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Efficiency of ultrafiltration/diafiltration in removing organic and elemental process equipment related leachables from biological therapeutics
Authors:Bin Sun  Mahsa Hadidi  Jose Santiago Nuñez  Benben Song  Gilbert E Tumambac  Ken Wong  Gregor Kalinowski  James J Hathcock
Institution:1. Scientific Laboratory Services, Cytiva, Westborough, Massachusetts, USA;2. Purification Process Development Laboratory, Sanofi, Framingham, Massachusetts, USA

Contribution: Data curation, ?Investigation;3. Scientific Laboratory Services, Cytiva, Westborough, Massachusetts, USA

Contribution: Formal analysis, ?Investigation;4. Scientific Laboratory Services, Cytiva, Westborough, Massachusetts, USA

Contribution: Methodology, Supervision;5. Regulatory and Validation Strategy, Cytiva, Westborough, Massachusetts, USA

Contribution: Formal analysis, Writing - original draft, Writing - review & editing;6. Critical Material Management (Prior role was Extractables and Leachables SME), Sanofi, Swiftwater, Pennsylvania, USA

Contribution: Methodology, Supervision;7. Scientific Laboratory Services, Cytiva, Westborough, Massachusetts, USA

Contribution: Formal analysis;8. Regulatory and Validation Strategy, Cytiva, Westborough, Massachusetts, USA

Abstract:In the production of biological therapeutics such as monoclonal antibodies (mAbs), ultrafiltration and diafiltration (UF/DF) are widely regarded as effective downstream processing steps capable of removing process equipment related leachables (PERLs) introduced upstream of the UF/DF step. However, clearance data available in the literature are limited to species with low partition coefficients (log P) such as buffer ions, hydrophilic organic compounds, and some metal ions. Additional data for a wide range of PERLs including hydrophobic compounds and elemental impurities are needed to establish meaningful, comprehensive safety risk assessments. Herein, we report the results from studies investigating the clearance of seven different organic PERLs representing a wide range of characteristics (i.e., log P (?0.3 to 18)), and four model elements with different chemical properties spiked into a mAb formulation at 10 ppm and analyzed during clearance using gas chromatography–mass spectrometry (GC–MS), liquid chromatography-photodiode-array-mass spectrometry (LC-PDA-MS), and inductively coupled plasma mass spectrometry (ICP-MS). The clearance data showed ideal clearance and sieving of spiked organic PERLs with log P < 4, partial clearance of PERLs with 4 < log P < 9, and poor clearance of highly hydrophobic PERLs (log P > 9) after nine diafiltration volumes (DVs). Supplemental clearance studies on seven additional PERLs present at much lower concentration levels (0.1–1.5 ppm) in the mAb formulation upstream of UF/DF and three PERLs associated with the tangential flow filtration (TFF) equipment also demonstrated the similar correlations between log P and % clearance. For model elements, the findings suggest that UF/DF in general provides ideal clearance for elements. Evidence showed that the UF/DF process does not only help mitigate leachables risk from PERLs introduced upstream of UF/DF, but also from the TFF operation itself as all three TFF-related PERLs were effectively cleared. Overall, the UF/DF clearance presented in this work demonstrated whereas highly hydrophobic PERLs and elements that exist as charged species, particularly transition metal ions, may not be as effectively cleared and thus warrant further risk assessment; hydrophilic and some hydrophobic PERLs (log P < 4) are indeed well-cleared and thus present a lower overall safety risk.
Keywords:diafiltration  extractables  leachables  tangential flow filtration  ultrafiltration
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