Production of aromatic amines

Abstract: Aminoanthraquinones which are materials for dyes are prepared by allowing nitroanthraquinones to react with carbon monoxide and water in a liquid phase in the presence of a homogeneous catalyst comprising rhodium compounds or ruthenium compounds and solvents therefor.

Description: The present invention relates to production of aminoanthraquinones from nitroanthraquinones, particularly production of 1-aminoanthraquinone from 1-nitroanthraquinone. More particularly, the present invention relates to production of aminoanthraquinones by allowing nitroanthraquinones to react in a liquid phase, with carbon monoxide (hereinafter referred to as CO) and water in the presence of a homogeneous catalyst comprising ruthenium compounds or rhodium compounds and solvents. The other aspect of the present invention relates to production of aromatic amines from aromatic nitro compounds excluding nitroanthraquinones (hereinafter referred to as aromatic nitro compounds) by use of CO and water. "EP-A-0,369,864 discloses production of aromatic amines by reduction of aromatic nitro compounds by use of CO and water in the presence of Ru-containing catalysts, amines and aqueous alkali solution. The process requires the presence of aqueous alkali solution. US-A-3,944,615 relates to production of aromatic amines by reducing aromatic nitro compounds with CO and water in the presence of Rh catalysts and nitrogen-containing compounds selected from tert. amines and amides". Aminoanthraquinones including 1-aminoanthraquinone are useful as intermediates of anthraquinone dyes. The 1-aminoanthraquinone is prepared, for example, by sulfonating anthraquinone before amination, or nitrating anthraquinone before reduction. Reduction of nitroanthraquinones which are the starting material of the present invention is carried out in various manners. One of the processes is reduction with metal powders such as iron in acid mediums such as sulfuric acid. Another process is reduction with, for example, alkali metal sulfide, alkali metal hydrogen-sulfide, hydrazin or glucose. Another process is allowing the nitroanthraquinones to react with ammonia until substitution with an amino group is effected. The other process is catalytic hydrogenation with, such as, palladium-carbon. None of the processes refers to production of aminoanthraquiones from nitroanthraquinones with CO and water. Many difficulties are encountered in the conventional production of the aminoanthraquinones. One of processes where anthraquinone is sulfonated and then aminated has problems, i.e., small yield and reactivity in addition to trouble on catalysts, i.e., toxicity of mercury compounds and after-treatments of wasted water. Another process where nitroanthraquinone obtained by nitration of anthraquinone is reduced has problems, too. Stoichiometric reduction with sulfides, for example, alkali metal hydrogen sulfide accompanies problems, e.g., a treatment of inorganic salts by-produced and contamination of the product with the inorganic salts. Reduction with palladium-carbon causes various side-reactions such as reduction of carbonyl groups as well as the nitro groups, thereby decreasing yield of the desired aminoanthraquinone. Furthermore, separation of the catalysts from the reduction product needs so much labor that the reduction as a whole, is not economical. Aromatic amines including aniline are useful as medicines, agricultural chemicals, dyes or pigments or intermediates thereof. The aromatic amines are produced by reducing aromatic nitro compounds in the presence of catalysts in a CO/water system. One of the processes, (1), is reduction of nitrobenzene in aqueous tetrahydrofuran/trimethylamine solution in the presence of rhodium or ruthenium catalysts (J. Am. Chem. Soc. 1978, 100, 3969). Another process, (2), is reduction of nitrobenzene or nitrotoluene in ethanol in the presence of chelate amines such as phenanthroline in addition to a rhodium or ruthenium catalyst (EP 0097592A; J. Mol. Catal., 18 , 113, 1983; J. Mol. Catal., 22 , 327, 1984). Reduction of the aromatic nitro compounds with CO and water has also problems. In (1) above, a large amount of hydrogen is by-produced and large amounts of water and CO are exhausted due to the other side reactions than the desired reduction of the nitro group. A large amount of the trimethylamine, e.g., 10³ times as much as the metal in the catalyst is employed. The ruthenium catalysts to which trimethylamine is added, e.g., Ru₃(CO)₁₂-NMe₃ aq., are specifically active to water-gas-shift reaction where hydrogen and carbon dioxide are produced from the water and the CO (A.C.S. Symp. Ser., 152 , 325, 1981). In the case of (2) above, the nitro compounds to which the process is applied are restricted, since the literature mentions that the nitro compounds to which the process in issue are able to be applied should have such inert substituents as alkyl groups, alkoxy groups or amino groups. The catalysts where rhodium is a main metal reduce ketone groups as well as olefins, in the case of reduction of benzylideneacetone (J. Mol. Catal., 22 , 327, 1984). In addition, catalytic activity is not so strong enough that high concentration of catalysts, high temperature, high pressure and a long period of time are necessary. Under such situation, investigation was made on the reaction of aromatic nitro compounds with CO and water in a liquid phase in the presence of homogeneous catalysts. As a result, homogeneous catalysts comprising rhodium compounds or ruthenium compounds and solvents are found to facilitate catalytic activity and reduction of nitro groups only with selectivity as high as substantially 100 % without damaging the anthraquinone skeleton, thereby obtaining aminoanthraquinones from nitroanthraquinones with selectivity of the