5625 - 5638 |
Multi-scale pharmaceutical process understanding: From particle to powder to dosage form Hamad ML, Bowman K, Smith N, Sheng XH, Morris KR |
5639 - 5650 |
Phase behavior and moisture sorption of deliquescent powders Kwok K, Mauer LJ, Taylor LS |
5651 - 5657 |
Breakage of drop nucleated granules in a breakage only high shear mixer Smith RM, Liu LAX, Litster JD |
5658 - 5668 |
Investigation of the effect of impeller rotation rate, powder flow rate, and cohesion on powder flow behavior in a continuous blender using PEPT Portillo PM, Vanarase AU, Ingram A, Seville JK, Ierapetritou MG, Muzzio FJ |
5669 - 5675 |
Controlled liquid antisolvent precipitation using a rapid mixing device Beck C, Dalvi SV, Dave RN |
5676 - 5686 |
Modeling of crystal morphology distributions. Towards crystals with preferred asymmetry Chakraborty J, Singh MR, Ramkrishna D, Borchert C, Sundmacher K |
5687 - 5698 |
Continuous blending of cohesive granular material Sarkar A, Wassgren C |
5699 - 5715 |
Local analysis of the tablet coating process: Impact of operation conditions on film quality Suzzi D, Radl S, Khinast JG |
5716 - 5727 |
Choked flow and importance of Mach I in freeze-drying process design Patel SM, Chaudhuri S, Pikal MJ |
5728 - 5733 |
Real-time monitoring of drug concentration in a continuous powder mixing process using NIR spectroscopy Vanarase AU, Alcala M, Rozo JIJ, Muzzio FJ, Romanach RJ |
5734 - 5746 |
PAT method to gather bioprocess parameters in real-time using simple input variables and first principle relationships Wechselberger P, Seifert A, Herwig C |
5747 - 5756 |
Discrete element simulation study of a Freeman powder rheometer Bharadwaj R, Ketterhagen WR, Hancock BC |
5757 - 5769 |
A model-based systems approach to pharmaceutical product-process design and analysis Gernaey KV, Gani R |
5770 - 5780 |
Reducing the mean size of API crystals by continuous manufacturing with product classification and recycle Griffin DW, Mellichamp DA, Doherty MF |