US20070142625A1 - Virus filtration of liquid Factor VII compositions - Google Patents

Virus filtration of liquid Factor VII compositions Download PDF

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Publication number
US20070142625A1
US20070142625A1 US11/439,828 US43982806A US2007142625A1 US 20070142625 A1 US20070142625 A1 US 20070142625A1 US 43982806 A US43982806 A US 43982806A US 2007142625 A1 US2007142625 A1 US 2007142625A1
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Prior art keywords
factor vii
fvii
composition
liquid
range
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Jesper Christensen
Erik Halkjaer
Turid Preuss
Thomas Hansen
Lene Tomoda
Nina Johansen
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Novo Nordisk Health Care AG
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Novo Nordisk Health Care AG
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Application filed by Novo Nordisk Health Care AG filed Critical Novo Nordisk Health Care AG
Assigned to NOVO NORDISK HEALTHCARE A/G reassignment NOVO NORDISK HEALTHCARE A/G ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: PREUSS, TURID, HANSEN, THOMAS BEDDE, JOHANSEN, NINA, HALKJAER, ERIK, TOMODA, LENE VAEDELE MADSEN, CHRISTENSEN, JESPER
Publication of US20070142625A1 publication Critical patent/US20070142625A1/en
Priority to US12/173,475 priority Critical patent/US20080274534A1/en
Priority to US13/349,980 priority patent/US9102762B2/en
Priority to US14/753,551 priority patent/US20150299685A1/en
Priority to US15/286,068 priority patent/US20170022482A1/en
Priority to US16/145,565 priority patent/US20190032026A1/en
Assigned to NOVO NORDISK HEALTHCARE AG reassignment NOVO NORDISK HEALTHCARE AG CORRECTIVE ASSIGNMENT TO CORRECT THE INVENTOR'S MIDDLE NAME PREVIOUSLY RECORDED AT REEL: 018372 FRAME: 0357. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Assignors: PREUSS, TURID, HANSEN, THOMAS BUDDE, JOHANSEN, NINA, HALKJAER, ERIK, TOMODA, LENE VAEDELE MADSEN, CHRISTENSEN, JESPER
Priority to US16/853,444 priority patent/US20200248150A1/en
Priority to US17/522,216 priority patent/US20220064605A1/en
Abandoned legal-status Critical Current

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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07K—PEPTIDES
    • C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/14—Extraction; Separation; Purification
    • C07K1/34—Extraction; Separation; Purification by filtration, ultrafiltration or reverse osmosis
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/14—Hydrolases (3)
    • C12N9/48—Hydrolases (3) acting on peptide bonds (3.4)
    • C12N9/50—Proteinases, e.g. Endopeptidases (3.4.21-3.4.25)
    • C12N9/64—Proteinases, e.g. Endopeptidases (3.4.21-3.4.25) derived from animal tissue
    • C12N9/6421—Proteinases, e.g. Endopeptidases (3.4.21-3.4.25) derived from animal tissue from mammals
    • C12N9/6424—Serine endopeptidases (3.4.21)
    • C12N9/6437—Coagulation factor VIIa (3.4.21.21)
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P7/00—Drugs for disorders of the blood or the extracellular fluid
    • A61P7/02—Antithrombotic agents; Anticoagulants; Platelet aggregation inhibitors
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P7/00—Drugs for disorders of the blood or the extracellular fluid
    • A61P7/04—Antihaemorrhagics; Procoagulants; Haemostatic agents; Antifibrinolytic agents
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07K—PEPTIDES
    • C07K14/00—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof
    • C07K14/435—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans
    • C07K14/745—Blood coagulation or fibrinolysis factors
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N7/00—Viruses; Bacteriophages; Compositions thereof; Preparation or purification thereof
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12Y—ENZYMES
    • C12Y304/00—Hydrolases acting on peptide bonds, i.e. peptidases (3.4)
    • C12Y304/21—Serine endopeptidases (3.4.21)
    • C12Y304/21021—Coagulation factor VIIa (3.4.21.21)
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N2740/00—Reverse transcribing RNA viruses
    • C12N2740/00011—Details
    • C12N2740/10011—Retroviridae
    • C12N2740/13011—Gammaretrovirus, e.g. murine leukeamia virus
    • C12N2740/13061—Methods of inactivation or attenuation
    • C12N2740/13063—Methods of inactivation or attenuation by chemical treatment

Definitions

  • the present invention relates to a novel method for improving the viral safety of liquid Factor VII compositions, in particular those comprising active Factor VII polypeptides (a Factor VIIa polypeptide).
  • Factor VII a plasma glycoprotein.
  • Haemostasis is initiated by the formation of a complex between Tissue Factor (TF) being exposed to the circulating blood following an injury to the vessel wall, and Factor VIIa which is present in the circulation in an amount corresponding to about 1% of the total Factor VII protein mass.
  • Factor VII exists in plasma mainly as a single-chain zymogen which is cleaved by FXa into its two-chain, activated form, Factor VIIa.
  • Recombinant activated Factor VIIa (rFVIIa) has been developed as a pro-haemostatic agent.
  • rFVIIa offers a rapid and highly effective pro-haemostatic response in haemophilic subjects with bleedings, who cannot be treated with other coagulation Factor products due to antibody formation. Also bleeding in subjects with Factor VII deficiency or subjects having a normal coagulation system but experiencing excessive bleeding can be treated successfully with Factor VIIa.
