IP Library Granted Patent US 7,468,428
Granted Patent B2
US 7,468,428 · App. 10/802,282 · Granted Dec 23, 2008

Lyophilized azithromycin formulation

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 7,468,428
App. No.
10/802,282
Granted
Dec 23, 2008
Kind
B2
Abstract

The invention provides among other things a stable, sterile pharmaceutical formulation comprising lyophilized azithromycin and ethanol. The invention also provides a method of producing a stable, sterile pharmaceutical product comprising lyophilized azithromycin. The invention also provides a pharmaceutical dosage form comprising the pharmaceutical formulation, as well as a method of treating a disease in a patient comprising administering a solution of the pharmaceutical formulation to a patient.

Claims (27)

1. A method of producing a stable, sterile pharmaceutical formulation comprising lyophilized azithromycin, which method comprises:

(a) preparing a liquid composition comprising an ethanolate of azithromycin, an acid selected from the group consisting of citric acid, hydrochloric acid, lactic acid, glycolic acid, acetic acid, phosphoric acid, and tartaric acid, and an aqueous solvent,

(b) chilling the composition to a temperature from about −10° C. to about 15° C., wherein the temperature is maintained for at least about 20 minutes to about 2 hours,

(c) freezing the composition to a temperature of from about −30° C. to about −50° C., to produce a frozen mixture, wherein the temperature is maintained for at least about 1 hour,

(d) subjecting the frozen mixture to a primary drying stage, which comprises applying a vacuum to reduce the pressure by an amount effective to remove aqueous solvent from the frozen mixture, and, while applying the vacuum, changing the temperature of the frozen mixture to a primary drying temperature, wherein the primary drying temperature is from about 0° C. to about 20° C., and wherein the primary drying temperature is maintained for at least about 20 hours to about 40 hours, to produce a first intermediate, and

(e) subjecting the first intermediate to a secondary drying stage, which comprises applying a vacuum to reduce the pressure by an amount effective to remove aqueous solvent from the first intermediate, and, while applying the vacuum, (i) changing the temperature of the first intermediate to a first secondary drying temperature, wherein the first secondary drying temperature is from about 20° C. to about 40° C., and wherein the first secondary drying temperature is maintained for at least about 10 hours to about 20 hours, and (ii) changing the temperature of the first intermediate to a second secondary drying temperature, wherein the second secondary drying temperature is from about 30° C. to about 50° C., and wherein the second secondary drying temperature is maintained for at least about 10 hours to about 20 hours, to produce the pharmaceutical formulation, wherein ethanol is present in an amount from about 0.005% to about 0.5% by weight of the pharmaceutical formulation.

2. The method of claim 1 , wherein the composition is chilled to a temperature from about 0° C. to about 10° C.

3. The method of claim 1 , wherein the composition is frozen to a temperature of about −40° C.

4. The method of claim 1 , wherein the primary drying temperature is about 8° C.

5. The method of claim 1 , wherein the primary drying temperature in the primary drying stage is maintained for at least about 36 hours.

6. The method of claim 1 , wherein the primary drying stage is carried out at a pressure of about 200 micron Hg or less.

7. The method of claim 6 , wherein the primary drying stage is carried out at a pressure of about 80 micron Hg.

8. The method of claim 1 , wherein the first secondary drying temperature is about 35° C.

9. The method of claim 1 , wherein the second secondary drying temperature is about 45° C.

10. The method of claim 1 , wherein the temperature of the frozen mixture in the secondary drying stage is changed at a rate of about 1° C. per minute or less.

11. The method of claim 10 , wherein the temperature of the frozen mixture in the secondary drying stage is changed at a rate from about 0.05 to about 0.1° C. per minute.

12. The method of claim 1 , wherein the first secondary drying temperature in the secondary drying stage is maintained for at least about 15 hours.

13. The method of claim 1 , wherein the second secondary drying temperature in the secondary drying stage is maintained for at least about 18 hours.

14. The method of claim 1 , wherein the secondary drying stage is carried out at a pressure of about 200 micron Hg or less.

15. The method of claim 14 , wherein the secondary drying stage is carried out at a pressure of about 80 micron Hg.

16. The method of claim 1 , wherein the composition is aseptically filtered and aseptically filled into a container after the completion of step (a) and before the completion of step (b).

