PROCESS FOR PREPARING AROMATIC URETHANE

Abstract: A process for preparing aromatic urethane by reacting an aromatic nitro compound, a hydroxy group-containing organic compound having at least one hydroxy group, and carbon monoxide at elevated temperatures under high pres­ sure in the presence of a catalyst comprising a platinum group metal and/or a compound thereof, a Lewis acid, and a tertiary amine, which comprises allowing ferrous hydroxide and/or ferric hydroxide to coexist in the reaction system. This process so remarkably accelerates the reaction that it is com­ pleted in a short time, and the process enables the prepara­ tion of aromatic urethane in a high yield using a small amount of the platinum group metal catalyst.

Description: Field of the Invention This invention relates to an improved process for the preparation of aromatic urethane compounds by reacting an aromatic nitro compound, an organic compound having at least one hydroxyl group (hereinafter referred to as a hydroxyl-containing compound), and carbon monoxide at high temperature and pressure in the presence of a catalyst. Description of the Prior Art Conventionally, urethanes have been mainly prepared from isocyanates and hydroxyl-containing compounds. In recent years, novel processes for the preparation of urethanes have been developed in view of the shortage of raw materials for the manufacture of isocyanates, the steep rise in their prices, the strong toxicity of intermediate products, and the like. However, these newly developed processes have a number of serious disadvantages, which have precluded them from being put into practice on an industrial scale. For example, there has been proposed a process for preparing urethanes from an alcohol, carbon monoxide and an aromatic nitro compound in the presence of rhodium chlorocarbonyl as a catalyst (Japanese Patent Publication No. 1420/67). In this process, however, the yield of the desired product is low even if the catalyst is used in large quantities and the reaction is carried out for a long period of time. Accordingly, it cannot be regarded as an economical process for preparing urethanes of high purity. As a modification of the process of Japanese Patent Publication No. 1420/67, there has been proposed a process using a carbonyl-containing compound of a metal belonging to group VIII of the periodic table and a salt (e.g., ferric chloride) of a metal existing in two or more valence states (Japanese Patent Publication No. 23939/68). In this process, however, the yield of the product is low even when a mononitro compound is used as a raw material and it is still lower when a dinitro compound is used as a raw material. In U.S. Patent 3,531,512, there has been proposed a process using a catalyst composed of palladium and a Lewis acid. Even when a dinitro compound is used as a raw material, this process can produce urethanes in a fairly good yield of 80 to 90%. However, severe conditions including an initial pressure of carbon monoxide of 190 to 350 kg/cm2 and a temperature of 1900 to 2000C are required for the attainment of such a high yield. Furthermore, in the process disclosed in Japanese Patent Laid-open No. 98240/76, a catalyst system composed of a platinum group metal, a Lewis acid and a tertiary amine is used. Thus, aromatic urethanes can be obtained under mild conditions and in high yield. However, the platinum group metal used in this process is expensive. From an industrial point of view, therefore, it is desirable to reduce the amount of the platinum group metal to a minimum. Disclosure of the Invention .The present inventors have made repeated studies of a process for the preparation of urethanes by reacting an aromatic nitro compound, a hydroxyl-containing compound and carbon monoxide in the presence of a catalyst system composed of (a) a platinum group metal and/or a compound thereof, (b) a Lewis acid and (c) a tertiary amine, and have discovered that a high yield of aromatic urethanes can be obtained without the above-described disadvantages of prior art processes and with a short reaction time by allowing ferrous hydroxide and/or ferric hydroxide to coexist in the reaction system. The present invention has been perfected on the basis of this discovery. According to the process of the present invention, the reaction is accelerated so greatly that it is completed in a short period of time, the amount of platinum group metal catalyst used can be saved, and the desired aromatic urethanes can be obtained in high yield. Best Mode of Practicing the Invention The aromatic nitro compound which is used as the main raw