Sterile filtration is an integral step in the manufacturing process of biological therapeutics. Protein adsorption to the surface of the filter is an unfortunate, common occurrence that can result in manufacturing difficulties, such as filter fouling or product loss. Although many filters have surface modifications to minimize adsorption, under certain conditions binding can still occur. We observed the loss of high molecular weight species (HMWS) during sterile filtration of eight different therapeutic monoclonal antibodies formulated at low protein concentrations across a commonly used hydrophilic polyvinylidene fluoride or polyvinylidene difluoride (PVDF) filter membrane. The protein absorption was specific to HMWS, and each antibody exhibited different degrees of filter adsorption. Debye screening length parameters of the solution (e.g. ionic strength) were adjusted, and influenced the amount of HMWS lost during filtration. Additionally, HMWS of a representative antibody (mAb1) were observed to be more positively charged than other size variants by ion-exchange chromatography. From these results, it is concluded that this HMWS loss is due to electrostatic interactions between HMWS and the filter surface. This adsorption can be reduced by increasing the ionic strength of the buffer matrix, demonstrating the influence of the Debye screening length in the filtration of low concentration proteins.
Keywords: Adsorption; Monoclonal antibody; Processing; Protein aggregation; Protein binding; Protein formulations.
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