nitro groups of substantially 100 %. The present invention is based on this finding. According to one of aspects of the present invention, a process for preparing aminoanthraquinones is provided where nitroanthraquinones are allowed to react with CO and water in liquid phase in the presence of a homogeneous catalyst comprising rhodium compounds or ruthenium compounds and solvents. The present invention also provides an improvement in the process for preparing aminoanthraquinones by allowing nitroanthraquinones to react with CO and water in the presence of a homogeneous catalyst comprising rhodium compounds or ruthenium compounds and solvents, which is effected in the presence of amine compounds as well in the catalyst. The present invention also provides a further improvement in the process for preparing aminoanthraquinones by allowing nitroanthraquinones to react, in a liquid phase, with CO and water in the presence of a homogeneous catalyst comprising ruthenium compounds and solvents, which is carried out by allowing copper compounds as well as the amine compounds to be present together in the catalyst. In another aspect of the present invention where aromatic nitro compounds are allowed to react with CO and water in the presence of a homogeneous catalyst comprising ruthenium compounds and solvents until aromatic amine compounds are obtained, co-presence of specific amines facilitates selective reduction of the nitro groups without losing catalytic activity and controlling by-reactions such as water-gas-shift reaction. That is, in a process where the aromatic nitro compounds excluding nitroanthraquinones are allowed to react with CO and water in the absence of an aqueous alkali solution in the presence of a homogeneous catalyst comprising ruthenium compounds and solvents to produce aromatic amine compounds, amines of the formula H NR⁴ R⁵ (II) wherein R⁴ and R⁵ are as defined below, are allowed to be present together. The present invention is explained in detail hereinunder. The present process uses CO/water as a hydrogen source. Starting compounds In one of the aspects of the present process for preparing aminoanthraquinones, it proceeds as mentioned hereinunder when the starting nitroanthraquinones are, for example, 1-nitroanthraquinone: CO (3 moles) is required to the nitro group (1 mol) and CO₂ is by-produced. The present nitroanthraquinones are compounds having one or two nitro groups on anthraquinone skeleton or those having such substituents as a sulfonate group, a halogen atom, a carboxyl group, or a hydroxyl group thereon. They are, for example, 1-nitroanthraquinone, 2-nitroanthraquinone, 1,2-, 1,3-, 1,4-, 1,5-, 1,6-, 1,7-, 1,8-, 2,3-, 2,6- or 2,7-dinitroanthraquinone, sodium 1-nitroanthraquinone-5-sulfonate, 1-nitroanthraquinone-5-carboxylic acid, 2-bromo-4-hydroxy-1-nitroanthraquinone, 2,4-dibromo-1-nitroanthraquinone, sodium 4-bromo-1-nitroanthraquinone-2-sulfonate or mixtures thereof. Preference is a nitrated mixture containing mainly 1-nitroanthraquinone obtained by mono-nitrating anthraquinone and, as by-products, dinitroanthraquinone, etc., or pure 1-nitroanthraquinone obtained by purification of the above, from an economical viewpoint. The aromatic nitro compounds, the starting material in the other aspect of the present process, are those having at least one nitro group on the aromatic ring, e.g., hydrocarbon ring such as benzene, naphthalene, anthracene, etc. or heterocyclic ring such as pyridine, quinoline, etc. The aromatic nitro compounds may have substituents such as an alkyl group, a halogen atom, an amino group, a hydroxyl group, a carboxyl group, an alkoxyl group, a cyano group or a sulfonic group. The aromatic nitro compounds usually employed are nitrobenzene, o-nitrotoluene, m-nitrotoluene, p-nitrotoluene, 2-nitro-p-xylene, o-chloronitrobenzene, m-chloronitrobenzene, p-chloronitrobenzene, p-cyanonitrobenzene, o-nitroaniline, m-nitroaniline, p-nitroaniline, o-dinitrobenzene, m-dinitrobenzene, p-dinitrobenzene, 2,4-dinitrotoluene, o-nitrophenol, m-nitrophenol, p-nitrophenol, o-nitroanisole, m-nitroanisole, p-nitroanisole, α-nitronaphthalene, β-nitronaphthalene, 2′-nitroacetophenone, 3′-nitroacetophenone, 3-nitrobenzophenone, 4-nitrobenzophenone, 4-nitroimidazole, o-nitrobenzonitrile, m-nitrobenzonitrile, p-nitrobenzonitrile, o-nitrobenzenesulfonic acid, m-nitrobenzenesulfonic acid, p-nitrobenzenesulfonic acid, o-nitrobenzenesulfonamide, m-nitrobenzenesulfonamide, p-nitrobenzenesulfonamide, o-(β-hydroxyethylsulfonyl)nitrobenzene, m-(β-hydroxyethylsulfonyl)nitrobenzene and p-(β-hydroxyethylsulfonyl)nitrobenzene. Catalysts The homogeneous catalyst for preparing the aminoanthraquinones or aromatic amine compounds is that at least a part of the rhodium compounds or ruthenium compounds is dissolved in solvents. The rhodium compounds or ruthenium compounds are used for preparing aminoanthraquinones in the first aspect of the present invention. They are, preferably, complex compounds having carbonyl ligands, compounds which are able to form rhodium·carbonyl complexes or ruthenium·carbonyl complexes in the reaction system, or compounds which are able to form complexes with phosphine or phosphite. Compounds which are able to form carbonyl complexes under the reaction conditions are, for instance, carbonyl compounds, acetylacetonate salts, carboxylic acid salts, oxides, hydroxides, halides, nitrates, phosphates or ligand compounds. Compounds which are able to form complexes with phosphine or phosphite in a reaction system form the compounds of the formulas (III) - (V): RhX(CO) n (PR₃) 3-n (III) RuH m Y 2-m (CO) p (PR₃) 4-p (IV) Ru(CO) r (PR₃) 5-r (V) wherein X is a hydrogen atom, a fluorine atom, a chlorine atom, a bromine atom or an iodine atom; Y is a fluorine atom, a chlorine atom, a bromine atom or an iodine atom; PR₃ is PPh₃, PEtPh₂, PEt₂Ph or P(OPh)₃; n is zero or an integer up to 3; m is zero or an integer up to 2; p is zero or an integer up to 4; and r is zero or an integer up to 5. Examples of the compounds of (III) - (V) are Rh(CO)₂(acac), [RhCl(COD)]₂, Rh₄(CO)₁₂, Rh₆(CO)₁₆, [Rh(CO)₂Cl]₂, Rh₂(OAc)₄, Rh(acac)₃, Rh₂O₃, RhO₂·2H₂O, Rh₂O₃· 5H₂O, Rh(NO₃)₃, Rh₂(SO₄)₃, RhCl₃, RhBr₃, RhI₃, RhH(PPh₃)₃, PhF(PPh₃)₃, RhCl(PPh₃)₃, RhBr(PPh₃)₃, RhI(PPh₃)₃, RhH(CO)(PPh₃)₂, RhF(CO)(PPh₃)₂, RhCl(CO)(PPh₃)₂, RhBr(CO)(PPh₃)₂, RhI(CO)(PPh₃)₂, RhH(CO)₂(PPh₃), RhF(CO)₂(PPh₃), RhCl(CO)₂(PPh₃), RhBr(CO)₂(PPh₃), RhI(CO)₂(PPh₃), RhH(PEtPh₂)₃, RhF(PEtPh₂)₃, RhCl(PEtPh₂)₃, RhBr(PEtPh₂)₃, RhI(PEtPh₂)₃, RhH(CO)(PEtPh₂)₂, RhF(CO)(PEtPh₂)₂, RhCl(CO)(PEtPh₂)₂, RhBr(CO)(PEtPh₂)₂, RhI(CO)(PEtPh₂)₂, RhH(CO)₂(PEtPh₂), RhF(CO)₂(PEtPh₂), RhCl(CO)₂(PEtPh₂), RhBr(CO)₂(PEtPh₂), RhI(CO)₂(PEtPh₂), RhH(PEt₂Ph)₃, RhF(PEt₂Ph)₃, RhCl(PEt₂Ph)₃, RhBr(PEt₂Ph)₃, RhI(PEt₂Ph)₃, RhH(CO)(PEt₂Ph)₂, RhF(CO)(PEt₂Ph)₂, RhCl(CO)(PEt₂Ph)₂, RhBr(CO)(PEt₂Ph)₂, RhI(CO)(PEt₂Ph)₂, RhH(CO)₂(PEt₂Ph), RhF(CO)₂(PEt₂Ph), RhCl(CO)₂(PEt₂Ph), RhBr(CO)₂(PEt₂Ph), RhI(CO)₂(PEt₂Ph), RhH(PEt₃)₃, RhF(PEt₃)₃, RhCl(PEt₃)₃, RhBr(PEt₃)₃, RhI(PEt₃)₃, RhH(CO)(PEt₃)₂, RhF(CO)(PEt₃)₂, RhCl(CO)(PEt₃)₂, RhBr(CO)(PEt₃)₂, RhI(CO)(PEt₃)₂, RhH(CO)₂(PEt₃), RhF(CO)₂(PEt₃), RhCl(CO)₂(PEt₃), RhBr(CO)₂(PEt₃), RhI(CO)₂(PEt₃), RhH(P(OPh)₃)₃, RhF(P(OPh)₃)₃, RhCl(P(OPh)₃)₃, RhBr(P(OPh)₃)₃, RhI(P(OPh)₃)₃, RhH(CO)(P(OPh)₃)₂, RhF(CO)(P(OPh)₃)₂, RhCl(CO)(P(OPh)₃)₂, RhBr(CO)(P(OPh)₃)₂, RhI(CO)(P(OPh)₃)₂, RhH(CO)₂(P(OPh)₃), RhF(CO)₂(P(OPh)₃), RhCl(CO)₂(P(OPh)₃), RhBr(CO)₂(P(OPh)₃), RhI(CO)₂(P(OPh)₃), Ru₃(CO)₁₂, H₄Ru₄(CO)₁₂, [RuCl₂(COD)] n , [RuCl₂(CO)₃]₂, Ru(CO)₅, RuO₂, RuCl₃, RuBr₃, RuI₃, Ru(acac)₃, Ru(NO)(NO₃)₃, Ru(NO)Cl₃, H₃Ru(SO₃)₂OH, RuH₂(PPh₃)₄, RuH₂(CO)(PPh₃)₃, RuH₂(CO)₂(PPh₃)₂, RuH₂(CO)₃(PPh₃), RuH₂(CO)₄, RuHCl(PPh₃)₄, RuHCl(CO)(PPh₃)₃, RuHCl(CO)₂(PPh₃)₂, RuHCl(CO)₃(PPh₃), RuHCl(CO)₄, RuCl₂(PPh₃)₄, RuCl₂(CO)(PPh₃)₃, RuCl₂(CO)₂(PPh₃)₂, RuCl₂(CO)₃(PPh₃), RuCl₂(CO)₄, RuHBr(PPh₃)₄, RuHBr(CO)(PPh₃)₃, RuHBr(CO)₂(PPh₃)₂, RuHBr(CO)₃(PPh₃), RuHBr(CO)₄, RuBr₂(PPh₃)₄, RuBr₂(CO)(PPh₃)₃, RuBr₂(CO)₂(PPh₃)₂, RuBr₂(CO)₃(PPh₃), RuBr₂(CO)₄, RuHI(PPh₃)₄, RuHI(CO)(PPh₃)₃, RuHI(CO)₂(PPh₃)₂, RuHI(CO)₃(PPh₃), RuHI(CO)₄, RuI₂(PPh₃)₄, RuI₂(CO)(PPh₃)₃, RuI₂(CO)₂(PPh₃)₂, RuI₂(CO)₃(PPh₃), RuI₂(CO)₄, RuH₂(PEtPh₂)₄, RuH₂(CO)(PEtPh₂)₃, RuH₂(CO)₂(PEtPh₂)₂, RuH₂(CO)₃(PEtPh₂), RuHCl(PEtPh₂)₄, RuHCl(CO)(PEtPh₂)₃, RuHCl(CO)₂(PEtPh₂)₂, RuHCl(CO)₃(PEtPh₂), RuCl₂(PEtPh₂)₄, RuCl₂(CO)(PEtPh₂)₃, RuCl₂(CO)₂(PEtPh₂)₂, RuCl₂(CO)₃(PEtPh₂), RuHBr(PEtPh₂)₄, RuHBr(CO)(PEtPh₂)₃, RuHBr(CO)₂(PEtPh₂)₂, RuHBr(CO)₃(PEtPh₂), RuBr₂(PEtPh₂)₄, RuBr₂(CO)(PEtPh₂)₃, RuBr₂(CO)₂(PEtPh₂)₂, RuBr₂(CO)₃(PEtPh₂), RuHI(PEtPh₂)₄, RuHI(CO)(PEtPh₂)₃, RuHI(CO)₂(PEtPh₂)₂, RuHI(CO)₃(PEtPh₂), RuI₂(PEtPh₂)₄, RuI₂(CO)(PEtPh₂)₃, RuI₂(CO)₂(PEtPh₂)₂, RuI₂(CO)₃(PEtPh₂), RuH₂(P(OPh)₃)₄, RuH₂(CO)(P(OPh)₃)₃, RuH₂(CO)₂(P(OPh)₃)₂, RuH₂(CO)₃(P(OPh)₃), RuHCl(P(OPh)₃)₄, RuHCl(CO)(P(OPh)₃)₃, RuHCl(CO)₂(P(OPh)₃)₂, RuHCl(CO)₃(P(OPh)₃), RuCl₂(P(OPh)₃)₄, RuCl₂(CO)(P(OPh)₃)₃, RuCl₂(CO)₂(P(OPh)₃)₂, RuCl₂(CO)₃(P(OPh)₃), RuHBr(P(OPh)₃)₄, RuHBr(CO)(P(OPh)₃)₃, RuHBr(CO)₂(P(OPh)₃)₂, RuHBr(CO)₃(P(OPh)₃), RuBr₂(P(OPh)₃)₄, RuBr₂(CO)(P(OPh)₃)₃, RuBr₂(CO)₂(P(OPh)₃)₂, RuBr₂(CO)₃(P(OPh)₃), RuHI(P(OPh)₃)₄, RuHI(CO)(P(OPh)₃)₃, RuHI(CO)₂(P(OPh)₃)₂, RuHI(CO)₃(P(OPh)₃), RuI₂(P(OPh)₃)₄, RuI₂(CO)(P(OPh)₃)₃, RuI₂(CO)₂(P(OPh)₃)₂, RuI₂(CO)₃(P(OPh)₃), Ru(CO)₄(PPh₃), Ru(CO)₃(PPh₃)₂, Ru(CO)₂(PPh₃)₃, Ru(CO)(PPh₃)₄, Ru(PPh₃)₅, Ru(CO)₄(PEtPh₂), Ru(CO)₃(PEtPh₂)₂, Ru(CO)₂(PEtPh₂)₃, Ru(CO)(PEtPh₂)₄, Ru(PEtPh₂)₅, Ru(CO)₄(P(OPh)₃), Ru(CO)₃(P(OPh)₃)₂, Ru(CO)₂(P(OPh)₃)₃, Ru(CO)(P(OPh)₃)₄, Ru(P(OPh)₃)₅, etc. Among them, preference are Rh₄(CO)₁₂, Rh₆(CO)₁₆, Ru₃(CO)₁₂, [RuCl₂(COD)] n , [RuCl₂(CO)₃]₂, RuO₂, Ru(acac)₃, RuCl₂(CO)₂(PPh₃)₂, RuCl₂(CO)₃(PPh₃), RuCl₂(CO)₃(P(OPh)₃), Ru(CO)₄(PPh₃), etc. An amount of the catalyst varies depending on reaction conditions but usually is 10⁻¹ - 10⁻⁵ mol per mol of the substrates for production of aminoanthraquinone. On the other hand, the catalyst used for preparing the present aromatic amines in the other aspect of the present invention is ruthenium compounds. Preference are complexes having a carbonyl ligand, compounds which are able to form ruthenium·carbonyl complex and compounds which are able to form complexes with phosphine or phosphite. In concrete, ruthenium compounds are used which are referred to in production of the aminoanthraquinones in the first aspect of the present invention. Preference is Ru₃(CO)₁₂. An amount of the catalyst is usually 10⁻¹ - 10⁻⁵ mol, sometimes less than that, per mol of the substrate, although it may vary depending on reaction conditions. Solvents The presence of solvents is essential in the present processes. Some examples of the solvents for preparing the present aminoanthraquinones or aromatic amines are alcohols such as methanol, ethanol, isopropyl alcohol, n-propyl alcohol, n-butyl alcohol, isobutyl alcohol, n-pentyl alcohol, isoamyl alcohol and tert-amyl alcohol; glymes such as diethylene glycol dimethyl ether, triethylene glycol dimethyl ether, tetraethylene glycol dimethyl ether, 2-methoxyethanol, 2-ethoxyethanol, 2-butoxyethanol, ethylene glycol, diethylene glycol, ethylene glycol dimethyl ether, ethylene glycol diethyl ether and ethylene glycol monoethyl ether acetate; ethers such as tetrahydrofuran, 1,4-dioxane and anisole; and ketons such as acetone, methylethylketone and methylisobutylketone. Preference for preparing the aminoanthraquinones in the first aspect of the present invention are methanol, ethanol, isopropyl alcohol, n-butyl alcohol, diethylene glycol dimethyl ether, triethylene glycol dimethyl ether and ethylene glycol monoethyl ether acetate. Preference for preparing the aromatic amines in the other aspect of the present invention are methanol, ethanol, isopropyl alcohol, n-butyl