17. A method of producing a stable, sterile pharmaceutical formulation comprising lyophilized azithromycin, which method comprises:

(a) preparing a liquid composition comprising an ethanolate of Azithromycin, citric acid, and an aqueous solvent,

(b) chilling the composition to a temperature from about −10° C. to about 15° C., wherein the temperature is maintained for at least about 20 minutes to about 2 hours,

(c) freezing the composition to a temperature of from about 10° C. to about 70° C., to produce a frozen mixture, wherein the temperature is maintained for at least about 30 minutes to about 20 hours,

(d) subjecting the frozen mixture to a primary drying stage, which comprises applying a vacuum to reduce the pressure by an amount effective to remove aqueous solvent from the frozen mixture, and, while applying the vacuum, changing the temperature of the frozen mixture to a primary drying temperature, wherein the primary drying temperature is from about −30° C. to about 20° C., and wherein the primary drying temperature is maintained for at least about 15 hours to about 50 hours, to produce a first intermediate, and

(e) subjecting the first intermediate to a secondary drying stage, which comprises applying a vacuum to reduce the pressure by an amount effective to remove aqueous solvent from the first intermediate, and, while applying the vacuum, (i) changing the temperature of the first intermediate to a first secondary drying temperature, wherein the first secondary drying temperature is from about 0° C. to about 45° C., and wherein the first secondary drying temperature is maintained for at least about 5 hours to about 30 hours, and (ii) changing the temperature of the first intermediate to a second secondary drying temperature, wherein the second secondary drying temperature is from about 0° C. to about 60° C., and wherein the second secondary drying temperature is maintained for at least about 5 hours to about 30 hours, to produce the pharmaceutical formulation, wherein ethanol is present in an amount from about 0.005% to about 0.5% by weight of the pharmaceutical formulation.

Assignments (10)
RELEASE OF SECURITY INTEREST IN UNITED STATES PATENTS Recorded Jan 21, 2009
From: DEUTSCHE BANK AG, LONDON BRANCH, AS INTERCOMPANY BRIDGE COLLAGERAL AGENT
To: APP PHARMACEUTICALS, LLC
Reel/Frame 022127/0212 →
NOTICE OF GRANT OF SECURITY INTEREST IN UNITED STATES PATENTS Recorded Oct 20, 2008
From: APP PHARMACEUTICALS, LLC
To: DEUTSCHE BANK AG, LONDON BRANCH, AS INTERCOMPANY BRIDGE COLLAGERAL AGENT
Reel/Frame 021701/0018 →
NOTICE OF GRANT OF SECURITY INTEREST IN UNITED STATES PATENTS Recorded Oct 20, 2008
From: APP PHARMACEUTICALS, LLC
To: DEUTSCHE BANK AG, LONDON BRANCH, AS INTERCOMPANY PRIMARY COLLATERAL AGENT
Reel/Frame 021701/0024 →
RELEASE OF SECURITY INTEREST Recorded Oct 20, 2008
From: DEUTSCHE BANK AG, NEW YORK BRANCH, ("AGENT")
To: APP PHARMACEUTICALS, LLC
Reel/Frame 021701/0115 →
NOTICE OF GRANT OF SECURITY INTEREST IN UNITED STATES PATENTS Recorded Oct 20, 2008
From: APP PHARMACEUTICALS, LLC
To: DEUTSCHE BANK AG, LONDON BRANCH, AS COLLATERAL AGENT
Reel/Frame 021701/0001 →
NOTICE OF GRANT OF SECURITY INTEREST Recorded Dec 13, 2007
From: APP PHARMACEUTICALS, LLC
To: DEUTSCHE BANK AG NEW YORK BRANCH
Reel/Frame 020243/0447 →
MERGER Recorded Nov 13, 2007
From: ABRAXIS BIOSCIENCE, INC.
To: ABRAXIS BIOSCIENCE, LLC
Reel/Frame 020098/0562 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 13, 2007
From: ABRAXIS BIOSCIENCE, LLC
To: APP PHARMACEUTICALS LLC
Reel/Frame 020098/0588 →
MERGER Recorded May 11, 2006
From: AMERICAN PHARMACEUTICAL PARTNERS, INC.
To: ABRAXIS BIOSCIENCE, INC.
Reel/Frame 017596/0965 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 29, 2004
From: WOO, BYUNG HO; KWOK, K. KEITH; YANG, KANG YONG
To: AMERICAN PHARMACEUTICAL PARTNERS, INC.
Reel/Frame 014790/0464 →