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Plasma fractionation and viral inactivation/removal procedures
Thierry Burnouf, PhD
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Human plasma: a unique & complex raw material
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Human plasma: a unique & complex raw material
+/- 60 g proteins / liter 2 abundant proteins hundreds of other proteins (some present as traces) ~20 medicinal, plasma-derived products
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established clinical value
Close to 55 out of 60 g have established clinical value
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Modern Fractionation: interconnection of production lines
Produce several products from each pool for optimal use of plasma and selective hemotherapy albumin IgG Clotting factors Anti-Proteases Anti-coagulants
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Plasma product range Coagulation factors Factor VIII
Prothrombin complex Fibrinogen Von Willebrand Factor Factor VII Factor XI Factor XIII Albumin Protease inhibitors Alpha 1-antitrypsin C1-inhibitor Anticoagulants Antithrombin WHO model list of essential medicines
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Immunoglobulins POLYVALENT Intravenous Intramuscular Sub-cutaneous
HYPERIMMUNE Anti-D (Rhesus) Anti-Hepatitis B Anti-tetanus Anti-Rabies Anti-Varicella/Zoster Anti-Cytomegamovirus Anti-hepatitis A WHO model list of essential medicines
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Flow-chart of plasma fractionation
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PREPARATION OF PLASMA RAW MATERIAL
Storage of plasma donations [Freezer, °C] Preparation of plasma donations for pooling
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LARGE-SCALE PROCESSING
POOLING and LARGE-SCALE PROCESSING Opening of bags Cryoprecipitation (2-4°C) Bulk fractionation steps (Ethanol fractionation + chromatography) Protein purification and viral Inactivation In-process filtration steps Batch size: L
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Air-classified environment
POOLING and LARGE-SCALE PROCESSING Opening of bags Cryoprecipitation (2-4°C) Bulk fractionation steps (Ethanol fractionation + chromatography) Protein purification and viral Inactivation In-process filtration steps Batch size: L Air-classified environment
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Sterile filtration (0.2 m)
(Nanofiltration) ASEPTIC DISPENSING Sterile filtration (0.2 m) Aseptic filling +/- Freeze-drying
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QUARANTINE – QUALITY CONTROL
LABELLING – PACKAGING BOXING - SHIPMENT
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Fractionation methods
Step Protein target Cryoprecipitation Factor VIII, vWF, Fibrinogen Chromatography Coagulation factors, Protease inhibitors Anticoagulants Ethanol fractionation Albumin, IgG, alpha 1-AT
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cryoprecipitation Ethanol precipitation
Integrated plasma protein fractionation process cryoprecipitation Ethanol precipitation Burnouf, T. Transfusion Medicine Reviews, 2007;21:
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Cryoprecipitation Batch size: L
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Processing of cryoprecipitate
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Capture of labile proteins from cryo-poor plasma
PCC, PC, PS C1-esterase Antithrombin Ethanol
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Ethanol precipitations and chromatography
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Evolving production methods of IVIG to improve recovery
Radosevich & Burnouf Vox Sang. 2010:98:12-28 Traditional method
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Chromatography Protein purification Viral inactivation
Fractionation into several therapeutic protein products Removal of unwanted proteins (e.g. IgA; FXIa) Removal of viral inactivating agents (solvent/detergent)
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Chromatographic methods
1 – 500 liters column Anion-exchange Cation-exchange Affinity (e.g. heparin; copper; gelatin) Immuno-affinity (anti-FVIII; -FIX) Hydrophobic interaction Size-exclusion
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Ethanol fractionation
4000 Liters Stainless-steel tank
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Protein separation Separation of Precipitates by depth Filtration
(or centrifugation) 24 24
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Ethanol precipitations
Protein purification Viral safety Separate proteins into pre-purified fractions: albumin, IgG, alpha 1-antitrypsin These fractions can be stored frozen Contributing factor to the removal/inactivation of some viruses
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Viral safety keys Donor screening
Testing of donations and manufacturing plasma pool Viral reduction treatments GMP 26 26
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Viral reduction technologies
HIV HBV HCV HAV B19V WNV, DENV, CHIKV, etc. robustness
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Viral reduction Two major methods to ensure viral safety
Inactivation = virus destruction/kill by alteration of its capacity to replicate Removal = partitioning of viruses and plasma proteins in different fractions
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Viral reduction treatments
Inactivation = virus destruction by alteration of: Lipid structure Proteins (enzymes) Nucleic acids Examples: Chemicals Heat Low pH Irradiation (UV)
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Viral reduction treatments
Removal = virus partitioning/separation from the protein of interest Dedicated/ on purpose treatment Nanofiltration Non dedicated/non specific treatments, e.g. Centrifugation Chromatography
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Target of viral reduction treatments
Balanced compromise between the extent of microbial kill and the unwanted side effects on active ingredients of the product: Coagulation factors Immunoglobulins Albumin Etc.
