Susceptibility of mouse minute virus to inactivation by heat in two cell culture media types

Viral contaminations of biopharmaceutical manufacturing cell culture facilities are a significant threat and one for which having a risk mitigation strategy is highly desirable. High temperature, short time (HTST) mammalian cell media treatment may potentially safeguard manufacturing facilities from such contaminations. HTST is thought to inactivate virions by denaturing proteins of the viral capsid, and there is evidence that HTST provides ample virucidal efficacy against nonenveloped or naked viruses such as mouse minute virus (MMV), a parvovirus. The aim of the studies presented herein was to further delineate the susceptibility of MMV, known to have contaminated mammalian cell manufacturing facilities, to heat by exposing virus‐spiked cell culture media to a broad range of temperatures and for various times of exposure. The results of these studies show that HTST is capable of inactivating MMV by three orders of magnitude or more. Thus, we believe that HTST is a useful technology for the purposes of providing a barrier to adventitious contamination of mammalian cell culture processes in the biopharmaceutical industry. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Review: High temperature short time treatment of cell culture media and feed solutions to mitigate adventitious viral contamination in the biopharmaceutical industry

Events of viral contaminations occurring during the production of biopharmaceuticals have been publicly reported by the biopharmaceutical industry. Upstream raw materials were often identified as the potential source of contamination. Viral contamination risk can be mitigated by inactivating or eliminating potential viruses of cell culture media and feed solutions. Different methods can be used alone or in combination on raw materials, cell culture media, or feed solutions such as viral inactivation technologies consisting mainly of high temperature short time, ultraviolet irradiation, and gamma radiation technologies or such as viral removal technology for instance nanofiltration. The aim of this review is to present the principle, the advantages, and the challenges of high temperature short time (HTST) technology. Here, we reviewed effectiveness of HTST treatment and its impact on media (filterability of media, degradation of components), on process performance (cell growth, cell metabolism, productivity), and product quality based on knowledge shared in the literature.     

Implementing high-temperature short-time media treatment in commercial-scale cell culture manufacturing processes

The production of therapeutic proteins by mammalian cell culture is complex and sets high requirements for process, facility, and equipment design, as well as rigorous regulatory and quality standards. One particular point of concern and significant risk to supply chain is the susceptibility to contamination such as bacteria, fungi, mycoplasma, and viruses. Several technologies have been developed to create barriers for these agents to enter the process, e.g. filtration, UV inactivation, and temperature inactivation. However, if not implemented during development of the manufacturing process, these types of process changes can have significant impact on process performance if not managed appropriately. This article describes the implementation of the high-temperature short-time (HTST) treatment of cell culture media as an additional safety barrier against adventitious agents during the transfer of a large-scale commercial cell culture manufacturing process. The necessary steps and experiments, as well as subsequent results during qualification runs and routine manufacturing, are shown.     

Identification and characterization of a Triton X-100 replacement for virus inactivation

Triton X-100 detergent treatment is a robust enveloped virus inactivation unit operation included in biopharmaceutical manufacturing processes. However, the European Commission officially placed Triton X-100 on the Annex XIV authorization list in 2017 because a degradation product of Triton X-100, 4-(1,1,3,3-tetramethylbutyl) phenol (also known as 4-tert-octylphenol), is considered to have harmful endocrine disrupting activities. As a result, the use of Triton X-100 in the European Economic Area (EEA) would not be allowed unless an ECHA issued authorization was granted after the sunset date of January 4, 2021. This has prompted biopharmaceutical manufacturers to search for novel, environment-friendly alternative detergents for enveloped virus inactivation. In this study, we report the identification of such a novel detergent, Simulsol SL 11W. Simulsol SL 11W is an undecyl glycoside surfactant produced from glucose and C11 fatty alcohol. We report here that Simulsol SL 11W was able to effectively inactive enveloped viruses, such as xenotropic murine leukemia virus (XMuLV) and pseudorabies virus (PRV). By using XMuLV as a representative enveloped virus, the influence of various parameters on the effectiveness of virus inactivation was evaluated. Virus inactivation by Simulsol SL 11W was effective across different clarified bioreactor harvests at broad concentrations, pH, and temperature ranges. Simulsol SL 11W concentration, temperature of inactivation, and treatment time were identified as critical process parameters for virus inactivation. Removal of Simulsol SL 11W was readily achieved by Protein A chromatography and product quality was not affected by detergent treatment. Taken together, these results have shown the potential of Simulsol SL 11W as a desirable alternative to Triton X-100 for enveloped virus inactivation that could be readily implemented into biopharmaceutical manufacturing processes.     

