Method for making homogeneous spray-dried solid amorphous drug dispersions utilizing modified spray-drying apparatus
View Patent ↗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.
1. A process for producing a pharmaceutical composition comprising the steps:
(a) forming a feed solution comprising a drug, a polymer and a solvent, wherein said 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, vinyl polymers and copolymers having at least one substituent selected from the group consisting of hydroxyl, alkylacyloxy, and cyclicamido, and polyvinyl alcohols that have at least a portion of their repeat units in hydrolyzed form, polyvinyl pyrrolidone, poloxamers, and blends thereof;
(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 1.0 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 amorphous dispersion of said drug homogeneously distributed throughout 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 particles have an average diameter of at least 40 μm.
6. The process of claim 1 wherein said particles have an average diameter of at least 50 μm.
7. The process of claim 1 wherein said spray-drying apparatus further comprises a gas disperser for dispersing said gas into said drying chamber.
8. The process of claim 7 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.