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Viral reduction treatments
Inactivation Removal Solvent-detergent Pasteurisation Low pH Caprylic acid Dry-heat treatment Nanofiltration Chromatography Precipitation Non- Dedicated, Contributing steps
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Solvent Detergent Incubation of plasma protein solution in the presence of Tri n-butyl phosphate (TnBP) and detergent(s) [e.g.Tween-80 and/or Triton X-100] 25 – 35 ˚C (validated) 1 - 6 hr (validated) Target: HIV, HBV, HCV, WNV, DENV, CHIKV etc. Coagulation factors, IVIG, alpha 1-AT, etc.
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SOLVENT-DETERGENT TREATMENT AT LARGE SCALE
Up to 1% TnBP Up to 1% detergent (Tween 80, Triton X-100, Triton X-45) 20-35°C 1 to 6 hrs Depending upon validation data Protein solution Mixing device
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Elimination of the SD agents
Proteins + SD Hydrophobic interaction chromatography Chromatographic column SD are adsorbed proteins
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Elimination of the SD agents
Proteins + SD Ion-exchange chromatography Chromatographic column Proteins are adsorbed S/D
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Elimination of the SD agents
Oil extraction Oil + SD Proteins + SD + OIL Mixing and decantation proteins
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Pasteurisation Heat-treatment of a protein solution 60˚C 10 hr
Protein stabilizers Target: HIV, HBV, HCV, WNV, DENV, HAV, B19V Albumin, FVIII, IVIG, alpha 1-AT Risk of protein denaturations to be controlled
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Low-pH treatment Treatment in the liquid state: pH 4.0 30-37°C
> 24 hrs HIV, HBV, HCV, [HAV, B19V] Only IgG products (historically performed to allow IV infusion)
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Caprylic acid treatment
Treatment in the liquid state: < pH 6.0 1 hr 20-25°C HIV, HBV, HCV, WNV, CHIKV etc. Only IgG products (also a purification method)
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Nanofiltration Filtration on dedicated small pore-size filters (15, 20, or 35 nm, or equivalent) HIV, HBV, HCV, WNV, DENV, CHIKV, HAV, B19V Coagulation factors, IgG, AT, alpha 1-AT, etc;
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Removal mechanism Multi-step filtration with multi-layered structure
Product solution passes through capillary-void structure repeatedly. Product, smaller than the size of capillary, passes through effectively, whereas, viruses relatively larger than the size of capillary, are trapped effectively. Layer Layer Layer150 VIRUS PROTEIN
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Dry heat treatment (historical use)
60 +/- 0.1°C for 96 hrs 68 +/- 0.1°C for 96 hrs 80 +/- 0.1°C for 72 hrs 100 +/- 0.1°C for 30 min HIV inactivation HCV inactivation HAV /B19 inactivation
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Combination of treatments
SD Pasteurisation Acid pH Nanofiltration Dry-heat F VIII or FIX X F VIII vWF AT IgG
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Combination of treatments
SD Pasteurisation Acid pH Nanofiltration Dry-heat F VIII or FIX X F VIII vWF AT IgG Combine treatments with different mechanisms of viral inactivation or removal
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Each treatment has limits: Viral validations are needed (relevant viruses and model viruses)
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In vitro validation of viral reduction treatments
Scientific understanding of the capacity of a process to inactivate / remove viruses in a robust and consistent manner Determination of process robustness > 4 logs of reduction of infectivity under conditions demonstrated to be not significantly affected by potential process variations (pH, temperature, content of inactivating agents, etc.)
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“Good implementation viral reduction practices”
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Product batch release specifications
Potency / Specific activity Residual “contaminant” proteins Specialized assays [e.g. thrombogenicity] Ingredients [stabilizers] Residual content in virus sterilizing agents Physicochemical tests Sterility Pyrogen / endotoxin tests Toxicity assays Quality and safety of each batch is intimately dependent upon process validation and process monitoring through GMP
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Thank you for your attention
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