IP Library Granted Patent US 8,288,440
Granted Patent B2
US 8,288,440 · App. 12/686,812 · Granted Oct 16, 2012

Formulations of suberoylanilide hydroxamic acid and methods for producing same

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Quick Facts
Patent No.
US 8,288,440
App. No.
12/686,812
Granted
Oct 16, 2012
Kind
B2
Abstract

The present invention provides a pharmaceutical composition or crystalline composition with a specific dissolution profile, which comprises suberoylanilide hydroxamic acid or a pharmaceutically acceptable salt or hydrate thereof as an active ingredient. The present invention provides a process of producing said crystalline composition or pharmaceutical composition. The present invention also provides compositions with a specific particle size distribution.

Claims (32)

1. A process of producing a pharmaceutical composition comprising suberoylanilide hydroxamic acid or a pharmaceutically acceptable salt or hydrate thereof as an active ingredient, comprising the steps of:

(a) blending about 60-5% of a first batch of crystalline suberoylanilide hydroxamic acid or a pharmaceutically acceptable salt or hydrate thereof active ingredient having a mean particle size of less than about 60 μm and about 40-95% of a second batch of crystalline suberoylanilide hydroxamic acid or a pharmaceutically acceptable salt or hydrate thereof active ingredient having a mean particle size of about 100-250 μm; and

(b) encapsulating a portion of the blended crystalline active ingredient to produce the pharmaceutical composition.

2. The process of claim 1 , wherein the first batch of crystalline active ingredient has a mean particle size of less than about 50 μm and the second batch of crystalline active ingredient has a mean particle size of about 120-160 μm.

3. The process of claim 1 , wherein 95% of the first batch of crystalline active ingredient is less than about 100 μm and 95% of the second batch of crystalline active ingredient is less than about 300 μm.

4. The process of claim 1 , wherein step a) is

blending about 40-20% of a first batch of crystalline active ingredient having a mean particle size of about 25 to 45 μm and about 60-80% of a second batch of crystalline active ingredient having a mean particle size of about 130-180 μm.

5. The process of claim 1 , wherein step a) is

blending about 30% of a first batch of crystalline active ingredient having a mean particle size of about 25 to 45 μm and about 70% of a second batch of crystalline active ingredient having a mean particle size of about 130-180 μm.

6. The process of claim 1 , wherein the active ingredient is suberoylanilide hydroxamic acid.

7. The process of claim 2 , wherein the active ingredient is suberoylanilide hydroxamic acid.

8. The process of claim 3 , wherein the active ingredient is suberoylanilide hydroxamic acid.

9. The process of claim 4 , wherein the active ingredient is suberoylanilide hydroxamic acid.

10. The process of claim 5 , wherein the active ingredient is suberoylanilide hydroxamic acid.

11. The process of claim 1 , wherein about 100 mg of the blended crystalline active ingredient in the pharmaceutical composition has an in vitro dissolution profile with a similarity factor (f 2 ) of at least 50 to 100 compared to the reference dissolution profile of 52.7% dissolved at 10 minutes, 61.7% dissolved at 15 minutes, 67.7% dissolved at 20 minutes, 75.5% dissolved at 30 minutes, 82.6% dissolved at 45 minutes, and 87.0% dissolved at 60 minutes in vitro, wherein the dissolution profile is measured using a USP Dissolution Apparatus II with a helical sinker in 900 mL of 2.0% Tween at a temperature of 37±0.5° C., and paddles rotated at 100 rpm.

12. The process of claim 2 , wherein about 100 mg of the blended crystalline active ingredient in the pharmaceutical composition has an in vitro dissolution profile with a similarity factor (f 2 ) of at least 50 to 100 compared to the reference dissolution profile of 52.7% dissolved at 10 minutes, 61.7% dissolved at 15 minutes, 67.7% dissolved at 20 minutes, 75.5% dissolved at 30 minutes, 82.6% dissolved at 45 minutes, and 87.0% dissolved at 60 minutes in vitro, wherein the dissolution profile is measured using a USP Dissolution Apparatus II with a helical sinker in 900 mL of 2.0% Tween at a temperature of 37±0.5° C., and paddles rotated at 100 rpm.

