respect to the solvent. For this reason, the solution after the reaction is simply cooled to precipitate N,N'-di-substituted urea as crystals. Therefore, the resultant solution is filtered to obtain solid N,N'-di-substituted urea. The catalyst is obtained as a solution together with the solvent. The solvent containing the catalyst can be used again. The organic compound containing N,N'-di-substituted urea and a hydroxyl group reacts according to the following formula to prepare aromatic primary amine and aromatic urethane: The organic compound containing a hydroxyl group comprises monoalcohols and monophenols. Examples of such a compound are monoalcohols [e.g., methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, and t-butyl) and alkyl phenols (e.g., phenol, chlorophenol, and methyl, ethyl, n-propyl, and isopropyl substituted phenol). The reaction temperature generally falls within the range of 80 to 300°C and preferably 120 to 200°C. The reaction pressure is a pressure naturally obtained at a reaction temperature of the hydroxyl group-containing organic compound or solvent. The reaction time varies according to other conditions but generally falls within the range of 1 to 10 hours. This reaction can be achieved without using a catalyst. After the end of reaction, distillation is performed to recover aromatic urethane as a distillation residue. On the other hand, aromatic primary amine is recovered by distillation. Aromatic primary amine is used again in the production of N,N'-di-substituted urea in the first-step reaction. According to the present invention, since N,N'-di-substituted urea produced in the first-step reaction has low solubility in the solvent, it can be easily crystallized, and N,N'-di-substituted urea can be effectively recovered by filtration. In addition, the catalyst is contained together with the solvent in the filtered solution. The catalyst can be reused in the first-step reaction. The catalyst contains a compound containing a platinum group metal as a major constituent. A halogen compound need not be used. For this reason, the metal members required for the reaction are little corroded, and any expensive material need not be used. The first-step reaction is free from a side reaction and can produce N,N'-di-substituted urea at a high yield. An excessive amount of aromatic primary amine is added in the urea production reaction, and aromatic primary amine is used as a solvent to increase the reaction rate. In the second-step reaction, the catalyst need not be used. Aromatic urethane is not eluted and can be recovered as a distillation residue. Aromatic primary amine as a distilled material and the compound containing a residual hydroxyl group have relatively low boiling points. Therefore, distillation can be performed at moderate conditions, thus simplifying the operations. In addition, the recovered aromatic primary amine can be reused in the first-step reaction. The second-step reaction results in little side reaction in the same manner as in the first-step reaction. Therefore, aromatic urethane can be prepared in the two-step reaction at a high yield. Examples The present invention will be described in detail by way of examples. In the following examples, the term "alkyl carbamate" is used instead of the term "urethane", and the individual material names are indicated. Example 1 3,82 g of nitrobenzene, 2,85 g of aniline, 34,58 g of toluene, and 0,10 g of Ru₃(CO)₁₂ were charged in an electromagnetic stirring type autoclave having an inner volume of 200 mℓ. Carbon monoxide was supplied to the autoclave at a pressure of 50 kg/cm². The materials were stirred and reacted at a temperature of 160°C for 6 hours. After the reaction, the mixture was cooled to room temperature. The autoclave was then evacuated, and the reaction solution was filtered to obtain 5,91 g of crystals. The crystals were analyzed by liquid chromatography and found to have a 90% yield of N,N'-diphenyl urea for nitrobenzene. In addition, the reactive filtered solution containing the catalyst after the separation of N,N'-diphenyl urea was used to repeat the above test under identical conditions. The yield of N,N'-diphenyl urea was 90%. 