PROCESS FOR PRODUCING BENZOPHENONE-AZINES

Abstract: A process for producing a benzophenone-azine which comprises reacting a benzophenone-imine with molecular oxygen in the presence of a catalyst composed of dissolved copper in amount of 0.0005 - 0.01 mol per 1 mol of the benzophenone-imine in terms of copper atom.

Description: PROCESS FOR PRODUCING BENZOPHENONE-AZINES This invention relates to a process for producing a benzophenone-azine which comprises reacting a benzophenoneimine with molecular oxygen in the presence of dissolved copper in amount of 1/100 - 1/2000 mol per 1 mol of the benzophenone-imine in terms of copper atom. A benzophenone-azine is useful as an intermediate for producing hydrazine from benzophenones. Many processes for producing benzophenone-azines by oxidizing benzophenone-imines are known in the art. A process for producing a benzophenone-azine by oxidizing benzophenoneimines in the presence of a copper halide, particularly cuprous chloride is known from USP No. 2,870,206. A process for producing a benzophenone-azine by oxidizing a benzophenone-imine in the presence of excess amount of pyridine by using copper (II) halide methoxide is known from Japanese Patent Publication (laid open) No. 147047/1978. Japanese Patent Publication (laid open) No. 71045/1978 discloses that copper acetates, copper thiocyanate, copper cyanide and the like are useful for preparing benzophenoneazines from benzophenone-imines. Japanese Patent Publication (laid open) No. 131987/1977 discloses that a high molecular catalyst obtained by coordinating cuprous halide in a resin, the functional group of which is pyridines, is useful for oxidizing benzophenone-imines. However, in these processes an expensive copper salt in a high concentration that is, 0.01 - 1 mol of copper salt per 1 of benzophenone-imine, is used. When copper salts are used as liquid phase homogeneous catalyst, it is necessary to control the valency of the copper, to keep the ratio of copper ion to anion constant, or to introduce a ligand, such as expensive pyridine into the catalyst for keeping the reaction activity of the catalyst. In addition, since the prior catalyst is dissolved in the reaction solution, the prior processes need complicated operations to recover copper salt as a catalyst from the solution. For example, operations, such as separation of the copper salt from the solution and regeneration of the copper catalyst, etc. are necessary. So, the cost of equipment increases and a loss of energy is incurred in operation. Further, expensive anticorrosive material should be used for the equipment in order to prevent corrosion of the equipment by the halogen constituting the catalyst. Accordingly, the processes are unsuitable from an industrial point of view. When high molecular catalyst coordinating copper ion is used, copper ion is released from the catalyst during the reaction and the copper ion is not completely reabsorbed even at the end of the reaction. In addition, special resins having unidentate pyridine as functional group must be used. Therefore, the process is not satisfactory from an industrial point of view. We carried out research for overcoming the above shortcoming and found that a catalyst selected from the group consisting of transition elements belonging to the fourth, fifth and sixth periods of the Periodic Table, typical elements belonging to the fifth and sixth periods of the Periodic Table and compounds of these metals are effective for converting a benzophenone imine to the corresponding benzophenone-azine. We also found metallic copper to be excellent for converting a benzophenone-imine to the corresponding benzophenone-azine with respect to selectivity and activity (see British patent application 8015492, of which Examples 20 to 55 illustrate the use of various forms of copper, copper alloy and copper oxide) and at the time of that discovery considered that the active catalyst was undissolved copper, undissolved copper alloy or undissolved copper compound. We have since carried out further research to find a better catalyst. As a result, unexpectedly, we found that a small amount of dissolved copper is a useful catalyst for producing benzophenone-azines from benzophenone-imines. Accordingly, the