material in the process of the present invention is an aromatic compound having at least one nitro group as a nuclear substituent, and this aromatic compound may have either one nitro group of two or more nitro groups. That is, the aromatic compound may be either a mononitro compound or a polynitro compound. The aromatic compound may have other substituents in addition to the nitro group or groups. The useful nitro compounds include, for example, substituted and unsubstituted nitrobenzenes, dinitrobenzenes, dinitrotoluenes, nitronaphthalenes, nitroanthracenes, nitrobiphenyls, bis(nitrophenyl)alkanes, bis(nitrophenyl)ethers, bis(nitrophenyl)thioethers, bis(nitrophenyl)sulfones, nitrodiphenoxyalkanes, heterocyclic aromatic compounds such as nitrophenothiazines and 5-nitropyrimidine, and the like. Specific examples thereof are nitrobenzene, o-, m- and p-nitrotoluenes, o-nitro-p-xylene, l-nitronaphthalene, m- and p-dinitrobenzenes, 2,4-and 2,6-dinitrotoluenes, dinitromesitylene, 4 ?4 ' -dinitrobiphenyl, 2,4-dinitrobiphenyl, 4, 4'-dinitrodibenzyl, bis(4-nitrophenyl)methane, bisC4-nitrophenyl)ether, bis(2,4-dinitrophenyl)ether, bist4-nitrophenyl)thioether, bis(4-nitrophenyl)sulfone, bisC4-nitrophenoxy)ethane,' a, a'-dinitro--xylene, a, a' - dinitro-m-xylene, 2,4,6-trinitrotoluene, o-, m- and E-chloronitrobenzenes, 2,3-, 3,4- and 2,5-' dichloronitrobenzenes, l-chloro-2,4-dinitrobenzene, l-bromo-4-nitrobenzene., l-fluoro-2,4-'dinitrobenzene, o-, m- and p-nitrophenyl carbamates,o-, m- and E-nitroanisoles, 2,4-dinitrophenetole,ethyl p-nitrobenzoate, m-nitrobenzenesulfonyl chloride,. 3-nitrophthalic anhydride, 3,3'-dimethyl-4,41-dinitrobiphenyl, 1,5-dinitronaphthalene and the like. Isomers and mixtures of these aromatic nitro compounds, as well as homologues thereof, can also be used. In addition, aromatic nitroso compounds, azo compounds and azoxy compounds can also be used similarly to the aromatic nitro compounds. Among the foregoing aromatic nitro compounds, mononitro compounds such as nitrobenzene, o-, m- and p-chloronitrobenzenes., 2,3- and 3, 4-dichloronitrobenzenes, etc. and aromatic dinitro compounds such as m- and p- dinitrobenzenes, 2,4- and 2,6-dinitro toluenes, 1,5dinitronaphthalene, etc. are particularly preferred. This is because these nitro compounds facilitate the reaction and give a high yield of the end products which have many uses as raw materials for the manufacture of drugs, agricultural chemicals, polyurethanes and the like. The hydroxyl-containing compounds which can be used in the process of the present invention include monohydric or polyhydric alcohols containing a primary, secondary or tertiary hydroxyl group or groups, and monohydric or polyhydric phenols. Typical examples thereof are ethanol and phenol. The useful alcohols can be represented by the formula R(OH)n where R is a straight-chain or branched alkyl, cycloalkyl, alkylene, cycloalkyl.ene or aralkyl group and n is a whole number of 1 or more. These alcohols may also have one or more substituents containing an oxygen, nitrogen, halogen, or sulfur atom or atoms, such as halogen atoms, sulfoxide group, sulfone group, carbonyl group, carboxylate group, etc. Specific examples of the alcohols represented by the formula R(OH) n include monohydric alcohols such as methyl alcohol, ethyl alcohol, n-propyl alcohol, isopropyl alcohol, n-butyl alcohol, isobutyl alcohol, tert-butyl alcohol, straight-chain or branched amyl alcohol, hexyl alcohol, cyclohexyl alcohol, lauryl alcohol, cetyl alcohol, benzyl alcohol, chlorobenzyl alcohol, methoxybenzyl alcohol, etc.; dihydric alcohols such as ethylene glycol, diethylene glycol, propylene glycol, dipropylene glycol, etc.; trihydric alcohols such asglycerol,hexanetriol, etc.; and higher polyols. The useful phenols include phenol, chlorophenol, cresol, ethylphenol, straight-chain or branched propyl-, butyl-and higher alkylphenols, catechol, resorcinol, 4,4'-dihydroxydiphenylmethane, 2,2'-isopropylidenediphenol, anthranol, phenanthrolj pyrogallol, phloroglucinol and the like. Among the foregoing hydroxyl-containing compounds, methanol, ethanol and isobutanol are particularly preferred. This is because these alcohols give a higher reaction rate and a higher yield of the end product than other hydroxyl- containing compounds. The amounts of aromatic nitro compound, hydroxyl- containing compound and carbon monoxide used in the process of the present invention are desirably such that the hydroxyl group of the hydroxyl-containing compound and the carbon monoxide are present in amounts equimolar with the nitro group of the aromatic nitro compound. The