13. The process of claim 3 , wherein about 100 mg of the blended crystalline active ingredient in the pharmaceutical composition has an in vitro dissolution profile with a similarity factor (f 2 ) of at least 50 to 100 compared to the reference dissolution profile of 52.7% dissolved at 10 minutes, 61.7% dissolved at 15 minutes, 67.7% dissolved at 20 minutes, 75.5% dissolved at 30 minutes, 82.6% dissolved at 45 minutes, and 87.0% dissolved at 60 minutes in vitro, wherein the dissolution profile is measured using a USP Dissolution Apparatus II with a helical sinker in 900 mL of 2.0% Tween at a temperature of 37±0.5° C., and paddles rotated at 100 rpm.

14. The process of claim 4 , wherein about 100 mg of the blended crystalline active ingredient in the pharmaceutical composition has an in vitro dissolution profile with a similarity factor (f 2 ) of at least 50 to 100 compared to the reference dissolution profile of 52.7% dissolved at 10 minutes, 61.7% dissolved at 15 minutes, 67.7% dissolved at 20 minutes, 75.5% dissolved at 30 minutes, 82.6% dissolved at 45 minutes, and 87.0% dissolved at 60 minutes in vitro, wherein the dissolution profile is measured using a USP Dissolution Apparatus II with a helical sinker in 900 mL of 2.0% Tween at a temperature of 37±0.5° C., and paddles rotated at 100 rpm.

15. The process of claim 5 , wherein about 100 mg of the blended crystalline active ingredient in the pharmaceutical composition has an in vitro dissolution profile with a similarity factor (f 2 ) of at least 50 to 100 compared to the reference dissolution profile of 52.7% dissolved at 10 minutes, 61.7% dissolved at 15 minutes, 67.7% dissolved at 20 minutes, 75.5% dissolved at 30 minutes, 82.6% dissolved at 45 minutes, and 87.0% dissolved at 60 minutes in vitro, wherein the dissolution profile is measured using a USP Dissolution Apparatus II with a helical sinker in 900 mL of 2.0% Tween at a temperature of 37±0.5° C., and paddles rotated at 100 rpm.

16. The process of claim 6 , wherein about 100 mg of the blended crystalline active ingredient in the pharmaceutical composition has an in vitro dissolution profile with a similarity factor (f 2 ) of at least 56 to 100 compared to the reference dissolution profile of 52.7% dissolved at 10 minutes, 61.7% dissolved at 15 minutes, 67.7% dissolved at 20 minutes, 75.5% dissolved at 30 minutes, 82.6% dissolved at 45 minutes, and 87.0% dissolved at 60 minutes in vitro, wherein the dissolution profile is measured using a USP Dissolution Apparatus II with a helical sinker in 900 mL of 2.0% Tween at a temperature of 37±0.5° C., and paddles rotated at 100 rpm.

17. The process of claim 7 , wherein about 100 mg of the blended crystalline active ingredient in the pharmaceutical composition has an in vitro dissolution profile with a similarity factor (f 2 ) of at least 56 to 100 compared to the reference dissolution profile of 52.7% dissolved at 10 minutes, 61.7% dissolved at 15 minutes, 67.7% dissolved at 20 minutes, 75.5% dissolved at 30 minutes, 82.6% dissolved at 45 minutes, and 87.0% dissolved at 60 minutes in vitro, wherein the dissolution profile is measured using a USP Dissolution Apparatus II with a helical sinker in 900 mL of 2.0% Tween at a temperature of 37±0.5° C., and paddles rotated at 100 rpm.

18. The process of claim 8 , wherein about 100 mg of the blended crystalline active ingredient in the pharmaceutical composition has an in vitro dissolution profile with a similarity factor (f 2 ) of at least 56 to 100 compared to the reference dissolution profile of 52.7% dissolved at 10 minutes, 61.7% dissolved at 15 minutes, 67.7% dissolved at 20 minutes, 75.5% dissolved at 30 minutes, 82.6% dissolved at 45 minutes, and 87.0% dissolved at 60 minutes in vitro, wherein the dissolution profile is measured using a USP Dissolution Apparatus II with a helical sinker in 900 mL of 2.0% Tween at a temperature of 37±0.5° C., and paddles rotated at 100 rpm.