present invention provides a process for producing a benzophenone-azine having the formula EMI3.1 wherein R1 and R2 may be the same or different, and each of R1 and R2 is independently aliphatic, alicyclic or aromatic hydrocarbon having 1 - 10 carbon atoms, EMI3.2 wherein 4 5 6 R6, R7, R8, Rg, R10 and R11 are indepen- dently alkyl having 1 - 10 carbon atoms; halogen; hydroxy; nitro; or cyano; or R1 and R2 when taken together form a single bond or substituted or unsubstituted methylene wherein the substituent is methyl; m is O or integer of 1 - 5; and n is O or integer of 1 - 5, which comprises reacting a benzophenone-imine having the formula EMI3.3 wherein R1, R2, m and n are as defined above with molecular oxygen in the presence of a catalyst composed of dissolved copper in an amount of 0.0005 - 0.01 mol per 1 mol of the benzophenone-imine in terms of copper atom. By the term "dissolved copper" is meant copper being present in the form of complex. The chemical structure of the complex can not be specified, because the benzophenone-imine solution contains various compounds, depending on processes for producing benzophenone-imines and on copper salts employed as a copper source. Benzophenone-imines are represented by formula II. Examples of benzophenone-imines employed in the practice of this invention include benzophenone-imine, 2-, 3- or 4-methylbenzophenone-imine, 2-, 3- or 4-ethylbenzophenone-imine, 2-, 3- or 4-n-propylbenzophenone-imine, 2-, 3-, or 4-isopropylbenzophenone-imine, 2-, 3- or 4-n-butylbenzophenoneimine, 2-, 3- or 4-iso-butylbenzophenone-imine, 2-, 3- or 4-tert.-butylbenzophenone-imine, 2-, 3- or 4-amylbenzophenoneimine, 2-, 3- or 4-decylbenzophenone-imine, 2-, 3- or 4methoxybenzophenone-imine, 4-cyclohexylbenzophenone-imine, 4-phenylbenzophenone-imine, 2,4-dimethylbenzophenone-imine, 2, 3-dimethylbenzophenone-imine, 3,4-dimethylbenzophenoneimine, 2,4-diethylbenzophenone-imine, 2, 3-diethylbenzophenone- imine, 3,4-diethylbenzophenone-imine, 2-methyl-4-ehylbenzo- phenone-imine, 2-methyl-4-butylbenzophenone-imine, 2,2'-, 3,3'-, 4,4'-, 2,3'-, 2,4'- or 3,4'-dimethylbenzophenone-imine, 2-, 3- or 4-chlorobenzophenone-imine, 2-chloro-4-methylbenzo- phenone-imine, 4-chloro-4'-methylbenzophenone-imine, 4,4'dichlorobenzophenone-imine, 4-nitrobenzophenone-imine, 2,4 dinitrobenzophenone-imine, 4-hydroxybenzophenone-imine, 4-N; N- dimethylaminobenzophenone-imine, 4-acetylbenzophenone-imine, 4-methoxycarbonylbenzophenone-imine, 4-N ,N-dimethylcarbamcy1- benzophenone-imine, 4-hydroxybenzophenone-imine, 4-cyanobenzophenone-imine, fluorenone-imine, anthron-imine and 10-methyl anthron-imine. Other benzophenones are also usable in the practice of this invention. The benzophenone-imines represented by formula II may be prepared by reacting the corresponding benzophenones with ammonia by reacting benzonitrile with aryl magnesium bromide or by dehydrating diaryl aminoalcohol. The benzophenoneimines prepared by any one of these processes can be used in the present invention as a raw material. Benzophenone-imine and benzophenone-imines having monoor di-substituent on a 1 and/or 2 position are preferred. Dissolved copper catalyst employed in the practice of this invention excludes copper dissolved in benzophenone-imine in the form of copper halide, copper thiocyanide, copper cyanide and copper sulfate. The dissolved copper can not be separated from the benzophenone-imine by filtration or centrifuging. The copper dissolved in a benzophenone-imine may be in the state of metallic copper, monovalent copper or divalent copper. Materials which contain copper and can dissolve in a benzophenone-imine can be used as a raw material for preparing the catalyst of this invention. In general, metallic copper, copper alloy and copper compounds may be used as the raw material. Metallic copper may be used as it is. Metallic copper supported on a carrier may be used. Copper compounds which may be used as the raw material include, for example, copper oxides, copper hydroxide, copper carbonate, copper sulfide, organic acid salts of copper, salts of phenols and copper and copper complexes. Examples of the copper oxide include cuprous oxide and cupric oxide. Basic copper carbonate is also included in the copper carbonate. Examples of organic acid constituting the organic acid salts of copper include aliphatic carboxylic acids or substituted aliphatic carboxylic acids, such as formic acid, acetic acid, oxalic acid, lactic acid and pyruvic acid, alicyclic carboxylic acids, such as naphthenic acid; and aromatic carboxylic acids or substituted aromatic carboxylic acids, such as benzoic acid, toluic acid, phthalic acid, isophthalic acid, terephthalic acid, alicylic acid, benzoylbenzoic acid, oxybenzoylbenzoic acid, and anthranilic acid. 