Process for the production of N-[3-(3-cyanopyrazolo[1,5-a] pyrimidin-7-yl) phenyl]-N-ethylacetamide (zaleplon)
View Patent ↗A process for the production of N-[3-(3-cyanopyrazolo[1,5-a]pyrimidin-7-yl)phenyl]-N-ethylacetamide (zaleplon) that involves reacting N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide or a salt thereof with 3-amino-4-cyanopyrazole or a salt thereof under acidic conditions in a reaction medium comprising a mixture of water and a water-miscible organic compound produces zaleplon in high yield and high purity. A regioisomer of zaleplon (N-[3-(3-cyanopyrazolo[1,5-a]pyrimidin-5-yl)phenyl]-N-ethylacetamide) is useful as a reference standard for monitoring the composition of production batches of zaleplon.
1. A process for producing zaleplon comprising:
a.) providing a mixture of N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide and 3-amino-4-cyanopyrazole in a liquid reaction medium of water and at least one water-miscible organic compound free of carboxylic acid groups, wherein the at least one water-miscible organic compound is selected from the group consisting of C 1 -C 6 alcohols, nitriles, ethers, nitro compounds, and sulfoxides,
b.) forming zaleplon under acidic conditions via an intermediate that is soluble in the reaction medium, and
c.) recovering zaleplon from the reaction medium.
2. The process according to claim 1 where the water-miscible organic compound is selected from the group consisting of methanol, ethanol, propanol, acetonitrile, propionitrile, tetrahydrofuran, dioxane, nitromethane, nitroethane, and dimethylsulfoxide.
3. The process according to claim 1 wherein the reaction medium contains from about 10% to about 90% (v/v) of at least one water-miscible organic compound in water.
4. The process according to claim 3 wherein the reaction medium contains from about 30% to about 40% (v/v) of at least one water-miscible organic compound in water.
5. The process according to claim 1 wherein the solution contains an acid selected from the group consisting of inorganic acids and water-miscible organic acids.
6. The process according to claim 5 wherein the acid is an inorganic acid.
7. The process according to claim 6 wherein the inorganic acid is selected from the group consisting of hydrochloric acid, hydrobromic acid, sulfuric acid, phosphoric acid and boric acid.
8. The process according to claim 5 wherein the acid is a water-miscible organic acid.
9. The process according to claim 8 wherein the water-miscible organic acid is selected from the group consisting of formic acid, acetic acid, propionic acid, oxalic acid, malonic acid, and tartaric acid.
10. The process according to claim 5 wherein the acid is present in at least 1 molar equivalent with respect to whichever of N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide and 3-amino-4-cyanopyrazole is present in lesser molar quantity.
11. The process according to claim 5 wherein providing the mixture comprises adding an acid addition salt of N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide to the reaction medium.
12. The process according to claim 11 wherein the acid and the acid of the N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide acid addition salt are the same.
13. The process according to claim 5 wherein providing the mixture comprises adding an acid addition salt of 3-amino-4-cyanopyrazole to the reaction medium.
14. The process according to claim 13 wherein the acid and the acid of the 3-amino-4-cyanopyrazole acid addition salt are the same.
15. The process according to claim 1 wherein the zaleplon is formed at a temperature of from about 10° C. to about 100° C.
16. The process according to claim 15 wherein the temperature is from about 20° C. to about 25° C.
17. The process according to claim 1 wherein the zaleplon is recovered in about 0.2 hours to about 8 hours after providing the mixture.
18. The process according to claim 17 wherein the zaleplon is recovered in about 2 hours to about 4 hours after providing the mixture.
19. The process according to claim 1 wherein zaleplon precipitates from the reaction medium and is recovered by separating the reaction medium and dissolved substances from the precipitate.
20. The process according to claim 5 wherein the reaction medium is about 30% to about 40% (v/v) methanol in water, the acid is hydrochloric acid, and the hydrochloric acid is used in an amount of from about 1 to about 2 molar equivalents with respect to whichever of N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide and 3-amino-4-cyanopyrazole is present in lesser molar quantity.
21. The process according to claim 19 wherein zaleplon is formed at a temperature of from about 20° C. to about 25° C. and is recovered about 2 to about 4 hours after providing the mixture.
22. The process according to claim 5 wherein the reaction medium is about 30% to about 40% (v/v) methanol in water, the acid is phosphoric acid, and the phosphoric acid is used in an amount of about 1 to about 2 molar equivalents with respect to whichever of N-[3-[3-(dimethylamino)-1-oxo-2-propenyl]phenyl]-N-ethylacetamide and 3-amino-4-cyanopyrazole is present in lesser molar quantity.
23. The process according to claim 22 wherein zaleplon is formed at temperature of from about 20° C. to about 25° C. and recovered in about 2 to about 4 hours after providing the mixture.
24. The process according to claim 1 wherein the at least one water-miscible organic compound is selected from the group consisting of C 1 -C 6 alcohols, nitriles, ethers, nitro compounds and sulfoxides.