Hydrogenation of aromatic amines to alicyclic amines using a lithium aluminate-based catalyst
View Patent ↗The present invention relates to processes for the catalytic hydrogenation of aromatic amines to their acyclic counterparts using a ruthenium catalyst on a lithium aluminate support. The hydrogenation process comprises contacting an aromatic amine with hydrogen in the presence of a ruthenium catalyst under temperature and pressure conditions suitable to effect ring hydrogenation. The process is especially useful for hydrogenating aniline to cyclohexylamine.
1. A process for catalytically hydrogenating aromatic amines to their ring hydrogenated counterparts, the process comprising:
contacting the aromatic amine with hydrogen in the presence of a catalyst consisting of ruthenium on a lithium aluminate support, wherein the ratio of ruthenium to lithium aluminate support is from about 2 to about 8 weight parts ruthenium per 100 weight parts support.
2. The process of claim 1 , wherein the aromatic amine is selected from the group consisting of compounds of Formula I,
wherein:
R is hydrogen, halogen, linear or branched C 1 -C 12 alkyl, linear or branched C 1 -C 12 alkoxy, linear or branched C 1 -C 12 alkoxyalkyl, or C 1 -C 12 alkylamino;
R 1 and R 2 independently are a hydrogen or linear or branched C 1 -C 12 alkyl;
X is linear or branched C 1 -C 6 alkylene;
m is 0, 1, 2, or 3;
n is 1 or 2; and
p is 0 or 1.
3. The process of claim 1 , wherein the aromatic amine is selected from the group consisting of compounds of Formula II,
wherein:
R is hydrogen, halogen, linear or branched C 1 -C 12 alkyl, linear or branched C 1 -C 12 alkoxy, linear or branched C 1 -C 12 alkoxyalkyl, or C 1 -C 12 alkylamino;
R 1 and R 2 independently are a hydrogen or linear or branched C 1 -C 12 alkyl;
m is 0, 1, 2, or 3; and
n is 1 or 2.
4. The process of claim 1 wherein the aromatic amine is aniline.
5. The process of claim 1 wherein the aromatic amine is methylene dianiline.
6. The process of claim 1 wherein the hydrogenation is carried out in the presence of a solvent or diluent.
7. The process of claim 6 wherein the solvent or diluent is selected from the group consisting of aliphatic and alicyclic hydrocarbons, aliphatic and alicyclic ethers, alcohols, water, and mixtures thereof.
8. The process of claim 6 wherein the solvent or diluent is substantially tetrahydrofuran.
9. The process of claim 1 wherein the hydrogenation pressure is from about 50 psig to about 4000 psig.
10. The process of claim 1 , wherein the process is carried out at a temperature from about 50° C. to about 300° C.
11. A process of claim 1 , wherein the process is carried out continuously or batchwise.
12. A process for catalytically hydrogenating aromatic amines of Formula I or Formula II,
wherein:
R is hydrogen, halogen, linear or branched C 1 -C 12 alkyl, linear or branched C 1 -C 12 alkoxy, linear or branched C 1 -C 12 alkoxyalkyl, or C 1 -C 12 alkylamino;
R 1 and R 2 independently are a hydrogen or linear or branched C 1 -C 12 alkyl;
X is linear or branched C 1 -C 6 alkylene;
m is 0, 1, 2, or 3;
n is 1 or 2; and
p is 0 or 1,
the process comprising:
contacting the aromatic amine with hydrogen in the presence of a catalyst consisting of ruthenium on a lithium aluminate support, wherein the ratio of ruthenium to lithium aluminate support is from about 2 to about 8 weight parts ruthenium per 100 weight parts support.
13. The process of claim 12 wherein the aromatic amine is aniline.
14. The process of claim 12 wherein the aromatic amine is methylene dianiline.
15. The process of claim 12 wherein the hydrogenation is carried out in the presence of a solvent or diluent.
16. The process of claim 15 wherein the solvent or diluent is selected from the group consisting of aliphatic and alicyclic hydrocarbons, aliphatic and alicyclic ethers, alcohols, water, and mixtures thereof.
17. The process of claim 15 wherein the solvent or diluent is substantially tetrahydrofuran.
18. The process of claim 12 wherein the hydrogenation pressure is from about 50 psig to about 4000 psig.
19. The process of claim 12 wherein the process is carried out at a temperature from about 50° C. to about 300° C.
20. A process of claim 12 wherein the process is carried out continuously or batchwise.
21. A process for catalytically hydrogenating aniline to cyclohexylamine, the process comprising:
contacting aniline in a solvent or diluent with hydrogen in the presence of a catalyst consisting of ruthenium on a lithium aluminate support, wherein the ratio of ruthenium to lithium aluminate support is from about 2 to about 8 weight parts ruthenium per 100 weight parts support.
22. The process of claim 21 wherein the solvent or diluent is tetrahydrofuran.
23. The process of claim 21 wherein the hydrogenation is carried out at a pressure of from about 200 psig to about 1500 psig and at a temperature of from about 50° C. to about 300° C.
24. The process of claim 1 , wherein the ruthenium is from about 0.1% to about 10% of the total weight of the catalyst.