The first recombinant human coagulation factor VIII of human origin: human cell line and manufacturing characteristics.

INTRODUCTION: Since the early 1990s, recombinant human clotting factor VIII (rhFVIII) produced in hamster cells has been available for haemophilia A treatment. However, the post-translational modifications of these proteins are not identical to those of native human FVIII, which may lead to immunogenic reactions and the development of inhibitors against rhFVIII. For the first time, rhFVIII produced in a human host cell line is available. AIM: We describe here the establishment of the first human production cell line for rhFVIII and the manufacturing process of this novel product. METHODS AND RESULTS: A human cell line expressing rhFVIII was derived from human embryonic kidney (HEK) 293 F cells transfected with an FVIII expression plasmid. No virus or virus-like particles could be detected following extensive testing. The stringently controlled production process is completely free from added materials of animal or human origin. Multistep purification employing a combination of filtration and chromatography steps ensures the efficient removal of impurities. Solvent/detergent treatment and a 20 nm pore size nanofiltration step, used for the first time in rhFVIII manufacturing, efficiently eliminate any hypothetically present viruses. In contrast to hamster cell-derived products, this rhFVIII product does not contain hamster-like epitopes, which might be expected to be immunogenic. CONCLUSIONS: HEK 293 F cells, whose parental cell line HEK 293 has been used by researchers for decades, are a suitable production cell line for rhFVIII and will help avoid immunogenic epitopes. A modern manufacturing process has been developed to ensure the highest level of purity and pathogen safety.

Contribution to safety of immunoglobulin and albumin from virus partitioning and inactivation by cold ethanol fractionation: a data collection from Plasma Protein Therapeutics Association member companies.

BACKGROUND: Virus removal by partitioning into different fractions during cold ethanol fractionation has been described by several authors, demonstrating that cold ethanol fractionation can provide significant contribution to virus removal, even in those cases where virus removal is limited and must be supported by additional measures for virus inactivation during further processing. STUDY DESIGN AND METHODS: Plasma Protein Therapeutics Association (PPTA) member companies collected and evaluated 615 studies on virus removal by the steps of the cold ethanol fractionation process. The studies describe the precipitation and separation of Fraction (F)III or FI/III in the immunoglobulin fractionation process and precipitation and separation of FII/III, FI/II/III, and FIV/IV in the albumin fractionation process. RESULTS: The data indicate a significant contribution of cold ethanol fractionation to the overall clearance of a broad spectrum of viruses, at varied process variables such as pH, temperature, and alcohol concentration and demonstrate the robustness of virus removal by the cold ethanol fractionation process. CONCLUSIONS: The data presented here support the importance of the partitioning steps for virus safety for immunoglobulins and albumin. However, virus removal by cold ethanol fractionation alone cannot provide viral safety of human albumin and immunoglobulins and therefore must be completed by other virus inactivation and removal procedures.

Robustness of solvent/detergent treatment of plasma derivatives: a data collection from Plasma Protein Therapeutics Association member companies.

BACKGROUND: Solvent/detergent (S/D) treatment is an established virus inactivation technology that has been applied in the manufacture of medicinal products derived from human plasma for more than 20 years. Data on the inactivation of enveloped viruses by S/D treatment collected from seven Plasma Protein Therapeutics Association member companies demonstrate the robustness, reliability, and efficacy of this virus inactivation method. STUDY DESIGN AND METHODS: The results from 308 studies reflecting production conditions as well as technical variables significantly beyond the product release specification were evaluated for virus inactivation, comprising different combinations of solvent and detergent (tri(n-butyl) phosphate [TNBP]/Tween 80, TNBP/Triton X-100, TNBP/Na-cholate) and different products (Factor [F]VIII, F IX, and intravenous and intramuscular immunoglobulins). RESULTS: Neither product class, process temperature, protein concentration, nor pH value has a significant impact on virus inactivation. A variable that did appear to be critical was the concentration of solvent and detergent. CONCLUSION: The data presented here demonstrate the robustness of virus inactivation by S/D treatment for a broad spectrum of enveloped test viruses and process variables. Our data substantiate the fact that no transmission of viruses such as human immunodeficiency virus, hepatitis B virus, hepatitis C virus, or of other enveloped viruses was reported for licensed plasma derivatives since the introduction of S/D treatment.

Prion safety of transfusion plasma and plasma-derivatives typically used for prophylactic treatment.

Reports about transfusion-related transmissions of variant Creutzfeldt-Jakob disease have urged the need for more information regarding the risk for prion contaminated units in the blood supply and the safety of transfusion plasma and biopharmaceuticals derived from this precious raw material. According to a possible epidemiological model, the risk in many European countries is the same or lower than that of human immunodeficiency virus. Comprehensive investigations have shown that the prion safety margin of both single-donor and pooled solvent/detergent treated transfusion plasma is high. Furthermore, prophylactic treatment using plasma-derivatives poses a very low risk in terms of prion disease despite extensive lifetime exposure.