IP Library Granted Patent US 8,946,463
Granted Patent B2
US 8,946,463 · App. 14/000,400 · Granted Feb 3, 2015

Process for the direct amination of alcohols using ammonia to form primary amines by means of a xantphos catalyst system

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Quick Facts
Patent No.
US 8,946,463
App. No.
14/000,400
Granted
Feb 3, 2015
Kind
B2
Abstract

The present invention relates to a chemocatalytic liquid-phase process for the direct one-stage amination of alcohols to primary amines by means of ammonia in high yields using a catalyst system containing at least one transition metal compound and a xantphos ligand.

Claims (29)

1. A process for preparing a primary amine, comprising:

contacting a solution of an alcohol in a fluid, nongaseous phase,

with free ammonia, an ammonia-liberating compound, or both, and a homogeneous catalyst system comprising carbonylchlorohydrido[9,9-dimethyl-4,5-bis(diphenylphosphino)xantheno]ruthenium(II)] as a xantphos ligand; and

optionally isolating the primary amine obtained in the contacting.

2. The process according to claim 1 ,

wherein the alcohol is an aliphatic, linear ω-hydroxycarboxylic acid having a carbon chain comprising at least 8 carbon atoms.

3. The process according to claim 1 ,

wherein the alcohol has a concentration of from 0.1 to 1000 mmol/l, based on the fluid phase.

4. The process according claim 1 ,

wherein the contacting comprises contacting with liquid or supercritical ammonia, with a solution of ammonium salts in a solvent, or both.

5. The process according to claim 1 ,

wherein in the contacting, the ammonia has a molar ratio to hydroxyl groups in the alcohol of at least 5:1.

6. The process according to claim 1 ,

wherein the contacting is carried out at a pressure of from 1 to 1000 bar.

7. The process according to claim 1 ,

wherein the contacting is carried out in a temperature range of from 80 to 220° C.

8. The process according claim 1 ,

wherein a volume ratio of a liquid phase to a gas phase in the contacting is at least 0.05.

9. The process according to claim 1 ,

wherein the process is carried out in the absence of hydrogen.

10. The process according to claim 1 , wherein the alcohol has a concentration of from 0.1 to 100 mmol/l based on the fluid phase.

11. The process according to claim 1 , wherein the alcohol has a concentration of from 0.1 to 10 mmol/l based on the fluid phase.

12. The process according to claim 1 , wherein in the contacting, the ammonia has a molar ratio to hydroxyl groups in the alcohol of at least 50:1.

13. The process according to claim 1 , wherein in the contacting, the ammonia has a molar ratio to hydroxyl groups in the alcohol of at least 500:1.

14. The process according to claim 1 , wherein the contacting is carried out at a pressure of from 5 to 500 bar.

15. The process according to claim 1 , wherein the contacting is carried out at a pressure of from 5 to 20 bar.

16. The process according to claim 1 , wherein the contacting is carried out in a temperature range of from 100 to 200° C.

17. The process according to claim 1 , wherein the contacting is carried out in a temperature range of from 120 to 170° C.

18. The process according to claim 1 , wherein a volume ratio of a liquid phase to a gas phase in the contacting is greater than or equal to 0.1.

Assignments (2)
CHANGE OF NAME Recorded Jan 31, 2020
From: EVONIK DEGUSSA GMBH
To: EVONIK OPERATIONS GMBH
Reel/Frame 051765/0166 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 22, 2013
From: KLASOVSKY, FLORIAN; TACKE, THOMAS; PFEFFER, JAN CHRISTOPH; HAAS, THOMAS; BELLER, MATTHIAS; MARTIN, ANDREAS; DEUTSCH, JENS; KOECKRITZ, ANGELA; IMM, SEBASTIAN; HABERLAND, JUERGEN
To: EVONIK DEGUSSA GMBH
Reel/Frame 031059/0093 →