Title of Invention

"A PROCESS FOR PREPARING COMPOUNDS OF 2,3-DISUBSTIUTTED 4-HYDROXYANILINES"

Abstract

A process for preparing compounds of 2,3-dlsubstltuted 4-hydroxyanlllnes of formula (1)wherein X and T Independently of one another each represent halogen and CN, said process comprising reacting (c) phenols of the formula (II) wherein X and Y are as defined above, in an aqueous medium at a temperature between 0 to 50 C with diazonium salts of the formula (III) wherein n represents a number 8 to 5 Z represents halogen, alkyl, NO2COOH, CN and SO^H.2 in the case of a2 optionally having different meanings, A represents a counterion and dT subsequent reduction of the dlazene of the formula (IV) wherein X and Y independently of one another each represent halogen andCN, n represents halogen, alkyl, NO CN, COOH and 302H,2 In the case of n 2 optionally having different meanings, with proviso -chat when n 0,X and Y are not chliarLne simultaneously; obtainaole by process. step(a) , by hydrogenatlon in the presence of inert solvents to give the target cpmpound

Full Text

The application relates to the preparation of 2,3-disubstituted 4-hydroxyanilines by the reaction of 2,3-disubstituted phenols with diazonium salts and subsequent reduction. 2,3-Disubstituted 4-hydroxyanilines are important intermediates for preparing crop protection agents and are described in DE-4 040 853. A novel process for preparing 2,3-disubstituted 4-hydroxyanilines has now been found which has very high and reproducible yields, simple purification and work-up steps and gentle reaction condition and in which no byproducts and inactive isomers are formed. The application accordingly provides a process for preparing compounds of 2,3-disubstituted 4-hydroxyanilines of formula (I) (Formula Removed) wherein X and Y independently of one another each represent halogen, and CN, a) said process comprising reacting phenols of the formula (II) (Formula Removed) wherein X and Y are as defined above in an aqueous medium at a temperature between 0 to 50°C with diazonium salts of the formula (III) (Formula Removed) wherein n represents a number 0 to 5, Z represents halogen, alkyl, N02, COOH, CN and S03H, Z in the case of n > 2 optionally having different meanings, A represents a counterion, and b) subsequent reduction of the diazene of the formula (IV), (Formula Removed) wherein X and Y independently of one another each represent halogen, and CN, n represents a number 0 to 5, Z represents halogen, alkyl, N02, CN, COOH and S03H, Z in the case of n > 2 optionally having different meanings, with the proviso that when n = 0, X and Y are not chlorine simultaneously; obtainable by process step (a), by hydrogenation in the presence of inert solvent to give the target compound. The process step a) is preferably carried out by adding a solution of the diazonium salts of the formula (III) to an aqueous solution of the phenols of the formula (II). The reaction is carded out at temperatures from 0 to SUT:. preferably 0 to 20C. The pH value of the solution is preferably higher than the pKs value of the phenol of the formula (II). The mixture is then adjusted to a pH value The process step b) is preferably carried out by hydrogenating the diazene of the formula (1V) obtainable by process step a) in the presence of inert solvents such as. preferably, water, alcohols such as methanol, ethanol or butanol, hydrocarbons such as, for example, toluene or dioxane, pyridine, dimethylformamide or mixtures of these solvents. The reaction solution obtained by process a) is preferably reacted directly according to process b) without any further purification. The hydrogenation is preferably carried out using hydrogen or hydrazines in the presence of a catalyst and, if appropriate, in the presence of auxiliaries;, or using metals or metal salts in the presence of acids, or using sodium dithionite or hydrobdic acid. If required, the reaction solution has to be neutralized (pH - 7) with mineral acids prior to the hydrogenation. Preferred embodiments of the