alcohol, diethylene glycol dimethyl ether, triethylene glycol dimethyl ether and acetone. More preference are methanol, ethanol, diethylene glycol dimethyl ether and acetone. Amine compounds and copper compounds So far as preparing aminoanthraquinones in the first aspect of the present invention is concerned, the homogeneous catalyst comprising the rhodium compounds or ruthenium compound and the solvents in the presence or absence of amine compounds, facilitates catalytic activity for preparing the aminoanthraquinones. Co-presence of the amine compounds mentioned above in the same catalyst as above greatly improves the catalytic activity. Furthermore, the use of the copper compounds mentioned below in addition to the amine compounds above in the case of homogeneous catalyst comprising the ruthenium compounds and the solvents improves more and more catalytic activity. The amine compounds used in the first aspect of the present process, i.e., for preparing the present aminoanthraquinones are at least one amine compound selected from amines having the formula (I) NR¹R²R³ (I), pyridines, imidazoles and chelate diamines. In the amines of the formula (I), R¹, R² and R³ are each a hydrogen atom, an alkyl group or an aryl group but all of R¹, R² and R³ are not hydrogen atoms. When one of R¹, R² and R³ is a hydrogen atom and R¹, R² and R³ all together form a ring, mention may be made of, for example, -(CH)₄-, -(CH₂)₄-, -(CH₂)₅- or -(CH₂)₂-NH-(CH₂)₂-. The pyridines are compounds having a pyridine skeleton and the imidazoles are compounds having an imidazole skeleton. The chelate diamines are chelate amines having two nitrogen atoms at 2,2′-, 1,2-, 2,3-, 9,10-, 1,3-, 1,4-, 1,5-, 1,8- or 1,10-positions. Examples of the amine compounds used for preparing the present aminoanthraquinones in the first aspect of the invention are amines having C₁₋₅ alkyl groups such as trimethylamine, triethylamine, triisopropylamine, tri-n-propylamine, tri-n-butylamine, dimethylamine, diethylamine, diisopropylamine, di-n-butylamine, ethylamine, isopropylamine, n-propylamine, n-butylamine or ethyldiisopropylamine; amines having aryl groups such as aniline, 1-aminoanthraquinone, 2-aminoanthraquinone, N-methylaniline or N-ethylaniline; cyclic amines such as pyrrole, pyrrolidine, piperidine or piperazine; pyridines such as pyridine, α-picoline, β-picoline, γ-picoline, 4,4-dimethylaminopyridine, 2-cyanopyridine, 3-cyanopyridine, 4-cyanopyridine, 2-hydroxypyridine, 3-hydroxypyridine or 4-hydroxypyridine; imidazoles such as imidazole, N-methylimidazole, N-ethylimidasole, benzimidazole, 2-methylbenzimidazole or N-methylbenzimidazole; chelate diamines such as 9,10-diaminophenanthrene, 1,10-phenanthroline, 3,4,7,8-tetramethyl-1,10-phenanthroline, 3,4,5,6,7,8-hexamethyl-1,10-phenanthroline, o-phenylenediamine, N,N,N′N′-tetramethyl-o-phenylenediamine, 2,3-naphthalenediamine, 1,8-naphthalenediamine, 1,5-naphthalenediamine, 1,8-bis(dimethylamino)naphthalene or 2,3-bis(dimethylamino)naphthalene. Preferable amine compounds are triethylamine, tri-n-propylamine, diethylamine, diisopropylamine, 1-aminoanthraquinone, piperidine, 4-cyanopyridine, 2-methylbenzimidazole, 1,8-bis(dimethylamino)naphthalene and N,N,N′,N′-tetramethyl-o-phenylenediamine. The amine compounds are usually used in such an amount of 0.01 to 500, preferably 0.01 to 300 times, in mol as much as metal atoms in the catalyst. Amines used in the other aspect of the present process, i.e., for preparing the present aromatic amines are those having the formula (II) NHR⁴R⁵ (II) wherein R⁴ and R⁵ are each a hydrogen atom, an alkyl group which may have substituents, a cycloalkyl group which may have substituents, an aralkyl group, an aryl group which may have substituents, but both R⁴ and R⁵ are not hydrogen atoms. The substituents are an alkyl group, a halogen atom, a hydroxyl group or an alkoxy group. When R⁴ and R⁵ together form a ring, mention is made of -(CH)₄-, -(CH₂)₄-, -(CH₂)₅- or -(CH₂)₂-NH-(CH₂)₂-. Examples of the amines of the formula (II) are C₁ - C₈ alkyl amines which may have substituents, such as methylamine, ethylamine, n-propylamine, iso-propylamine, n-butylamine, iso-butylamine, tert.-butylamine, n-pentylamine, n-hexylamine, n-heptylamine, n-octylamine, dimethylamine, diethylamine, di-n-propylamine, di-isopropylamine, di-n-butylamine, di-isobutylamine, di-n-pentylamine, di-n-hexylamine, di-n-heptylamine, di-n-octylamine, ethylisopropylamine, 3-dimethylaminopropanol, 2-aminopropanol, 2-ethylhexylamine, 3-methoxypropylamine, 3-ethoxypropylamine, 2-chloroethylamine, bis(2-chloroethyl)amine or 3-chloroethylamine; C₅ - C₆ cycloalkyl amines which may have substituents, such as cyclohexylamine, cyclopentylamine, dicyclohexylamine or 2,3-dimethylcyclohexylamine; aralkylamines such as benzylamine, dibenzylamine, N-benzylmethylamine or N-benzylethanolamine; arylamines which may have substituents, such as aniline, diphenylamine, o-toluidine, m-toluidine, p-toluidine, o-chloroaniline, m-chloroaniline, p-chloroaniline, o-anisidine, m-anisidine, p-anisidine, o-aminophenol, m-aminophenol or p-aminophenol; cyclic amines such as pyrrole, pyrrolidine, piperidine or piperazine. Preference for preparing the aromatic amine compounds are diethylamine, diisopropylamine, di-n-butylamine, n-butylamine, pyrrolidine, piperidine, piperazine, dicyclohexylamine, benzylamine and o-chloroaniline. The amines of the formula (II) are usually employed in an amount of 0.01 to 500, preferably, 0.01 to 100 times in mol as much as the atoms in the catalyst. Copper compounds used in the first aspect of the present process for producing aminoanthraquinones are copper compounds having a valence of one or two, i.e., oxides, halides, hydroxides, carboxylates, sulphates, nitrates and carbonates. For instance, they are cuprous oxide, cupric oxide, cuprous