IP Library Granted Patent US 12,233,076
Granted Patent B2
US 12,233,076 · App. 17/831,926 · Granted Feb 25, 2025

Stable liquid formulations of cyclophosphamide and processes to prepare the same

Inventors: Riyaz Ahmed Shaik (Hyderabad, IN); Ananya Saha (Asansol, IN); Svb Janardhan Garikipati (Visakhapatnam, IN); Akash Chaurasiya (Agra, IN); Bhavesh Vallabhbhai Patel (Hyderabad, IN); Harshal Bhagwatwar (Hyderabad, IN); Sumitra Ashok Pillai (Ahmedabad, IN)
Assignee: Avyxa Holdings, LLC
A61K31/664A61K9/0019A61K9/08A61K9/19A61K31/675A61K47/10A61K47/26A61K47/44B01D15/08
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Quick Facts
Patent No.
US 12,233,076
App. No.
17/831,926
Granted
Feb 25, 2025
Kind
B2
Abstract

The present invention relates to stable liquid pharmaceutical formulations of cyclophosphamide comprising cyclophosphamide and at least one pharmaceutically acceptable excipient wherein moisture content of the liquid formulation is less than about 2.0% by weight. The invention further relates to stable liquid formulations of cyclophosphamide prepared by a process comprising a step of reducing the moisture content from cyclophosphamide or liquid compositions of cyclophosphamide or both. The invention further relate to method of using such stable liquid formulations of cyclophosphamide for parenteral administration either as ready-to-use or ready-to-dilute for treating various cancer disorders.

Claims (47)

1. A process for preparing a stable liquid formulation of cyclophosphamide, wherein the process comprises reducing the moisture content from cyclophosphamide or liquid compositions of cyclophosphamide or both by a drying process or by means of adsorbents.

2. The process according to claim 1 , wherein the moisture content of cyclophosphamide is reduced by a drying process selected from the group consisting of vacuum drying, lyophilization, and solvent evaporation.

3. The process according to claim 2 , wherein the drying process is vacuum drying.

4. The process according to claim 3 , wherein the vacuum drying is performed at a temperature ranging from about 5° C. to about 50° C.

5. The process according to claim 3 , wherein the vacuum drying is carried out for a time period ranging from about 1 hour to about 24 hours.

6. The process according to claim 1 , wherein the moisture content from liquid composition of cyclophosphamide is reduced by means of adsorbents selected from the group consisting of molecular sieves, silica gel, activated alumina, and activated charcoal.

7. The process according to claim 6 , wherein the liquid formulation is prepared by a process comprising the steps of:

a) preparing the bulk solution of cyclophosphamide by dissolving cyclophosphamide in a solvent,

b) incubating the solution of cyclophosphamide of step a) with adsorbents for suitable period of time,

c) filtering the cyclophosphamide solution of step b) by using filter.

8. The process according to claim 7 , wherein the incubation is carried out for a time period ranging from about 1 hour to about 24 hours.

9. The process according to claim 6 , wherein the liquid formulation is prepared by a process comprising the steps of:

a) preparing the bulk solution of cyclophosphamide by dissolving cyclophosphamide in a solvent,

b) preparing a column by using an adsorbent or mixture of adsorbents,

c) passing the cyclophosphamide solution from step a) through the column of step b),

d) optionally filtering the solution obtained from step c) by using filter.

10. The process according to claim 7 , wherein the cyclophosphamide solution is prepared by dissolving cyclophosphamide in the solvent by stirring at a speed ranging from about 50 to about 2000 rpm.

11. The process according to claim 7 , wherein the solvent is selected from the group consisting of alcohol, polyethylene glycol, propylene glycol, dimethyl acetamide, glycerol and mixtures thereof.

12. The process according to claim 11 , wherein the solvent is alcohol or its combinations.

13. The process according to claim 12 , wherein the solvent is ethanol or its combinations.

14. The process according to claim 7 , wherein the adsorbent is selected from the group consisting of molecular sieves, silica gel, activated charcoal and mixtures thereof.

15. The process according to claim 14 , wherein the adsorbent is molecular sieves.

16. The process according to claim 15 , wherein the molecular sieves include different grades of molecular sieves selected from the group consisting of grade 3A, grade 4A, grade 5A, grade 10X, and grade 13X.

