1,2-diaminocyclohexane and chemical process
Disclosed is a process for the preparation of 1,2-cycloaliphatic diamines from 1,2-aromatic diamines. In one embodiment, the process provides a method for making 1,2-diaminocyclohexane by the reaction of 1,2-phenylenediamine contained in a polar, protic solvent with hydrogen in the presence of a supported rhodium catalyst, ammonia, and an inorganic borohydride, and having enhanced overall conversion and selectivity.
1. A process for making 1,2-cycloaliphatic diamines comprising contacting a 1,2-aromatic diamine with hydrogen in polar, protic solvent in the presence of an inorganic borohydride, ammonia and a heterogeneous catalyst comprising at least one selected from the group consisting of Ru, Rh, Pd and Pt.
2. The process of claim 1 wherein said polar, protic solvent has the structure ROH where R is hydrogen or an alkyl group.
3. The process of claim 2 wherein said alkyl group has from 1 to 6 carbons.
4. The process of claim 1 wherein said inorganic borohydride is an alkali metal borohydride.
5. The process of claim 4 wherein said inorganic borohydride is selected from the group consisting of sodium borohydride, lithium borohydride, potassium borohydride, and sodium cyanoborohydride.
6. The process of claim 5 wherein said inorganic borohydride is sodium borohydride.
7. The process of claim 1 wherein said heterogeneous catalyst comprises at least one selected from the group consisting of Ru and Rh.
8. The process of claim 1 wherein the sum of the weights of Ru, Rh, Pd and Pt comprises from 1 to 10 weight percent of said heterogeneous catalyst.
9. The process of claim 8 wherein the sum of the weights of Ru, Rh, Pd and Pt comprises from 3 to 5 weight percent of said heterogeneous catalyst.
10. The process of claim 1 wherein said heterogeneous catalyst comprises an oxide of at least one selected from the group consisting of Ru, Rh, Pd and Pt.
11. The process of claim 10 wherein said heterogeneous catalyst consists essentially of said oxide.
12. The process of claim 8 wherein said heterogeneous catalyst comprises a support that is substantially inert to amines under reaction conditions for converting 1,2-aromatic diamines to cycloaliphatic diamines.
13. The process of claim 8 wherein said heterogeneous catalyst comprises at least one support selected from the group consisting of alumina, titania, zeolites and microporous layered materials.
14. The process of claim 1 further comprising contacting with hydrogen at a temperature from about 120° to about 200° C., and at a pressure of from about 1000 to about 2500 psig.
15. A process for making 1,2-diaminocyclohexane comprising contacting 1,2-phenylenediamine contained in a polar, protic solvent with hydrogen in the presence of an inorganic borohydride, ammonia and a supported rhodium catalyst, wherein said polar, protic solvent is selected from the group consisting of water, methanol, ethanol, isopropanol, and mixtures thereof.
16. The process of claim 15 further comprising contacting with hydrogen at a temperature from about 120° to about 200° C., and at a pressure of from about 1000 to about 2500 psig.
17. The process of claim 15 wherein said supported rhodium catalyst comprises rhodium on carbon and wherein said supported rhodium catalyst contains from about 1 to about 10 weight percent rhodium.
18. The process of claim 15 wherein said supported rhodium catalyst contains from about 3 to about 5 weight percent rhodium.
19. The process of claim 1 , wherein the process is an aqueous process.
20. The process of claim 15 , wherein the process is an aqueous process.