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Continuous and Semi-continuous Cell Culture for Production of Blood Clotting Factors

Continuous and Semi-continuous Cell Culture for Production of Blood Clotting Factors. Sunil G. Desai, Ph. D. Sr. Manager, Manufacturing Sciences and Technology. Grange Castle, Ireland. Pearl River, NY. Sanford , NC. Pfizer Biotech. Andover, MA. Strangnas , Sweden. Algete , Spain. CMOs.

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Continuous and Semi-continuous Cell Culture for Production of Blood Clotting Factors

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  1. Continuous and Semi-continuous Cell Culture for Production of Blood Clotting Factors Sunil G. Desai, Ph. D. Sr. Manager, Manufacturing Sciences and Technology

  2. Grange Castle, Ireland Pearl River, NY Sanford , NC Pfizer Biotech Andover, MA Strangnas, Sweden Algete, Spain CMOs Biologics Vaccines Biosimilars Robust pipeline

  3. BeneFIX or rFIX • Recombinant therapy for Factor IX deficiency (hemophilia B) • 55 kDazymogen with 12 γ-carboxylation sites • Several other complex post-translational modifications • Extensive structure and functionality assays • First approved recombinant factor IX product (1997) • CHO-based batch re-feed process • ADRM free culture medium from the beginning

  4. 50 43 ReFacto AF/ Xyntha or BDD-rFVIII • Recombinant therapy for Factor VIII deficiency (hemophilia A) • FVIII gene sequenced in 1984 • Engineered version of FVIII (B domain deleted), maintains procoagulant function • Increased transcription efficiency • ReFacto approved in U.S., EU (1st licensed in 1999) • ReFacto AF approved in 2008 • CHO-based perfusion process • DS manufactured at an external partner site for Pfizer ReFacto Activated ReFacto 90 80 NH2 COOH Full Length FVIII 90 B 80 NH2 COOH Me2+ 73 3D picture reference: Orlova et al., 2013, ActaNaturae, 5(2).

  5. Key Process Challenges • Low level expression (transcription/ translation level) • Growth associated expression • Labile product • Degradation during processing • Activation during processing • Complex post-translational modifications • Disulfide bond formation (11 for rFIX) • N-linked and O-linked glycosylation • Tyrosine sulfation (rFVIII, rFIX) • Metal ion binding • Heavy and light chain cleavage • γ-carboxylation sites • Process changes while maintaining quality/ comparability • Removal of ADRMs (Albumin) from culture medium (BDD-rFVIII) • Changes in production sites/ scales • Use of disposables • Ongoing process updates (PAT, vendor changes, ICH guidelines) • Supply sensitive customer base

  6. Cell culture process - BeneFIX Re-feed Process Low cell density High cell density Retained culture Low cell density Seed Bioreactor After n days Harvest Re-feed Recovery Nutrient media

  7. BeneFIX production data BeneFIX (1997 – present) 2.5kL 6kL 12kL Number of batches 1 2 3 4 5 6 7 8 9 10 11 Bioreactor Non-validated database of GMP data

  8. Benefits/ challenges of continuous process • Productivity vs Titer • Perfusion/ re-feed processes reduce BRX turn-around time • Lower product quality risk than increasing specific productivity of cells • Easy to model volumetric productivity vs titer benefit analysis Cell Specific Productivity LCL 0 Bioreactor batch Non-validated database of GMP data • Data from multiple bioreactors • Range of variation in productivity yet consistent product quality

  9. Benefits/ challenges of continuous process • Campaign lengths • Several weeks to months • Multiple bioreactors allow back up inoculation sources • Savings in reduced SIP/ CIP cycles of bioreactors • Number of cell generations • Extensive LIVCA studies required • At scale EOP samples tested for genetic stability • Routine testing for culture purity (mycoplasma and virus)at EOP only • Additional product characterization to account for cell age (early-mid-late stage campaign effects) • CHO, in general, stable for extended number of generations

  10. Specific growth rate vs generations • Growth rate is independent of cell generation number • Range in growth rate giving consistent product quality Specific growth rate LCL 0 85 Culture generations Non-validated database of GMP data

  11. Benefits/ challenges of continuous process • Maintenance of aseptic BRX conditions for extended time • A major concern with extended period cell culture • SIP / CIP procedures have vastly improved • Years of experience • Multiproduct facilities • Rigorous PM and engineering controls (o-rings!) • Disposable use with minimum open operations Contaminated batches Period with non contaminations Batch count Campaign Non-validated database of GMP data 1.3% contaminated Two of eleven bioreactors were never contaminated

  12. Cell culture process – ReFacto AF Perfusion Process Harvest of product containing broth Culture medium Return of CHO cells to the bioreactor Bioreacto To clarification, primary capture Cell separator Bioreactor Harvest tank

  13. ReFacto AF ReFacto 2.0 1.6 • New MCB for HSA-free ReFacto • Same cell lineage, BDD-rFVIII genotype unchanged • Albumin-free media for production • Replace hybridoma-derived MAb column • Analytical Comparability • Very similar biochemical profile • Relationship to historical ranges well understood • Non-clinical/Clinical Comparability 1.2 0.8 0.4 0 2 4 5 1 3 80 kDa 90:1 LaneSample 1 MW Markers 2 Blank 3 ReFacto(Site 1) 4 ReFacto(Site 2) 5 ReFactoAF 170 kDa 90:2 2.4 ReFactoAF 2.0 1.6 1.2 0.8 0.4 0 15 20 25 30 35 40 45 50 55 Time (minutes) Kelley et al., 2009, Haemophilia.

  14. ReFacto AF production data ~5 years of data shown UCL Sp. Activity LCL % Product Isoform 1 UCL LCL Consistent product quality data over the years Non-validated database of GMP data

  15. Benefits/ challenges of continuous process Batch definition • Critical for biologics from a compliance perspective • Each DS lot traces back to a single cell bank thaw event • Pooling of multiple batch streams during purification • Batch stream could originate from multiple scales

  16. Conclusions • Semi-continuous (re-feed) and continuous (perfusion) processes of complex recombinant proteins commercially successful for over 15 yrs • Product/ process life-cycle changes successfully implemented • Large data sets demonstrate process robustness and cell line stability • Increased plant productivity with shorter bioreactor turn-around times • Manageable contamination rates over extended periods of operation add substantial operational savings

  17. Acknowledgements • Almost two decades of contributions towards continuous development and manufacturing of BeneFIX and ReFacto AF/ Xyntha • Pfizer Global Supply (Tanya Alcorn) • Site Operations (Erin Beal, Erik Roos) • Quality • Manufacturing Sciences and Technology (Dan Lasko, Enda Moran, Kesav Reddy, Jim Booth) • Pharmaceutical Sciences (Tim Charlebois, Mike Jankowski, Shamik Sharma) • External supply partners

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