Diltiazem controlled release formulation and method of manufacture

• US 6,524,620 B2
• Filed: 07/20/1998
• Issued: 02/25/2003
• Est. Priority Date: 07/20/1998
• Status: Expired due to Term

• Current Assignee: Andrx Pharmaceuticals LLC (Abbvie Incorporated)
• Original Assignee: Andrx Pharmaceuticals (NC), Inc. (Abbvie Incorporated)
• Inventors: Chen, Chih-Ming, Jan, Steve, Cheng, Xiu Xiu
• Primary Examiner(s): Low, Christopher S. F.
• Assistant Examiner(s): Gupta, Anish
• Application Number:
  US09/119,323
• Publication Number:
  US 20010007681A1
• Time in Patent Office: 1,681 Days
• Field of Search: 424/494, 424/490, 424/528, 424/493, 424/497, 514/211.07, 514/777, 514/785, 514/786, 514/970
• US Class Current: 424/490
• CPC Class Codes: A61K 31/554 having at least one nitrogen and one sulfur as ring hetero atoms, e.g. clothiapine, diltiazem
• CPC Class Codes: A61K 9/5078 with drug-free core
• CPC Class Codes: A61K 9/5084 Mixtures of one or more drugs in different galenical forms, at least one of which being granules, microcapsules or (coated) microparticles according to A61K9/16 or A61K9/50, e.g. for obtaining a specific release pattern or for combining different drugs tablets containing such a mixture A61K9/2077

Abstract

A controlled release diltiazem dosage formulation comprising a plurality of active pellets coated with an extended release coating wherein the active pellets contain diltiazem or a pharmaceutically acceptable salt, a pharmaceutically acceptable inert seed and a binder and the extended release coating contains a water insoluble water permeable polymer, a channeling agent, a lubricant and optionally a surfactant. A single batch intermittent method of manufacturing a heterogeneous population of extended release pellets for use as a dosage formulation is also disclosed.

Claims

1. A process for manufacturing a controlled release diltiazem dosage formulation comprising the steps of:

a) adding a first allotment of active pellets containing diltiazem to a coating equipment;

b) coating the first allotment of active pellets with a first amount of extended release coating;

c) adding a second allotment of active pellets containing diltiazem to the equipment;

d) coating the first and second allotment of active pellets with a second amount of extended release coating;

e) optionally adding a third allotment of active pellets containing diltiazem to the equipment; and

f) optionally coating the first, second and third allotments of active pellets with an optional third amount of extended release coating.

2. The process as defined in claim 1 wherein the weight of the first allotment of active pellets comprise 34-90% of the total weight of the active pellets to be coated, the weight of the second allotment of active pellets comprise 5-33% of the total weight of active pellets to be coated and the weight of the third allotment of active pellets is not optional and comprises 5-43% of the total weight of the active pellets to be coated, where the combined weight of the three allotments is 100%.

3. The process as defined in claim 2 wherein the weight of the first allotment of active pellets comprise 65-80% of the total weight of the active pellets to be coated, the weight of the second allotment of active pellets comprise 5-15% of the total weight of the active pellets to be coated and the weight of the third allotment of active pellets comprises 15-25% of the total weight of the active pellets to be coated, where the combined weight of the three allotments is 100%.

4. The process as defined in claim 1 wherein the weight of the first amount of extended release coating comprises 10-33% of the total amount of extended release coating to be applied to all active pellets, the weight of the second amount of extended release coating comprises 34-80% of the total amount of extended release coating to be applied to all the active pellets and the weight of the third amount of extended release coating is not optional and comprises 10-40% of the total amount of extended release coating to be applied to all the active pellets, where the combined weight of the extended release coating is 100%.

5. The process as defined in claim 4 wherein the weight of the first amount of extended release coating comprises 15-25% of the total amount of extended release coating to be applied to all the active pellets, the weight of the second amount of extended release coating to be applied to all the active pellets comprises 50-75% of the total amount of extended release coating to be applied to all the active pellets and the weight of the third amount of extended release coating comprises 15-30% of the total amount of extended release coating to be applied to all the active pellets, where the combined weight of the extended release coating is 100%.

6. A process for manufacturing a controlled release diltiazem dosage formulation comprising the steps of:

a) adding a first allotment of active pellets which consist essentially of;

(i) from 10-30% of a pharmaceutically acceptable inert core based on the total weight of the active pellets;

(ii) from 50-85% of diltiazem or a pharmaceutically acceptable salt thereof based on the total weight of the active pellets;

(iii) from 0.25-5% of a water soluble binder based on the total weight of the active pellets; and

(iv) from 0.75-10% of a water insoluble binder based on the total weight of the active pellets;

to a fluidized bed coating equipment wherein the active pellets are prepared by applying a suspension of the diltiazem, water soluble binder and the water insoluble binder to the inert core;

b) coating the first allotment of active pellets with a first amount of extended release coating suspension which consists essentially of;

(i) from 60-85% of a water insoluble water permeable polymer based on the total weight of the extended release coating;

(ii) from 0.5-5% of a channeling agent based on the total weight of the extended release coating;

(iii) from 5-20% of talc based on the total weight of the coating;

