Formulations and pharmacokinetics of deuterated benzoquinoline inhibitors of vesicular monoamine transporter 2
US-9233959-B2 · Jan 12, 2016 · US
US10513488B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10513488-B2 |
| Application number | US-201715472779-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 29, 2017 |
| Priority date | Dec 3, 2013 |
| Publication date | Dec 24, 2019 |
| Grant date | Dec 24, 2019 |
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The present invention relates to new methods of manufacturing benzoquinoline inhibitors of vesicular monoamine transporter 2 (VMAT2), and intermediates thereof.
Opening claim text (preview).
What is claimed is: 1. A process of preparing a racemic mixture of (RR,SS)-d 6 -tetrabenazine (RR, SS)-d 6 -tetrabenazine wherein the deuterium enrichment of the (RR, SS)-d 6 -tetrabenazine is no less than about 10%, comprising: reacting d 6 -6,7-dimethoxy-3,4-dihydroisoquinoline, or a salt thereof: d 6 -6,7-dimethoxy-3,4-dihydroisoquinoline with a salt of 2-acetyl-N,N,N,4-tetramethyl-1-pentanaminium: wherein X is halogen, alkyl sulfate, alkyl sulfonate, halosulfonate, perhaloalkyl sulfonate, aryl sulfonate, alkylaryl sulfonate, dialkyloxonium, alkylphosphate, or alkyl carbonate; and an optional base; in the presence of a solvent mixture that is a combination of water and an alcohol that is methanol or ethanol; for a period of time and at a temperature sufficient to produce the (RR,SS)-d 6 -tetrabenazine having a diastereomeric purity of at least 99%, based on high performance liquid chromatography. 2. The process of claim 1 , wherein the solvent mixture is a combination of methanol and water. 3. The process of claim 2 , wherein the ratio of methanol:water is about 5:1 to about 1:1. 4. The process of claim 2 , wherein the ratio of methanol:water is about 3:1. 5. The process of claim 2 , wherein the ratio of methanol:water is about 1:1. 6. The process of claim 1 , wherein the solvent mixture is a combination of ethanol and water. 7. The process of claim 1 , wherein the d 6 -6,7-dimethoxy-3,4-dihydroisoquinoline is a salt form of d 6 -6,7-dimethoxy-3,4-dihydroisoquinoline. 8. The process of claim 7 , wherein the salt form of d 6 -6,7-dimethoxy-3,4-dihydroisoquinoline is d 6 -6,7-dimethoxy-3,4-dihydroisoquinoline hydrochloride. 9. The process of claim 8 , wherein the process is carried out in the presence of a base. 10. The process of claim 9 , wherein the base is K 2 CO 3 . 11. The process of claim 1 , wherein X is halogen. 12. The process of claim 11 , wherein the halogen is iodide. 13. The process of claim 1 , wherein the period of time is about 24 hours to about 63 hours. 14. The process of claim 1 , wherein the temperature is about 40° C. to about 60° C. 15. The process of claim 1 , wherein the diastereomeric purity is at least 99.1%. 16. The process of claim 1 , wherein the diastereomeric purity is at least 99.2%. 17. The process of claim 1 , wherein the diastereomeric purity is at least 99.5%. 18. The process of claim 1 , wherein the diastereomeric purity is at least 99.6%. 19. The process of claim 1 , wherein the diastereomeric purity is at least 99.9%. 20. The process of claim 1 , wherein the deuterium enrichment of the (RR,SS)-d 6 -tetrabenazine is no less than about 50%. 21. The process of claim 1 , wherein the deuterium enrichment of the (RR,SS)-d 6 -tetrabenazine is no less than about 90%. 22. The process of claim 1 , wherein the deuterium enrichment of the (RR,SS)-d 6 -tetrabenazine is no less than about 98%. 23. The process of claim 4 , wherein a salt form of d 6 -6,7-dimethoxy-3,4-dihydroisoquinoline is reacted and the salt form is d 6 -6,7-dimethoxy-3,4-dihydroisoquinoline hydrochloride. 24. The process of claim 23 , wherein the process is carried out in the presence of K 2 CO 3. 25. The process of claim 24 , wherein Xis halogen. 26. The process of claim 25 , wherein the halogen is iodide. 27. The process of claim 26 , wherein the diastereomeric purity is at least 99.1%. 28. The process of claim 4 , wherein Xis halogen. 29. The process of claim 28 , wherein the halogen is iodide. 30. The process of claim 4 , wherein the deuterium enrichment of the (RR,SS)-d 6 -tetrabenazine is no less than about 50%. 31. The process of claim 4 , wherein the deuterium enrichment of the (RR,SS)-d 6 -tetrabenazine is no less than about 90%. 32. The process of claim 4 , wherein the deuterium enrichment of the (RR,SS)-d 6 -tetrabenazine is no less than about 98%. 33. The process of claim 23 , wherein the deuterium enrichment of the (RR,SS)-d 6 -tetrabenazine is no less than about 50%. 34. The process of claim 23 , wherein the deuterium enrichment of the (RR,SS)-d 6 -tetrabenazine is no less than about 90%. 35. The process of claim 23 , wherein the deuterium enrichment of the (RR,SS)-d 6 -tetrabenazine is no less than about 98%. 36. The process of claim 4 , wherein a salt form of d 6 -6,7-dimethoxy-3,4-dihydroisoquinoline is reacted and the salt form is d 6 -6,7-dimethoxy-3,4-dihydroisoquinoline hydrochloride, X is iodide, and the diastereomeric purity is at least 99.1. 37. The process of claim 36 , wherein the process is carried out in the presence of K 2 CO 3.
Preparation of compounds containing amino groups and doubly-bound oxygen atoms bound to the same carbon skeleton · CPC title
containing benzo [a] quinolizine ring systems · CPC title
with hydrocarbon or substituted hydrocarbon radicals attached to the ring nitrogen atom · CPC title
from carboxylic acids or from esters, anhydrides, or halides thereof by reaction with ammonia or amines · CPC title
Isotopically modified compounds, e.g. labelled · CPC title
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