'Examples of phenols constituting the salts of phenols and copper include phenols or substituted phenols, such as phenol, cresol xylenol, trimethylphenol, catechol, resorcin, hydroquinone, aminophenol and hydroxybenzophenone. Examples of compounds which form complexes with copper include amines or its derivatives, such as ethylenediamine, pyridine, piperidine, and imidazole; aminopolycarboxylic acids, such as iminodiacetic acid, nitrilotriacetic acid, N,N'ethylenediaminediacetic acid, N'-hydroxyethyl-N,N,N'-triacetic acid, and ethylenediamine tetraacetic acid; amino acids, such as glycine; ss-ketones or oxine, such as acetyl acetone, and 8-hydroxyquinoline; and phthalocyanine. The catalyst of this invention can be prepared by merely dissolving metallic copper or a copper compound (sometimes referred to as copper component) in a benzophenone-imine. However, when the solubility of copper component in a benzophenone-imine is not sufficient, or in order to increase dissolving speed, a mixture of copper component and a benzophenone-imine may be heated and/or stirred. Contact of the mixture of copper component and a benzophenone-imine with oxygen hydrogen or ammonia effectively accelerates dissolving of copper component in a benzophenone-imine, -for example, in order to dissolve metallic copper in a benzophenone-imine, it is preferable to use oxygen. Whereas in order to dissolve cuprous oxide, cupric oxide, copper hydroxide or copper carbonate it is preferable to use hydrogen; and in order to dissolve copper hydroxide or copper carbonate, it is preferable to use ammonia. An inert gas, such as nitrogen, argon or helium may be used with oxygen, hydrogen or ammonia. Air, carbon monoxide, carbon dioxide or water vapor may be used under specific conditions in order to accelerate dissolving of copper component in a benzophenone-imine. The amount of the catalyst employed in this invention is much less than the amount of catalyst employed in the prior art processes. The catalyst of this invention is used in an amount of 1/2000 - 1/100 mol per 1 mol of benzophenoneimine, preferably 1/1800 - 1/150 mol, and more preferably 1/1600 - 1/200 mol. Presence of undissolved metallic copper or copper compounds does not inhibit the reaction of the benzophenone-imine with molecular oxygen. The reaction conditions under which the oxidation reaction of benzophenone-imine is carried out depend on activity of catalyst employed and state of the reaction system. In general, the reaction temperature is in the range of 60 to 3000C, preferably 70 to 2500C and more preferably 90 to 2300C. The reaction time depends on activity at the catalyst and the degree of conversion of benzophenone-imines. In general, the time is in the range of 0.1 hour to several tens of hours. The molecular oxygen may include pure oxygen, oxygen enriched gas and mixture of oxygen and nitrogen, namely air. The reaction pressure may be reduced pressure, atmospheric pressure or super atmospheric pressure. In general, when oxygen alone is used as molecular oxygen, the reaction pressure is in the range of 1 to 20 atms. When air is used as molecular oxygen, the reaction pressure is in the range of 1 - 40 atms. The way of introducing oxygen or an oxygen-containing gas into the reaction system is not critical. The oxygen gas or oxygen-containing gas may be introduced into the reaction system by blowing the gas into the liquid continuously, or it may be present as a super atmospheric gas in an enclosed reaction system containing the liquid. Preferably, the molecular oxygen is blown into the liquid in order to prevent hydrolysis of benzophenone-imines. It is preferable to use dry oxygen gas or dry oxygen-containing gas as molecular oxygen. The