main catalyst used in the process of the present invention comprises a platinum group metal and/or a compound thereof. The useful platinum group metals and compounds thereof include elemental palladium, rhodium and ruthenium as well as compounds thereof, and they may be used alone or in admixture. Specific examples thereof are elemental palladium, rhodium and ruthenium; halides, cyanides, thiocyanides, isocyanides, oxides, sulfates, nitrates and carbonyl compounds thereof; addition compounds or complexes thereof with tertiary amines such as triethylamine, pyridine, isoquinoline, etc.; complexes thereof with organic phosphorus compounds such as triphenylphosphine, etc.; and the like. These substances may be used either directly for purposes of reaction or after being supported on a'carrier such as alumina, silica, carbon, barium sulfate, calcium sulfate, asbestos, bentonite, diatomaceous earth, fuller's earth, organic ion exchange resin, inorganic ion exchange resin, magnesium silicate, aluminum silicate, molecular sieve, etc. Alternatively, this carrier may be charged into a reactor separately from the main catalyst comprising palladium, rhodium ruthenium or a compound thereof. Among the foregoing substances, palladium and its compounds are particularly preferred as the main catalyst. Specific examples thereof are metallic palladium, palladium chloride, palladium bromide, and palladium supported on carbon or alumina. The amount of platinum group metal used may vary widely according to the type of platinum group metal used and other reaction conditions. However, the platinum group metal is generally used in such an amount that the weight ratio of platinum group metal to nitro compound is in the range of 1 to 1 X 10 5 and preferably 5 X 10 1 to 1 X 10 4. In the process of the present invention, a Lewis acid and a tertiary amine are used as co-catalysts. The term "Lewis acid" as used herein denotes those compounds which are described, for example, in Jack Hine, "Physical Organic Chemistry" (McGraw-Hill Book Co., New York, 1962), and is intended to include Brhnsted acids. The useful Lewis acids include, for example, halides, oxyhalides, sulfates, acetates, phosphates, nitrates and the like of metals such as tin, titanium, germanium, aluminum, iron, copper, vanadium, nickel, zinc, cobalt, manganese and the like. Specific examples thereof are ferric chloride, ferrous chloride, stannic chloride, stannous chloride, aluminum chloride, cupric chloride, cuprous chloride, copper acetate and the like. Among these Lewis acids, ferrous chloride and ferric chloride are particularly preferred. The amount of Lewis acid used as a co-catalyst is such that the weight ratio of Lewis acid to nitro group is in the range of 2 to 2 X 10 3 and preferably 1 to 5 X X.10 2. The useful tertiary amines are aliphatic, aliphatic-aromatic, alicyclic, aromatic and heterocyclic aromatic amines. These tertiary amines may either be in the unsubstituted form or have one or more suitable substituents inert to the reaction of the present invention, such as halogen atoms, alkyl groups, aryl groups, alkenyl groups, cyano group, aldehyde group, alkoxy.groups, phenoxy groups, thioalkoxy groups, thiophenoxy groups, carbamyl group, carboalkoxy groups, thiocarbamyl group, etc. They include, for example, aliphatic tertiary amines such as trimethylamine, triethylamine, tripropylamine, tributylamine, etc.; aliphatic-aromatic amines such as N,N-dimethylaniline, N,N-diethylaniline, N,Ndiisopropylaniline, etc.; alicyclic tertiary amines such as N,N-dimethylcyclohexylamine, N,N-diethylcyclohexylamine, N,N-diisopropylcyclohexylamine, 1,4-diazabicyclo [2.2.2] octane, etc.; aromatic tertiary amines such as triphenylamine, etc.; and nitrogen-containing heterocyclic aromatic compounds such as pyridine, quinoline, isoquinoline, etc. Among these tertiary amines, nitrogen-containing heterocyclic aromatic compounds bring about a remarkable effect in enhancing the yield of the desired urethane and the reaction rate. Further specific examples of the useful nitrogen-containing heterocyclic aromatic compounds are l-methylpyrrole, 1-phenylpyrrole, l-methylimidazole, l-methylindole, l-phenylindole, indolenine, 2-isobenzazole, indolizine, l-methylcarbazole, 2-chloropyridine, 2-bromopyridine, 2-fluoropyridine, 4-phenylpyridine, 2-,3- and 4methylpyridines, 2-methyl-5-ethylpyridine; 2,6dimethylpyridine, 2,4,6-trimethylpyridine, 2-vinylpyridine, 2-styrylpyridine, 3-chloropyridine, 2,6-dichloropyridine, 2-chloro-4-methylpyridine, 4-phenylthiopyridine, 2-methoxypyridine, 4-dimethylaminopyridine, a-picolinic acid phenyl