Insights into virus inactivation by polysorbate 80 in the absence of solvent

Triton X-100 has long been used either alone or in combination with solvent to inactivate enveloped viruses in biopharmaceutical manufacturing. However, European Chemicals Agency (ECHA) officially placed Triton X-100 on the Annex XIV authorization list in 2017 because 4-(1,1,3,3-tetramethylbutyl) phenol, a degradation product of Triton X-100, is of harmful endocrine disrupting activities. As a result, any use of Triton X-100 in the European Economic Area would require an ECHA issued authorization after the sunset date of January 4, 2021. In search of possible replacements for Triton X-100, we discovered that polysorbate 80 (PS80) in absence of any solvents was able to effectively inactive enveloped viruses such as xenotropic murine leukemia virus and pseudorabies virus with comparable efficacy as measured by log reduction factors. Interestingly, PS80 did not show any virucidal activities in phosphate buffered saline (PBS) while achieving robust virus inactivation in cell-free Chinese hamster ovary (CHO) bioreactor harvests. This intriguing observation led us to speculate that virus inactivation by PS80 involved components in the cell-free CHO bioreactor harvests that were absent in PBS. Specifically, we hypothesized that esterase and/or lipases in the cell-free bioreactor harvests hydrolyzed PS80 to yield oleic acid, a known potent virucidal agent, which in turn inactivated viruses. This theory was confirmed using purified recombinant lysosomal phospholipase A2 isomer (rLPLA2) in PBS. Subsequent characterization work has indicated that virus inactivation by PS80 is effective and robust within temperature and concentration ranges comparable to those of Triton X-100. Similar to Triton X-100, virus inactivation by PS80 is dually dependent on treatment time and temperature. Unlike Triton X-100, PS80 inactivation does not correlate with concentrations in a simple manner. Additionally, we have demonstrated that PS20 exhibits similar virus inactivation activities as PS80. Based on the findings described in the current work, we believe that PS80 is potentially a viable replacement for Triton X-100 and can be used in manufacturing processes for wide spectrum of biopharmaceuticals to achieve desirable virus clearance. Finally, the advantages and disadvantages of using PS80 for virus inactivation are discussed in the contexts of GMP manufacturing.     

Characterization of ionic strength for X-MuLV inactivation by low pH treatment for monoclonal antibody purification

In the production of monoclonal antibodies (mAbs) intended for use in humans, it is a global regulatory requirement that the manufacturing process includes unit operations that are proven to inactivate or remove adventitious agents to ensure viral safety. Viral inactivation by low pH hold (LPH) is typically used to ensure this viral safety in the purification process of mAbs and other biotherapeutics derived from mammalian cell lines. To ascertain the effectiveness of the LPH step, viral clearance studies have evaluated LPH under worst-case conditions of pH above the manufacturing set point and hold duration at or below the manufacturing minimum. Highly acidic conditions (i.e., pH < 3.60) provide robust and effective enveloped virus inactivation but may lead to reduced product quality of the therapeutic protein. However, when viral inactivation is operated above pH 3.60 to ensure product stability, effective (>4 log₁₀ reduction factor) viral inactivation may not be observed under these worst-case pH conditions in viral clearance studies. A multivariate design of experiments was conducted to further characterize the operating space for low pH viral inactivation of a model retrovirus, xenotropic murine leukemia virus (X-MuLV). The statistically designed experiment evaluated the effect of mAb isotype, pH, temperature, acid titrant, sodium chloride (NaCl) concentration, virus spike timing, and post-spike filtration on X-MuLV inactivation. Data from the characterization study were used to generate predictive models to identify conditions that reliably achieve effective viral inactivation at pH ≥ 3.60. Results of the study demonstrated that NaCl concentration has the greatest effect on virus inactivation in the range studied, and pH has a large effect when the load material has no additional NaCl. Overall, robust and effective inactivation of X-MuLV at pH 3.65–3.80 can be achieved by manipulating either the pH or the NaCl concentration of the load material. This study contributes to the understanding of ionic strength as an influential parameter in low pH viral inactivation studies.     