  • Factor VII and Factor VIIa are susceptible to mechanical degradation by shear forces during purification and filtration. Further, Factor VIIa is an active proteolytic enzyme that degrades other proteins including Factor VIIa. Degradation of Factor VIIa mainly involves cleavage in the heavy chain of Factor VIIa, particularly at amino acids no. 290 and 315 in the molecule. Finally, methionine residues in Factor VII and Factor VIIa may be oxidized.
  • An object of the present invention is to provide a method for the removal or inactivation of viruses from liquid Factor VII compositions by which method the integrity of the Factor VII constituents is substantially preserved.
  • WO 96/00237 discloses a method of virus-filtration of a solution that contains a macromolecular, e.g. a protein such as the plasma protein Factor IX.
  • WO 98/37086 discloses removal of viruses from plasma-derived protein solutions by nanofiltration using a membrane having an average pore size of 15 nm.
  • the preset invention relates to methods for the removal and/or inactivation of viruses from Factor VII composition.
  • virus as used herein means any ultramicroscopic infectious agent that replicates itself only within cells of living hosts, or noninfectious particles derived thereof. In one embodiment the virus is infectious. In one embodiment the virus is a non-infectious virus particle.
  • a first aspect of the present invention relates to a method for removing viruses from a liquid Factor VII composition, said method comprising subjecting said solution to nanofiltration using a nanofilter having a pore size of at the most 80 nm.
  • a second aspect of the present invention relates to a method for removing viruses from a liquid Factor VII composition, said composition comprising one or more Factor VII polypeptides, at least 5% of said one or more Factor VII polypeptides being in the activated form, said method comprising subjecting said solution to nanofiltration using a nanofilter having a pore size of at the most 80 nm.
  • a third aspect of the invention relates to a method for removing viruses from a liquid Factor VII composition, said composition comprising one or more Factor VII polypeptides, said liquid composition being substantially serum-free, said method comprising subjecting said solution to nanofiltration using a nanofilter having a pore size of at the most 80 nm.
  • a further aspect of the invention relates to a method for removing viruses from a liquid Factor VII composition, said composition comprising one or more Factor VII polypeptides, said method comprising subjecting said solution to nanofiltration using a nanofilter having a pore size of at the most 80 nm, said nanofilter having a membrane manufactured from one or more materials selected from cuprammonium regenerated cellulose, hydrophilic polyvinylidene fluoride (PVDF), composite PVDF, surface modified PVDF, and polyether sulfone.
  • PVDF hydrophilic polyvinylidene fluoride
  • a further aspect of the invention relates to a method for inactivating viruses in a liquid Factor VII composition, said composition comprising one or more Factor VII polypeptides, the method comprising the step of combining said composition with a detergent.
  • a further aspect of the invention relates to a method for high-level elimination of the presence of active viruses in a liquid Factor VII composition, the method comprising the steps of (i) inactivating viruses, and (ii) removing viruses.
  • FIG. 1 is a schematic illustration of a system suitable for methods of the invention.
  • the system includes a pressure tank ( 1 ) with a supply of compressed air, a pre-filter ( 2 ) for removing particles that would otherwise clog the virus filter, a pressure gauge (P), a virus filter ( 3 ), and a pool tank ( 4 ).
  • the present invention provides methods for removing or inactivating viruses, including non-enveloped viruses, from a liquid Factor VII composition which typically comprises a significant ratio of activated and thereby proteolytically active Factor VII polypeptides.
  • the method includes the step of subjecting the liquid Factor VII composition to nanofiltration using a nanofilter having a pore size of at the most 80 nm.
  • the method is particularly useful for the removal of enveloped viruses as well as non-enveloped viruses such as Murine Leukemia virus (enveloped) which may be removed by filters with a pore size around 50 nm, and Porcine Parvovirus (non-enveloped) which may be removed by filters with a pore size around 20 nm.
  • enveloped Murine Leukemia virus
  • non-enveloped Porcine Parvovirus
  • the liquid Factor VII compositions e.g. those comprising a significant ratio of activated Factor VII polypeptides, can in principle be prepared from the dry Factor VII constituents, but are more typically obtained from large-scale production processes, e.g. processes involving recombinant techniques.
  • a cell culture supernatant is typically harvested and subsequently subjected to one or more processing steps to obtain the desired protein, including, without limitation, centrifugation or filtration to remove cells that were not immobilized in the carriers; affinity chromatography, hydrophobic interaction chromatography; ion-exchange chromatography; size exclusion chromatography; electrophoretic procedures (e.g., preparative isoelectric focusing (IEF), differential solubility (e.g., ammonium sulfate precipitation), or extraction and the like.
  • IEF isoelectric focusing
  • differential solubility e.g., ammonium sulfate precipitation
  • Factor VII polypeptides may also involve, e.g., affinity chromatography on an anti-Factor VII antibody column (see, e.g., Wakabayashi et al., J. Biol. Chem. 261:11097, 1986; and Thim et al., Biochem. 27:7785, 1988) and activation by proteolytic cleavage, using Factor XIIa or other proteases having trypsin-like specificity, such as, e.g., Factor IXa, kallikrein, Factor Xa, and thrombin. See, e.g., Osterud et al., Biochem. 11:2853 (1972); Thomas, U.S. Pat.