chloride, cupric chloride, cuprous bromide, cupric bromide, cuprous iodide, cupric iodide, copper hydroxide, copper acetate, copper oxalate, copper formate, copper naphthenate, copper stearate, copper sulphate, copper nitrate and copper carbonate. Preference are cupric oxide, copper carbonate, cupric bromide and copper acetate. The copper compounds are usually employed in such an amount as 0.01 - 500 times, preferably 0.01 - 100 times in mol in terms of copper atom as much as the metal atoms in the catalyst. Reaction conditions Reaction temperature is usually 0 to 250 °C, preferably 20 to 200 °C. CO pressure is not critial but usually 1 to 100 atm., although higher pressure may be employed. One of the aspect of the present process for preparing aminoanthraquinones proceeds under CO/H₂O in a liquid phase, keeping catalytic activity at high level. Reduction of the nitro group only is effected with high selectivity, resulting in obtaining the desired aminoanthraquinones with high yield. The aminoanthraquinones are readily separated by filtration from the catalysts which are recycled with ease, since the aminoanthraquinones are hardly dissolved and precipitated in the crystal form. Another aspect of the present process for preparing aromatic amine compounds enjoys production of the corresponding aromatic amine compounds with high selectivity and high yield, since nitro groups only are selectively reduced while catalyst activity is not substantially damaged. Reduction of the nitro group proceeds with priority, while such side-reactions as water-gas-shift reaction are controlled. Examples Example 1 In an autoclave (100 cc) made of stainless steel and equipped with a stirrer drivable by magnetic force, were charged Ru₃(CO)₁₂ (0.005 mmol), methanol (15 ml), water (5 ml) and 1-nitroanthraquinone (3.0 g, 10.2 mmol, produced by Tokyo Kasei, Japan, purity: 86.2 %, anthraquinone: 13.8 %). The contents were stirred under CO (20 Kg/cm²) (2.0 x 10⁶ Pa) at 150 °C for 2 hours. Reaction product was assayed by gas chromatography and liquid chromatography. Identification was made by comparison of retention time of chromatogram, elemental assay and GC-MS. Index of catalytic activity was based on total turn-over number (TN). Total turn-over number (TN) = amount of aminoanthraquinones or aromatic amine compounds produced (mmol)/amount of catalyst (mmol) The assay of the reaction product showed that there was only 1-aminoanthraquinone (4.8 mmol) and no by-product. Selectivity of nitro group = 100 %, TN = 969. The same assay procedure was repeated in the following examples and comparison examples. Examples 2 - 40 Example 1s were repeated except that the solvents mentioned in Table 1 were used in place of the methanol and the amine compounds mentioned in Table 1 were added to. Assay of the reaction products showed that there were only 1-aminoanthraquinones and no by-products. Selectivity of nitro group each: 100 %. The results are shown in Table 1. Examples 41 - 43 Example 1s were repeated except that Rh₆(CO)₁₆ (0.005 mmol) and the solvents mentioned in Table 2 were used in place of the Ru₃(CO)₁₂ (0.005 mmol) and the methanol, respectively. Assay of the reaction products showed that there were only 1-aminoanthraquinones and no by-products. Selectivity of nitro group each: 100 %. The results are shown in Table 2. Example Nos. Solvents 1-Aminoanthraquinones produced (mmol) TN 41 Methanol 6.12 1224 42 Ethylene glycol Monoethyl ether 5.79 1158 43 Ethanol 5.10 1020 Examples 44 - 48 Example 42s were repeated except that amine compounds shown in Table 3 were added to. Assay of the reaction products showed that there were only 1-aminoanthraquinones and no by-products. Selectivity of nitro group each = 100 %. The results are shown in Table 3. Example Nos. Amine compounds Mol ratios 1) 1-Aminoanthraquinones produced (mmol) TN 44 Triethylamine 50 7.53 1506 45 Tri-n-propylamine 10 7.50 1500 46 9,10-Diaminophenanthrene 10 7.11 1422 47 Imidazole 1 6.78 1356 48 Diisopropylamine 50 9.12 1824 Note: Mol ratios = amine compounds (mmol)/metal atoms in catalyst (mmol) Example 49 Example 1 was repeated except that Rh₄(CO)₁₂ (0.005 mmol), 3,4,7,8-tetramethyl-1,10-phenanthroline (0.005 mmol) and ethanol were used in place of the Ru₃(CO)₁₂ (0.005 mmol), 1-nitroanthraquinone and methanol, respectively. Assay of the reaction product showed that there was only 1-aminoanthraquinone (1.72 mmol) and no by-product. Selectivity of nitro group = 100 %, TN = 345. Example 50 Example 49 was repeated except that 4,4-dimethylaminopyridine (1.5 mmol) and 2-methoxyethanol were used in place of the 3,4,7,8-tetramethyl-1,10-phenanthroline (0.005 mmol) and ethanol. Assay of the reaction product showed that there was only 1-aminoanthraquinone (1.68 mmol) and no by-product. Selectivity of nitro group = 100 %, TN = 337. Examples 51 - 55 Example 1s were repeated except that triethylamine (1.5 mmol) each was added and the reactions were carried out under reaction temperatures and CO pressures as shown in Table 4 in place of 150 °C and 20 Kg/cm², (2.0 x 10⁶ Pa) respectively. In Examples 53 - 55, reactions were effected for 90 min. in place of the 2 hours. Assay of the reaction products showed that there were only 1-aminoanthraquinones and no by-products. Selectivity of nitro group each: 100 %. The results are shown in Table 4. Example Nos. Reaction temperatures (°C) CO pressures (Kg/cm²) 1-Amino anthraquinones produced (mmol) TN 51 120 20 3.11 622 52 180 20 9.85 1971 53 150 10(9.8 x 10⁵ Pa) 3.22 643 54 150 20 4.26 852 55 150 30(2.9 x 10⁶ Pa) 5.81 1162 Examples 56 and 57 Example 1s were repeated except that 0.002 mmol each of Ru₃(CO)₁₂ was used in place of the 0.005 mmol, triethylamine (1.5 mmol) each was added to, 180 °C was used in place of the 150 °C and the solvents shown in Table 5 were used in place of the