Process for hydrogenating an aromatic amine in the presence of a supported ruthenium catalyst
View Patent ↗The invention relates to a process for hydrogenating an aromatic amine that has at least one amino group bound to an aromatic nucleus with hydrogen in the presence of a supported catalyst that contains at least ruthenium as active metal. The catalyst support has a BET surface area in the range from greater than 30 m 2 /g to less than 70 m 2 /g and more than 50% of the pore volume of the catalyst support is formed by macropores having a pore diameter of greater than 50 nm and less than 50% are mesopores having a pore diameter of 2 to 50 nm.
1. A supported catalyst comprising, as active metal, ruthenium alone or together with at least one metal selected from the group consisting of the first, seventh or eighth subgroup of the periodic system in an amount of 0.01 to 20 wt % of active metal, based on the supported catalyst, and a support, support, selected from the group consisting of Al 2 O 3 , TiO 2 , ZrO 2 SiO 2 MgO, ZnO, spinels, aluminium silicates and active carbons and mixtures thereof, wherein the support has a BET surface area ranging from 32 m 2 /g to 67 m 2 /g, and wherein at least 55% of the pore volume of the catalyst support are macropores having a pore diameter of greater than 50 nm and less than 45% are mesopores having a pore diameter of 2 to 50 nm.
2. A process for preparing the catalyst claimed in claim 1 , comprising applying the active metal to the support by spraying the support with at least one dilute salt solution of the active metal at a temperature of at least 80° C. and then drying the material obtained.
3. The supported catalyst according to claim 1 , wherein the active metal has a penetration depth into the support in the range of 5 to 250 μm.
4. The supported catalyst according to claim 3 , wherein the active metal has a penetration depth into the support in the range of 50 to 120 μm.
5. The supported catalyst according to claim 1 , wherein the ratio of the surface area of the active metal, determined by CO pulse chemisorption, and of the support, determined by BET, is in the range from 0.01 to 0.5.
6. The supported catalyst according to claim 5 , wherein the ratio of the surface area of the active metal, determined by CO pulse chemisorption, and of the support, determined by BET, is in the range from 0.03 to 0.06.
7. The supported catalyst according to claim 1 , wherein the penetration depth of the active metal in the support is in the range from 50 to 200 μm and wherein ruthenium is present in an amount m the range of 0.2 to 3 wt. %, based on the supported catalyst.
8. The supported catalyst according to claim 1 , wherein from 55 to 85% of the pore volume of the support is formed by macropores.
9. The supported catalyst according to claim 1 , wherein from 25 to 45 % of the pore volume of the support is formed by mesopores.