reaction method may be continuous or batchwise. In order to Increase the rate of reaction, it is preferable to use a multi-vessel continuous process, the so called cascade process. The reaction of this invention proceeds without using' any solvent. However, a solvent may be used in order to promote dissolution of the benzophenone-azines or to keep the reaction system in a solution state. It is preferable to use a solvent which is not subjected to decomposition in the ammoxydation of benzophenones and in the oxidation of benzophenone-imines, and promotes dissolution of the benzophenone-azines formed by oxidation reaction of benzophenone-imines and which does not mix well with water. Examples of the solvents include benzene, toluene, o-, m- or p-xylene, ethylbenzene, mesitylene, cumene, pseudocumene, amylbenzene, aromatic hydrocarbons having 6 - 16 carbon atoms and mixtures thereof, chlorobenzene, 0-, m- or p-dichlorobenzene, nitrobenzene, o-, m- or p-dinitrobenzene, o-, m- or p-chlorotoluene, diphenyl, phenanthrene, anisole, diphenyl ether, acetophenone, dibenzoyl, benzophenone, hexane, heptane, cyclohexane, cyclooctane, ethylcychlohexane, ethylene dichloride, tetrachloroethylene, diisopropyl ether, buthyl acetate, butyl benzoate, phenyl benzoate, dimethyl phthalate, pyridines and the like. It is preferable in the present invention to use benzophenone-imines obtained from benzophenones. In this case, the unreacted benzophenone acts as a solvent. Although according to the present invention the amount of the catalyst employed is much less than that in the prior art processes, the reaction proceeds with a high selectivity and while maintaining high catalytic activity. In addition, since the amount of catalyst employed in this invention is very small, only a small amount of chemicals need be employed for recovering dissolved copper from the reaction system in which the reaction has been effected. For example, in case of recovering dissolved copper from the reaction system by extraction, the amount of a sulfuric acid solution, hydrochloric acid or ammonia solution employed for extraction is small. Furthermore, such recovering operation can be effected even by using small scale apparatus or facilities. The present invention is further illustrated by the following Examples. However, this invention is not limited by these examples, and changes and modifications within the spirit and scope of this invention can be effected. Yield is by mol percent. In these examples, selectivity means ratio of mol of object product obtained to mol of raw material employed. The percents and parts on proportion of components are by weight, unless otherwise specified. Example 1 Into a reactor was charged 30 grs. (imine 39.2 milli mol) of benzophenone-imine (benzophenone-imine 23.6%; the remainder was benzophenone). While blowing an oxygen gas, the solution was heated to 140 C. To the solution was added 1.5 grs. of commercially available powdered copper (produced by Wako Jun-yaku Co.). Thereafter, oxygen was blown from the bottom or reactor at one atmospheric pressure for 2 hours at speed of 100 ml/min. with stirring Undissolved copper powder was removed by using glass filter (filter size G-4). The filtrate was analyzed by gas chromatography. The analysis showed that benzophenone-azine was formed in yield of 28% (5.5 milli mol). Colorimetry analysis showed that dissolved copper (250 ppm) was contained in the system. Thereafter, the filtrate (imine:copper = 1:1/240 by mol) was charged into the reactor and then the reaction was continued for an additional 2 hours by blowing oxygen into the filtrate under the same conditions as above. The gas chromatography analysis showed that benzophenone-azine was formed in yield of 92% (18.0 milli mol). No by-products were detected. Example 2 Into a reactor was chraged 30 grs. (imine 39.2 milli mol) of benzophenone-imine (benzophenone-imine 23.68; the remainder was benzophenone). To the solution was added 1.5 grs. of commercially available powdered copper (produced by Wako Jun-yaku Co.). Thereafter, nitrogen was blown from the bottom at one atmospheric pressure for 1 hour at a velocity of 100 ml/min. with stirring. Undissolved copper powder was removed by using glass filter (filter