“…mMA:
Denser product compared to fluidized bed, reduced compressibility and dissolution rate ( 275 – 278 ) Extruder | Melt extrusion (Hot fusion) and shaping through die (Solid dispersion) Downstream auxiliary equipment for cooling, further shaping ( e.g., pellets) and particle size reduction ( 279 ) | • Adaptable for heat sensitive drugs: application of low recrystallizing excipients ( 43 ), reduction of residence time, or addition of antioxidants ( 279 ) • High content uniformity ( 280 ) • Various downstream processing methods and dosage forms are available ( 280 , 281 ) • Fast, continuous manufacturing feasible (comparably easy scale up) ( 282 , 283 ) • Wide variety of suitable formulation strategies ( e.g., bioavailability enhancement ( 284 ), controlled release, taste masking ( 281 ) etc. ) | • High level of know how required, high modularity of process • Formulation development time- and material-consuming ( 282 ) • Additional expensive downstream equipment required • Storage stability might be an issue ( e.g., recrystallization of amorphous drug) ( 284 ) |
Spray dryer | Spray congealing Hot fusion before spraying into cooling chamber Depending on nozzle type: Microsphere (Matrix) Microcapsule (core/shell) | • Fast cooling step • Highly spherical particles with smooth surface ( 285 , 286 ) • Different atomization methods applicable: wide particle size range (~10–6 mm) ( 286 ) and high through put achievable ( 287 ) • Comparably easy upscaling ( 285 ) • PAT-tools: laser diffraction, NIR ( 288 , 289 ) | • Limited drug load (solid API: 30%, liquid API: 50%) ( 285 ) • Unsuitable for heat sensitive drugs, degradation in melt ( 285 ) • Original particle size must be significantly smaller than desired product size. Additional milling step might be necessary ( 286 ) • Additional melt-mixing equipment required • Resolidification of larger particles requires longer ... |
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