  • a Factor VII polypeptide may be activated by passing it through an ion-exchange chromatography column, such as Mono Q® (Pharmacia) or the like.
  • the methods of the present invention are particularly useful for large-scale production processes.
  • large-scale is typically meant methods wherein the volume of the liquid Factor VII polypeptide compositions is at least 100 L, such as at least 500 L, e.g. at least 1000 L, or at least 5000 L. This is not to be limiting in any way, as the present invention will also work for liquid Factor VII polypeptide compositions of less than 100 L.
  • nanofiltration may be applied even after the Factor VII polypeptide bulk has been partially or fully activated.
  • the methods of the invention are applicable as one of the steps of the overall purification process for the Factor VII polypeptide, typically one of the final steps of the purification process.
  • a typical purification process starting from harvested material from the a fermentation broth can be outlined as follows: Possible stages Purification step for virus filtration Harvest 1 ⁇ Capture 2 ⁇ Intermediate 3 purification ⁇ Polishing 4 ⁇ Drug substance
  • the content of Factor VII polypeptide in the activated form is initially (i.e. from the harvest step) typically around 2%, and increases in the course of the purification process to 90% or more before the polypeptide is obtained as a drug substance.
  • the liquid Factor VII composition subjected to nanofiltration comprises one or more Factor VII polypeptides in a suitable solvent.
  • the solvent is typically water or an aqueous mixture/solution, such as pure water, an aqueous buffer, a water/ethanol mixture, a water/DMSO mixture, or an aqueous salt solution, e.g. saline, a urea solution or guanidine solution.
  • a suitable aqueous liquid may also comprise a detergent (surfactant).
  • the liquid Factor VII composition is obtained, or originates, from a cell culture supernatant, e.g. a cell culture supernatant obtained as disclosed in WO 02/29084.
  • the liquid Factor VII composition is serum-free, i.e. free from animal-derived components.
  • the cell cultures may be cultivated in a medium lacking animal derived components.
  • Factor VII polypeptide(s) is/are produced by cell culture in CHO cells, e.g. in CHO cells in a medium free from any components of animal origin, or a medium lacking animal-derived components and lacking proteins (“protein-free”).
  • the medium for CHO cells may be any commercially available protein-free CHO medium lacking animal-derived components or an in-house produced medium for CHO cells.
  • the cells used in practicing the present invention are adapted to suspension growth in medium lacking animal-derived components, such as, e.g., medium lacking serum.
  • animal-derived components such as, e.g., medium lacking serum.
  • Such adaptation procedures are described, e.g., in Scharfenberg, et al., Animal Cell Technology Developments towards the 21 st Century , E. C. Beuvery et al. (Eds.), Kluwer Academic Publishers, pp. 619-623, 1995 (BHK and CHO cells); Cruz, Biotechnol. Tech. 11:117-120, 1997 (insect cells); Keen, Cytotechnol.
  • the host cells are BHK 21 or CHO cells that have been engineered to express human Factor VII or a Factor VII polypeptide and that have been adapted to grow in the absence of serum or animal-derived components.
  • the Factor VII polypeptide(s) is/are produced by cell culture in the presence of bovine or fetal calf serum.
  • a feature is that a significant ratio, i.e. at least 5%, such as at least 7%, e.g. at least 10%, of the one or more Factor VII polypeptides are in the activated form (i.e. the bioactive, cleaved form of a Factor VII polypeptide (i.e. a Factor VIIa polypeptide)).
  • the Factor VIIa polypeptide represents 5-70%, such as 7-40%, e.g. 10-30%, of the mass of the one or more Factor VII polypeptides.
  • the Factor VIIa polypeptide represents 50-100%, such as 70-100%, e.g.
  • the Factor VIIa polypeptide represents 20-80%, such as 30-70%, e.g. 30-60%, of the mass of the one or more Factor VII polypeptides.
  • the solution comprises a Factor VII polypeptide in inactivated form as well as a bioactive Factor VIIa polypeptide, i.e. the Factor VIIa polypeptide represents less than 100% of the mass of the one or more Factor VII polypeptides.
  • the composition comprises a(n) (activated) Factor VIIa polypeptide that corresponds to an (inactive) Factor VII polypeptide, i.e. the Factor VIIa polypeptide is the Factor VII polypeptide in the activated form.
  • the Factor VIIa polypeptide is somewhat different from the activated form of the inactivated Factor VII polypeptide.
  • the composition in particular embodiments may comprise more than one Factor VII polypeptide and more than one Factor VIIa polypeptide.
  • Factor VII polypeptides encompasses wild-type Factor VII (i.e. a polypeptide having the amino acid sequence disclosed in U.S. Pat. No. 4,784,950), as well as variants of Factor VII exhibiting substantially the same or improved biological activity relative to wild-type Factor VII.
  • the term “Factor VII” is intended to encompass Factor VII polypeptides in their uncleaved (zymogen) form, as well as those that have been proteolytically processed to yield their respective bioactive forms, which may be designated Factor VIIa. Typically, Factor VII is cleaved between residues 152 and 153 to yield Factor VIIa.
  • the term “Factor VIIa” specifically means an activated (i.e. bioactive, cleaved) Factor VII polypeptide. Thus, “Factor VIIa” is a subgroup relative to “Factor VII”.
