Virus inactivation by solvent/detergent treatment using Triton X-100 in a high purity factor VIII

Virus inactivation by solvent/detergent treatment using 0.3% tri-n-butyl phosphate and 1% Triton X-100 in the high purity factor VIII concentrate Replenate((R)) has been investigated. A wide range of model enveloped viruses were confirmed to be inactivated by >4 to >6log after 30min at 22 degrees C under standard conditions. Using Sindbis as a representative enveloped virus, the effect of various parameters on the inactivation process was tested. Virus inactivation was confirmed to be effective in different batches of product and was not influenced by changing the process conditions with regard to protein and salt concentration or pH. Virus inactivation was effective even at a temperature as low as 4-5 degrees C. Although solvent/detergent concentration was the most critical parameter, a concentration as low as 0.15% TnBP/0.5% Triton X-100 was still completely effective. At a lower concentration an extended incubation period was required. These studies demonstrate the robustness of this solvent/detergent procedure based on Triton X-100 and allow suitable process limits to be set for this manufacturing step.     

Virus reduction in an intravenous immunoglobulin by solvent/detergent treatment, ion-exchange chromatography and terminal low pH incubation

Virus reduction by several steps in the manufacturing process for the intravenous immunoglobulin Vigam^®, has been investigated. The solvent/detergent step based on treatment with 0.3% tri-n-butyl phosphate and 1% polysorbate 80 at 37 °C, was confirmed to be effective for a range of enveloped viruses. Virus infectivity was undetectable i.e. >6 log inactivation within 30 min of the standard 6 h process. This was consistent over the range of conditions tested i.e. solvent/detergent and protein concentration, temperature and pH. The ion-exchange chromatography step in the process was also able to remove some viruses. Virus spiked followed by blank column runs confirmed the effectiveness of the sanitisation step for ensuring there was no virus cross contamination between column runs. The terminal low pH incubation step was also able to inactivate enveloped viruses, as well as some non-enveloped viruses. The combination of these three steps ensures a high margin of virus safety for this product.     

Characterization of operating parameters for XMuLV inactivation by low pH treatment

To ensure the viral safety of protein therapeutics made in mammalian cells, purification processes include dedicated viral clearance steps to remove or inactivate adventitious and endogenous viruses. One such dedicated step is low pH treatment, a robust and effective method commonly used in monoclonal antibody production to inactivate enveloped viruses. To characterize the operating space for low pH viral inactivation, we performed a statistically designed experiment evaluating the effect of pH, temperature, hold duration, acid type, and buffer concentration on inactivation of the retrovirus model, XMuLV. An additional single factor experiment was performed to study the effect of protein concentration. These data were used to generate predictive models of inactivation at each time point studied, which can be used to identify conditions for robust and effective XMuLV inactivation. At pH 3.6, XMuLV inactivation was rapid, robust, and relatively unaffected by the other factors studied, providing support for this as a generic viral inactivation condition for products that can tolerate this low pH. At pH 3.7 and 3.8, other factors besides pH affected XMuLV inactivation. By understanding the impact of each factor on inactivation, the factors can be manipulated within the operating space to ensure effective inactivation while achieving desired product quality goals. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 32:89–97, 2016     

Investigations of prion and virus safety of a new liquid IVIG product.

A highly purified, liquid, 10% immunoglobulin product stabilized with proline, referred to as IgPro10 has recently been developed. IgG was purified from human plasma by cold ethanol fractionation, octanoic acid precipitation and anion-exchange chromatography. The manufacturing process includes two distinctly different partitioning steps and virus filtration, which were also assessed for the removal of prions. Prion removal studies used different spike preparations (brain homogenate, microsomes, purified PrP(sc)) and three different detection methods (bioassay, Western blot, conformation-dependent immunoassay). All of the investigated production steps were shown to reduce significantly all different spike preparations, resulting in an overall reduction of >10log(10). Moreover, the biochemical assays proved equally effective to the bioassay for the demonstration of prion elimination. Four of the manufacturing steps cover three different mechanisms of virus clearance. These are: i) virus inactivation; ii) virus filtration; and iii) partitioning. These mechanisms were assessed for their virus reduction capacity. Virus validation studies demonstrated overall reduction factors of >18log(10) for enveloped and >7log(10) for non-enveloped model viruses. In conclusion, the IgPro10 manufacturing process has a very high reduction potential for prions and for a wide variety of viruses resulting in a state-of-the-art product concerning safety towards known and emerging pathogens.     

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.     

Low pH, caprylate incubation as a second viral inactivation step in the manufacture of albumin. Parametric and validation studies.

