IP Library Granted Patent US 6,977,301
Granted Patent B1
US 6,977,301 · App. 10/920,434 · Granted Dec 20, 2005

Process for preparing (S) and (R)—2-[4-(4-chlorobenzhydryl)piperazin-1-yl]-ethoxyacetamide

Assignee: UCB, S.A.
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Quick Facts
Patent No.
US 6,977,301
App. No.
10/920,434
Granted
Dec 20, 2005
Kind
B1
Abstract

The present invention relates to a process for preparing (S)-2-[4-(4-chlorobenzhydryl)piperazin-1-yl]-ethoxyacetamide and (R)-2-[4-(4-chlorobenzhydryl)piperazin-1-yl]-ethoxyacetamide by separation of a racemic mixture using multiple column chromatography.

Claims (13)

1. Process for preparing (S)—2-[4-(4-chlorobenzhydryl)piperazin-1-yl]-ethoxyacetamide and (R)—2-[4-(4-chlorobenzhydryl)piperazin-1-yl]-ethoxyacetamide, by enantiomeric resolution of racemic 2-[4-(4-chlorobenzhydryl)piperazin-1-yl]-ethoxyacetamide using simulated mobile bed chromatography.

2. Process according to claim 1 , wherein at least three columns filled with chiral stationary phase are used.

3. Process according to claim 2 , wherein the chiral stationary phase is chosen from phases based on silica gel supporting polymeric compounds.

4. Process according to claim 2 , wherein the chiral stationary phase is a phase based on silica gel supporting an ester or a carbamate of cellulose or of amylose.

5. Process according to claim 1 , wherein the simulated moving bed chromatographic system uses at least one column packed with an optical resolution packing material, said packing material consisting of silica gel supporting amylose tris(3,5-dimethylphenylcarbamate) or a chemically modified form thereof.

6. Process according to claim 5 , wherein the average particle diameter of the packing material is 1 to 300 μm.

7. Process according to claim 6 wherein the particles of the packing material are porous.

8. Process according to claim 7 , wherein the pore diameter of the particles is 10 Å–5000 Å.

9. Process according to claim 5 , wherein the amylose tris(3,5-dimethylphenylcarbamate) or chemically modified form thereof is 1 to 99% weight percent of the silica gel support.

10. Process according to claim 1 , wherein it is performed at a temperature of 5–50° C.

11. Process according to claim 1 , wherein it uses a simulated mobile bed system comprising eight columns.

12. Process according to claim 1 , wherein the simulated mobile bed system uses an eluent selected from methanol, or a mixture of n-heptane and n-propanol.

13. Process according to claim 3 , wherein the polymeric compounds are selected from polysaccharide derivatives, polyacrylic derivatives and polyamide derivatives.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 21, 2008
From: UCB, S.A.
To: UCB PHARMA, S.A.
Reel/Frame 021773/0126 →
Continuity (3)
Continuation 1044107300 · May 20, 2003
Continuation In Part 1021474400 · Aug 9, 2002
Continuation 0986561800 · May 29, 2001