Synthesis of amino acid, N-carboxyanhydrides
View Patent ↗A process for producing N-carboxyanhydrides is disclosed. The process produces N-carboxyanhydrides as a product and HCl as a by-product. The HCl by-product is purged from the reaction mixture by passing a purge gas through the reaction mixture as a carbonylation reagent is reacting with an amino acid or a salt thereof. The N-carboxyanhydrides produced by this process have a relatively lower chloride impurity content, relatively higher yields can be achieved, and the N-carboxyanhydrides can be produced on a larger scale.
1. A process for the preparation of an N-carboxyanhydride, the process comprising:
forming a reaction mixture comprising an amino acid or a salt thereof, a solvent, and a carbonylation reagent selected from the group consisting of phosgene, diphosgene, triphosgene and mixtures thereof whereby the carbonylation reagent reacts with the amino acid or a salt thereof to yield an N-carboxyanhydride as a product and HCl as a by-product,
purging the HCl by-product from the reaction mixture by passing a purge gas through the reaction mixture as the carbonylation reagent is reacting with the amino acid or a salt thereof, and
treating the purge gas after it has passed through the reaction mixture to reduce the concentration of carbonylation reagent therein.
2. The process according to claim 1 wherein the carbonylation reagent is phosgene.
3. The process according to claim 2 wherein the purge gas is a gas selected from the group consisting of nitrogen, helium, argon, neon, and mixtures thereof.
4. The process according to claim 2 wherein the purge gas is predominantly nitrogen.
5. The process according to claim 2 wherein the solvent is selected from the group consisting of tetrahydrofuran, dioxane, diethyl ether, isopropyl ether, dichloromethane, chloroform, 1,2-dichloroethane, N,N′-dimethylformamide, acetonitrile, acetone, ethyl acetate, and combinations thereof.
6. The process according to claim 3 wherein the solvent is selected from the group consisting of tetrahydrofuran, dioxane, diethyl ether, isopropyl ether, dichloromethane, chloroform, 1,2-dichloroethane, N,N′-dimethylformamide, acetonitrile, acetone, ethyl acetate, and combinations thereof.
7. The process according to claim 2 wherein the carbonylation reagent is introduced into the reaction mixture in the form of a liquid.
8. The process according to claim 2 wherein the amino acid is selected from the group consisting of the γ-benzyl ester of glutamic acid, the γ-ethyl ester of glutamic acid, and N6-CBZ-L-lysine and their salts.
9. The process according to claim 6 wherein the amino acid is selected from the group consisting of the γ-benzyl ester of glutamic acid, the γ-ethyl ester of glutamic acid, and N6-CBZ-L-lysine and their salts.
10. The process according to claim 3 wherein the purge gas is treated by passing the purge gas through a condenser to condense the carbonylation reagent from the purge gas.
11. The process according to claim 6 wherein the purge gas is treated by passing the purge gas through a condenser to condense the carbonylation reagent from the purge gas.
12. The process according to claim 9 wherein the purge gas is treated by passing the purge gas through a condenser to condense the carbonylation reagent from the purge gas.
13. The process according to claim 10 wherein the purge gas is further treated by passing the purge gas through a scrubber which neutralizes the carbonylation reagent in the purge gas after the purge gas is passed through the condenser.
14. The process according to claim 11 wherein the purge gas is further treated by passing the purge gas through a scrubber which neutralizes the carbonylation reagent in the purge gas after the purge gas is passed through the condenser.
15. The process according to claim 12 wherein the purge gas is further treated by passing the purge gas through a scrubber which neutralizes the carbonylation reagent in the purge gas after the purge gas is passed through the condenser.
16. The process according to claim 3 wherein the purge gas is treated by passing the purge gas through a scrubber which neutralizes the carbonylation reagent in the purge gas.
17. The process according to claim 6 wherein the purge gas is treated by passing the purge gas through a scrubber which neutralizes the carbonylation reagent in the purge gas.
18. The process according to claim 9 wherein the purge gas is treated by passing the purge gas through a scrubber which neutralizes the carbonylation reagent in the purge gas.
19. The process according to claim 13 wherein the carbonylation reagent is neutralized with a base selected from the group consisting of ammonium hydroxide, potassium hydroxide, sodium hydroxide and combinations thereof.
20. The process according to claim 14 wherein the carbonylation reagent is neutralized with a base selected from the group consisting of ammonium hydroxide, potassium hydroxide, sodium hydroxide and combinations thereof.
21. The process according to claim 15 wherein the carbonylation reagent is neutralized with a base selected from the group consisting of ammonium hydroxide, potassium hydroxide, sodium hydroxide and combinations thereof.
22. The process according to claim 16 wherein the carbonylation reagent is neutralized with a base selected from the group consisting of ammonium hydroxide, potassium hydroxide, sodium hydroxide and combinations thereof.
23. The process according to claim 17 wherein the carbonylation reagent is neutralized with a base selected from the group consisting of ammonium hydroxide, potassium hydroxide, sodium hydroxide and combinations thereof.
24. The process according to claim 19 wherein the base is sodium hydroxide.
25. The process according to claim 23 wherein the base is sodium hydroxide.
26. The process according to claim 3 wherein the purge gas and the carbonylation reagent are added over a period of time, wherein the average relative rate of addition on a molar basis over the period of time is between 0.15:1 and 0.4:1, respectively.
27. The process according to claim 12 wherein the purge gas and the carbonylation reagent are added over a period of time, wherein the average relative rate of addition on a molar basis over the period of time is between 0.15:1 and 0.4:1, respectively.
28. The process according to claim 3 wherein the N-carboxyanhydride product is recovered and the product contains less than 0.1% by weight HCl.
29. The process according to claim 12 wherein the N-carboxyanhydride product is recovered and the product contains less than 0.1% by weight HCl.
30. The process according to claim 26 wherein the N-carboxyanhydride product is recovered and the product contains less than 0.1% by weight HCl.