US2007167420A1PendingUtilityA1
Process for preparing a crystalline form of halobetasol propionate
Est. expiryApr 7, 2025(expired)· nominal 20-yr term from priority
C07J 7/00C07J 7/0085
55
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Claims
Abstract
The present invention provides a process for preparing a crystalline form of halobetasol propionate, comprising the step of crystallizing halobetasol propionate from absolute ethanol or a mixture of ethanol and water, wherein the crystalline form of halobetasol propionate is characterized by an x-ray powder diffraction pattern having peaks at 10.0, 11.6, 12.9, 13.4, 14.5, 16.4, 17.6, and 23.5±0.2 degrees 2θ.
Claims
exact text as granted — not AI-modified1 . A process for preparing a crystalline form of halobetasol propionate, comprising the step of crystallizing halobetasol propionate from absolute ethanol or a mixture of ethanol and water, wherein the crystalline form of halobetasol propionate is characterized by an x-ray powder diffraction pattern having peaks at 10.0, 11.6, 12.9, 13.4, 14.5, 16.4, 17.6, and 23.5±0.2 degrees 2θ.
2 . The process of claim 1 , wherein the crystalline form of halobetasol propionate is further characterized by an infrared spectrum having absorption peaks at 1741, 1709, 1665, 1627, and 1611±4 cm −1 .
3 . The process of claim 1 , wherein the crystalline form of halobetasol propionate is further characterized by a melting point of about 220° C. to about 221° C.
4 . The process of claim 1 , wherein the ethanol and water is present in the mixture at a vol/vol ratio of about 50:50 to about 100:0.
5 . The process of claim 1 , wherein the ethanol and water is present in the mixture at a vol/vol ratio of about 50:50 to about 67:33.
6 . The process of claim 1 , wherein the ethanol and water is present in the mixture at a vol/vol ratio of about 50:50.
7 . The process of claim 1 , wherein the crystallizing step is performed by a process comprising the steps of:
(a) preparing a solution of halobetasol propionate in absolute ethanol or a mixture of ethanol and water; and (b) inducing precipitation of a crystalline form of halobetasol propionate.
8 . The process of claim 7 , wherein step (a) is performed by heating the solution of halobetasol propionate to an elevated temperature.
9 . The process of claim 8 , wherein the elevated temperature is between about 60° C. to about 80° C.
10 . The process of claim 7 , wherein step (b) is performed by cooling the prepared solution.
11 . The process of claim 7 , wherein step (b) is performed by cooling the prepared solution to a temperature of about 0° C. to about 25° C.
12 . The process of claim 7 , wherein step (b) is performed by adding water to the prepared solution.
13 . The process of claim 7 , wherein step (b) is performed by adding water to the prepared solution over the course of about 30 minutes to about 90 minutes.
14 . The process of claim 1 , further comprising the step of isolating the crystallized halobetasol propionate from the mixture of ethanol and water.
15 . The process of claim 14 , wherein the isolating step is performed by filtration.
16 . The process of claim 1 , wherein the crystallizing step is repeated at least once.
17 . The process of claim 1 , wherein the crystalline form of halobetasol propionate has a purity of at least about 99.0% (w/w).
18 . The process of claim 1 , wherein the crystalline form of halobetasol propionate has a purity of at least about 99.8% (w/w).
19 . The process of claim 1 , wherein the crystalline form of halobetasol propionate contains about 0.1% (w/w) or less of each individual impurity.
20 . The process of claim 1 , wherein the crystalline form of halobetasol propionate contains about 0.02% (w/w) or less of diflorasone.
21 . The process of claim 1 , wherein the crystalline form of halobetasol propionate contains about 0.02% (w/w) or less of halobetasol.
22 . The process of claim 1 , wherein the crystalline form of halobetasol propionate contains about 0.03% (w/w) or less of diflorasone 21-propionate.
23 . The process of claim 1 , wherein the crystalline form of halobetasol propionate contains about 0.03% (w/w) or less of diflorasone 17-propionate 21-mesylate.
