Process for the manufacture of 2-(2-hydroxyphenyl)benztriazoles

Claim 2

A process for the manufacture of a 2-(2-hydroxyphenyl)-benzotriazole of the formula I ##STR6## wherein R 1 denotes hydrogen, chlorine or bromine, R 2 denotes hydrogen, alkyl having 1 to 8 carbon atoms, alkoxy having 1 to 12 carbon atoms, alkylsulphonyl having 1 to 12 carbon atoms, acylamino having 2 to 12 carbon atoms, --SO 3 H, --COOH, bromine or chlorine, R 3 denotes hydrogen, alkyl having 1 to 12 carbon atoms, cycloalkyl having 6 to 8 carbon atoms, aralkyl having 7 to 11 carbon atoms, phenyl, chlorine or bromine, R 4 denotes hydrogen, methyl, alkoxy having 1 to 12 carbon atoms, or OH, and R 5 denotes hydrogen, alkyl having 1 to 12 carbon atoms, cycloalkyl having 6 to 8 carbon atoms, aralkyl having 7 to 11 carbon atoms, phenyl, carboxyalkyl having 2 to 13 carbon atoms, alkoxy having 1 to 12 carbon atoms, acylamino having 2 to 12 carbon atoms, chlorine or bromine, which comprises reacting in a molar ratio 1 mole of a 2-(2-hydroxyphenyl)benzotriazole-1-oxide of formula III ##STR7## with 0.5 to 0.6 moles of hydrazine hydrate in the presence of a base and at a temperature above 100° C in an ether solvent with a boiling point over 140° C and selected from the group consisting of phenyl methyl ether, phenyl ethyl ether, diphenyl ether, ethylene glycol dibutyl ether, diethylene glycol dimethyl ether, diethylene glycol diethyl ether, diethylene glycol dibutyl ether, triethylene glycol dimethyl ether, and tetraethylene glycol dimethyl ether, and removing the water formed by azeotropic distillation.

Claim 3

A process according to claim 1 wherein the ether solvent is diethylene glycol dimethyl ether or diethylene glycol diethyl ether.

Claim 4

A process according to claim 1 wherein the temperature is maintained between 100° and 180° C.

Claim 5

A process according to claim 3 wherein the temperature is maintained between 120° and 150° C.

Claim 6

A process for the manufacture of a 2-(2-hydroxyphenyl)-benzotriazole of the formula I ##STR8## wherein R 1 denotes hydrogen, chlorine or bromine, R 2 denotes hydrogen, alkyl having 1 to 8 carbon atoms, alkoxy having 1 to 12 carbon atoms, alkylsulphonyl having 1 to 12 carbon atoms, acylamino having 2 to 12 carbon atoms, --SO 3 H, --COOH, bromine or chlorine, R 3 denotes hydrogen, alkyl having 1 to 12 carbon atoms, cycloalkyl having 6 to 8 carbon atoms, aralkyl having 7 to 11 carbon atoms, phenyl, chlorine or bromine, R 4 denotes hydrogen, methyl, alkoxy having 1 to 12 carbon atoms, or OH, and R 5 denotes hydrogen, alkyl having 1 to 12 carbon atoms, cycloalkyl having 6 to 8 carbon atoms, aralkyl having 7 to 11 carbon atoms, phenyl, carboxyalkyl having 2 to 13 carbon atoms, alkoxy having 1 to 12 carbon atoms, acylamino having 2 to 12 carbon atoms, chlorine or bromine, which comprises first reducing in a molar ratio 1 mole of a 2-nitro-2'-hydroxyazobenzene of formula II ##STR9## with 0.5 moles of hydrazine hydrate in the presence of a base and at a temperature between 70° C and 100° C in an ether solvent having a boiling point over 140° C and selected from the group consisting of phenyl methyl ether, phenyl ethyl ether, diphenyl ether, ethylene glycol dibutyl ether, diethylene glycol dimethyl ether, diethylene glycol diethyl ether, diethylene glycol dibutyl ether, triethylene glycol dimethyl ether and tetraethylene glycol dimethyl ether to form a 2-(2-hydroxyphenyl)benzotriazole-1-oxide of formula III ##STR10## removing the water formed by azetropic distillation and raising the temperature of the reaction mixture to over 100° C, and adding an additional 0.5 to 0.6 moles of hydrazine hydrate to complete at a temperature over 100° C the reduction of the compound of formula III to the desired product of formula I concomitantly removing the water formed by azeotropic distillation.

Claim 7

A process for the manufacture of a 2-(2-hydroxyphenyl)-benzotriazole of the formula I ##STR8## wherein R 1 denotes hydrogen, chlorine or bromine, R 2 denotes hydrogen, alkyl having 1 to 8 carbon atoms, alkoxy having 1 to 12 carbon atoms, alkylsulphonyl having 1 to 12 carbon atoms, acylamino having 2 to 12 carbon atoms, --SO 3 H, --COOH, bromine or chlorine, R 3 denotes hydrogen, alkyl having 1 to 12 carbon atoms, cycloalkyl having 6 to 8 carbon atoms, aralkyl having 7 to 11 carbon atoms, phenyl, chlorine or bromine, R 4 denotes hydrogen, methyl, alkoxy having 1 to 12 carbon atoms, or OH, and R 5 denotes hydrogen, alkyl having 1 to 12 carbon atoms, cycloalkyl having 6 to 8 carbon atoms, aralkyl having 7 to 11 carbon atoms, phenyl, carboxyalkyl having 2 to 13 carbon atoms, alkoxy having 1 to 12 carbon atoms, acylamino having 2 to 12 carbon atoms, chlorine or bromine, which comprises first reducing in a molar ratio 1 mole of a 2-nitro-2'-hydroxyazobenzene of formula II ##STR9## with 0.5 moles of hydrazine hydrate in the presence of a base and at a temperature between 70° C and 100° C in an ether solvent having a boiling point over 140° C and selected from the group consisting of phenyl methyl ether, phenyl ethyl ether, diphenyl ether, ethylene glycol dibutyl ether, diethylene glycol dimethyl ether, diethylene glycol diethyl ether, diethylene glycol dibutyl ether, triethylene glycol dimethyl ether and tetraethylene glycol dimethyl ether to form a 2-(2-hydroxyphenyl)benzotriazole-1-oxide of formula III ##STR10## removing the water formed by azetropic distillation and raising the temperature of the reaction mixture to over 100° C, and adding an additional 0.5 to 0.6 moles of hydrazine hydrate to complete at a temperature over 100° C the reduction of the compound of formula III to the desired product of formula I concomitantly removing the water formed by azeotropic distillation.

Claim 8

A process according to claim 5 wherein the ether solvent is diethylene glycol dimethyl ether or diethylene glycol diethyl ether.

Claim 9

A process according to claim 5 wherein the temperature of the reduction reaction of a compound of formula II to a compound of formula III is maintained at 80° to 90° C.

Claim 10

A process according to claim 5 wherein the temperature of the reaction mixture is maintained during the reduction of a compound of formula III to the product of formula I between 100° and 180° C.

Claim 11

A process according to claim 8 wherein the temperature is maintained between 120° and 150° C.