(iv) 5-20% of magnesium stearate based on the total weight of the coating; and

(v) 0 to less than 1% of a surfactant based on the total weight of the coating;

c) adding a second allotment of active pellets as defined in step (a) to the equipment;

d) coating the first and second allotment of active pellets with a second amount of extended release coating suspension as defined in step (b);

e) adding a third allotment of active pellets as defined in step (a) to the equipment; and

f) coating the first, second and third allotments of active pellets with a third amount of extended release coating suspension as defined in step (b) wherein the first allotment of active pellets comprise 34-90% of the total weight of active pellets to be coated, the second allotment of active pellets comprise 5-33% of the total weight of the active pellets to be coated and the third allotment of active pellets comprises 5-43% of the total weight of the active pellets to be coated and the first amount of extended release coating suspension comprises 10-30% of the total amount of extended release coating suspension to be applied to all the active pellets, the second amount of extended release coating suspension comprises 34-80% of the total amount of extended release coating suspension to be applied to all the active pellets and the third amount of extended release coating suspension comprises 10-40% of the total amount of extended release coating suspension to be applied to all the active pellets.

7. The process as defined in claim 6 wherein the first allotment of active pellets comprise 65-80% of the total weight of active pellets to be coated, the second allotment of active pellets comprise 5-15% of the total weight of the active pellets to be coated and the third allotment of active pellets comprises 15-25% of the total weight of the active pellets to be coated and the first amount of extended release coating comprises 15-25% of the total amount of extended release coating to be applied to all the active pellets, the second amount of extended release coating comprises 50-75% of the total amount of extended release coating to be applied to all the active pellets and the third amount of extended release coating comprises 15-30% of the total amount of extended release coating to be applied to all the active pellets.

8. A product prepared according to the process defined in claim 6 that exhibits the following dissolution profile when tested in a United States Pharmacopoeia type 2 apparatus at 100 rpm in 900 ml of 0.1 N HCL and at 37°

C.;

after 2 hours 0-30% of the diltiazem is released;

after 4 hours 5-45% of the diltiazem is released;

after 8 hours 20-70% of the diltiazem is released;

not less than 45% of the diltiazem is released after 12 hours;

not less than 55% of the diltiazem is released after 18 hours;

and not less than 65% of the diltiazem is released after 20 hours.

9. The product as defined in claim 8 that exhibits the following dissolution profile when tested in a United States Pharmacopoeia type 2 apparatus at 100 rpm in 900 ml of 0.1 N HCL and at 37°

C.;

after 2 hours 5-25% of the diltiazem is released;

after 4 hours 10-35% of the diltiazem is released;

after 8 hours 35-65% of the diltiazem is released;

not less than 50% of the diltiazem is released after 12 hours;

not less than 60% of the diltiazem is released after 18 hours;

and not less than 70% of the diltiazem is released after 20 hours.

10. The process as defined in claim 6 wherein the diltiazem or a pharmaceutically acceptable salt is micronized.

11. The process as defined in claim 6 wherein the binder employed in the active pellets is selected from the group consisting of polyvinyl pyrrolidone, hydroxyethylcellulose, hydroxypropyl cellulose, hydroxypropyl methylcellulose, polyacrylate and ethylcellulose or a mixture thereof.

12. The process as defined in claim 6 wherein the binder employed in the active pellet is a combination of a water soluble binder and a water insoluble binder.

13. The process as defined in claim 12 wherein the ratio of water soluble binder to water insoluble binder is about 1:

1 to about 1;

3.

14. The process as defined in claim 13 wherein the ratio of water soluble binder to water insoluble binder is about 1:

2.

15. The process as defined in claim 12 wherein the water soluble binder is polyvinyl pyrrolidone and a water insoluble binder is ethylcellulose.

16. The process as defined in claim 12 wherein the water soluble binder comprises about 0.25-5% of the total weight of the active pellet and the water insoluble binder comprises about 0.75-10% of the total weight of the active pellet.

17. The process as defined in claim 6 wherein the water insoluble water permeable polymer of the extended release coating is selected from the group consisting of ethylcellulose, cellulose acetate, polyacrylates or mixtures thereof.

18. The process as defined in claim 17, wherein the water insoluble water permeable polymer is a poly(ethylacrylate methylmethacrylate) copolymer.

19. The process as defined in claim 6 wherein the channeling agent employed in the extended release coating is a water or acid soluble pharmaceutically acceptable substance selected from the group consisting of polyvinyl pyrolidone, hydroxyethylcellulose, hydroxypropyl cellulose, hydroxypropyl methycellulose, polyacrylate, sucrose, diltiazem, a pharmaceutically acceptable salt of diltiazem and any combination of the foregoing.

20. The process as defined in claim 19 wherein the channeling agent is hydroxypropyl methylcellulose.

21. The process as defined in claim 6 wherein the lubricant is selected from the group consisting of talc, magnesium stearate, silicon dioxide, kaolin and a mixture of the foregoing.

22. The process as defined in claim 21 wherein the lubricant is a mixture of talc and magnesium stearate.

23. The process as defined in claim 22 wherein the ratio of talc to magnesium stearate is about 1:

2 to about 2;

1.

24. The process as defined in claim 6 wherein the surfactant is polysorbate 80.

25. The process as defined in claim 8 wherein the inert core is a non-pareil seed of sugar or starch having a diameter ranging from about 15-50 mesh.

26. The process as defined in claim 6 wherein the first, second, and third allotment of active pellets are coated with varying number of layers of extended release coating wherein said extended release coating consists of a homogeneous mixture comprising about 60-85% of poly (ethyl acrylate methylacrylate) copolymer and a channeling agent.