24 . The process of claim 1 , wherein the crystalline form of halobetasol propionate contains about 0.05% (w/w) or less of 6α,9α-difluoro-10-hydroxy-16β-methyl-3-oxoandrosta-1,4-diene-17(R)-spiro-2′-[4′-chloro-5′-ethylfuran-3-(2′H)-one].
25 . The process of claim 1 , wherein the crystalline form of halobetasol propionate is prepared as a single batch of at least about 100 grams.
26 . The process of claim 1 , wherein the crystalline form of halobetasol propionate is prepared as a single batch of at least about 500 grams.
27 . The process of claim 1 , wherein the crystalline form of halobetasol propionate is prepared as a single batch of at least about one kilogram.
28 . A process for preparing a crystalline form of halobetasol propionate, comprising the steps of:
(a) crystallizing halobetasol propionate from a first ethanol; (b) isolating the crystallized halobetasol propionate from the first ethanol; (c) crystallizing the isolated halobetasol propionate from a second ethanol; and (d) isolating the crystallized halobetasol propionate from the second ethanol, wherein the crystalline form of halobetasol propionate is characterized by an x-ray powder diffraction pattern having peaks at 10.0, 11.6, 12.9, 13.4, 14.5, 16.4, 17.6, and 23.5±0.2 degrees 2θ.
29 . The process of claim 28 , wherein the first ethanol further comprises water.
30 . The process of claim 29 , wherein the first ethanol and water is present at a vol/vol ratio of about 1:1
31 . The process of claim 28 , wherein the second ethanol further comprises water.
32 . The process of claim 31 , wherein the second ethanol and water is present at a vol/vol ratio of about 2:1.
33 . The process of claim 28 , wherein the crystalline form of halobetasol propionate has a purity of at least about 99.0% (w/w).
34 . The process of claim 28 , wherein the crystalline form of halobetasol propionate has a purity of at least about 99.8% (w/w).
35 . The process of claim 28 , wherein the crystalline form of halobetasol propionate contains about 0.1% (w/w) or less of each individual impurity.
36 . A commercial scale composition of a crystalline form of halobetasol propionate prepared by the process of claim 1 .
37 . A commercial scale composition of a crystalline form of halobetasol propionate characterized by an x-ray powder diffraction pattern having peaks at 10.0, 11.6, 12.9, 13.4, 14.5, 16.4, 17.6, and 23.5±0.2 degrees 2θ, wherein the composition contains about 0.1% or less of each of diflorasone, diflorasone 17-propionate, halobetasol, diflorasone 21-propionate, diflorasone 17-propionate 21-mesylate, and 6α,9α-difluoro-11β-hydroxy-16β-methyl-3-oxoandrosta-1,4-diene-17(R)-spiro-2′-[4′-chloro-5′-ethylfuran-3-(2′H)-one].
38 . The commercial scale composition of claim 37 , wherein the composition contains about 0.1% (w/w) or less of each impurity present in the composition.
39 . The commercial scale composition of claim 37 , wherein the composition contains about 0.05% (w/w) or less of each of diflorasone, halobetasol, diflorasone 21-propionate, diflorasone 17-propionate 21-mesylate, and 6α,9α-difluoro-11β-hydroxy-16β-methyl-3-oxoandrosta-1,4-diene-17(R)-spiro-2′-[4′-chloro-5′-ethylfuran-3-(2′H)-one].
40 . The commercial scale composition of claim 37 , wherein the composition contains about 0.03% (w/w) or less of each of diflorasone, halobetasol, diflorasone 21-propionate, and diflorasone 17-propionate 21-mesylate.
41 . The commercial scale composition of claim 37 , wherein the composition contains about 0.02% (w/w) or less of each of diflorasone and halobetasol.
42 . The commercial scale composition of claim 37 , wherein the commercial scale composition has a purity of at least about 99.5% (w/w).
43 . The commercial scale composition of claim 42 , wherein the commercial scale composition has a purity of at least about 99.8% (w/w).
44 . The commercial scale composition of claim 37 , wherein the composition is produced as a single batch of at least about 500 grams.
45 . The commercial scale composition of claim 44 , wherein the composition is produced as a single batch of at least about one kilogram.Cited by (0)
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