hydrogenation and in particular catalysts and auxiliaries are described in DE-4 428 53:5 which is incorporated into the present application by reference Preference is given to a process for the catalytic hydrogenation in the presence of catalysts characterized in that the hydrogenation is carried out in the liquid phase and in the presence of a catalyst comprising at least one metal or one metal compound from the group consisting of nickel, cobalt and the noble metals and in the presence of at least one sulpho compound of the formula (V) (Formula Removed) in which R1 and R2independently of one another each represent straight-chain or branched ,-C,2-alkyl, hydroxyC,-C12-alkyl, carboxy-C,-C12-alkyl or phenyl, R' may additionally represent hydrogen or CO-C,-C12-alkyl R1 and R2 together may also represent -CH=CH-CH=CH-, -(CH2)4-, -(CH2)5- or -(CH2)2-X-(CH2)2 where X = oxygen or sulphur and n represents zero or 1. Preferred sulphur compounds of the formula (V) are those in which R, and R2 are identical and represent hydroxy-C1-C6-alkyl. Very particular preference is given to bis-(2-hydroxyethyl)sulphide which gives higher yield of compound of formula 1. Suitable noble metals for the catalyst are, for example, ruthenium, rhodium, palladium, osmium, iridium and platinum. Preference is given to platinum. N ickel, cobalt, noble metals or compounds thereof may optionally be present on a carrier. A preferred carrier material is carbon. The amount of the catalyst is not critical and may be varied within wide limits. For example, 0.02 to 3 % by weight, preferably 0.1 to 1 % by weight, of noble . 1 (a metal catalyst, based on the compound of the formula (IV) may be used. The weight ratio of sulphur compound of the formula (V) to catalyst may be, for example, 0.001 to 0.125:1. Preferably, the weight ratio is from 0.0025 to 0.025 I, particularly preferably from 0.005 to 0.0125:1. The sulphur compounds of the formula (V) may be used as individual compounds or as mixtures of various individual compounds. Preference is given to using the sulphur compounds in the form of solutions. They may be added to the reaction mixture for example in the form of a 0.01 to 1 % strength by weight solution in water or toluene. It is also possible to mix the sulphur compounds with the catalyst prior to the reaction. Particularly preferably the hydrogenation is carried out using hydrogen or hydrazine hydrate in the presence of Rartey nickel and bis(2-hydroxyethyI) sulphide or using iron powder or zinc powder in the presence of hydrochloric acid. The reaction temperatures are preferably 0 to 150°C, in particular 10 to 50°C. The reaction is preferably carried out at pressures of 1 to 100 bar, in particular 1 to 20 bar. Work-up is carried out by conventional methods, preferably by distilling off the solvents and the aniline that may still be present, setting a suitable pH value by the addition of mineral acids or bases (pH = isoelectric point of the hydroxyaniline) and purifying the crude product by washing or recrys:allization from an inert solvent, such as, for example, water or toluene. The aniline which may have been recovered can be recycled into the process. The amount of eiazonium salt used is 1 to 1.5 mol, based on 1 mol of phenol t the amount of diazene compound, an excess may be used. Metal and mineral acid are also used in at least twice the molar amount, based on the amount of diazer e compound or metal, respectively. Preference is given to using compounds of the formula (II) in which X and Y independently of one another each represent chlorine, bromine, fluorine, methoxy, ethoxy and CN. Particular preference is given to using compounds of the formula (II) in which X represents chlorine and Y represents chlorine. Preference is given to using compounds of the formula (III) in which n represents a number 0, 1, 2 or 3 and 2 represents chlorine, fluorine, bromine, N02, COOH, CM, S03H, methyl and ethyl, Z in the case of n 22 optionally having different meanings. Particular preference is given to using compounds of