  • the term “inactive Factor VII” specifically means Factor VII not being Factor VIIa.
  • Factor VII polypeptide also encompasses polypeptides, including variants, in which the Factor VIIa biological activity has been substantially modified or somewhat reduced relative to the activity of wild-type Factor VIIa, as well as Factor VII derivatives and Factor VII conjugates. These polypeptides include, without limitation, Factor VII or Factor VIIa into which specific amino acid sequence alterations have been introduced that modify or disrupt the bioactivity of the polypeptide.
  • Factor VII derivative is intended to designate wild-type Factor VII, variants of Factor VII exhibiting substantially the same or improved biological activity relative to wild-type Factor VII and Factor VII-related polypeptides, in which one or more of the amino acids of the parent peptide have been chemically and/or enzymatically modified, e.g. by alkylation, glycosylation, PEGylation, acylation, ester formation or amide formation or the like. This includes but is not limited to PEGylated human Factor VIIa, cysteine-PEGylated human Factor VIIa and variants thereof.
  • Non-limiting examples of Factor VII derivatives includes GlycoPegylated FVII derivatives as disclosed in WO 03/31464 and US Patent applications US 20040043446, US 20040063911, US 20040142856, US 20040137557, and US 20040132640 (Neose Technologies, Inc.); FVII conjugates as disclosed in WO 01/04287, US patent application 20030165996, WO 01/58935, WO 03/93465 (Maxygen ApS) and WO 02/02764, US patent application 20030211094 (University of Minnesota).
  • PEGylated human Factor VIIa means human Factor VIIa, having a PEG molecule conjugated to a human Factor VIIa polypeptide. It is to be understood, that the PEG molecule may be attached to any part of the Factor VIIa polypeptide including any amino acid residue or carbohydrate moiety of the Factor VIIa polypeptide.
  • cyste-PEGylated human Factor VIIa means Factor VIIa having a PEG molecule conjugated to a sulfhydryl group of a cysteine introduced in human Factor VIIa.
  • the biological activity of Factor VIIa in blood clotting derives from its ability to (i) bind to Tissue Factor (TF) and (ii) catalyze the proteolytic cleavage of Factor IX or Factor X to produce activated Factor IX or X (Factor IXa or Xa, respectively).
  • Factor VII biological activity may be quantified by measuring the ability of a preparation to promote blood clotting using Factor VII-deficient plasma and thromboplastin, as described, e.g., in U.S. Pat. No. 5,997,864 or WO 92/15686.
  • biological activity is expressed as the reduction in clotting time relative to a control sample and is converted to “Factor VII units” by comparison with a pooled human serum standard containing 1 unit/mL Factor VII activity.
  • Factor VIIa biological activity may be quantified by (i) measuring the ability of Factor VIIa (or the Factor VII polypeptide) to produce activated Factor X (Factor Xa) in a system comprising TF embedded in a lipid membrane and Factor X. (Persson et al., J. Biol. Chem. 272:19919-19924, 1997); (ii) measuring Factor X hydrolysis in an aqueous system (“In Vitro Proteolysis Assay”, see below); (iii) measuring the physical binding of Factor VIIa (or the Factor VII polypeptide) to TF using an instrument based on surface plasmon resonance (Persson, FEBS Letts.
  • Factor VII variants having substantially the same or improved biological activity relative to wild-type Factor VIIa encompass those that exhibit at least about 25%, such as at least about 50%, such as at least about 75%, such as at least about 90% of the specific activity of Factor VIIa that has been produced in the same cell type, when tested in one or more of a clotting assay, proteolysis assay, or TF binding assay as described above.
  • the biological activity is more than 80% of the biological activity of recombinant wild type human Factor VIIa.
  • the biological activity is more than 90% of the biological activity of recombinant wild type human Factor VIIa.
  • the biological activity is more than 100% of the biological activity of recombinant wild type human Factor VIIa.
  • the biological activity is more than 120% of the biological activity of recombinant wild type human Factor VIIa. In a further embodiment the biological activity is more than 200% of the biological activity of recombinant wild type human Factor VIIa. In a further embodiment the biological activity is more than 400% of the biological activity of recombinant wild type human Factor VIIa.
  • Factor VII variants having substantially reduced biological activity relative to wild-type Factor VIIa are those that exhibit less than about 25%, such as less than about 10%, such as less than about 5%, such as less than about 1% of the specific activity of wild-type Factor VIIa that has been produced in the same cell type when tested in one or more of a clotting assay, proteolysis assay, or TF binding assay as described above.
  • Factor VII variants having a substantially modified biological activity relative to wild-type Factor VII include, without limitation, Factor VII variants that exhibit TF-independent Factor X proteolytic activity and those that bind TF but do not cleave Factor X.
  • Variants of Factor VII include, without limitation, polypeptides having an amino acid sequence that differs from the sequence of wild-type Factor VII by insertion, deletion, or substitution of one or more amino acids.
  • Non-limiting examples of Factor VII variants having substantially the same biological activity as wild-type Factor VII include S52A-FVIIa, S60A-FVIIa (Lino et al., Arch. Biochem. Biophys. 352: 182-192, 1998); Factor VIIa variants exhibiting increased proteolytic stability as disclosed in U.S. Pat. No. 5,580,560; Factor VIIa that has been proteolytically cleaved between residues 290 and 291 or between residues 315 and 316 (Mollerup et al., Biotechnol. Bioeng. 48:501-505, 1995); oxidized forms of Factor VIIa (Kornfelt et al., Arch. Biochem. Biophys.