3,00 g of the resultant crystals and 50,00 g of methyl alcohol were filled in another electromagnetic stirring type autoclave having an inner volume of 200 mℓ and were stirred and reacted at a temperature of 160°C for 3 hours. When the reacted solution was analyzed, it had a 94% yield for N-phenylmethyl carbamate and a 95% yield for aniline. Example 2 Following the same procedures as in Example 1 except that 0,13 g of Ru₃(CO)₁₂ was used as the catalyst, nitrobenzene, aniline and carbon monoxide were reacted to prepare 5,94 g of N,N'-diphenyl urea crystals. The yield of N,N'-diphenyl urea for nitrobenzene was 94%. Following the same procedures as in Example 1, 3,00 g of the crystals and 50,00 g of ethyl alcohol were reacted to obtain a 93% yield for N-phenylethyl carbamate and a 95% yield for aniline. Example 3 Following the same procedures as in Example 1 except that 0,31 g of Ru(CO)₃(PPh₃)₂ was used in place of Ru₃(CO)₁₂ as the catalyst, nitrobenzene, aniline and carbon monoxide were reacted to prepare 5,77 g of N,N'-diphenyl urea crystal. The yield of N,N'-diphenyl urea for nitrobenzene was 90%. Following the same procedures as in Example 1, 3,00 g of the crystals and 50,00 g of ethyl alcohol were reacted to obtain a 92% yield for N-phenylmethyl carbamate and a 93% yield for aniline. Example 4 Following the same procedures as in Example 1 except that 0,31 g of Ru(acac)₃ was used in place of Ru₃(CO)₁₂ as the catalyst nitrobenzene and that the reaction time was 8 hours, aniline and carbon monoxide were reacted to prepare 6,04 g of N,N'-diphenyl urea crystals. The yield of N,N'-diphenyl urea for nitrobenzene was 96%. Following the same procedures as in Example 1, 3,00 g of the crystals and 30,00 g of methyl alcohol were reacted to obtain a 93% yield for N-phenylmethyl carbamate and a 92% yield for aniline. Example 5 3,77 g of nitrobenzene, 2,78 g of aniline, 34,03 g of toluene, 0,38 g of Rh₆(CO)₁₆, and 1,24 g of triphenylphosphine were charged in an electromagentic stirring type autoclave having an inner volume of 200 mℓ. Carbon monoxide was supplied to the autoclave at a pressure of 50 kg/cm². The materials were stirred and reacted at a temperature of 160°C for 9 hours. After the reaction, the mixture was cooled to room temperature. The autoclave was then evacuated, and the reaction solution was filtered to obtain 6,05 g of crystals. The crystals were analyzed by liquid chromatography and found to have a 93% yield for N,N'-diphenyl urea based on nitrobenzene. 3,00 g of the resultant crystals and 50,00 g of methyl alcohol were filled in another electromagnetic stirring type autoclave having an inner volume of 200 mℓ and were stirred and reacted at a temperature of 160°C for 3 hours. When the reaction mixture was analyzed, it had a 93% yield for N-phenylmethyl carbamate and a 94% yield for aniline. Example 6 Following the same procedures as in Example 5 except that 0,39 g of Rh₄(CO)₁₂ was used as the catalyst nitrobenzene and the reaction time was 10 hours, nitrobenzene, aniline and carbon monoxide were reacted to prepare 5,76 g of N,N'-diphenyl urea crystals. The yield of N,N'-diphenyl urea based on nitrobenzene was 95%. Following the same procedures as in Example 5, 3,00 g of the crystals and 50,00 g of ethyl alcohol were reacted to obtain a 93% yield for N-phenylethyl carbamate and a 95% yield for aniline. Example 7 Following the same procedures as in Example 5 except that 0,38 g of Rh₆(CO)₁₆ was used as the catalyst and triphenylphosphine was not added, nitrobenzene, aniline and carbon monoxide were reacted to prepare 1,16 g of N,N'-diphenyl urea crystals. The resultant crystals and the solution were analyzed to obtain a nitrobenzene conversion of 20% and a 93% selectivity for converted nitrobenzene. Following the same procedures as in Example 5, 1,00 g of the crystals and 20,00 g of methyl alcohol were reacted to obtain a 92% yield for N-phenylmethyl carbamate and a 93% yield for aniline. Example 8 3,71 g of nitrobenzene, 40,0 mℓ of aniline, and 0,0509 g of Ru₃(CO)₁₂ were charged in an electromagnetic stirring type autoclave having an inner volume of 200 mℓ. Carbon monoxide was supplied to the autoclave at a pressure of 50 kg/cm². The materials were stirred and reacted at a temperature of 160°C for 1,5 hours. After the reaction, the mixture was cooled to room temperature. The autoclave was then evacuated, and the reaction solution was filtered to obtain 5,42 g of crystals. The filtered solution was analyzed by liquid chromatography and found to contain 0,37 g of N,N'-diphenyl urea. However, no nitrobenzene was detected. The yield of N,N'-diphenyl urea separated from the solution was 85%. If N,N'-diphenyl urea contained in the solution was included, a total yield thereof was 91%. A turn over rate of the catalyst was 84 (mol-PhNo₂/mol-Ru·h ). 