Inactivation of adenovirus type 5 by caustics

Adenovirus shows significant promise as a vehicle for transfer of therapeutic genes into humans. Based on the importance of this viral vector, it is critical that adequate decontamination procedures are implemented during its large-scale production in multiproduct manufacturing facilities to prevent cross-product contamination and to reduce the risk of personnel exposure. Liquid decontamination procedures based on caustics are easily implemented in a manufacturing setting and are not corrosive to stainless steel surfaces at the concentrations found to inactivate viral proteins and nucleic acids. In this study, we have conducted small-scale experiments to determine the effectiveness of caustic inactivation procedures on adenovirus type 5 and have evaluated the robustness of the process to different sample matrices and adenovirus constructs. We find that the pH of a sample post-addition of caustic solution is a more accurate indicator of the effectiveness of the caustic than its concentration. We have demonstrated that a greater than 6 log reduction in the potency of adenovirus type 5 may be obtained upon exposure of the sample to sodium hydroxide and CIP-100 at concentrations greater than 0.09 M and 0.9%, respectively, at times greater than 10 min.     

Destruction of Cucumber green mottle mosaic virus by heat treatment and rapid detection of virus inactivation by RT-PCR

Heat treatment is commonly used to control viral contamination of seeds. To study virus inactivation, virus was purified from seeds contaminated with Cucumber green mottle mosaic virus (CGMMV) after various heat treatments. CGMMV particles were observed to be physically disrupted by high temperature. Analysis of viral RNA revealed that the 5' and 3' termini of the genome were protected whereas regions between 2-2.5, 3.2-3.7 and 4-4.8 kb from the 5' terminus were not. Heat inactivation of virus on seeds was confirmed by RT-PCR using primers for a heat-sensitive region. The RT-PCR approach developed here may prove preferable to time- and labor-intensive bioassays for assessing virus heat inactivation.     

Optimization of non-detergent treatment for enveloped virus inactivation using the Taguchi design of experimental methodology (DOE)

Abstract

In mammalian cell culture technology, viral contamination is one of the main challenges; and, so far, various strategies have been taken to remove or inactivate viruses in the cell-line production process. The suitability and feasibility of each method are determined by different factors including effectiveness in target virus inactivation, maintaining recombinant protein stability, easiness—in terms of the process condition, cost-effectiveness, and eco-friendliness. In this research, Taguchi design-of-experiments (DOE) methodology was used to optimize a non-detergent viral inactivation method via considering four factors of temperature, time, pH, and alcohol concentration in an unbiased (orthogonal) fashion with low influence of nuisance factors. Herpes Simplex Virus-1 (HSV1) and Vero cell-line were used as models for enveloped viruses and cell-line, respectively. Examining the cytopathic effects (CPE) in different dilutions showed that pH (4), alcohol (15%), time (120?min), and temperature (25?°C) were the optimal points for viral inactivation. Evaluating the significance of each parameter in the HSV-1 inactivation using Taguchi and ANOVA analyses, the contributions of pH, alcohol, temperature and time were 56.5%, 19.2%, 12%, and 12%, respectively. Examining the impact of the optimal viral treatment condition on the stability of model recombinant protein-recombinant human erythropoietin, no destabilization was detected.     