  • Non-limiting examples of Factor VII variants having increased biological activity compared to wild-type Factor VIIa include Factor VII variants as disclosed in WO 01/83725, WO 02/22776, WO 02/077218, WO 03/27147, WO 03/37932; WO 02/38162 (Scripps Research Institute); and Factor VIIa variants with enhanced activity as disclosed in JP 2001061479 (Chemo-Sero-Therapeutic Res Inst.).
  • Non-limiting examples of Factor VII variants having substantially reduced or modified biological activity relative to wild-type Factor VII include R152E-FVIIa (Wildgoose et al., Biochem 29:3413-3420, 1990), S344A-FVIIa (Kazama et al., J. Biol. Chem. 270:66-72, 1995), FFR-FVIIa (Hoist et al., Eur. J. Vasc. Endovasc. Surg. 15:515-520, 1998), and Factor VIIa lacking the Gla domain, (Nicolaisen et al., FEBS Letts. 317:245-249, 1993).
  • Factor VII polypeptides include, without limitation, wild-type Factor VII, L305V-FVII, L305V/M306D/D309S-FVII, L305I-FVII, L305T-FVII, F374P-FVII, V158T/M298Q-FVII, V158D/E296V/M298Q-FVII, K337A-FVII, M298Q-FVII, V158D/M298Q-FVII, L305V/K337A-FVII, V158D/E296V/M298Q/L305V-FVII, V158D/E296V/M298Q/K337A-FVII, V158D/E296V/M298Q/L305V/K337A-FVII, K157A-FVII, E296V-FVII, E296V/M298Q-FVII, V158
  • the Factor VIIa polypeptide is human Factor VIIa (hFVIIa), such as recombinantly made human Factor VIIa (rhFVIIa).
  • the one or more Factor VII polypeptides comprise a Factor VII sequence variant.
  • the one or more Factor VII polypeptides have a glycosylation different from wild-type Factor VII.
  • the liquid Factor VII composition is subjected to nanofiltration using a nanofilter having a pore size of at the most 80 nm.
  • the pore size of the nanofilter is more particularly at the most 50 nm, e.g. at the most 30 nm, such as in the range of 10-30 nm.
  • pore size typically means the size of the smallest viruses that are withheld by the filter.
  • Nanofilters examples include Asahi Planove 15 N, Asahi Planove 20 N, Asahi Planova 35 N, and Asahi Planova 75 N, all from Asahi Chemical, Tokyo, Japan; Millipore NFR, Millipore NFP, Millipore Viresolve 70, and Millipore Viresolve 180, all from Millipore; and Pall DV20, Pall DV 50, Pall Omega VR 100 K; and Bemberg Microporous Membrane-15 nm (BMM-15).
  • the nanofilter membrane may, e.g., be manufactured from one or more materials selected from cuprammonium regenerated cellulose, hydrophilic polyvinylidene fluoride (PVDF), composite PVDF, surface modified PVDF, polyether sulfone and similar materials.
  • the material is selected from polyvinylidene fluoride-based materials and polyether sulfone-based materials.
  • the nanofiltration may be conducted by in the tangential filtration mode or in the dead-end filtration mode as will be understood by the skilled artisan. In one embodiment, the nanofiltration is conducted in the dead-end filtration mode.
  • the pH value of the liquid Factor VII composition upon nanofiltration is not considered particularly critical.
  • the pH value is normally given by in view of the conditions applied in the process steps immediately preceding the nanofiltration step.
  • the pH value is adjusted so that the liquid composition has a pH of in the range of 5.5-10, such as in the range of 7.0-9.5, e.g. in the range of 7.6-9.4, such as in the range of 7.7-9.3, e.g. in the range of 8.0-9.0 or in the range of 8.3-8.7.
  • the pH is in the range of 5-7.
  • the pH is higher than 9.5, such as in the range of 9.5-10.
  • concentration of the Factor VII polypeptide in the liquid composition is typically also given by the preceding process steps, but will normally lie in the range of 0.01-5 mg/mL, such as in the range of 0.05-2.0 mg/mL.
  • the nanofiltration process may be conducted using a filtration system as illustrated in FIG. 1 .
  • the process may be conducted as in the following illustrative example:
  • the pressure tank ( 1 ) is filled with water for injection (WFI), and the pressure in the tank is raised to 3.5 bars before the virus filter ( 3 ), and the filter is flushed for 10 minutes.
  • the pressure is reduced to 2 bars and the virus filter ( 3 ) is flushed for another 10 minutes.
  • the pressure tank ( 1 ) is emptied from WFI and the process is optionally repeated with a buffer before the liquid Factor VII composition is filled into the pressure tank ( 1 ).
  • the pressure is raised to 2 bars and is kept substantially constant during the filtration.
  • the virus filter ( 3 ) may subsequently be tested for integrity by standard procedures.
  • the filtrate is collected in a pool tank and can further be processed in order to obtain a pharmaceutical composition comprising a Factor VIIa polypeptide as a drug substance.
  • a pre-filtration step before the nanofiltration step in order to remove larger particles, aggregates, etc. that would otherwise cause the nanofilter to become clogged.