Caprylate has long been used as a stabiliser for albumin solutions, as well as a precipitation agent for immunoglobulins, ceruloplasmin and more recently in removing contaminants during albumin purification. Its virucidal properties have been explored and it has been proposed that the non-ionised form of the caprylate acid disrupts the integrity of the lipid bilayer and membrane associated proteins of enveloped viruses. The studies reported here further explore the use of this fatty acid to inactivate lipid-enveloped viruses in albumin manufactured for therapeutic use.Caprylate concentrations considered above solubility limits were adopted. Acidic pH was used to maximise the percentage of non-ionised caprylate and elevated temperatures were used to enhance inactivation rates. Parameters were manipulated to determine the relationship between pH, temperature and caprylate: protein ratio.These studies demonstrated that elevated temperature and low pH were critical in achieving significant reduction in virus infectivity and that the rate and extent of inactivation was sensitive to changes in caprylate:protein ratio and to changes in pH. Final inactivation conditions of 10% w/v protein, 16 mM caprylate, pH 4.5 and 30 degrees C were chosen to minimise protein dimerisation and to achieve greater than 4 log(10)inactivation of the most resistant virus tested, bovine viral diarrhoea virus.Validation studies using both model and relevant blood borne viruses demonstrated this to be a robust and effective viral inactivation step and is complementary to the commonly used pasteurisation viral inactivation step, thus providing an additional margin of safety to this valuable therapeutic blood product.     

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   

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.     

Enveloped virus inactivation using neutral arginine solutions and applications in therapeutic protein purification processes

For the manufacturing of recombinant protein therapeutics produced from mammalian cell culture, demonstrating the capacity of the purification process to effectively clear infectious viruses is a regulatory requirement. At least two process steps, using different mechanisms of virus removal and/or inactivation, should be validated in support of the regulatory approval process. For example, exposure of the product stream to low pH, detergents or solvent/detergent combinations is commonly incorporated in protein purification processes for the inactivation of lipid‐enveloped viruses. However, some proteins have limited stability at low pH or in the presence of the detergents, and alternative techniques for achieving the inactivation of enveloped viruses would be beneficial. We present here an alternative and novel approach for the rapid inactivation of enveloped viruses using pH‐neutral buffer solutions containing arginine. The implementation of this approach in a monoclonal antibody or Fc‐fusion protein purification process is described and illustrated with several different therapeutic proteins. The use of the neutral pH arginine solution was able to effectively inactivate two enveloped model viruses, with no measurable effect on the product quality of the investigated proteins. Thus, the use of pH‐neutral arginine containing buffer solutions provides an alternative means of virus inactivation where other forms of virus inactivation, such as low pH and/or solvent/detergent treatments are not possible or undesirable due to protein stability limitations. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 30:108–112, 2014     

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.     

Comparable virus inactivation by bovine or vegetable derived Tween 80 during solvent/detergent treatment.

A mixture of Tri-n-butyl phosphate (TNBP) and Polysorbate 80 (Tween 80) is often used for virus inactivation during the manufacture of medicinal products derived from human plasma. This procedure, known as solvent/detergent treatment, is of high effectiveness for inactivation of enveloped viruses. Tween 80 can be manufactured from bovine tallow or from vegetable material. As the bovine-derived Tween 80 is normally used for the solvent/detergent treatment, the question has been raised whether vegetable-derived Tween 80 can be applied as an alternative substance for the solvent/detergent treatment. Comparable inactivation studies were therefore performed using Vesicular Stomatitis Virus (VSV), Pseudorabiesvirus (PRV), Semliki Forest Virus (SFV) and Bovine Diarrhoea Virus (BVDV). In principle, no differences were observed in the effectiveness of the solvent/detergent treatment when bovine or vegetable-derived Tween 80 was used. The comparability in the efficiency of both detergents for virus inactivation was shown to be independent of solvent/detergent concentration, of temperature (16 degrees C and 6 degrees C vs. 27 degrees C and 25 degrees C) and protein concentration (10% and 5% human albumin). In summary, vegetable-derived Tween 80 is of the same effectiveness as bovine-derived Tween 80, when used for virus inactivation by the solvent/detergent treatment.     

S/D处理人纤维蛋白原的病毒灭活验证

在人纤维蛋白原制备工艺中增加Ｓ／Ｄ处理灭活病毒步骤,ＴＮＢＰ和Ｔｗｅｅｎ８０终浓度分别为０．３％和１％,在２５℃处理６小时能有效灭活指示病毒ＶＳＶ（〉３．７５Ｌｏｇ）、Ｓｉｎｄｂｉｓ（〉４．４６Ｌｏｇ）、ＨＩＶ（〉３．６７Ｌｏｇ）,盲传三代未检出病毒     

Inactivation of enveloped and non-enveloped viruses on seeded human tissues by gamma irradiation