methanol. Assay of the reaction products showed that there were only 1-aminoanthraquinones and no by-products. Selectivity of nitro group each = 100 %. The results are shown in Table 5. Example Nos. Solvents 1-Aminoanthraquinones produced (mmol) TN 56 Methanol 5.41 2705 57 Diethylene glycol Dimethyl ether 4.70 2348 Example 58 Example 1 was repeated except that Ru₃(CO)₁₂ (0.01 mmol) was used in place of the (0.005 mmol), triethylamine (1.5 mmol) was added to and ethanol was used in place of the methanol. Assay of the reaction product showed that there was only 1-aminoanthraquinone and no by-product. Selectivity of nitro group = 100 %, TN = 1020. Example 59 Example 28 was repeated except that 5 hours for reaction period of time was used in place of the 2 hours. Assay of the reaction product showed that there was only 1-aminoanthraquinone and no by-product. Selectivity of nitro group = 100 %, TN = 2040. Assay of gas obtained after the reaction was over gave CO₂ 30.2 mmol H₂ 0.02 mmol. An amount of H₂ was very small. Example 60 Example 14 was repeated except 5 hours for reaction period of time, Ru₃(CO)₁₂ (0.01 mmol) and pyrrolidine (0.045 mmol) were used in place of 2 hours, 0.005 mmol and 0.015 mmol (= 0.005 mmol x 3), repsectively. Assay of the reaction product showed that there was only 1-aminoanthraquinone (10.2 mmol) and no by-product. Selectivity of nitro group = 100 %, TN = 1020. Assay of gas obtained after the reaction was over gave CO₂ 34.2 mmol H₂ 0.08 mmol. An amount of H₂ was very small. Example 61 In an autoclave (110 cc) made of stainless steel and equipped with a stirrer drivable by magnetic force, were charged Ru₃(CO)₁₂ (0.01 mmol), methanol (15 ml), water (5 ml), triethylamine (1.5 mmol) and nitroanthraquinone (2 g). Stirring was made under CO (20 Kg/cm²) (2.0 x 10⁶ Pa) at 150 °C for 6 hours. The nitroanthraquinone contained mononitroanthraquinone (74.9 %), dinitroanthraquinone (23.5 %) and anthraquinone (1.6 %). Assay of the reaction product showed that there were no nitro groups left unchanged but only the corresponding 1-aminoanthraquinone, 2-aminoanthraquinone, 1,5-diaminoanthraquinone and 1,8-diaminoanthraquinone. Selectivity of nitro group = 100 %. Yield of aminoanthraquinones = 99 % or more. Example 62 Example 61 was repeated except that isopropyl alcohol was used in place of the methanol. Assay of the reaction product showed that there were no nitro groups left unchanged in the reaction product but only the corresponding aminoanthraquinones. Selectivity of nitro group = 100 %. Yield of aminoanthraquinones = 99 % or more. Example 63 Example 61 was repeated except that diethylene glycol dimethyl ether and piperidine (0.09 mmol) were used in place of the methanol and triethylamine (1.5 mmol). Assay of the reaction product showed that 98 % of the 1-nitroanthraquinone was reduced to produce 1-aminoanthraquinone and the nitro groups all of the other nitroanthraquinones were reduced to produce the corresponding aminoanthraquinones. Selectivity of nitro group = 100 %. Yield of aminoanthraquinones = 98 % or more. Example 64 In an autoclave (260 ml) equipped with a thermometer, a stirrer with turbine blades, cooling pipes and a CO gas feeder at the bottom, were charged Ru(acac)₃, (0.10 mmol), ethylene glycol monoethyl ether acetate (60 ml), water (23 ml), aminoanthraquinone (0.11 g) and nitroanthraquinone (10 g). Stirring (800 rpm) was made under CO (20 Kg/cm², 500 ml/min.) at 170 °C for 3 hours. The nitroanthraquinone fed contained 74.9 % of mononitroanthraquinone, 23.5 % of dinitroanthraquinone and 1.6 % of anthraquinone. The aminoanthraquinone fed contained 74.9 % of monoaminoanthraquinone, 23.5 % of diaminoanthraquinone and 1.6 % of anthraquinone. Assay of the reaction product showed that there were no nitro group left unchanged but only the corresponding 1-aminoanthraquinone, 2-aminoanthraquinone, 1,5-diaminoanthraquinone and 1,8-diaminoanthraquinone. Selectivity of nitro group = 100 %. Yield of aminoanthraquinones = 99.9 % or more. Example 65 Example 64 was repeated except that Ru₃(CO)₁₂ (0.04 mmol), n-butyl alcohol, the same aminoanthraquinone (88 mg) and 2 hours of reaction period of time were used in place of the Ru(acac)₃, ethylene glycol monoethyl ether acetate, 0.11 g and 3 hours, respectively. Assay of the reaction product showed that there were no nitro group left unchanged but only the corresponding 1-aminoanthraquinone, 2-aminoanthraquinone, 1,5-diaminoanthraquinone and 1,8-diaminoanthraquinone. Selectivity of nitro group = 100 %. Yield of aminoanthraquinones = 86 %. Example 66 Example 65 was repeated except that ethylene glycol monoethyl ether acetate was used in place of the n-butyl alcohol. Assay of the reaction product showed that there were no nitro group left unchanged but only the corresponding 1-aminoanthraquinone, 2-aminoantraquinone, 1,5-diaminoanthraquinone and 1,8-diaminoanthraquinone. Selectivity of nitro group = 100 %. Yield of aminoanthraquinones = 90 %. Examples 67 - 70 Example 66s were repeated except that [RuCl₂(COD)] n (0.1 mmol, produced by Kanto Kagaku, Japan) or RuO₂ (0.1 mmol) to which the additives shown in Table 6 were added and 3 hours for reaction period of time in place of the Ru₃(CO)₁₂ and 2 hours. Assay of the reaction products showed that there were no nitro group left unchanged and only the corresponding 1-aminoanthraquinones, 2-aminoanthraquinones, 1,5-diaminoanthraquinones and 1,8-dimainoanthraquinones. Selectivity of nitro group = 100 %. The results are shown in Table 6 wherein TNs per nitro group were used as indexes for catalytic activities. Example Nos. Catalysts Additives (mmol) TN 67 [RuCl₂(COD)] n Triphenylphosphine 0.32 412 68 [RuCl₂(COD)] n Triphenylphosphite 0.10 375 69 [RuCl₂(COD)] n ----- 264 70 RuO₂ Triphenylphosphine 0.08 402 Examples 71 - 74 In an autoclave (110 