3,00 g of the singly separated N,N'-diphenyl urea and 50,00 g of methyl alcohol were filled in another electromagnetic stirring autoclave having an inner volume of 200 mℓ and were stirred and reacted at a temperature of 160°C for 3 hours. After the reaction, the solution was analyzed to result in a 94% yield for N-phenylmethyl carbamate and a 95% yield for aniline. Examples 9 to 12 Following the same procedures and apparatus as in Example 8, the production test of N,N'-diphenyl urea was performed. The obtained results are summarized in Table 1 below. Example 13 The same procedures as in Example 8 were followed except that the starting materials were 1,08 g of nitrobenzene, 40,0 mℓ of aniline, and 0,0800 g of Ru(acac)₃, the reaction temperature was 160°C, 50 kg/cm² of CO were supplied, and the reaction time was 2,0 hours. As a result, 2,80 g of crystals were obtained. Nitrobenzene was not detected in the filtered solution but 0,27 g of N,N'-diphenyl urea was contained therein. The yield of the singly separated N,N'-diphenyl urea was 90%. If N,N'-diphenyl urea contained in the solution was included, a total yield was 99%. A turn over rate of the catalyst was 36 (mol-PhNo₂/mol-Ru·h ). Following the same procedures as in Example 8, a total amount of N,N'-diphenyl urea crystal was reacted with 50,00 g of ethyl alcohol. After the reaction, the reaction mixture was analyzed to obtain a 93% yield for N-phenylethyl carbamate and a 95% yield for aniline. Example 14 The same procedures as in Example 8 were followed except that the starting materials were 2,32 g of nitrobenzene, 40,0 mℓ of aniline, and 0,0817 g of Ru(CO)₃(PPh₃)₂, the reaction temperature was 160°C, 50 kg/cm² of CO were supplied, and the reaction time was 1,5 hours. As a result, 3,38 g of crystals were obtained. Nitrobenzene was not detected in the filtered solution but 0,31 g of N,N'-diphenyl urea was contained therein. The yield of the singly separated N,N'-diphenyl urea was 85%. If N,N'-diphenyl urea contained in the solution was included, a total yield was 93%. A turn over rate of the catalyst was 109 (mol-PhNo₂/mol-Ru·h ). Following the same procedures as in Example 8, 3,00 g of N,N'-diphenyl urea crystals were reacted with 50,00 g of methyl alcohol. After the reaction, the reaction mixture was analyzed to obtain a 93% yield for N-phenylethyl carbamate and a 94% yield for aniline. Comparative Example 1 6,12 g of nitrobenzene, 37,00 g of methanol, and 0,11 g of Ru₃(CO)₁₂ were filled in an electromagnetic stirring type autoclave having an inner volume of 200 mℓ. Carbon monoxide was supplied to the autoclave at a pressure of 50 kg/cm² so as to obtain a CO atmosphere. The starting materials were stirred and reacted at a temperature of 160°C for five hours. After the reaction, the solution was analyzed by liquid cromatography and found to have a nitrobenzene conversion rate of 32%. The conversion rate of N-phenylmethyl carbamate was as low as 13%, and the conversion rate of by-produced aniline was 40%. In other words, the yield of N-phenylmethyl carbamate was 4%, and the yield of aniline was 13%. Comparative example 2 4,63 g of aniline, 6,12 g of nitrobenzene, 37,00 g of methanol, and 0,11 g of Ru₃(CO)₁₂ were filled in an electromagnetic stirring type autoclave having an inner volume of 200 mℓ. Carbon monoxide was supplied to the autoclave at a pressure of 50 kg/cm² so as to obtain a CO atmosphere. The starting materials were stirred and reacted at a temperature of 160°C for five hours. After the reaction, the solution was analyzed by liquid cromatography and found to have a 61% yield for N-phenylmethyl carbamate and a 4% yield for N,N'-diphenyl urea. The resultant solution was placed in a -5°C refrigerator for 24 hours, but no crystals were precipitated. Comparative Example 3 3,82 g of nitrobenzene, 2,85 g of aniline, 34,58 g of toluene, and 0.10 g of Ru₃(CO)₁₂ were filled in an electromagnetic stirring type autoclave having an inner volume of 200 mℓ. Carbon monoxide was filled at a pressure of 50 kg/cm² to obtain a CO atmosphere in the autoclave. The starting materials were stirred and reacted at a temperature of 160°C for six hours. After the reaction, the solution was cooled to room-temperature, and the reacted solution after the autoclave was evacuated was filtered to obtain 5,91 g of N,N'-diphenyl urea. The filtered solution was analyzed by liquid chromatography. No nitrobenzene was detected. The yield of the singly separated N,N'-diphenyl urea was 90%, and a turn over rate of the catalyst was 11 (mol-PhNO₂/mol-Ru·h ). 3,00 g of the resultant crystals and 50,00 g of methyl alcohol were filled in another electromagnetic stirring type autoclave having an inner volume of 200 mℓ. The starting materials were stirred and reacted at a temperature of 160°C for three hours. After the reaction, the reaction mixture was analyzed and found to have a 94% yield for N-phenylmethyl carbamate and a 95% yield for aniline.