  • a pre-filter typically has a pore size of at in the range of 0.05-0.5 ⁇ m.
  • the pre-filter is Millipore NFR filter.
  • a liquid pump placed after the pressure tank may provide the necessary pressure for the filtration.
  • the composition may subsequently be subjected to an activation step, e.g. as described in Bj ⁇ rn. S. & Thim, L. Res. Disclosures (1986) 269, 564-565, Pedersen, A. H. & al., Biochemistry (1989), 28, 9331-9336, and Tomokiyo, K. & al., Vox Sang. 84, 54-64 (2003).
  • an activation step e.g. as described in Bj ⁇ rn. S. & Thim, L. Res. Disclosures (1986) 269, 564-565, Pedersen, A. H. & al., Biochemistry (1989), 28, 9331-9336, and Tomokiyo, K. & al., Vox Sang. 84, 54-64 (2003).
  • compositions and final formulation as a pharmaceutical product may be conducted as disclosed in Jurlander, B. & al., Seminars in Thrombosis and Hemostasis 27, 4, 373-383 (2001).
  • One separate aspect of the invention which may include some or all of the above characteristics, relates to a method for removing viruses from a liquid Factor VII composition, said composition comprising one or more Factor VII polypeptides, said liquid composition being substantially serum-free, said method comprising subjecting said solution to nanofiltration using a nanofilter having a pore size of at the most 80 nm.
  • Factor VII polypeptide(s) is/are produced by cell culture in CHO cells, e.g. in CHO cells in a medium free from any components of animal origin.
  • This aspect of the invention is not particularly limited to liquid Factor VII compositions in which a certain proportion of the Factor VII polypeptide(s) is/are in the activated form.
  • the conditions mentioned above for the first aspect of the invention also applies for this, the second aspect of the invention, mutatis mutandis.
  • Another separate aspect of the invention which may include some or all of the above characteristics, relates to a method for removing viruses from a liquid Factor VII composition, said composition comprising one or more Factor VII polypeptides, said method comprising subjecting said solution to nanofiltration using a nanofilter having a pore size of at the most 80 nm, said nanofilter having a membrane manufactured from one or more materials selected from cuprammonium regenerated cellulose, hydrophilic polyvinylidene fluoride (PVDF), composite PVDF, surface modified PVDF, and polyether sulfone.
  • PVDF hydrophilic polyvinylidene fluoride
  • the material is selected from polyvinylidene fluoride-based materials and polyether sulfone-based materials.
  • This aspect of the invention is not particularly limited to liquid Factor VII compositions in which a certain proportion of the Factor VII polypeptide(s) is/are in the activated form.
  • the conditions mentioned above for the first aspect of the invention also applies for this, the third aspect of the invention, mutatis mutandis.
  • the present invention also relates to a method for inactivating viruses in a liquid Factor VII composition, said composition comprising one or more Factor VII polypeptides, the method comprising the step of combining said composition with a detergent.
  • the detergent is selected from non-ionic detergents such as those selected from octylphenoxy polyethoxyethanol, polysorbates, poloxamers, polyoxyethylene alkyl ethers, polyethylene/polypropylene block co-polymers, polyethyleneglycol (PEG), polyoxyethylene stearates, and polyoxyethylene castor oils.
  • non-ionic detergents such as those selected from octylphenoxy polyethoxyethanol, polysorbates, poloxamers, polyoxyethylene alkyl ethers, polyethylene/polypropylene block co-polymers, polyethyleneglycol (PEG), polyoxyethylene stearates, and polyoxyethylene castor oils.
  • non-ionic detergents are Triton X-100, Tween®, polysorbate 20, polysorbate 60, polysorbate 80, Brij-35 (polyoxyethylene dodecyl ether), poloxamer 188, poloxamer 407, PEG8000, Pluronic® polyols, polyoxy-23-lauryl ether, Myrj 49, and Cremophor A.
  • a particularly useful detergent is a octylphenoxy polyethoxyethanol of the formula p-((CH 3 ) 3 CH 2 C(CH 2 ) 2 )—C 6 H 4 —O—(CH 2 CH 2 O) n —H wherein n is in the range of 5-15, in particular one where n is 9-10, such the detergent Triton X-100.
  • the detergent is combined with the liquid Factor VII composition to obtain a concentration of the detergent in the composition of in the range of 0.01-0.5% by weight, such as in the range of 0.05-0.4% by weight, such as in the range of 0.05-0.3% by weight, such as in the range of 0.05-0.2% by weight, such as in the range of 0.05-0.1% by weight.
  • the detergent is combined with the composition at a temperature of in the range of 2-12° C., such as in the range of 2-9° C.
  • the detergent may be substantially free of trialkylphosphate solvents such as tri(n-butyl)phosphate.
  • the method comprises the steps of combining the Factor VII polypeptide composition with Triton X-100 to a concentration of 0.05-0.2% by weight at a temperature in the range of 2-9° C., with the proviso that detergent is substantially free of trialkylphosphate solvents such as tri(n-butyl)phosphate.
  • This aspect of the invention is not particularly limited to liquid Factor VII compositions in which a certain proportion of the Factor VII polypeptide(s) is/are in the activated form.
  • the conditions mentioned above for the first aspect of the invention also applies for this, the fourth aspect of the invention, mutatis mutandis.