ml) made of stainless steel and equipped with a stirrer drivable with magnetic force were charged Ru(CO)₁₂ (0.005 mmol), ethylene glycol monoethyl ether acetate (15 ml), water (5 ml), triethylamine (1.5 mmol), nitroanthraquinone (2 g) and one of the copper compounds shown in Table 7. Stirring was effected under CO (20 Kg/cm²)(2.0 x 10⁶ Pa) at 150 °C for 2 hours. The nitroanthraquinone above was the same as in that in Example 64. Assay of the reaction products showed that there were only aminoanthraquinones and no by-products. Selectivity of nitro group = 100 %. Total turn-over numbers per nitro group were used as indexes of catalyst activities. The results are shown in Table 7. Example Nos. Copper compounds Mol ratios TN 71 Cupric oxide 20 1679 72 Copper carbonate 16 1532 73 Cupric bromide 30 1203 74 Copper acetate 25 1193 Example 75 Example 72 was repeated except that Ru₃(CO)₁₂ (0.003 mmol), nitroanthraquinone (3 g), temperature of 180 °C and CO (50 Kg/cm²) (4.9 x 10⁶ Pa) were used in place of the Ru(CO)₁₂ (0.005 mmol), nitroanthraquinone (2 g), 150 °C and 20 Kg/cm², respectively. Assay of the reaction product showed that there were no nitro group left unchanged but only the corresponding 1-aminoanthraquinone, 2-aminoanthraquinone, 1,5-diaminoanthraquinone and 1,8-diaminoanthraquinone, without any by-product. Selectivity of nitro group = 100 %. TN = 4932. Examples 76 - 80 In an autoclave (50 cc) made of stainless steel and equipped with a stirrer drivable by magnetic force were charged Ru₃(CO)₁₂(0.003 mmol), ethanol (5 ml), water (2 ml), one of amines shown in Table 8 and nitrobenzene (about 5 mmol). Sitrring was made under CO (20 Kg/cm²) (2.0 x 10⁶ Pa) at 150 °C for 100 min. Assay of the reaction products showed that there were anilines without any by-products. The results are shown in Table 8. Comparison Example 1 Example 76 was repeated except that 3,4,7,8-tetramethyl-1,10-phenanthroline (0.0045 mmol) was used in place of the diisopropylamine. Assay of the reaction product showed that there was only aniline without any by-product. The result is shown in Table 8. Examples 81 - 87 Example 76s were repeated except that ethanol (10 ml), water (4 ml), nitrobenzene (about 10 mmol) and amines shown in Table 9 were used in place of the ethanol (5 ml), water (2 ml), nitrobenzene (about 5 mmol) and diisopropylamine, respectively. Assay of the reaction products showed that there were anilines without by-proudcts. The results are shown in Table 9. Example Nos. Amines Mol ratios TN 81 Pyrrolidine 5 1573 82 Piperidine 3 1524 83 Diisopropylamine 50 1683 84 Diisopropylamine 70 2016 85 Diethylamine 25 1510 86 Di-n-butylamine 35 1833 87 Dicyclohexylamine 50 1694 Examples 88 - 90 Example 81s were repeated except that one of the amines shown in Table 10 and reaction temperature of 180 °C were used in place of the pyrrolidine and 150 °C, respectively. Assay of the reaction products showed that there were only anilines and no by-products. The results are shown in Table 10. Example Nos. Amines Mol ratios TN Yields % 88 Piperidine 3 3422 >97 89 Diisopropylamine 50 3421 >98 90 Diethylamine 25 3448 >98 Examples 91 - 94 Example 84s were repeated except that one of the solvents shown in Table 11 was used in place of the ethanol. Assay of the reaction products showed that there were only anilines and no by-products. The results are shown in Table 11. Example Nos. Solvents TN 91 Methanol 1707 92 Isoamyl alcohol 1665 93 Diethylene glycol dimethyl ether 1944 94 Acetone 1919 Example 95 In an autoclave (110 cc) equipped with a stirrer were charged Ru₃(CO)₁₂ (0.01 mmol), diisopropylamine (1.5 mmol), diethylene glycol dimethyl ether (15 ml), water (5 ml) and o-chloronitrobenzene (5 mmol). Stirring was effected under CO (20 Kg/cm²) (2.9 x 10⁶ Pa) at 150 °C for 2 hours in order to allow a reaction to proceed. After the reaction was over, assay of the reaction product showed that there was only o-chloroaniline and no by-product. Yield of o-chloroaniline = 99 % or more. Assay of the gas after the reaction was over gave H₂ 0.4 mmol CO 72.3 mmol CO₂ 14.7 mmol. Example 96 Example 95 was repeated except that an autoclave (50 cc) equipped with a stirrer drivable by magnetic force and o-bromonitrobenzene were used in place of the autoclave (110 cc) and o-chloronitrobenzene. Assay of the reaction product showed that there was only o-bromoaniline (yield = 99 % or more) and no by-product. Example 97 Example 96 was repeated except that p-chloronitrobenzene was used in place of the o-bromonitrobenzene. Assay of the reaction product showed that there was only p-chloroaniline (yield = 99 % or more) and no by-products. Example 98 Example 96 was repeated except that p-cyanonitrobenzene was used in place of the o-bromonitrobenzene. Assay of the reaction product showed that there was only p-aminobenzonitrile (yield = 99 % or more) and no by products. Example 99 Example 96 was repeated except that p-nitrobenzophenone was used in place of the o-bromonitrobenzene. Assay of the reaction product showed that there was only p-aminobenzophenone (yield = 99 % or more) and no by-products. Comparison Example 2 Example 96 was repeated except that acetophenone was used in place of the o-bromonitrobenzene. Assay of the reaction product showed that there was only acetophenone with no other compounds. Comparison Example 3 Example 96 was repeated except that phenylacetylene was used in place of the o-bromonitrobenzene. Assay of the reaction product showed that there was only phenylacetylene with no other compounds. Comparison Example 4 Example 95 was repeated except that benzonitrile was used in place of the o-chloronitrobenzene. Assay of the reaction product showed that there was only benzonitrile with no other compounds. Assay of the gas after the reaction was over gave H₂ 0.4 mmol CO 94.9 mmol CO₂ - .

