scholarly journals Quantitative Assessment of Mass Flow Boundaries in Continuous Twin-screw Granulation

2016 ◽  
Vol 70 (9) ◽  
pp. 604-609 ◽  
Author(s):  
Adrian Schmidt ◽  
Hans de Waard ◽  
Klaus-Peter Moll ◽  
Markus Krumme ◽  
Peter Kleinebudde
Pharmaceutics ◽  
2021 ◽  
Vol 13 (2) ◽  
pp. 293
Author(s):  
Alexander Ryckaert ◽  
Michael Ghijs ◽  
Christoph Portier ◽  
Dejan Djuric ◽  
Adrian Funke ◽  
...  

The drying unit of a continuous from-powder-to-tablet manufacturing line based on twin-screw granulation (TSG) is a crucial intermediate process step to achieve the desired tablet quality. Understanding the size reduction of pharmaceutical granules before, during, and after the fluid bed drying process is, however, still lacking. A first major goal was to investigate the breakage and attrition phenomena during transport of wet and dry granules, the filling phase, and drying phase on a ConsiGma-25 system (C25). Pneumatic transport of the wet granules after TSG towards the dryer induced extensive breakage, whereas the turbulent filling and drying phase of the drying cells caused rather moderate breakage and attrition. Subsequently, the dry transfer line was responsible for additional extensive breakage and attrition. The second major goal was to compare the influence of drying air temperature and drying time on granule size and moisture content for granules processed with a commercial-scale ConsiGma-25 system and with the R&D-scale ConsiGma-1 (C1) system. Generally, the granule quality obtained after drying with C1 was not predictive for the C25, making it challenging during process development with the C1 to obtain representative granules for the C25.


Pharmaceutics ◽  
2018 ◽  
Vol 10 (4) ◽  
pp. 207 ◽  
Author(s):  
Jens Wesholowski ◽  
Andreas Berghaus ◽  
Markus Thommes

Over recent years Twin-Screw-Extrusion (TSE) has been established as a platform technology for pharmaceutical manufacturing. Compared to other continuous operation, one of the major benefits of this method is the combination of several unit operations within one apparatus. Several of these are linked to the Residence Time Distribution (RTD), which is typically expressed by the residence time density function. One relevant aspect for pharmaceutical processes is the mixing capacity, which is represented by the width of this distribution. In the frame of this study the influence of the mass flow, the temperature and the screw-barrel clearance were investigated for a constant barrel load (specific feed load, SFL). While the total mass flow as well as the external screw diameter affected the mixing performance, the barrel temperature had no influence for the investigated range. The determined results were additionally evaluated with respect to a fit to the Twin-Dispersion-Model (TDM). This model is based on the superimposition of two mixing functions. The correlations between varied process parameters and the obtained characteristic model parameters proved this general physical view on extrusion.


2016 ◽  
Vol 110 ◽  
pp. 43-53 ◽  
Author(s):  
Sushma V. Lute ◽  
Ranjit M. Dhenge ◽  
Michael J. Hounslow ◽  
Agba D. Salman

2020 ◽  
Vol 576 ◽  
pp. 119004 ◽  
Author(s):  
Christoph Portier ◽  
Kenny Pandelaere ◽  
Urbain Delaet ◽  
Tamas Vigh ◽  
Giustino Di Pretoro ◽  
...  

2015 ◽  
Vol 276 ◽  
pp. 89-102 ◽  
Author(s):  
Tim Chan Seem ◽  
Neil A. Rowson ◽  
Andy Ingram ◽  
Zhenyu Huang ◽  
Shen Yu ◽  
...  

2020 ◽  
Vol 591 ◽  
pp. 119941
Author(s):  
Kristina E. Steffens ◽  
Marvin B. Brenner ◽  
Michael U. Hartig ◽  
Marius Monschke ◽  
Karl G. Wagner

2019 ◽  
Vol 568 ◽  
pp. 118541 ◽  
Author(s):  
Aquino L. Mundozah ◽  
Jiankai Yang ◽  
Claire C. Tridon ◽  
James J. Cartwright ◽  
Chalak S. Omar ◽  
...  

Sign in / Sign up

Export Citation Format

Share Document