  • the present invention relates to a method for high-level elimination of the presence of active viruses in a liquid Factor VII composition, the method comprising the steps of (i) inactivating viruses by the method defined under “Virus inactivation by addition a detergent”, and (ii) removing viruses by the any of the methods defined herein under “Nanofiltration”, in any order.
  • the step of inactivating viruses precedes the step of removing viruses.
  • the two methods can be considered as at least partially “orthogonal” in the sense that certain viruses may be more difficult to eliminate by one of the methods, whereas the same of the certain viruses can more easily be eliminated by the other method, and vice versa.
  • combination of the two methods will provide an even higher level of safety for the patient for which the Factor VII polypeptide is intended, and not the least for the medical doctor prescribing the Factor VII polypeptide medicament, and for the regulatory authorities approving the medicament.
  • the combination of the two methods may have a high commercial value.
  • the present invention relates to the removal or inactivation of virus particles.
  • the reduction of the amount of virus particles at a particular process step is usually described in log-units (log 10 logarithm, or log 10 ), wherein the reduction factor is calculated as the amount of virus particles after the step relative to the amount of virus particles before the process step.
  • the reduction is 10 4 , or 4 log 10 .
  • the total reduction of virus particles from the complete process is described in the same way and may be calculated by addition of the virus clearance from each step in the process, the word “clearance” meaning both removal of virus and inactivation of virus
  • virus clearance step it is preferred to have a virus reduction of at least 4 log 10 .
  • a filtration step reduces the amount of virus particles with at least about 4 log 10 . In one embodiment of the present invention, a filtration step reduces the amount of virus particles with at least about 5 log 10 .
  • a step of combining said FVII composition with a detergent inactivates at least about 4 log 10 of virus. In one embodiment of the present invention, a step of combining said FVII composition with a detergent inactivates at least about 5 log 10 of virus.
  • TCID 50 assays tissue culture infectious dose 50% endpoint per mL
  • plaque assays plaque assays
  • PCR assays PCR assays
  • a method for removing viruses from a liquid Factor VII composition comprising one or more Factor VII polypeptides, at least 5% of said one or more Factor VII polypeptides being in the activated form, said method comprising subjecting said solution to nanofiltration using a nanofilter having a pore size of at the most 80 nm.
  • liquid composition has a pH of in the range of 7.0-9.5, e.g. in the range of 7.6-9.4, such as in the range of 7.7-9.3, e.g. in the range of 8.0-9.0 or in the range of 8.3-8.7.
  • the pore size of the nanofilter is at the most 50 nm, e.g. at the most 30 nm, such as in the range of 10-30 nm.
  • the membrane of the nanofilter is manufactured from one or more materials selected from cuprammonium regenerated cellulose, hydrophilic polyvinylidene fluoride (PVDF), composite PVDF, surface modified PVDF, and polyether sulfone.
  • PVDF hydrophilic polyvinylidene fluoride
  • composite PVDF composite PVDF
  • surface modified PVDF surface modified PVDF
  • polyether sulfone polyether sulfone
  • liquid Factor VII composition is obtained, or originates, from a cell culture supernatant.
  • liquid composition is substantially serum-free.
  • a method for removing viruses from a liquid Factor VII composition comprising one or more Factor VII polypeptides, said liquid composition being substantially serum-free, said method comprising subjecting said solution to nanofiltration using a nanofilter having a pore size of at the most 80 nm.
  • liquid Factor VII composition is obtained, or originates, from a cell culture supernatant.
  • liquid composition has a pH of in the range of 7.0-9.5, e.g. in the range of 7.6-9.4, such as in the range of 7.7-9.3, e.g. in the range of 8.0-9.0 or in the range of 8.3-8.7.
  • the pore size of the nanofilter is at the most 50 nm, e.g. at the most 30 nm, such as in the range of 10-30 nm.
  • the membrane of the nanofilter is manufactured from one or more materials selected from cuprammonium regenerated cellulose, hydrophilic polyvinylidene fluoride (PVDF), composite PVDF, surface modified PVDF, and polyether sulfone.
  • PVDF hydrophilic polyvinylidene fluoride
  • composite PVDF composite PVDF
  • surface modified PVDF surface modified PVDF
  • polyether sulfone polyether sulfone
  • a method for removing viruses from a liquid Factor VII composition comprising one or more Factor VII polypeptides, said method comprising subjecting said solution to nanofiltration using a nanofilter having a pore size of at the most 80 nm, said nanofilter having a membrane manufactured from one or more materials selected from cuprammonium regenerated cellulose, hydrophilic polyvinylidene fluoride (PVDF), composite PVDF, surface modified PVDF, and polyether sulfone.
  • PVDF hydrophilic polyvinylidene fluoride
  • the pore size of the nanofilter is at the most 50 nm, e.g. at the most 30 nm, such as in the range of 10-30 nm.
  • a method for inactivating viruses in a liquid Factor VII composition comprising one or more Factor VII polypeptides, the method comprising the step of combining said composition with a detergent.
  • a method for high-level elimination of the presence of active viruses in a liquid Factor VII composition comprising the steps of (i) inactivating viruses by the method defined in any of the embodiments 35-41, and (ii) removing viruses by the any of the methods defined in any of the embodiments 1-35, in any order.
  • a CHO K1 cell line transformed with a Factor VII-encoding plasmid was adapted to growth in suspension culture in a medium free of animal derived components.
