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Role of membrane structure on the filtrate flux during monoclonal antibody filtration through virus retentive membranes
Authors:Matthew Billups  Mirko Minervini  Melissa Holstein  Hasin Feroz  Swarnim Ranjan  Jessica Hung  Haiying Bao  Zheng Jian Li  Sanchayita Ghose  Andrew L. Zydney
Affiliation:1. Department of Chemical Engineering, The Pennsylvania State University, University Park, Pennsylvania, USA

Contribution: Data curation (lead), Formal analysis (lead), Writing - original draft (lead);2. Department of Chemical Engineering, The Pennsylvania State University, University Park, Pennsylvania, USA

Contribution: Data curation (supporting), Formal analysis (supporting), ​Investigation (supporting), Writing - review & editing (supporting);3. Bristol Myers Squibb Biologics Process Development, Global Product Development and Supply, Devens, Massachusetts, USA;4. Department of Chemical Engineering, The Pennsylvania State University, University Park, Pennsylvania, USA;5. Bristol Myers Squibb Biologics Process Development, Global Product Development and Supply, Devens, Massachusetts, USA

Contribution: Funding acquisition (supporting), Project administration (supporting), Resources (supporting), Writing - review & editing (supporting);6. Bristol Myers Squibb Biologics Process Development, Global Product Development and Supply, Devens, Massachusetts, USA

Contribution: Conceptualization (supporting), Funding acquisition (supporting), Project administration (supporting), Supervision (supporting);7. Bristol Myers Squibb Biologics Process Development, Global Product Development and Supply, Devens, Massachusetts, USA

Contribution: Conceptualization (supporting), Funding acquisition (equal), Methodology (supporting), Project administration (equal), Supervision (supporting)

Abstract:Virus removal filtration is a critical step in the manufacture of monoclonal antibody products, providing a robust size-based removal of both enveloped and non-enveloped viruses. Many monoclonal antibodies show very large reductions in filtrate flux during virus filtration, with the mechanisms governing this behavior and its dependence on the properties of the virus filter and antibody remaining largely unknown. Experiments were performed using the highly asymmetric Viresolve® Pro and the relatively homogeneous Pegasus™ SV4 virus filters using a highly purified monoclonal antibody. The filtrate flux for a 4 g/L antibody solution through the Viresolve® Pro decreased by about 10-fold when the filter was oriented with the skin side down but by more than 1000-fold when the asymmetric filter orientation was reversed and used with the skin side up. The very large flux decline observed with the skin side up could be eliminated by placing a large pore size prefilter directly on top of the virus filter; this improvement in filtrate flux was not seen when the prefilter was used inline or as a batch prefiltration step. The increase in flux due to the prefilter was not related to the removal of large protein aggregates or to an alteration in the extent of concentration polarization. Instead, the prefilter appears to transiently disrupt reversible associations of the antibodies caused by strong intermolecular attractions. These results provide important insights into the role of membrane morphology and antibody properties on the filtrate flux during virus filtration.
Keywords:fouling  membrane structure  monoclonal antibody  ultrafiltration  virus filtration
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