size G-4). The filtrate was analyzed by gas chromatography. The analysis showed that benzophenone-azine in amount of less than 0.1% was formed. Colorimetry analysis showed that dissolved copper (77 ppm) was contained in the system. Thereafter, the filtrate (imine:copper = 1:1/1080 by mol) was charged into the reactor. While blowing oxygen from the bottom of reactor at one atmospheric pressure at a speed of 100 ml/min. the reaction was effected for 2.5 hours at 1400C. Gas chromatography analysis showed that benzophenoneazine was formed in a yield of 35% (6.9 milli mol). Example 3 Commercially available powdered copper (produced by Wako Jun-yaku Co.) (2 g) was heated to 1400C in electric furnace and then heat-treated for 3 hours while blowing air thereinto. Dissolving of copper in benzophenone-imine, introducing of nitrogen and filtering of undissolved copper repeated in the same way as in Example 1 except that 1.5 g of heattreated copper was used. The filtrate (imine:copper = 1:1/300 by mol) was charged into a reactor. The reaction was effected in the same way as in Example 2. Gas chromatography analysis showed that benzophenone-azine was formed in yield of 97% (19 milli mol). Example 4 Into a reactor were charged 30 g of benzophenone-imine (benzophenone-imine 23.98; the remainder was benzophenone) and 0.5 g of commercially available powdered cupric oxide (Wako Jun-yaku Co.). When nitrogen was blown into the mixture at one atmospheric pressure at a speed of 100 ml/min., the mixture was heated to 1400C. When the temperature raised to 1400C, supply of nitrogen was discontinued. The hydrogen was blown into the mixture for 40 minutes at speed of 200 ml/min with stirring. Solid material containing undissolved copper component was removed from the solution by using glass filter (filter size G-4). Colorimetry analysis showed that copper concentration in the filtrate was 700 ppm. Gas chromatography analysis showed that benzophenone-azine was formed in a yield of 0.3%. Thereafter, the filtrate (imine:copper = 1:1/120 by mol) was charged into the reactor while blowing oxygen fro the bottom of reactor at one atmospheric pressure at speed of 100 ml/min. the reaction was effected for 1 hour at 14O0C. Gas chromatography analysis showed that benzophenone-azine was formed in a yield of 30% (5.9 milli mol). Example 5 Into a reactor was charged 40 g of benzophenone-imine (benzophenone-imine 23.08; the remainder was benzophenone). The solution was heated at 1400chile blowing nitrogen thereinto. Cuprous oxide (2 g) (Wako Jun-yaku Co.) was added to the solution, and then the mixture was stirred for 2 hours. The solid material was removed from the solution by using glass filter (filter size G-4). Thereafter, the filtrate (imine:copper = 1:1/270 by mol) was charged into the reactor while blowing oxygen from the bottom of reactor at one atmospheric pressure at sp-ced of 100 Nml/min. The reaction was effected for 2.0 hours at io0OC with stirring. Gas chromatography analysis showed that benzophenone-azine was formed in a yield of 80%. Example 6 Into a reactor was charged 30 g (imine 41.8 milli mol) of benzophenone-imine (benzophenone-imine 25.2%; the remainder was benzophenone). The solution was heated to 1400C while blowing oxygen into the solution. Copper formate, Cu(HCOO)2. 2H2O (21 mg) as a catalyst was added to the solution (m olar ratio of imine:copper in the solution was 1:1/385) while blowing oxygen into the solution from the bottom of reactor at speed of 100 ml/min. The reaction was effected at 1400C at one atmospheric pressure for 2.5 hours. Gas chromatography analysis showed that benzophenone-azine was formed in a yield of 85% (17.8 milli mol). Example 7 The procedure of Example 6 was repeated except that cupric acetyl acetonate (2.5 mg) was used as a catalyst and that the reaction was effected for 3 hours the yield of benzophenone-azine was 9% (1.9 milli mol). Example 8 Into a reactor was charged 30 g (imine 41.8 milli mol) of benzophenone-imine (benzophenone-inine 25.2%; the remainder was benzophenone). Copper hydroxide, Cu(OH)2 (9.0 mg, 0.092 milli mol) was added to the solution while blowing an ammonia gas (20 ml/min.). The mixture was heated to 1600C and then was stirred for 1 hour to dissolve the