Enveloped virus inactivation by caprylate: a robust alternative to solvent-detergent treatment in plasma derived intermediates.

Solvent-detergent treatment, although used routinely in plasma product processing to inactivate enveloped viruses, substantially reduces product yield from the human plasma resource. To improve yields in plasma product manufacturing, a new viral reduction process has been developed using the fatty acid caprylate. As licensure of plasma products warrants thorough evaluation of pathogen reduction capabilities, the present study examined susceptibility of enveloped viruses to inactivation by caprylate in protein solutions with varied pH and temperature. In the immunoglobin-rich solutions from Cohn Fraction II+III, human immunodeficiency virus, Type-1, bovine viral diarrhea virus (BVDV), and pseudorabies virus were inactivated by caprylate concentrations of >/=9 mM, >/=12 mM, and >/=9 mM, respectively. Compared to solvent-detergent treatment, BVDV inactivation in Fraction II+III solution was significantly faster (20-60 fold) using 16 mM caprylate. Caprylate-mediated inactivation of BVDV was not noticeably affected by temperature within the range chosen manufacturing the immunoglobulin product. In Fraction II+III solutions, IgG solubility was unaffected by 相似文献   

Assessment of Needs for Plasma for Fractionation in Europe

In the early 1990s, a series of outbreaks of hepatitis C (HCV) infections clustering among recipients of certain lots of plasma-derived medicinal products (PDMP) alarmed regulatory authorities, manufacturers and the public alike. Also, a few episodes of Hepatitis A (HAV) infections occurred in haemophiliacs receiving solvent-detergent-treated factor VIII concentrates. Thus, several measures were brought into effect to reestablish the safety of the incriminated products and to further increase the margin of safety of PDMP in general. Therefore, intramuscular immunoglobulins had to be free of HCV RNA as shown by nucleic acid amplification technology (NAT) in the final products. Furthermore, the manufacturing process of PDMP had to be validated for both viral inactivation and elimination. Finally, HCV-NAT was to be standardised and implemented as a validated test of plasma pool samples.In 1994, a joint meeting of EPFA, EAPPI and Regulatory Authorities was held in Brussels to outline the state of the art and to delineate the actions to be taken. Five years later, in 1999, the incidence rates of HIV, HBV and HCV in unpaid blood donors have been minimized, especially in European countries. With probabilities for window period donations as low as 0.6 in 1 million for both HIV and HCV and 2.1 in 1 million for HBV in Switzerland, labile blood products have reached extreme, but not absolute safety. The introduction of HCV-NAT roughly doubles this safety resulting in a 1 in 3 million probability of a window donation.Concomittantly, extensive viral validation studies document effective inactivation and removal of viruses in PDMP. The demonstrated margins of safety, expressed as logarithmical reduction factors (LRF), range from 4 to over 20 log(10), depending on product, virus, and inactivation procedure used. Further progress to even safer PDMP shall be acomplished by consolidating the GMP processes, abandoning of obsolete requirements and harmonising national regulations within Europe. Before introducing new measures for additional agents such as HAV or Parvovirus B 19, gains and risks and even potential new threats have to be carefully assessed. Alternative efforts for the safeguard of patients, e.g. vaccination for HAV, need to be balanced against the risks of changing established and validated manufacturing procedures of PDMP with long-lasting safety records.     

