Preparative-scale separation of enantiomers of chiral carboxylic acids
View Patent ↗High yields and purity are obtained in the purification of enantiomers of chiral carboxylic acids by preparative-scale chromatography by including a tertiary alcohol in the mobile phase in conjunction with an acidic modifier and a hydrophobic solvent. The tertiary alcohol is superior to other, more commonly used alcohols by reducing the extent of esterification of the enantiomer that otherwise lowers the yield and the purity.
1. A process for recovering a selected enantiomer from a mixture of first and second enantiomers of a chiral carboxylic acid selected from the group consisting of flurbiprofen, ibuprofen, and naproxen, said method comprising:
(a) preparing a feed solution of solutes dissolved in a hydrophobic alkane having a boiling point between 50° C. and 150° C., said solutes comprising said first and second enantiomers, an organic acid selected from the group consisting of C 1 -C 4 alkyl carboxylic acids and halogen-substituted C 1 -C 4 alkyl carboxylic acids, and a tertiary alcohol;
(b) passing said feed solution through a chromatographic separation system to achieve an extract and a raffinate as separate product solutions, said raffinate having dissolved therein said first enantiomer to the substantial exclusion of said second enantiomer, and said extract having dissolved therein said second enantiomer to the substantial exclusion of said first enantiomer; and
(c) collecting said product solution containing said selected enantiomer, concentrating said collected product solution by evaporation of said hydrocarbon solvent to form a concentrated product, and storing said concentrated product for at least one hour.
2. The process of claim 1 wherein said chromatographic separation system is a simulated moving bed chromatography system with synchronous shifting of inlet and outlet ports.
3. The process of claim 1 wherein said chromatographic separation system is a simulated moving bed chromatography system with non-synchronous shifting of inlet and outlet ports.
4. The process of claim 1 wherein said chiral carboxylic acid is flurbiprofen.
5. The process of claim 1 wherein said organic acid is a member selected from the group consisting of acetic acid, trifluoroacetic acid, and formic acid.
6. The process of claim 1 wherein said organic acid is acetic acid.
7. The process of claim 1 wherein said tertiary alcohol is a member selected from the group consisting of t-butanol, 2-methyl-2-butanol, 3-methyl-3-pentanol, and 2,3-dimethyl-2-butanol.
8. The process of claim 1 wherein said tertiary alcohol is t-butanol.
9. The process of claim 1 wherein said hydrocarbon solvent is a member selected from the group consisting of n-heptane and n-hexane.
10. The process of claim 1 wherein said chiral carboxylic acid is flurbiprofen, said organic acid is acetic acid, and said tertiary alcohol is t-butanol.
11. The process of claim 1 wherein said separation system is a simulated moving bed chromatography system utilizing a stationary phase comprising an amylose derivative on a solid support.
12. The process of claim 11 wherein said amylose derivative is amylose tris(3,5-dimethylphenylcarbamate) and said solid support is macroporous silica.
13. The process of claim 1 comprising concentrating said collected product solution in step (c) by evaporation of said hydrocarbon solvent at a temperature in excess of 20° C.
14. The process of claim 1 comprising concentrating said collected product solution in step (c) by evaporation of said hydrocarbon solvent at a temperature in excess of 40° C.
15. The process of claim 1 wherein step (c) comprises storing said concentrated product for at least ten hours.
16. The process of claim 1 wherein step (c) comprises storing said concentrated product for at least 24 hours.