Claims: A process for preparing aminoanthraquinones which comprises allowing nitroanthraquinones to react, in a liquid phase, with carbon monoxide and water in the presence of a homogeneous catalyst comprising rhodium compounds or ruthenium compounds and solvents therefor. A process for preparing aminoanthraquinones according to claim 1 wherein amine compounds are allowed to be present together in the catalyst. A process for preparing aminoanthraquinones according to claim 2 wherein the amine compounds are at least one of amine compounds selected from amines defined below, pyridines, imidazoles and chelate diamines, said amines having the formula NR¹R²R³ (I) whrein R¹, R² and R³ each is a hydrogen atom, an alkyl group or an aryl group but they are not hydrogen atoms at the same time, and they may form together a ring. A process for preparing aminoanthraquinones according to claim 2 wherein both amine compounds and copper compounds are allowed to be present in the homogeneous catalyst comprising the ruthenium compounds and the solvents therefor. A process for preparing aminoanthraquinones according to claim 1 wherein the rhodium compounds are complexes having carbonyl ligands, those which are capable of forming carbonyl complexes in the reaction system or those which are capable of forming complexes with phosphine or phosphite. A process for preparing aminoanthraquinones according to claim 5 wherein the rhodium compounds are Rh₄(CO)₁₂ or Rh₆(CO)₁₆. A process for preparing aminoanthraquinones according to claim 1 wherein the ruthenium compounds are complexes having carbonyl ligands, those which are capable of forming carbonyl complexes in the reaction system or those which are capable of forming complexes with phosphine or phosphite. A process for preparing aminoanthraquinones according to claim 7 wherein the ruthenium compounds are Ru₃(CO)₁₂, [RuCl₂(COD)] n , [RuCl₂(CO)₃]₂, RuO₂, Ru(acac)₃, RuCl₂(CO)₂(PPh₃)₂, RuCl₂(CO)₃(PPh₃), RuCl₂(CO)₃[P(OPh)₃] or Ru(CO)₄(PPh₃). A process for preparing aminoanthraquinones according to claim 3 wherein the amine compounds are amines of the formula (I) having C₁₋₅ alkyl groups. A process for preparing aminoanthraquinones according to claim 9 wherein the amine compounds are triethylamine, tri-n-propylamine, diethylamine or diisopropylamine. A process for preparing aminoanthraquinones according to claim 3 wherein the amine compounds are amines of the formula (I) having aryl groups. A process for preparing aminoanthraquinones according to claim 11 wherein the amine compounds are 1-aminoanthraquinone. A process for preparing aminoanthraquinones according to claim 3 wherein the amine compounds are cyclic amines. A process for preparing aminoanthraquinones according to claim 13 wherein the amine compounds are pyrrole, pyrrolidine, piperidine or piperazine. A process for preparing aminoanthraquinones according to claim 3 wherein the amine compounds are pyridines. A process for preparing aminoanthraquinones according to claim 15 wherein the amine compounds are 4-cyanopyridine. A process for preparing aminoanthraquinones according to claim 3 wherein the amine compounds are imidazoles. A process for preparing aminoanthraquinones according to claim 17 wherein the amine compounds are 2-methylbenzimidazole. A process for preparing aminoanthraquinones according to claim 3 wherein the amine compounds are chelate diamines. A process for preparing aminoanthraquinones according to claim 19 wherein the amine compounds are 1,8-bis(dimethylamino)naphthalene or N,N,N′N′-tetramethyl-o-phenylenediamine. A process for preparing aminoanthraquinones according to claim 2 wherein the amine compounds are employed in such an amount of 0.01 - 500 times in mol as much as metal atoms of the catalyst. A process for preparing aminoanthraquinones according to claim 21 wherein the amine compounds are 0.01 - 300 times in mol as much as metal atoms of the catalyst. A process for preparing aminoanthraquinones according to claim 4 wherein the copper compounds are oxides, halides, hydroxides, carboxylates, sulfates, nitrates or carbonates. A process for preparing aminoanthraquinones according to claim 23 wherein the copper compounds are cupric oxide, copper carbonates, cupric bromide or copper acetate. A process for preparing aminoanthraquinones according to claim 4 wherein the copper compounds are employed in such an amount of 0.01 - 500 times in mol in terms of copper atom as much as metal atoms of the catalyst. A process for preparing aminoanthraquinones according to claim 25 wherein the copper compounds are 0.01 - 100 times in mol in terms of copper as much as metal atoms of the catalyst. A process for preparing aminoanthraquinones according to claim 1 wherein the nitroanthraquinones are 1-nitroanthraquinone, 2-nitroanthraquinone, 1,2-, 1,3-, 1,4-, 1,5-, 1,6-, 1,7-, 1,8-, 2,3-, 2,6- or 2,7-dinitroanthraquinone, or mixtures thereof. A process for preparing aminoanthraquinones according to claim 27 wherein the nitroanthraquinones are 1-nitroanthraquinone. A process for preparing aminoanthraquinones according to claim 1 wherein the reaction is effected at 0° - 250°C. A process for preparing aminoanthraquinones according to claim 1 wherein the carbon monoxide is under pressure of 1 - 100 atm. A process for preparing aromatic amine compounds which comprises allowing aromatic nitro compounds excluding nitroanthraquinones to react with carbon monoxide and water in the absence of an aqueous alkali solution and in the presence of a homogeneous catalyst comprising ruthenium compounds and solvents therefor as well as amines having the formula (II) HNR⁴R⁵ (II) wherein R⁴ and R⁵ each is a hydrogen atom, an alkyl group which may have substituents, a cycloalkyl group which may have substituents, an aralkyl groups or an aryl group which may have substituents but both R⁴ and R⁵ are not hydrogen atoms, and R⁴ and R⁵ may form together a ring. A process for preparing aromatic amine compounds according to claim 31 wherein the ruthenium compounds are complexes having carbonyl ligands, those which are capable of forming carbonyl complexes in the reaction system or those which are capable of forming complexes with phosphine or phosphite. A process for preparing aromatic amine compounds according to claim 32 wherein the ruthenium compounds are Ru₃(CO)₁₂. A process for preparing aromatic amine compounds according to claim 31 wherein the amines of the formula (II) are diethylamine, diisopropylamine, di-n-butylamine, n-butylamine, pyrrolidine, piperidine, piperazine, benzylamine, o-chloroaniline or dicyclohexylamine. A process for preparing aromatic amine compounds according to claim 31 wherein the amines are used in such an amount of 0.01 - 500 times in mol as much as metal atoms of the catalyst. A process for preparing aromatic amine compounds according to claim 35 wherein the amine are used in such an amount of 0.01 - 100 times in mol as much as metal atoms of the catalyst. A process for preparing aromatic amine compounds according to claim 31 wherein the reaction is conducted at 0° - 250°C. A process for preparing aromatic amine compounds according to claim 31 wherein the carbon monoxide is under pressure of 1 - 100 atom.

Inventors: ISHINO MASARU, NOMURA KOTOHIRO, ISHINO, MASARU, NOMURA, KOTOHIRO
Applicants: SUMITOMO CHEMICAL CO, SUMITOMO CHEMICAL COMPANY, LIMITED
Application year: 1990
Main classification: C07C209
IPC codes: C07C221, C07C209, C07C255