the formula (III) in which n represents the number 0. The compounds of the formula (III) are obtained by conventional processes, for example by reacting 1 mol of aniline of the formula" (Ilia) (Formula Removed) in which n and Z are as defined above with 1 to 5 mol, preferably 1,5 to 2 mol, of nitrite compounds, such as for example and preferably NaN02, in dilute mineral acids, such as, for example, 15 % strength hydrochloric acid, at 0 to lO^C. The process according to the invention affords 2,3-disubstituted 4-hydroxyanilines in good yield with high selectivity and purity. It is very surprising that in process step a), with the given substitution pattern, reaction takes place exclusively at the position para to the OH group. The application also provides the compounds of the formula (IV) obtainable by process a) in which X, Y, Z and n are each as defined above. The invention is illustrated by the examples below. The invention is not limited to the examples. E*aropk 1 At 0 to 5°C, a solution of 7.6 g (0.11 mol) of NaN02 in 12 ml of H20 is added dropwise to 50 ml of aqueous HC1 (15 %) and 9.8 g (0.105 mol) of anilme in a 100 ml two-neck flask fitted with internal thermometer and magnetic stirrer. Aiter 10 minutes, this diazonium salt solution is added at 5 to 10C to a solution of 16.3 g(0.1 mol) of 2,3-dichlorophenol and 20 g(0.5 mol) ofNaOH in 200 ml of H2C The mixture is allowed to warm to room temperature, stirred for an additional 4 hours, neutralized with aqueous HC1 and extracted 3 with 100 ml of ethyl acetate each. The combined organic phases are washed with NaCl solution and dried with Na2SO4, and the solvent is distilled off using a rotary evaporator. 31.8 gof (2,3-dichloro-4-hydroxyphenyl)phenyldiazene are obtained. Recrystallization from 200 ml of toluene and 10 ml of methanol affords 25.8 g (96.6 % of theory) of the pure diazene (melting point: 277-279C). Example 2 In a 500 ml three-neck flask fitted with internal thermometer, stirrer and gas inlet tube, 31.8 g (0.1 mol) of non-purified (2,3-diehloro-4-hydroxyphenyOphenyldiazene as obtained from Example 1 are dissolved in 350 ml of methanol with gentle warming. The flask is flushed with argon, and 5 g of Raney nickel and 25µl of bis(2-hydroxyethyl) sulphide are then added. At room temperature, 4640 ml (0.2 mol) of hydrogen are then applied with a pressure of about 1 bar over 2.5 hours. The reaction mixture is admixed with a little activated charcoal, stirred for a further 15 minutes and filtered over a bed of silica gel. Removal of the solvent by distillation affords 28.3 g of crude product. By heating the crude product with 100 ml of toluene, filtration with suction and drying of the solid, 17.0 g (95.5 % of theory) of pure 4-rtydroxy-2,3-dichIoroaniline can be isolated (melting point: 148-150aC) Exanip|e 3 In a 50 ml two-neck flask fitted with internal thermometer and stirrer, 3.18 g (0.01 mol) of non-purified (2,3-dichloro-4-hydroxvphenyl)phenyldiazene as obtained from Example 1 are dissolved in 20 ml of methanol with gentle warming. 1.12 g(0.02 mol) of iron powder are added, and 3.5 ml (O.04 mol) of concentrated aqueous HCI are slowly added dropwise at room temperature. The suspension is stirred at room temperature tor 30 minutes and then neutralized with NaOH and extracted with 3 10 ml of ethyl acetate. -The combined organic phases are dried with Na2SC, and the solvent is distilled off using a rotary evaporator to give 2.01 g of crude product. By heating with 10 ml of toluene, filtration with suction and drying of the solid, 1.62 g(91.0 % of theory) of pure 4-hydroxy-2,3-dichlo;roaniline can be isolated (melting point: 148-150C). Example 4 At 0 to 5°C, a solution of 7.6 g (0.11 mol) ofNaN02 in 12 ml of H2C) is added dropwise to 50 ml of aqueous HCI (15 %) and 17.0 g (0.105 mol) of 2,3-dichloroaniline in a 100 ml two-neck flask fitted with internal thermometer and magnetic stirrer. After 10 minutes, this diazonium salt solution is added at 5 to lOC to a solution of 16.3 g(0.1 mol) of 2,3-dichlorophenol and 20 g(0.5 mol) of NaOH in 200 ml of H20. The mixture is allowed to warm to room temperature, stiired for an additional 4 hours, neutralized with aqueous HCI and extracted 3 with 200 ml of ethyl acetate each. The combined organic phases are filtered through diatomaceous earth, washed with N aCl solution and dried with Na2S04, and the solvent is distilled off using a rotary evaporator. 