| Literature DB >> 28464237 |
Youngbin Baek1, Nripen Singh2, Abhiram Arunkumar2, Michael Borys2, Zheng J Li2, Andrew L Zydney1.
Abstract
Ultrafiltration (UF) is used for the final concentration and formulation of essentially all antibody-based therapeutics including both monoclonal antibodies (mAbs) and Fc-fusion proteins. The objective of this study was to quantitatively compare the filtrate flux behavior for two highly purified mAbs and an Fc-fusion protein under identical flow and buffer conditions. Filtrate flux data were obtained using a Pellicon 3 tangential flow filtration cassette over a wide range of transmembrane pressures and bulk protein concentrations. Independent experimental measurements were performed to evaluate the protein osmotic pressure and solution viscosity. The maximum achievable protein concentration was directly correlated with the solution viscosity, which controls the pressure drop and extent of back-filtration in the cassette. The filtrate flux data were analyzed using a recently developed model that accounts for the effects of intermolecular interactions and transmembrane pressure gradients on the extent of concentration polarization. These results provide important insights into the factors controlling the filtrate flux during the UF of concentrated protein solutions and an effective framework for the design/analysis of UF processes for the formulation of antibody-based therapeutics. Biotechnol. Bioeng. 2017;114: 2057-2065.Keywords: Fc-fusion protein; concentration polarization; intermolecular interactions; monoclonal antibody; physical properties; ultrafiltration; viscosity
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Year: 2017 PMID: 28464237 DOI: 10.1002/bit.26326
Source DB: PubMed Journal: Biotechnol Bioeng ISSN: 0006-3592 Impact factor: 4.530