ester, y-picolinic acid methyl ester, 2,6-dicyanopyridine, a-picolinic aldehyde, a-picolinic acid amide, 5,6,7,8-tetrahydroquinoline, 2,2-dipyridyl, 2-chloroquinoline, acridine, phenanthridine, benzoquinoline, benzisoquinoline, naphthyridine, pyrazine, 4,6-dimethylpyrazine, 2,6-dimethylpyrazine, pyridazine, pyrimidine, quinoxaline, 2,3-dimethylquinoxaline, quinazoline, phthalazine, phenazine, cinnoline, pteridine and the like. These compounds may also be used in the form of a polymer such as polyvinylpyridine. The tertiary amine may be used either by adding it to a reactor separately from the reactants and other catalyst components or by previously treating it with a part of at least one catalyst component to form a suitable compound such as a complex or addition product thereof and thereafter adding this compound to the reactor. By way of example, palladium chloride, ferrous chloride and pyridine may be used either by adding them to the reactor separately from one another or by preparing a palladium chloridepyridine complex in advance and adding this complex, together with the ferrous chloride, to the reactor. They may also be used by preparing a ferrous chloridepyridine complex in advance and adding this complex, together with the palladium chloride, to the reactor. Furthermore, they may be used in the form of a mixture of complexes containing all of the palladium chloride, ferrous chloride and pyridine. Such complexes can be prepared according to any suitable procedure for the preparation of conventional complexes. For example, a complex can be'readily formed by agitating its components in a suitable solvent (such as benzene, monochlorobenzene, dichlorobenzene, ethanol, etc.) or an excess of a nitrogen-containing heterocyclic aromatic compound. A more active complex may be obtained if its preparation is carried out in an atmosphere of carbon monoxide. If necessary, the solvent or the excess of nitrogen-containing heterocyclic aromatic compound is distilled off. The amine is preferably used in an amount of 0.3 to 5 moles per mole of the anion of the Lewis acid. It is especially suitable to use the amine in an amount equimolar with the anion of the Lewis acid. If the amount of amine used is less than 0.3 mole, its effect is unsatisfactory.. On the other hand, it is possible to use more than 5 moles of the amine. In fact, the corrosion-inhibiting effect increases with the amount of amine used, but the reaction rate and yield show no significant improvement. Generally, it is unnecessary to use such a large excess of the amine. Addition of the amine permits most of the catalyst to be recovered. Although the identity of the recovered catalyst is not clear, it can be recycled either directly or after being purified by a suitable technique such as solvent cleaning.. Where a nitrogen-containing heterocyclic aromatic compound as described above, together with a Lewis acid, is used as a co-catalyst, the reaction rate can further be enhanced by adding a small amount of water. The water is added in an amount of 1 .to 70 moles and preferably 10 to 50 moles per mole of the aromatic nitro compound used as a raw material. If the amount of water added is less than 1 mole, practically no effect is produced, while if it is greater than 70 moles, the yield of the desired product is reduced greatly. The iron hydroxide which is allowed to coexist in the reaction system according to the process of the present invention can be ferrous hydroxide or ferric hydroxide, These compounds may be used alone or in admixture. Although no particular limitation is placed on the amount of iron hydroxide used, the iron hydroxide is generally used in such an amount that the weight ratio of iron hydroxide to aromatic nitro compound is in the range of 1 to 5 X 10 Although the process of the present invention can be carried out in the absence of solvent, any suitable solvent may be used. The solvents useful for this purpose include, for example, aromatic solvents such as benzene, toluene, xylene, etc.; nitriles such as acetonitrile, benzonitrile, etc.; sulfolane solvents such as sulfolane, etc.; halogenated aliphatic hydrocarbons such as 1,1,2trichloro-1,2,2-trifluoroethane, etc.; halogenated aromatic hydrocarbons such as monochlorobenzene, dichlorobenzene, trichlorobenzene, etc.; ketones; esters; tetrahydrofuran; 1,4-dioxane; l,2-dimethoxyethane; and the like. In carrying out the process of the present invention, no particular limitation is placed on the manner in which the raw materials and the catalyst components are charged to a reactor. However, the nitro compound and the Lexis acid are