  • a bank of the adapted cells was frozen. Cells from the bank were propagated in spinner bottles in suspension culture in medium free of animal derived components. As the cell number increased, the volume was gradually increased by addition of new medium. When the volume had reached 4 L, and the cell number had reached ⁇ 0.8*10 6 /ml, the contents of the spinner bottles were transferred into a 50 L stirred tank reactor (seed reactor). As the cell number increased in the 50 L reactor, the volume was gradually increased by addition of new medium.
  • the contents of the 50 L reactor were transferred into a 500 L stirred tank reactor (production reactor).
  • the 500 L reactor contained macroporous Cytopore 1 carriers (Amersham Biosciences) within which the cells became immobilized within 24 hours after inoculation.
  • the volume in the 500 L reactor was gradually increased by addition of new medium as the cell number increased.
  • the production phase was initiated and a medium change was performed every 24 hours: Agitation was stopped to allow for sedimentation of the cell-containing carriers, and 80% of the culture supernatant was then harvested and replaced with new medium.
  • the harvested culture supernatant was filtered to remove non-trapped cells and cell debris and was then transferred for further processing.
  • the 50 L as well as the 500 L bioreactor was instrumented for control of temperature, dissolved oxygen (sparging of oxygen through microsparger), agitation rate, headspace aeration rate and pH (downwards control by addition of CO 2 gas to headspace). Furthermore, the 500 L bioreactor was instrumented for control of dissolved CO 2 . Online CO 2 measurement was performed by means of an YSI 8500 CO 2 -instrument. The level of CO 2 was controlled by sparging of atmospheric air into the liquid through a tube according to the CO 2 signal.
  • the sparging rate was set to 0 L/min per L of culture liquid when the CO 2 concentration was at or below the set-point, and to 0.01-0.05 L/min per L of culture liquid when the CO 2 concentration was above the set-point.
  • the set-point for dissolved CO 2 was 160 mmHg.
  • no base was added to the bioreactor to control pH upwards.
  • the cell density reached 1-2 ⁇ 10 7 cells/ml, and the Factor VII concentration in the daily harvest 10-20 mg/L.
  • the pCO 2 was maintained within the range of 150-170 mmHg.
  • the pH was kept above 6.70, even though no base was added.
  • Protein solution to be filtered 25 L of FVII solution from the capture step, with the following characteristics
  • Protein solution to be filtered 185 ml of FVII solution from the capture step, with the following characteristics
  • Protein solution to be filtered 98 ml of FVIIa bulk substance, with the following characteristics
  • a Factor VII polypeptide solution (see Example 1) from the capture step comprising a Murine Leukemia Virus, titer YY plaque-forming units (pfu).
  • the filtration is conducted essentially as described herein with reference to FIG. 1 :
US11/439,828 2003-12-01 2006-05-23 Virus filtration of liquid Factor VII compositions Abandoned US20070142625A1 (en)

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US12/173,475 US20080274534A1 (en) 2003-12-01 2008-07-15 Virus Filtration of Liquid Factor VII Compositions
US13/349,980 US9102762B2 (en) 2003-12-01 2012-01-13 Virus filtration of liquid factor VII compositions
US14/753,551 US20150299685A1 (en) 2003-12-01 2015-06-29 Virus Filtration of Liquid Factor VII Compositions
US15/286,068 US20170022482A1 (en) 2003-12-01 2016-10-05 Virus Filtration of Liquid Factor VII Compositions
US16/145,565 US20190032026A1 (en) 2003-12-01 2018-09-28 Virus filtration of liquid factor VII compositions
US16/853,444 US20200248150A1 (en) 2003-12-01 2020-04-20 Virus filtration of liquid factor VII compositions
US17/522,216 US20220064605A1 (en) 2003-12-01 2021-11-09 Virus Filtration of Liquid Factor VII Compositions

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US13/349,980 Active 2027-02-27 US9102762B2 (en) 2003-12-01 2012-01-13 Virus filtration of liquid factor VII compositions
US14/753,551 Abandoned US20150299685A1 (en) 2003-12-01 2015-06-29 Virus Filtration of Liquid Factor VII Compositions
US15/286,068 Abandoned US20170022482A1 (en) 2003-12-01 2016-10-05 Virus Filtration of Liquid Factor VII Compositions
US16/145,565 Abandoned US20190032026A1 (en) 2003-12-01 2018-09-28 Virus filtration of liquid factor VII compositions
US16/853,444 Abandoned US20200248150A1 (en) 2003-12-01 2020-04-20 Virus filtration of liquid factor VII compositions
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US14/753,551 Abandoned US20150299685A1 (en) 2003-12-01 2015-06-29 Virus Filtration of Liquid Factor VII Compositions
US15/286,068 Abandoned US20170022482A1 (en) 2003-12-01 2016-10-05 Virus Filtration of Liquid Factor VII Compositions
US16/145,565 Abandoned US20190032026A1 (en) 2003-12-01 2018-09-28 Virus filtration of liquid factor VII compositions
US16/853,444 Abandoned US20200248150A1 (en) 2003-12-01 2020-04-20 Virus filtration of liquid factor VII compositions
US17/522,216 Abandoned US20220064605A1 (en) 2003-12-01 2021-11-09 Virus Filtration of Liquid Factor VII Compositions

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