IP Library Granted Patent US 8,343,550
Granted Patent B2
US 8,343,550 · App. 13/165,732 · Granted Jan 1, 2013

Method for making homogeneous spray-dried solid amorphous drug dispersions utilizing modified spray-drying apparatus

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 8,343,550
App. No.
13/165,732
Granted
Jan 1, 2013
Kind
B2
Abstract

Conventional spray-drying methods are improved by incorporation of a pressure nozzle and a diffuser plate to improve the flow of drying gas and a drying chamber extension to increase drying time, such improvements leading to the formation of homogeneous solid dispersions of drugs in concentration-enhancing polymers.

Claims (87)

1. A process for producing a pharmaceutical composition comprising the steps:

(a) forming a feed solution comprising a drug, a polymer and a solvent;

(b) directing said feed solution to a spray-drying apparatus comprising

(i) a drying chamber having a volume V dryer and a height H,

(ii) atomizing means for atomizing said feed solution into droplets, and

(iii) a source of heated drying gas for drying said droplets, said source delivering said drying gas to said drying chamber at a flow rate of G,

wherein

V dryer is measured in m 3 ,

H is at least 1 m,

G is measured in m 3 /sec,

and wherein the following mathematical relationship is satisfied

V

dryer

G

10

seconds

;

(c) atomizing said feed solution into droplets in said drying chamber by said atomizing means;

(d) contacting said droplets with said heated drying gas to form particulates of a solid dispersion of said drug and said polymer; and

(e) collecting said particulates.

2. The process of claim 1 wherein said droplets have an average diameter of at least 50 μm and a D 10 of at least 10 μm.

3. The process of claim 1 wherein at least 80 vol % of said particulates have diameters of greater than 10 μm.

4. The process of claim 1 wherein at least 90 vol % of said particulates have diameters of greater than 10 μm.

5. The process of claim 1 wherein said drug in said dispersion is substantially amorphous and said dispersion is substantially homogeneous.

6. The process of claim 1 wherein said polymer is a concentration-enhancing polymer.

7. The process of claim 6 wherein said concentration-enhancing polymer is selected from the group consisting of ionizable cellulosic polymers, non-ionizable cellulosic polymers, ionizable non-cellulosic polymers, non-ionizable non-cellulosic polymers, neutralized acidic polymers and blends thereof.

8. The process of claim 6 wherein said concentration-enhancing polymer is selected from the group consisting of hydroxypropyl methyl cellulose, hydroxypropyl cellulose, carboxymethyl ethyl cellulose, hydroxypropyl methyl cellulose acetate succinate, hydroxypropyl methyl cellulose phthalate, cellulose acetate phthalate, cellulose acetate trimellitate, polyvinyl alcohols that have at least a portion of their repeat units in hydrolyzed form, polyvinyl pyrrolidone, poloxamers, and blends thereof.

9. The process of claim 6 wherein said concentration-enhancing polymer is hydroxypropyl methyl cellulose acetate succinate.

10. The process of claim 1 wherein said particles have an average diameter of at least 40 μm.

11. The process of claim 1 wherein said particles have an average diameter of at least 50 μm.

12. The process of claim 1 wherein said spray-drying apparatus further comprises a gas disperser for dispersing said gas into said drying chamber.

13. The process of claim 12 wherein said drying gas is dispersed into said drying chamber such that the primary axis of flow of said drying gas is parallel to the axis of said atomizing means.

14. A process for producing a pharmaceutical composition comprising the steps:

(a) forming a feed solution comprising a drug, a polymer and a solvent;

(b) directing said feed solution to a spray-drying apparatus comprising

(i) a drying chamber having a volume V dryer and a height H,

(ii) atomizing means for atomizing said feed solution into droplets,

(iii) a source of heated drying gas for drying said droplets, said source delivering said drying gas to said drying chamber at a flow rate of G, and

(iv) a gas dispersing means for dispersing said gas into said drying chamber such that the primary axis of flow of said drying gas is parallel to the axis of said atomizing means;

wherein

V dryer is measured in m 3 ,

H is at least 1 m,

G is measured in m 3 /sec,

and wherein the following mathematical relationship is satisfied

V

dryer

G

10

seconds

;

(c) atomizing said feed solution into droplets in said drying chamber by said atomizing means;

(d) contacting said droplets with said heated drying gas to form particulates of a solid dispersion of said drug and said polymer; and

(e) collecting said particulates.

15. The process of claim 14 wherein said droplets have an average diameter of at least 50 μm and a D 10 of at least 10 μm.

16. The process of claim 14 wherein said polymer is a concentration-enhancing polymer.

17. A process for producing a pharmaceutical composition comprising the steps:

(a) forming a feed solution comprising a drug, a polymer and a solvent;

(b) directing said feed solution to a spray-drying apparatus comprising

(i) a drying chamber having a volume V dryer and a height H,

(ii) atomizing means for atomizing said feed solution into droplets,

(iii) a source of heated drying gas for drying said droplets, said source delivering said drying gas to said drying chamber at a flow rate of G, and

(iv) a gas dispersing means for dispersing said gas into said drying chamber such that the primary axis of flow of said drying gas is parallel to the axis of said atomizing means;

wherein

V dryer is measured in m 3 ,

H is at least 1 m,

G is measured in m 3 /sec,

and wherein the following mathematical relationship is satisfied

V

dryer

G

10

seconds

;

(c) atomizing said feed solution into droplets in said drying chamber by said atomizing means, said droplets having an average diameter of at least 50 μm and a D 10 of at least 10 μm;

(d) contacting said droplets with said heated drying gas to form particulates of a solid dispersion of said drug and said polymer; and

(e) collecting said particulates.

18. The process of claim 17 wherein said polymer is a concentration-enhancing polymer.

19. The process of claim 18 wherein said concentration-enhancing polymer is selected from the group consisting of hydroxypropyl methyl cellulose, hydroxypropyl cellulose, carboxymethyl ethyl cellulose, hydroxypropyl methyl cellulose acetate succinate, hydroxypropyl methyl cellulose phthalate, cellulose acetate phthalate, cellulose acetate trimellitate, polyvinyl alcohols that have at least a portion of their repeat units in hydrolyzed form, polyvinyl pyrrolidone, poloxamers, and blends thereof.

Assignments (4)
CHANGE OF NAME Recorded Feb 2, 2023
From: BEND RESEARCH, INC.
To: LONZA BEND INC.
Reel/Frame 062971/0292 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 11, 2013
From: BEND RESEARCH, INC.
To: PFIZER INC.
Reel/Frame 031182/0091 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 11, 2013
From: BEYERINCK, RONALD A.; DEIBELE, HEATHER L.M.; DOBRY, DAN E.; RAY, RODERICK J.; SETTELL, DANA M.; SPENCE, KEN R.
To: BEND RESEARCH, INC.
Reel/Frame 031182/0099 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 11, 2013
From: PFIZER INC.; PFIZER PRODUCTS INC.
To: BEND RESEARCH, INC.
Reel/Frame 031182/0110 →