RT Journal Article
SR Electronic
T1 Scalability of Sterilizing-Grade Filters in Different Filtration Modes
JF PDA Journal of Pharmaceutical Science and Technology
JO PDA J Pharm Sci Technol
FD Parenteral Drug Association (PDA)
SP 644
OP 659
DO 10.5731/pdajpst.2019.011254
VO 74
IS 6
A1 Dippel Jannik
A1 Handt Sebastian
A1 Hansmann BjÖrn
A1 Loewe Thomas
YR 2020
UL http://journal.pda.org/content/74/6/644.abstract
AB Scalability of filter throughput in normal flow filtration runs is an important consideration in the development of biopharmaceutical downstream processes. Depending on the filtration mode used, filter device geometry can significantly affect scalability. In this study, scaling of different polyethersulfone sterilizing-grade filters was performed in two filtration modes—at constant flow and at constant pressure—using a particulate model solution as well as a cell-free mAb solution as a representative example. Both filtration methods were compared regarding their practicability as well as their scalability of the final filter throughput and the filtration time. The pressure-dependent filter fouling that occurred with the mAb solution and the model solution showed that using different pressures for small- and process-scale filtration runs could potentially influence the predicted filter capacity. Overall, good scalability of the final filter throughput was determined for filters ranging from small-scale flat disc filters (4.5 cm2) to large pleated filter assemblies (5.4 m2) in filtration runs at constant flow as well as for filter capsules (0.6 m2) of up to 10” for filtration runs at constant pressure. Moreover, at constant flow, the filtration time could be accurately predicted because it was determined by the adjusted flow rate. However, at constant pressure, potential resistances in process-scale devices can result in lower fluid fluxes and, hence, a longer unpredictable filtration time compared with small-scale filter elements. This paper introduces a novel scaling method performed at constant pressure that compensates for the pressure losses resulting from process-scale device resistances. Improved scalability regarding final filter throughput and filtration time are shown here with this scaling method compared with scaling at constant pressure. Therefore, this study provides information essential in decision-making to achieve optimal scaling within biopharmaceutical process development.