Claims: A method of manufacturing aromatic urethane, comprising the following steps: an urea producing step of reaction an aromatic mononitro-compound, an aromatic primary amine, and carbon monoxide by using a catalyst having a platinum group metal-containing compound as a major constituent to prepare N,N'-di-substituted urea and of separating and recovering the resultant N, N' -di-substituted urea from a reaction solution, the aromatic primary amine being in an excessive amount to function as a solvent, the reaction being carried out in the absence of halogen or a halogen compound, and the catalyst being selected from the group consisting of Ru₃(CO)₁₂ , H₄Ru₄(CO)₁₂ , Ru(CO)₃(PPh₃)₂ , Ru(CO)₃(dppe) , Ru(CO)₂(HCO)₂P(C-C₆H₁₁)₃)₂ , Ru(acac)₃ , Rh₆(CO)₁₆ , RhH(CO)(PPh₃)₃ , Rh(acac)(CO)(PPh₃) , Rh(acac)(CO)₂ , and Rh(acac)₃ , wherein "dppe" represents diphenylphosphinoethane and "acac" represents acetylacetonato; a step of reacting the N,N'-di-substituted urea as an intermediate product prepared in the urea producing step with an organic compound containing a hydroxyl group to prepare an aromatic primary amine and aromatic urethane, and of separating the aromatic primary amine from the aromatic urethane, thereby obtaining the aromatic urethane; and a step of recirculating the separated aromatic primary amine to the urea producing step. The method according to claim 1, characterized in that the N,N'-di-substituted urea reacts with the hydroxyl group-containing organic compound without using a catalyst. A method of manufacturing ureas, comprising the following steps: reacting an aromatic mononitro-compound, an aromatic primary amine, and carbon monoxide by using a catalyst having a platinum group metal-containing compound as a major constituent to prepare N,N'-di-substituted urea and of separating and recovering the resultant N,N'-di-substituted urea from a reaction solution, the aromatic primary amine being in an excessive amount to function as a solvent, the reaction being carried out in the absence of halogen or a halogen compound, and the catalyst being selected from the group consisting of Ru₃(CO)₁₂ , H₄Ru₄(CO)₁₂ , Ru(CO)₃(PPh₃)₂ , Ru(CO)₃(dppe) , Ru(CO)₂(HCO)₂P(C-C₆H₁₁)₃)₂ , Ru(acac)₃ , Rh₆(CO)₁₆ , RhH(CO)(PPh₃)₃ , Rh(acac)(CO)(PPh₃) , Rh(acac)(CO)₂ , and Rh(acac)₃ , wherein "dppe" represents diphenylphosphinoethane and "acac" represents acetylacetonato.

Inventors: IKARIYA, TAKAO PATENT DIVISION, ITAGAKI, MASANORI PATENT DIVISION, MIZUGUCHI, MASATSUGU PATENT DIVISION, SAKAI, ITARU PATENT DIVISION, TAJIMA, OSAMU PATENT DIVISION
Applicants: NIPPON KOKAN KABUSHIKI KAISHA
Application year: 1986
Main classification: C07C271
IPC codes: C07C273