2-(3-(aminomethyl)-3,5,5-trimethylcyclohexyl)propane-1,3-diamine, a process for its production and use

1. A process for producing 2-(3-(aminomethyl)-3,5,5-trimethylcyclohexyl)propane-1,3-diamine by

A) reacting isophoronenitrile and malononitrile to afford intermediate 2-(3-cyano-3,5,5-trimethylcyclohexylidene)malononitrile, and

B) hydrogenating the 2-(3-cyano-3,5,5-trimethylcyclohexylidene)malononitrile in the presence of a catalyst.

2. The process according to claim 1 , wherein the hydrogenation in step B) is performed at 20-120° C. and at 20-300 bar.

3. The process according to claim 1 , wherein the hydrogenation in step B) is performed in two stages at 20-120° C. and at 20-300 bar.

4. The process according to claim 3 , wherein the hydrogenation in step B) is performed in two stages at 80-110° C. and at 80-140 bar.

5. The process according to claim 3 , wherein the hydrogenation is performed at 40-100° C. and 25-150 bar in the first stage and at 50-115° C. and 50-200 bar in the second stage.

6. The process according to claim 3 , wherein the hydrogenation is performed at 60-90° C. and 40-80 bar in the first stage and at 80-110° C. and 80-140 bar in the second stage.

7. The process according to claim 1 , wherein the catalyst is selected from the group consisting of nickel, copper, iron, palladium, rhodium, ruthenium and cobalt.

8. The process according to claim 1 , wherein the catalysts employed are palladium and/or cobalt catalysts.

9. The process according to claim 1 , wherein the catalysts are Raney-type catalysts or supported catalysts.

10. The process according to claim 1 , wherein the catalyst employed is a catalyst composed of activated Raney cobalt alloy pellets, wherein after activation the catalyst in its entirety has the following composition in weight percent (wt %), the proportions summing to 100 wt % based on the metals present:

cobalt: 57 to 84 wt %

and

with particle sizes of the catalyst, i.e. the pellet particles, having a statistical distribution between 3 to 7 millimeters (mm), wherein up to 10 percent of the particles may also be outside the stated range of the stated lower limit or upper limit but also in each case up to 10 percent may be outside the stated range of the stated lower limit and upper limit.

11. The process according to claim 1 , wherein the hydrogenation is performed in fixed-bed reactors, preferably in shaft furnaces, tray reactors or shell and tube reactors.

12. The process according to claim 2 , wherein the catalyst is selected from the group consisting of nickel, copper, iron, palladium, rhodium, ruthenium and cobalt.

13. The process according to claim 2 , wherein the catalysts are palladium and/or cobalt catalysts.

14. The process according to claim 2 , wherein the catalysts are Raney-type catalysts or supported catalysts.

15. The process according to claim 2 , wherein the catalyst is a catalyst composed of activated Raney cobalt alloy pellets, wherein after activation the catalyst in its entirety has the following composition in weight percent (wt %), the proportions summing to 100 wt % based on the metals present:

cobalt: 57 to 84 wt %

aluminium: 10 to 40 wt %

chromium: 1 to 2 wt %

nickel: 2 to 4 wt %

and

with particle sizes of the catalyst, i.e. the pellet particles, having a statistical distribution between 3 to 7 millimeters (mm), wherein up to 10 percent of the particles may also be outside the stated range of the stated lower limit or upper limit but also in each case up to 10 percent may be outside the stated range of the stated lower limit and upper limit.

16. The process according to claim 2 , wherein the hydrogenation is performed in fixed-bed reactors, preferably in shaft furnaces, tray reactors or shell and tube reactors.

17. The process according to claim 2 , wherein the catalyst is selected from the group consisting of nickel, copper, iron, palladium, rhodium, ruthenium and cobalt.

18. The process according to claim 2 , wherein the catalysts are palladium and/or cobalt catalysts.