19. The process of claim 9 , wherein about 100 mg of the blended crystalline active ingredient in the pharmaceutical composition has an in vitro dissolution profile with a similarity factor (f 2 ) of at least 56 to 100 compared to the reference dissolution profile of 52.7% dissolved at 10 minutes, 61.7% dissolved at 15 minutes, 67.7% dissolved at 20 minutes, 75.5% dissolved at 30 minutes, 82.6% dissolved at 45 minutes, and 87.0% dissolved at 60 minutes in vitro, wherein the dissolution profile is measured using a USP Dissolution Apparatus II with a helical sinker in 900 mL of 2.0% Tween at a temperature of 37±0.5° C., and paddles rotated at 100 rpm.

20. The process of claim 10 , wherein about 100 mg of the blended crystalline active ingredient in the pharmaceutical composition has an in vitro dissolution profile with a similarity factor (f 2 ) of at least 56 to 100 compared to the reference dissolution profile of 52.7% dissolved at 10 minutes, 61.7% dissolved at 15 minutes, 67.7% dissolved at 20 minutes, 75.5% dissolved at 30 minutes, 82.6% dissolved at 45 minutes, and 87.0% dissolved at 60 minutes in vitro, wherein the dissolution profile is measured using a USP Dissolution Apparatus II with a helical sinker in 900 mL of 2.0% Tween at a temperature of 37±0.5° C., and paddles rotated at 100 rpm.

21. A process of producing a pharmaceutical composition comprising suberoylanilide hydroxamic acid or a pharmaceutically acceptable salt or hydrate thereof as an active ingredient, wherein about 100 mg of the active ingredient has an in vitro dissolution profile with a similarity factor (f 2 ) of at least 50 to 100 compared to the reference dissolution profile of 52.7% dissolved at 10 minutes, 61.7% dissolved at 15 minutes, 67.7% dissolved at 20 minutes, 75.5% dissolved at 30 minutes, 82.6% dissolved at 45 minutes, and 87.0% dissolved at 60 minutes in vitro, wherein the dissolution profile is measured using a USP Dissolution Apparatus II with a helical sinker in 900 mL of 2.0% Tween at a temperature of 37±0.5° C., and paddles rotated at 100 rpm, comprising the steps of:

(a) milling crystalline suberoylanilide hydroxamic acid or a pharmaceutically acceptable salt or hydrate thereof to produce at least a first batch of milled crystalline active ingredient having a mean particle size in the range of about 25 to 45 μm;

(b) crystallizing suberoylanilide hydroxamic acid or a pharmaceutically acceptable salt or hydrate thereof to produce at least a second batch of crystalline active ingredient having a mean particle size in the range of about 130 to 180 μm;

(c) blending said at least first batch with said at least second batch of crystalline active ingredient; and

(d) producing said pharmaceutical composition from said blended first and second batch.

22. The process of claim 21 , wherein in step (c), about 60-80% of the second batch crystalline active ingredient is blended with about 40-20% of the first batch milled crystalline active ingredient.

23. The process of claim 21 , wherein step (d) is performed by encapsulating a portion of the blended crystalline active ingredient.

24. The process of claim 22 , wherein the active ingredient is suberoylanilide hydroxamic acid.

Assignments (3)
MERGER Recorded Aug 8, 2022
From: MERCK SHARP & DOHME CORP.
To: MERCK SHARP & DOHME LLC
Reel/Frame 061102/0145 →
MERGER Recorded Apr 2, 2013
From: MERCK SHARP & DOHME CORP.
To: SCHERING CORPORATION
Reel/Frame 030133/0200 →
CHANGE OF NAME Recorded Apr 2, 2013
From: SCHERING CORPORATION
To: MERCK SHARP & DOHME CORP.
Reel/Frame 030137/0837 →