copper component in benzophenone-imine. While blowing oxygen into the solution from the bottom of reactor at speed of 100 ml/min., the reaction was effected at 1400C at one atmospheric pressure for 1 hour. Gas chromatography analysis showed that benzophenone-azine was formed in a yield of 36% (7.5 milli mol). Example 9 The procedure of Example 1 was repeated- except that 30 g of 4-methyl-benzophenone-imine (4-methyl-benzophenoneimine was 20.08; the remainder was 4-methyl-benzophenone) was used. The filtrate was analyzed by colorimetry analysis. The yield of 4,4'-dimethylbenzophenone-azine was 25% (3.9 milli mol) and concentration of dissolved copper was 220 ppm. The filtrate (imine:cooper = 1:1/220 by mol) was charged into the reactor. While blowing oxygen at a velocity of 100 ml/min. the reaction was effected for 2 hours with stirring. Gas chromatography analysis showed that 4,4'dimethyl-benzophenone-azine was formed in yield of 93%. Example 10 The filtrate was prepared by repeating the procedure of Example 1. The filtrate (imine:copper = 1:1/180 by mol) was charged into autoclave, and then was heated to 1400C. 2 While blowing air under pressure of 4 Kg/cm2G into the mixture at a velocity speed of 750 ml/min. (as calculated for OOC and 1 atm), the reaction was effected for 2 hours. The yield of benzophenone-azine was 92%. Example 11 Into a flask equipped with agitator were charged 2.0 Kg of benzophenone-imine (benzophenone-imine 23.6%; the remainder was benzophenone) and200 g of commercially available powdered copper (Wako Jun-yaku Co.-). The reaction was effected at 1400C for 2 hours while blowing pure oxygen into the mixture. 45.3 percent of benzophenone-imine employed was converted to benzophenone-azine. The agitation was discontinued, so solid material was settled. The supernatant liquid was separated from the solid material. The supernatant liquid (concentration of imine = 12.9% by weight, dissolved copper = 305 ppm and imine:copper = 1:1/150 by mol) was used as a raw material. The raw material (120 g) was charged into a stainless steel bubbling column having sparger at its bottom, and then was heated to 1300C. Air under pressure was charged at speed of 6Nl/min. While maintaining the pressure of the column at 2 Kg/cm2G. After the reaction was continued for 1 hour, the remainder of the raw material was charged at a velocity speed of 40 g/hr by using a pump and the reaction product was discharged at a velocity of 40 g/hr from its bottom so as to keep the liquid level constant. Average residence time of the solution was 3 hours. Sampling was effected periodically and the sample was analyzed. The reaction was continued for 45 hours. The average yield of benzophenone-azine was 94.7%. Control Test 1 The procedure of Example 6 was repeated except that commercially available cuprous chloride (Wako Jun-yaku Co.) was used. The molar ratio of imine to dissolved copper was 1:1/260. The yield of benzophenone-azine was 1.5% (0.3 milli mol). Example 12 The procedure of Example 6 was repeated except that 34 mg (0.099 milli mol) of cupric benzoate (Kanto Chemical Co.) was used. The reaction was effected for 1 hour. The yield of benzophenone-azine was 32% (6.7 milli mol). Example 13 20 ml of an aqueous cupric formate solution containing 1.9 g of cupric formate was blended with 40 ml of ethanol solution containing 4 g (20 milli mol) of 2-hydroxybenzophenone at 600C to form crystalline material. The crystalline material was removed by filtration, washed with water, and washed with ethanol, and then vacuum-dried, whereby copper (II) salt of 2-hydroxybenzophenone was obtained. The salt contained Cu 13.2%, C 68.5%, and H 4.15%. The procedure of Example 6 was repeated except that 48 mg (0.100 milli mol) the copper (II) salt of 2-hydroxy benzophenone prepared above was used. The reaction was effected for 2.5 hours. The yield of benzophenone-azine was 18% (3.8 milli mol). Examples 14 - 17 The procedures of Example 6 were repeated except that each of catalysts shown in Table 1 was used. The results are shown in Table 1. Table 1 EMI14.1 <tb> Ex. <SEP> Catalyst <SEP> reaction <SEP> yield <SEP> of <SEP> benzo <tb> No. <SEP> Catalyst <SEP> time <SEP> phenone-azine <tb> <SEP> ethylene <SEP> diamine <SEP> tetraacetic <SEP> <SEP> . <SEP> <tb> 14 <SEP> acid <SEP> disodium <SEP> copper <SEP> salt <SEP> 2 <SEP> hrs. <SEP> mol) <tb> <SEP> (Dai-ichi <SEP> Kagaku <SEP> Yakuhin <tb> <SEP> Co.) <SEP> 40 <SEP> mg <SEP> (0.100 <SEP> milli <SEP> mol) <tb> <SEP> Cupric <SEP> acetate, <SEP> basic <tb> <SEP> 21% <SEP> (4.4 <SEP> milli <tb> 15 <SEP> Cu(CH3COO)2.CuO6H2O <SEP> 1 <SEP> hr. <SEP> mol) <SEP> <tb> <SEP> 18 <SEP> mg <SEP> (0.049 <SEP> milli <SEP> mol) <tb> 16 <SEP> Cupric <SEP> sulfide <SEP> 18% <SEP> (3.8 <SEP> milli <tb> 13 <SEP> 13 <SEP> mg <SEP> (0.136 <SEP> milli <SEP> mol) <SEP> 1 <SEP> hr. <SEP> mol) <tb> 17 <SEP> Phthalocyanine <SEP> Blue <SEP> B <SEP> 3 <SEP> hrs. <SEP> 15% <SEP> (3.1 <SEP> milli <tb> <SEP> 58 <SEP> mg <SEP> (0.101 <SEP> milli <SEP> mol) <SEP> 3 <SEP> hrs. <SEP> mol) <tb>

Claims: We claim: 1. A process for producing a benzophenone-azine having the formula EMI15.1 wherein R1 and R2 may be the same or different, and each of R1 and R2 is independently aliphatic, alicyclic or aromatic hydrocarbon having 1 - 10 carbon atoms, EMI15.2 wherein R3, 5 6 R6, R7, R81 Rg, R10 and R11 are indepen- dently alkyl having 1 - 10 carbon atoms; halogen; hydroxy; nitro; or cyano; or R1 and R2 when taken together form a single bond or substituted or unsubstituted methylene wherein the substituent is methyl: m is O or integer of 1 - 5: and n is O or integer of 1 - 5 which comprises reacting a benzophenoneimine having the formula EMI15.3 wherein R1, R2, m and n are as defined above with molecular oxygen, characterized in that the reaction is carried out in the presence of a catalyst composed of dissolved copper in amount 0.0005 - 0.01 mol per 1 mol of the benzophenoneimine in terms of copper atom. 2. The process as defined in Claim 1 wherein the dissolved copper is the one obtained by dissolving in the benzophenoneimine at least one material selected from the group consisting of metallic copper, copper alloys, copper compounds and mixtures thereof. * 3. The process as defined in Claim 1 wherein the copper compound is selected from the group consisting of copper oxides, copper hydroxide, copper carbonate, copper sulfide, organic acid salts of copper, salts of phenols and copper, copper complexes and mixtures thereof. 4. The process as defined in Claim 3 wherein the organic acid constituting the organic acid salt of copper is selected from the group consisting-of aliphatic carboxylic acids and substituted aliphatic carboxylic acids. 5. The process as defined in Claim 3 wherein the organic acid constituting the organic acid salt of copper is selected from the group consisting of aromatic carboxylic acids and substituted aromatic carboxylic acids. 6. The process as defined in Claim 3 wherein the copper complex is selected from the group consisting of complexes of copper and amine, derivatives of amine, aminopolycarboxylic acid, amino acids, ss-diketone or oxine and copper phthalocyanine. 7. The process as defined in Claim 2 wherein the dissolved copper is the one obtained by dissolving in the benzophenoneimine a material selected from metallic copper, copper alloy and copper compound by contacting the material with a gas. 8. The process as defined-in Claim 7 wherein the dissolved copper is the one obtained by dissolving in the benzophenoneimine metallic copper by contacting the copper with bxygen or an oxygen-containing gas. 9. The process as defined in Claim 7 wherein the dissolved copper is the one obtained by dissolving in the benzophenoneimine a material selected from cuprous oxide, cupric oxide, copper hydroxide, and copper carbonate by contacting the material with hydrogen or a hydrogen containing gas. 10. The process as defined in Claim 7 wherein the dissolved copper is the one obtained by dissolving in the benzophenoneimine a material selected from the group consisting of copper hydroxide and copper carbonate by contacting the material with ammonia gas. 11. The process as defined in Claim 1 wherein the dissolved copper is in the form ofcomplex.

Inventors: AOKI, OSAMU, ISSHIKI, TOMIYA, KOHZAHI, TOSHIAKI, SAKAGUCHI, SHUZABU, TAKEDA, NORIO
Applicants: MITSUBISHI GAS CHEMICAL COMPANY, INC.
Application year: 1981
Main classification: C07C109
IPC codes: B01J23, C07C253, C07C251, C07C241, C07C255, C07C67