Assessment of viral inactivation during pH 3.3 pepsin digestion and caprylic acid treatment of antivenoms

Antivenoms are manufactured by the fractionation of animal plasma which may possibly be contaminated by infectious agents pathogenic to humans. This study was carried out to determine whether pre-existing antivenom production steps, as carried out by EgyVac in Egypt, may reduce viral risks. Two typical manufacturing steps were studied by performing down-scaled viral inactivation experiments: (a) a pH 3.3 pepsin digestion of diluted plasma at 30 degrees C for 1h, and (b) a caprylic acid treatment of a purified F(ab')2 fragment fraction at 18 degrees C for 1h. Three lipid-enveloped (LE) viruses [bovine viral diarrhoea virus (BVDV), pseudorabies virus (PRV), and vesicular stomatitis virus (VSV)] and one non-lipid-enveloped (NLE) virus [encephalomyocarditis virus (EMC)] were used as models. Kinetics of inactivation was determined by taking samples at 3 time-points during the treatments. The pH 3.3 pepsin digestion resulted in complete clearance of PRV (>7.0 log(10)) and in almost complete reduction of VSV (>4.5 but < or =6.4 log(10)), and in a limited inactivation of BVDV (1.7 log(10)). EMC inactivation was > or =2.5 but < or =5.7 log(10). The caprylic acid treatment resulted in complete inactivation of the 3 LE viruses tested: BVDV (>6.6 log(10)), PRV (>6.6 log(10)), and VSV (>7.0 log(10)). For EMC no significant reduction was obtained (0.7 log(10)). Cumulative reduction was >13.6, >11.5, >8.3 and > or =2.5 for PRV, VSV, BVDV and EMC, respectively. Therefore the current manufacturing processes of at least some animal antisera already include production steps that can ensure robust viral inactivation of LE viruses and moderate inactivation of a NLE virus.     

Gamma irradiation of animal sera for inactivation of viruses and mollicutes – A review

Animal-derived materials such as animal sera represent a low, but finite, risk for introduction of an adventitious agent (virus or mollicute) into a biological bulk harvest during upstream manufacturing processes involving mammalian cell substrates. Viral and mollicute (Mycoplasma sp. and Acholeplasma sp.) contamination events have been relatively rare, but many of those that have been reported have been attributed to use of infected animal sera in growth media during cell expansion. The risk of introduction of viruses and mollicutes may be mitigated by elimination of the use of animal sera and implementation instead of chemically defined or serum- and animal-derived material-free cell culture media. When use of animal sera is unavoidable, however, mitigation of the risk of introducing an adventitious contaminant may involve treatment of the sera to inactivate potential contaminants. Gamma irradiation is one of the most widely employed methods for viral and mollicute inactivation in animal sera. In this article, we review the inactivation results reported for viral and mollicute inactivation in frozen serum. Studies performed to assess the impact of gamma irradiation on serum quality and performance are also discussed. The available data indicate that inactivation of mollicutes in serum is essentially complete at the gamma radiation doses normally employed (25–40 kGy), while the efficacy and kinetics for viral inactivation in serum by gamma irradiation appear to be dependent in part upon the size of the target virus.     

Virus contaminations of cell cultures – A biotechnological view

In contrast to contamination by microbes and mycoplasma, which can be relatively easily detected, viral contamination present a serious threat because of the difficulty in detecting some viruses and the lack of effective methods of treating infected cell cultures. While some viruses are capable of causing morphological changes to infected cells (e.g. cytopathic effect) which are detectable by microscopy some viral contaminations result in the integration of the viral genome as provirus, this causes no visual evidence, by means of modification of the cellular morphology. Virus production from such cell lines, are potentially dangerous for other cell cultures (in research labs)by cross contaminations, or for operators and patients (in the case of the production of injectable biologicals) because of potential infection. The only way to keep cell cultures for research, development, and the biotech industry virus-free is the prevention of such contaminations. Cell cultures can become contaminated by the following means: firstly, they may already be contaminated as primary cultures (because the source of the cells was already infected), secondly, they were contaminated due to the use of contaminated raw materials, or thirdly, they were contaminated via an animal passage. This overview describes the problems and risks associated with viral contaminations in animal cell culture, describes the origins of these contaminations as well as the most important virsuses associated with viral contaminations in cell culture. In addition, ways to prevent viral contaminations as well as measures undertaken to avoid and assess risks for viral contaminations as performed in the biotech industry are briefly described. This revised version was published online in August 2006 with corrections to the Cover Date.     