desirably added after being totally or partially dissolved in the.hydroxyl-containing compound or a suitable solvent. Similarly, no particular limitation is placed on the order of addition, though it is restricted by the type of apparatus used. By way of example, a suitable pressure reactor such as autoclave is charged with a hydroxyl-containing compound, a catalyst, an aromatic nitro compound and an iron hydroxide. Then, carbon monoxide is introduced under pressure. The resulting mixture is heated and stirred until the desired reaction is completed. It is also possible to eliminate the carbon dioxide formed in the course of the reaction and feed carbon monoxide intermittently or continuously. The reaction may be carried out in batchwise, semicontinuous or continuous operation. The-excess carbon monoxide remaining after completion of the reaction can be recycled to the process. The reaction temperature is generally maintained in the range of 800.to 230"C and preferably 1200 to 1900C. The reaction proceeds more rapidly as the temperature is raised, but reaction temperatures in the range of 1300 to 1700C will suffice for ordinary purposes. The reaction pressure, which is defined as the partial pressure of carbon monoxide, is in the range of 10 to 1000 kg/cm2 and preferably 30 to 500 kg/cmêG. It is one of the important effects produced by the process of the present invention that the reaction time can be shortened by adding an iron hydroxide to the reaction system. The reaction time may vary according to the nature of nitro compound used, reaction temperature, reaction pressure, type and amount of catalyst used, amount of iron hydroxide added, type of apparatus used, and the like. However, the reaction is generally carried out for a period of time ranging from 5 minutes to 6 hours. After completion of the reaction, the reaction mixture is cooled and the reactor is evacuated. Then, the reaction product is worked up according to a conventional procedure including filtration, distillation and other separation techniques, whereby the desired urethane is isolated from the unreacted materials, by-prodcts, solvent, catalyst and the like. The urethanes prepared by the process of the present invention have many uses as raw materials for the manufacture of agricultural chemicals, isocyanates and polyurethanes. The present invention is further illustrated by the following examples, but these examples are not to be construed to limit the scope of the invention. In all of these examples, the reaction was carried out by means of a magnetic stirring type autoclave made of stainless steel (SUS 32). The degrees of conversion and yields set forth in the examples were calculated from the results of analysis by gas chromatography and liquid chromatography. Example 1 Into an autoclave having a capacity of 200 ml were charged 10.92 g of 2,4-dinitrotoluene, 60 ml of absolute ethanol, 0.0038 g of palladium chloride, 1.64 g of a ferrous chloride-pyridine complex [formed by agitating a mixture (in a molar ratio of 1:2) of ferrous chloride and pyridine in ethanol], 0.21 g of water, and 1.2 g of ferric hydroxide. The resulting mixture was allowed to react at 2 an initial pressure of 90 kgjcm G and a temperature of 1650C.. The completion of the reaction was confirmed by the fact that, 130 minutes after the temperature was raised, the pressure ceased to drop. Analysis of the discharged reaction mixture revealed that 2,4-dinitrotoluene was unjetectable and the yield of diethyl toluene-2,4-dicarbamate (hereinafter referred to as diurethane) was 94.3%. Comparative Example 1 Reaction was carried out in the same manner as in Example 1, except that 0.0076 g of palladium chloride was used and the addition of ferric hydroxide was omitted. The absorption of carbon monoxide ceased in 150 minutes. Analysis of the reaction mixture revealed that the yield of diurethane was 92%. When the amount of palladium chloride was reduced to 0.0038 g, the time required for the reaction was as long as 360 minutes. Example 2 Reaction was carried out in the same manner as in Example 1, except that 0.045 g of 5 palladium-carbon was used in place of the palladium chloride (0.0038 g). The completion of the reaction was confirmed by the fact that, 180 minutes after the temperature was raised, the pressure ceased to drop. Analysis of the discharged reaction mixture revealed that the yield of diurethane was 93%. Example 3 Into an autoclave having a capacity of 200 ml were charged 10.92 g of 2,4-dinitrotoluene, 60 ml of isobutanol, 0.0076 g of palladium chloride, 0.82 g of a ferrous chloride-pyridine complex, 0.31 g