29.5 g of diazene are obtained. Recrystallization from 200 ml of toluene affords 28.9 g (86 % of theory) of pure (2,3dichl6ro-4-hydroxyphcnyI)-2,3-dichlorophenyldiazene (melting point 197-199°C). Example $ At 0 to 5C, a solution of 7.6 g(0.11 mol) of NaN02 in 12 mJ of H2O is added dropwise to 50 ml of aqueous HC1 (15 %) and 18.1 g (0.105 mol) of sulphanilic acid in a 100 mi two-neck flask fitted with internal thermometer anc magnetic stirrer. After 1 hour, this diazonium salt suspension is added at 5 to 10C to a solution of 16.3 g(0.1 mol) of 2,3-dichlorophenol and 20 g (0.5 mol) ofNaOH in 200 ml of H2C The mixture is allowed to warm to room temperature, stirred for a farther 4 hours and neutralized with aqueous HC1, and the precipitated solid is filtered off with suction using a suction filter. Recrystallization from 200 ml of toluene and 20 ml of methanol afibrds 26.3 g (83.5 % of nheory) of pure (2,3-dichloro-4-hydroxyphenyl)-4-suIphonylphenyldiazeiie. Example 6 At 0 to 5%:, a solution of 3.8 g (0.055 mol) ofNaN02 in 6 ml of H2C) is added dropwise to 25 ml of aqueous HC1 (15 %) and 4.9 g (0.0525 mol) of aniline in a 100 ml two-neck flask fitted with internal thermometer and magnetic stirrer. After 10 minutes, this diazonium salt solution is added at 5 to 10^ to a solution of 8.15 g (0.05 mol) of 2,3-dichlorophenol and 10 g (0.25 mol) of NaOH in 100 ml of H30. The mixture is allowed to warm to room temperature, stirred for a further 1 hour and neutralized with aqueous HC1 (pH =: 7). In a 500 ml three-neck flask fitted with internal thermometer, stirrer and gas inlet tube, this solution is admixed with 300 ml of methanol, 2.5 g of Raney nickel and 15 ul of bis(2-hydroxyethyl) sulphide, and the flask is flushed with argon. At 40 to 50=0, 2300 ml of hydrogen (0.1 mol) are then applied with a pressure of about 1 bar over 1.5 hours. The reaction mixture is admixed with a little activated charcoal, stirred for a further 15 minutes and filtered over a bed of silica gel. The methanol is distilled off and pure 4-hydroxy-2,3- dichloroaniline precipitates from the aqueous solution, giving a yield of 83 %. Example J. At 0-:5°C, a solution of 3.8 g (0.055 mol) of NaN02 in 6 ml of H20 is added dropwise to 25 ml of aqueous HC1 (15 %) and 4.9 g (0.0525 mol) of aniline in a 100 ml two-neck flask fitted with internal thermometer and magnetic stirrer. After 10 min, this diazonium salt solution is added at 5 to 10X1 to a solution of of 8.15 g (0.05 mol) of 2,3-dichlorophenol and 10 g (0.25 mol) of NaOH in 100 ml of H20. The mixture is allowed to warm to room temperature, stirred for a further 1 hour and neutralized with aqueous HC1 (pH = 7). In a 500 ml three-neck flask fitted with internal thermometer, stirrer and gas inlet tube, this solution is admixed with 300 ml of methanol, 2.5 g of Raney nickel and 15 ul of bis(2-hydroxyethyl) sulphide, and the flask is flushed with argon. At 40-50^, 2300 ml of hydrogen (0.1 mol) are then applied with a pressure of about 1 bar over 1.5 h. The reaction mixture is admixed with activated charcoal, ;3tirred for a further 15 min, filtered over a bed of silica gel and adjusted to pH =: 5.7 with aqueous HC1. The methanol is distilled on; and 8.4 g(94.4 % of theory) of pure 4-hydroxy-2,3-dichloroaniiine precipitate from the aqueous solution. At 0-5^C, a solution of 7.3 g (0.105 mol) of NaN02 in 22 ml of H20 is added dropwse to 50 ml of aqueous HC1 (15 %) and 9.3 g (0.1 mol) of aniline in a 250 mi two-neck flask fitted with internal thermometer and magnetic stirrer. After 30 min, this diazonium salt solution is added slowly at 5-ICC to a solution of 16.4 g (0.1 mol) of 2,3-dichlorophenol and 12.4 g (0.31 mol) of NaOH in 100 ml of H20. The suspension is allowed to warm to room temperature and stirred for a further 1 h, and 0.5 g of Raney nickel are then added. 