IP Library Granted Patent US 12,281,104
Granted Patent B2
US 12,281,104 · App. 17/606,248 · Granted Apr 22, 2025

Process for the production of ethyl 3-amino-1-[(3R,4S)-4-cyanotetrahydropyran-3-yl]pyrazole-4-carboxylate through chiral separation of a racemic mixture

Inventors: Christophe Pierre Alain Chassaing (Schwabenheim, DE); Karl-Heinz Grimm (Schwabenheim, DE)
Assignee: Intervet Inc.
C07D405/04
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Quick Facts
Patent No.
US 12,281,104
App. No.
17/606,248
Granted
Apr 22, 2025
Kind
B2
Abstract

A process for chiral separation of ethyl 3-amino-1-[(3R,4S)-4-cyanotetrahydropyran-3-yl]pyrazole-4-carboxylate (VI) from the racemic mixture of ethyl 3-amino-1-[(3R,4S)-4-cyanotetrahydropyran-3-yl]pyrazole-4-carboxylate and ethyl 3-amino-1-[(3S,4R)-4-cyanotetrahydropyran-3-yl]pyrazole-4-carboxylate (V).

Claims (27)

1. A process of producing a compound of Formula VI

from a mixture of enantiomers comprising separating the enantiomers of a racemic mixture of Formula V

by chiral chromatography using an eluent and a chiral stationary phase selected from amylose tris(3-chloro-4-methylphenylcarbamate) and amylose tris(3-chloro-5-methylphenylcarbamate) wherein the eluent is acetonitrile.

2. The process of claim 1 , wherein productivity of the process is greater than 2.0 KKD.

3. The process of claim 1 , wherein the chiral stationary phase is amylose tris(3-chloro-5-methylphenylcarbamate) immobilized on silica gel.

4. The process of claim 1 , wherein the chiral stationary phase is amylose tris(3-chloro-4-methylphenylcarbamate) coated on silica gel.

5. The process of claim 1 , wherein the productivity of the process is in the range of about 2.0 to about 6.0 KKD.

6. The process of claim 1 , wherein the selectivity of the process is the range of about 1.0 to about 4.0.

7. The process of claim 1 , wherein the process is conducted at a temperature between about 20° C. to about 40° C.

8. The process of claim 1 , wherein the process has a concentration of the racemic mixture (V) from about 100 g/L to about 300 g/L.

9. A method of isolating ethyl 3-amino-1-[(3R,4S)-4-cyanotetrahydropyran-3-yl]pyrazole-4-carboxylate (VI), substantially free of ethyl 3-amino-1-[(3S,4R)-4-cyanotetrahydropyran-3-yl]pyrazole-4-carboxylate, said method comprising

a) absorbing a racemic mixture of ethyl 3-amino-1-[(3R,4S)-4-cyanotetrahydropyran-3-yl]pyrazole-4-carboxylate and ethyl 3-amino-1-[(3S,4R)-4-cyanotetrahydropyran-3-yl]pyrazole-4-carboxylate (V) onto a chiral separation medium;

b) passing a solvent system through the chiral separation medium in an amount sufficient to elute ethyl 3-amino-1-[4-cyanotetrahydropyran-3-yl]pyrazole-4-carboxylate enantiomers from the separation medium;

c) isolating ethyl 3-amino-1-[(3R,4S)-4-cyanotetrahydropyran-3-yl]pyrazole-4-carboxylate (VI), substantially free of ethyl 3-amino-1-[(3S,4R)-4-cyanotetrahydropyran-3-yl]pyrazole-4-carboxylate;

wherein said chiral separation medium is amylose tris(3-chloro-5-methylphenylcarbamate) immobilized on silica gel or

amylose tris(3-chloro-4-methylphenylcarbamate) coated on silica gel.

10. The method of claim 9 , wherein the chiral separation medium is amylose tris(3-chloro-5-methylphenylcarbamate) immobilized on silica gel.

11. The method of claim 9 , wherein the chiral separation medium is amylose tris(3-chloro-4-methylphenylcarbamate) coated on silica gel.

12. The method of claim 9 , wherein the solvent system comprises is acetonitrile.

13. The method of claim 9 , wherein the process has a productivity of in the range of about 2.0 to about 6.0 KKD.

14. The method of claim 9 , wherein the selectivity of the process is the range of about 1.0 to about 4.0.

15. The method of claim 9 , wherein the temperature is between about 20° C. to about 40° C.

16. The method of claim 9 , wherein the concentration of the racemic mixture (V) is about 100 g/L to about 300 g/L.

17. The method of claim 5 , wherein the productivity of the process is in the range of about 3.0 to about 5.0 KKD.

18. The method of claim 6 , wherein the selectivity of the process is the range of about 1.5 to about 3.5.

19. The method of claim 7 , wherein the process is conducted at a temperature between about 25° C. to about 35° C.

20. The method of claim 8 , wherein the process has a concentration of the racemic mixture (V) of about 200 g/L.

Assignments (2)
CHANGE OF ADDRESS Recorded Sep 26, 2023
From: INTERVET INC.
To: INTERVET INC.
Reel/Frame 065028/0818 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 25, 2021
From: CHASSAING, CHRISTOPHE PIERRE ALAIN; GRIMM, KARL-HEINZ
To: INTERVET INC.
Reel/Frame 057904/0747 →
Priority Claims (1)
EP 19172248 · May 2, 2019 · regional
Continuity (1)
Related Publication 20220204483A1 · Jun 30, 2022
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