of water, and 1.23 g of ferric hydroxide. The resulting mixture was allowed to react at an initial pressure of 90 kg/cm2G and a temperature of 165"C. It was recognized that, 110 minutes after the temperature was raised, the pressure ceased to drop. Analysis of the discharged reaction mixture revealed that the yield of diurethane'was 94% Comparative Example 2 Reaction was carried out in the same manner as in Example 3, except that the addition of 1.23 g of ferric hydroxide was omitted. The absorption of carbon monoxide ceased in 290 minutes. Analysis of the reaction mixture revealed that the yield of diurethane was 92%. Example 4 Reaction was carried out in the same manner as in Example 3, except that 0.51 g of anhydrous ferric chloride and 0.99 g of isoquinoline were used in place of the ferrous chloride-pyridine complex (0.82 g). Analysis of the discharged reaction mixture revealed that the yield of diurethane was 938. Example 5 Into an autoclave having a capacity of 500 ml were charged 69 g of nitrobenzene, 140 ml of methanol, 17 mg of palladium chloride, 4 g of a ferrous chloridepyridine complex, 3.2 g of water, and 3 g of ferric hydroxide. The resulting mixture was allowed to react at an initial pressure of 90 kg/cmêG and a temperature of 1600C. It was recognized that, 50 minutes after the temperature was raised, the pressure ceased to drop. Analysis of the reaction mixture revealed that nitrobenzene was undetectable and the yield of phenylurethane was 97%. Comparative Example 3 Reaction was carried out in the same manner as in Example 5, except that the addition of ferric hydroxide was omitted. The time required for the reaction was as long as 130 minutes, and the yield of phenylurethane was 97%.

Claims: CLAIMS 1. A process for the preparation of aromatic urethanes by reacting an aromatic nitro compound, a hydroxyl-ontaining organic compound having at least one hydroxyl group, and carbon monoxide at high temperature and pressure in the presence of a catalyst composed of (a) a platinum group metal and/or a compound thereof, (b) a Lewis acid and (c) a tertiary amine, characterized in that an iron hydroxide is allowed to coexist in the reaction system. 2. A process as claimed in claim 1 wherein the aromatic nitro compound is an aromatic mono- or dinitro compound selected from the group consisting of nitrobenzene, o-, m- and p-chloronitrobenzenes, 2,3- and 3,4-dichloronitrobenzenes, m- and - dinitrobenzenes, 2,4- and 2,6-dinitrotoluenes, and 1,5-dinitronaphthalene. 3. A process as claimed in claim 1 wherein the aromatic nitro compound is a substituted or unsubstituted nitrobenzene. 4. A process as claimed in claim 1 wherein the aromatic nitro compound is a substituted or unsubstituted dinitrotoluen. 5. A process as claimed in claim 1 wherein the hydroxyl-containing organic compound is methanol, ethanol or isobutanol.. 6. A process as claimed in claim 1 wherein the platinum group metal and/or a compound thereof is palladium, a palladium compound, or a compound including a palladium compound. 7. A process as claimed 'in claim 1 wherein the Lewis acid is ferrous chloride or.ferric chloride. 8. A process as claimed in claim 1 wherein the tertiary amine is a nitrogen-containing heterocyclic aromatic compound. 9. A process as claimed in claim 1 wherein the Lewis acid' and the tertiary amine comprise a complex previously formed from ferrous chloride or ferric chloride and a nitrogen-containing heterocyclic aromatic compound. 10. A process as claimed in claim 1 wherein the reaction temperature is in the range of 80" to 2300C 11. A process as claimed in claim 1 wherein 2 the reaction pressure is in the range of 10 to 1000 kg/cm2G. 12. A process as claimed in claim 6 wherein the palladium compound is palladium chloride or palladium bromide. 13. A process as claimed in claim 6 wherein the palladium is supported on a carbon or alumina carrier. 14. A process as claimed in claim 8 or 9 wherein the nitrogen-containing heterocyclic aromatic compound is pyridine, quinoline or isoquinoline. 15. A process as claimed in claim 1 wherein the iron hydroxide is ferrous chloride. 16. A process as claimed in claim 1 wherein the iron hydroxide is ferric hydroxide. 17. A process as claimed in claim 1 wherein the iron hydroxide is used in such an amount that the weight ratio of iron hydroxide to aromatic nitro compound is in the range of 1 to 5 'X 10-2

Inventors: HASEGAWA, SEIJI, MIYATA, KATSUHARU
Applicants: MITSUI TOATSU CHEMICALS, INCORPORATED
Application year: 1980
Main classification: C07C125
IPC codes: B01J23, C07C67, C07B61, B01J27, C07C271, B01J31, C07C239, C07C269