6 g (0.06 mol) of hydrazine hydrate are then added at 40-50'C over a period of 2 h. After the addition, stirring is continued for 1 h and the solution is filtered over a bed of silica gel. With cooling, the solution is chen adjusted to pH = 5.7 with 20 % strength 11 CI. The precipitated solid is washed with 50 ml of water and 50 ml of toluene and dried. 16.8 g(94.3 % of theory) of pure 2,3- dichloro-4-hydroxyaniline are obtained. Example 9 At 0C, a solution of 2.9 g (0.042 mol) of NaN02 in 5 ml of H2O is added dropwise to 20 ml of aqueous HCl (15 %) and 3.7 g (0.04 mol) of aniline in a 100 ml two-neck flask fitted with internal thermometer and magnetic stirrer. After 10 minutes, this diazonium salt solution is added at S-IO'C to a solution of 5.0 g (0.038 mol) of 2,3-diiluorophenol and 6.1 g (0.152 mol) of NaOH in 60 ml of H20. The solution is allowed to warm to room temperature, stirred for a further 4 h, neutralized with aqueous HCl and extracted 3 * with 50 ml of ethyl acetate each. The combined organic phases are washed with NaCl solution and dried with Na2S04, and the solvent is distilled off using a rotary evaporator. 8.4 g (94.5 % of theory) of 2.3-(difluoro-4-hydroxyphenyl)phenyldiazene (melting point 141°C) are obtained. Exgmple 31Q At room temperature, 3,5 g (0.015 mol) of (2,3-difluoro-4-hydroxyphenyl)-phenyldiazene are dissolved in 30 ml of methanol in a 100 ml i:hree-neck flask fitted with internal thermometer, stirrer and gas inlet tube. The flask is flushed with argon, and 1.5 g of Raney nickel and 25 µl of bis(2-hydroxyethyl) sµlphide are then added. 692 ml of hydrogen (0.03 mol) are then applied at room temperature with a pressure of about 1 bar. The reaction mixture is admixed with activated charcoal, stirred for a further 15 minutes and filtered over a bed of silica gel. The solvent is distilled off and the residue is washed with n-hexane, affording 2.0 g(91.9 % of theory) of 4-hydroxy-2,3-difluoroaniline. WE CLAIM: 1. A process for preparing compounds of 2,3-disubstituted 4-hydroxyanilines of formula (I) (Formula Removed) wherein X and Y independently of one another each represent halogen, and CN, said process comprising reacting c) phenols of Hie formula (II) OH (Formula Removed)wherein X and Y are as defined above in an aqueous medium at a temperature between 0 to 50°C with diazonium salts of the formula (III) (Formula Removed)wherein n represents a number 0 to 5, Z represents halogen, alkyl, N02, COOH, CN and S03H, Z in the case of n > 2 optionally having different meanings, A represents a counterion, and d) subsequent reduction of the diazene of the formula (IV), (Formula Removed)wherein X and Y independently of one another each represent halogen, and CN, n represents a number 0 to 5, Z represents halogen, alkyl, N02, CN, COOH and S03H, Z in the case of n > 2 optionally having different meanings, with the proviso that when n = 0, X and Y are not chlorine simultaneously; obtainable by process step (a), by hydrogenation in the presence of inert solvents to give the target compound. 2. A plrbcess as claimed in claim 1, wherein the hydrogenation is carried out using hydrogen or hydrazine hydrate in the presence of a conventional auxiliary at temperature of 0 to 150°C. 3. A process as claimed in claim 1, wherein in said compounds of the formula (II) X and Y independently of one another each represent chlorine, bromine, fluorine, and CN. 4. A process as claimed in claim 1, wherein when in said compounds of the formula (III) n represents a number 0,1, 2 or 3 and Z represents chlorine, fluorine, N02, COOH, CN, S03H, methyl and ethyl, Z in the case where n > 2 optionally has different meanings. 5. A process for preparing compounds of 2,3-disubstituted 4-hydroxy anilines substantially as hereinbefore described with reference to the foregoing examples.

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