17. The process according to claim 7 , wherein the weight ratio of cyclophosphamide bulk solution to molecular sieves is in the range of about 1:0.01 to about 1:50.

18. The process according to claim 17 , wherein the weight ratio of cyclophosphamide bulk solution to molecular sieves is in the range of about 1:0.05 to about 1:25.

19. The process according to claim 18 , wherein the weight ratio of cyclophosphamide bulk solution to molecular sieves is in the range of about 1:0.1 to 1:10.

20. The process according to claim 9 , wherein the cyclophosphamide solution is passed through the column at a flow rate ranging from about 0.1 mL/minute to about 5 L/minute.

21. The process according to claim 9 , wherein the cyclophosphamide solution is passed through the column of adsorbents in a recirculation mode.

22. The process according to claim 7 , wherein in step b) the bulk solution is incubated with molecular sieves until the moisture content of the solution is less than about 2.0% by weight.

23. The process according to claim 9 , wherein in step b) the column is prepared by using molecular sieves and in step c) the cyclophosphamide solution is passed through the column in a recirculation mode until the moisture content of the solution is less than about 2.0% by weight.

24. A process for preparing a stable liquid formulation of cyclophosphamide having a moisture content of less than about 2.0% by weight, wherein the process comprises the steps of:

a) reducing the moisture content of cyclophosphamide by vacuum drying;

b) preparing bulk solution of cyclophosphamide by dissolving cyclophosphamide of step a) in ethanol;

c) incubating the cyclophosphamide bulk solution of step b) with molecular sieves or passing the cyclophosphamide bulk solution of step b) through a column of molecular sieves in a recirculation mode,

d) optionally filtering the solution obtained from step c) through a filter.

25. The process according to claim 1 , wherein the liquid formulation is intended for parenteral administration.

26. The process according to claim 25 , wherein the liquid formulation is ready-to-use formulation.

27. The process according to claim 25 , wherein the liquid formulation is ready-to-dilute formulation.

28. The process according to claim 9 , wherein the cyclophosphamide solution is prepared by dissolving cyclophosphamide in a solvent by stirring at a speed ranging from about 50 to about 2000 rpm.

29. The process according to claim 9 , wherein the solvent is selected from the group consisting of alcohol, polyethylene glycol, propylene glycol, dimethyl acetamide, glycerol and mixtures thereof.

30. The process according to claim 9 , wherein the adsorbent is selected from the group consisting of molecular sieves, silica gel, activated charcoal and mixtures thereof.

31. The process according to claim 9 , wherein the weight ratio of cyclophosphamide bulk solution to molecular sieves is in the range of about 1:0.01 to about 1:50.

32. The process according to claim 1 , wherein the total impurities are less than about 6% after storage at 2-8° C. for at least 6 months.

33. The process according to claim 1 , wherein the total impurities are less than about 6% after storage at 25° C. for at least 2 months.

34. The process according to claim 24 , wherein the total impurities are less than about 6% after storage at 2-8° C. for at least 6 months.

35. The process according to claim 24 , wherein the total impurities are less than about 6% after storage at 25° C. for at least 2 months.

36. The process according to claim 1 , wherein the moisture content of the formulation is less than about 2.0% by weight.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 19, 2024
From: DR. REDDY'S LABORATORIES LIMITED
To: AVYXA HOLDINGS, LLC
Reel/Frame 068327/0582 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 24, 2024
From: SHAIK, RIYAZ AHMED; SAHA, ANANYA; GARIKIPATI, SVB JANARDHAN; CHAURASIYA, AKASH; PATEL, BHAVESH VALLABHBHAI; BHAGWATWAR, HARSHAL; PILLAI, SUMITRA ASHOK
To: DR. REDDY’S LABORATORIES LIMITED
Reel/Frame 067818/0305 →
Priority Claims (2)
IN 3454/CHE/2014 · Jul 11, 2014 · national
IN 5215/CHE/2014 · Oct 17, 2014 · national
Continuity (3)
Division 15402712 · Jan 10, 2017
Continuation In Part PCTIB2015055285 · Jul 13, 2015
Related Publication 20220296617A1 · Sep 22, 2022
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