Hydrogen peroxide vapour (HPV) inactivation of adenovirus

Aims: Adenovirus contamination can be problematic in various settings including life science laboratories and during pharmaceutical manufacturing processes. Stringent and effective decontamination procedures are necessary to minimize the risk of personnel exposure or product cross‐contamination in these settings. Hydrogen peroxide vapour (HPV) is sporicidal, tuberculocidal and fungicidal with proven efficacy against some viruses. We investigate the efficacy of HPV for the inactivation of a recombinant adenovirus. Methods and Results: In this study, the survival of a dried recombinant adenovirus (Ad5GFP) was tested before and after HPV exposure to determine the efficacy of HPV at inactivating adenovirus. A > 8‐log TCID₅₀ reduction resulted from 45‐min exposure to HPV in a microbiological safety cabinet. Conclusions: HPV is effective for the inactivation of a recombinant adenovirus. Significance and impact of the study: The results suggest that HPV may be useful for adenovirus decontamination in life science laboratories or in manufacturing facilities.     

Partitioning and inactivation of viruses by the caprylic acid precipitation followed by a terminal pasteurization in the manufacturing process of horse immunoglobulins

Caprylic acid (octanoic acid), has been used for over 50 years as a stabilizer of human albumin during pasteurization. In addition caprylic acid is of great interest, by providing the advantage of purifying mammalian immunoglobulins and clearing viruses infectivity in a single step. Exploiting these two properties, we sequentially used the caprylic acid precipitation and the pasteurization to purify horse hyperimmune globulins used in the manufacturing of Sérocytol. To evaluate the effectiveness of the process for the removal/inactivation of viruses, spiking studies were carried out for each dedicated step. Bovine viral diarrhoea virus (BVDV), pseudorabies virus (PRV), encephalomyocarditis virus (EMCV) and minute virus of mice (MVM) were used for the virological validation. Our data show that the treatment with caprylic acid 5% (v/v) can effectively be used as well to purify or to ensure viral safety of immunoglobulins. Caprylic acid precipitation was very efficient in removing and/or inactivating enveloped viruses (PRV, BVDV) and moderately efficient against non-enveloped viruses (MVM, ECMV). However the combination with the pasteurization ensured an efficient protection against both enveloped and non-enveloped viruses. So that viruses surviving to the caprylic acid precipitation will be neutralized by pasteurization. Significant log reduction were achieved > or =9 log(10) for enveloped viruses and 4 log(10) for non-enveloped viruses, providing the evidence of a margin of viral safety achieved by our manufacturing process. Its a simple and non-expensive manufacturing process of immunoglobulins easily validated that we have adapted to a large production scale with a programmable operating system.     

Safety aspects in the manufacturing of plasma-derived coagulation factor concentrates.

Plasma-derived coagulation factor concentrates, prepared using traditional manufacturing processes, have transmitted viral diseases, especially AIDS, hepatitis B and hepatitis C to patients. To date, more extensive selection of blood donors, improved screening procedures of each plasma donation for direct and indirect viral markers, and newly developed virucidal procedures, especially pasteurization and solvent-detergent, together with extraction technologies of plasma proteins based on high-resolution chromatographic separations, have diminished considerably the risks of transmitting these pathogenic agents. To ensure safety, each production process must be carefully validated, following a rigorous scientific approach to assess its ability to inactivate or eliminate viruses. In addition, Good Manufacturing Practices must avoid any variation from these validated viral inactivation processes and must eliminate risks of potential downstream contamination of purified plasma fractions following viral inactivation or elimination steps. Other side-effects associated with conventional low-purity preparations, such as acute haemolytic anemia due to contamination by isohaemagglutinins, or immunosuppression possibly due to an overload in fibrinogen and immunoglobulins, have not been reported following infusion of highly purified coagulation factor concentrates. Present state-of-the-art virus inactivation and protein-purification technologies have significantly improved the safety of plasma coagulation factor concentrates.     

Comparability studies of new 3rd generation recombinant human factor VIII GreenGene F after improvement of formulation and viral inactivation/removal process

A new 3rd generation recombinant factor VIII (rFVIII), GreenGene F (WHO INN: beroctocog alfa), which is a highly homogenous B-domain deleted FVIII protein comprising of two peptides as heavy chain (A1 and A2 domain) and light chain (A3, C1, and C2 domain) at 80 and 90 kDa, was developed from its predecessor product GreenGene (2nd generation product previously approved by Korea FDA after clinical studies in South Korea) by process improvements of i) addition of Solvent/Detergent treatment for virus inactivation, ii) nanofiltration (20 nm pore size) for viral removal and iii) alterations to an albumin-free formulation to minimize the risk of viral contamination. An assessment of comparability between the two products was made to see if process improvements for safer product manufacturing affected the rFVIII structural and functional characteristics. Physicochemical and physiological characteristics were observed, in vivo efficacy following a single intravenous administration to FVIII knock-out mice and toxicity by various GLP in vivo tests were evaluated. All results showed equivalence, proving that no changes in protein characteristics of rFVIII occurred from process changes in formulation, viral inactivation, and viral removal which minimize the risk of pathogen transmission to enhance safety.     

Identification and quantitation of vesivirus 2117 particles in bioreactor fluids from infected Chinese hamster ovary cell cultures

The prevention of adventitious agent contamination is a top priority throughout the entire biopharmaceutical production process. For example, although viral contamination of cell banks or cell cultures is rare, it can result in serious consequences (e.g., shutdown and decontamination of manufacturing facilities). To ensure virus free production, numerous in vivo and in vitro adventitious agent assays and biophysical characterizations such as electron microscopy are conducted on cell banks, raw materials, process materials, and drug substances throughout the manufacturing process. Molecular assays such as PCR and other nucleotide‐based techniques are also routinely used for screening and identification of any viral agents. However, modern techniques in protein identification of complex protein mixtures have not yet been effectively integrated throughout the industry into current viral testing strategies. Here, we report the identification and quantitation of Vesivirus 2117 particles in bioreactor fluid from infected Chinese hamster ovary cell cultures by global protein sequencing using mass spectrometry in combination with multi‐dimensional liquid‐chromatography. Following mass spectrometric data acquisition and rigorous data analysis, six virus specific peptides were identified. These peptides were fragments of two structural proteins, capsid protein pre‐cursor (four unique peptides) and small structural protein (two unique peptides), from the same species: Vesivirus 2117. Using stable heavy isotope‐labeled peptides as internal standards, we also determined the absolute concentration of Vesivirus particles in the bioreactor fluid and the ratio of two capsid proteins (VP1:VP2) in the particles as approximately 9:1. The positive identification of Vesivirus 2117 was subsequently confirmed by RT‐PCR. Biotechnol. Bioeng. 2013; 110: 1342–1353. © 2012 Wiley Periodicals, Inc.     

Virus inactivation by protein denaturants used in affinity chromatography

Virus inactivation by a number of protein denaturants commonly used in gel affinity chromatography for protein elution and gel recycling has been investigated. The enveloped viruses Sindbis, herpes simplex-1 and vaccinia, and the non-enveloped virus polio-1 were effectively inactivated by 0.5 M sodium hydroxide, 6 M guanidinium thiocyanate, 8 M urea and 70% ethanol. However, pH 2.6, 3 M sodium thiocyanate, 6 M guanidinium chloride and 20% ethanol, while effectively inactivating the enveloped viruses, did not inactivate polio-1. These studies demonstrate that protein denaturants are generally effective for virus inactivation but with the limitation that only some may inactivate non-enveloped viruses. The use of protein denaturants, together with virus reduction steps in the manufacturing process should ensure that viral cross contamination between manufacturing batches of therapeutic biological products is prevented and the safety of the product ensured.