Human tissue allografts are widely used in a variety of clinical applications with over 1.5 million implants annually in the US alone. Since the 1990s, most clinically available allografts have been disinfected to minimize risk of disease transmission. Additional safety assurance can be provided by terminal sterilization using low dose gamma irradiation. The impact of such irradiation processing at low temperatures on viruses was the subject of this study. In particular, both human tendon and cortical bone samples were seeded with a designed array of viruses and the ability of gamma irradiation to inactivate those viruses was tested. The irradiation exposures for the samples packed in dry ice were 11.6-12.9 kGy for tendon and 11.6-12.3 kGy for bone, respectively. The viruses, virus types, and log reductions on seeded tendon and bone tissue, respectively, were as follows: Human Immunodeficiency Virus (RNA, enveloped), >2.90 and >3.20; Porcine Parvovirus (DNA, non-enveloped), 1.90 and 1.58; Pseudorabies Virus (DNA, enveloped), 3.80 and 3.79; Bovine Viral Diarrhea Virus (RNA, enveloped), 2.57 and 4.56; and Hepatitis A Virus (RNA, non-enveloped), 2.54 and 2.49, respectively. While proper donor screening, aseptic technique, and current disinfection practices all help reduce the risk of viral transmission from human allograft tissues, data presented here indicate that terminal sterilization using a low temperature, low dose gamma irradiation process inactivates both enveloped and non-enveloped viruses containing either DNA or RNA, thus providing additional assurance of safety from viral transmission.     

Bracketed generic inactivation of rodent retroviruses by low pH treatment for monoclonal antibodies and recombinant proteins

Viral safety is a predominant concern for monoclonal antibodies (mAbs) and other recombinant proteins (RPs) with pharmaceutical applications. Certain commercial purification modules, such as nanofiltration and low-pH inactivation, have been observed to reliably clear greater than 4 log(10) of large enveloped viruses, including endogenous retrovirus. The concept of "bracketed generic clearance" has been proposed for these steps if it could be prospectively demonstrated that viral log(10) reduction value (LRV) is not impacted by operating parameters that can vary, within a reasonable range, between commercial processes. In the case of low-pH inactivation, a common step in mAb purification processes employed after protein A affinity chromatography, these parameters would include pH, time and temperature of incubation, the content of salts, protein concentration, aggregates, impurities, model protein pI, and buffer composition. In this report, we define bracketed generic clearance conditions, using a prospectively defined bracket/matrix approach, where low-pH inactivation consistently achieves >or=4.6 log(10) clearance of xenotropic murine leukemia virus (X-MLV), a model for rodent endogenous retrovirus. The mechanism of retrovirus inactivation by low-pH treatment was also investigated.     

Virus elimination during the purification of monoclonal antibodies by column chromatography and additional steps

The theoretical potential for virus transmission by monoclonal antibody based therapeutic products has led to the inclusion of appropriate virus reduction steps. In this study, virus elimination by the chromatographic steps used during the purification process for two (IgG‐1 & ?3) monoclonal antibodies (MAbs) have been investigated. Both the Protein G (>7log) and ion‐exchange (5 log) chromatography steps were very effective for eliminating both enveloped and non‐enveloped viruses over the life‐time of the chromatographic gel. However, the contribution made by the final gel filtration step was more limited, i.e., 3 log. Because these chromatographic columns were recycled between uses, the effectiveness of the column sanitization procedures (guanidinium chloride for protein G or NaOH for ion‐exchange) were tested. By evaluating standard column runs immediately after each virus spiked run, it was possible to directly confirm that there was no cross contamination with virus between column runs (guanidinium chloride or NaOH). To further ensure the virus safety of the product, two specific virus elimination steps have also been included in the process. A solvent/detergent step based on 1% triton X‐100 rapidly inactivating a range of enveloped viruses by >6 log inactivation within 1 min of a 60 min treatment time. Virus removal by virus filtration step was also confirmed to be effective for those viruses of about 50 nm or greater. In conclusion, the combination of these multiple steps ensures a high margin of virus safety for this purification process. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1341–1347, 2014     

Virus inactivation in a factor VIII/VWF concentrate treated using a solvent/detergent procedure based on polysorbate 20

Treatment with solvent/detergent is a widely used method for ensuring the virus safety of plasma products. In the present study, virus inactivation by a novel solvent/detergent combination, i.e. TnBP (tri-n-butyl phosphate) and polysorbate 20 during the manufacture of the factor VIII/VWF concentrate Optivate^® has been investigated. The inactivation of most enveloped viruses was rapid, i.e. >5 log in 2 min, although the inactivation of vaccinia virus was slower, i.e. 4 log in 1 h. Virus inactivation was effective over a wide range of conditions, i.e. solvent/detergent concentration, protein concentration and temperature, irrespective of whether tested individually or in combination. This confirms the effectiveness and robustness of this alternative version of the solvent/detergent procedure, and allows appropriate control limits to be set for this manufacturing step. Polysorbate 20 provides an alternative to the non-ionic detergents currently in use with the solvent/detergent procedure.     

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.     

Arginine-enveloped virus inactivation and potential mechanisms

Arginine synergistically inactivates enveloped viruses at a pH or temperature that does little harm to proteins, making it a desired process for therapeutic protein manufacturing. However, the mechanisms and optimal conditions for inactivation are not fully understood, and therefore, arginine viral inactivation is not used industrially. Optimal solution conditions for arginine viral inactivation found in the literature are high arginine concentrations (0.7–1 M), a time of 60 min, and a synergistic factor of high temperature (≥40°C), low pH (≤pH 4), or Tris buffer (5 mM). However, at optimal conditions full inactivation does not occur over all enveloped viruses. Enveloped viruses that are resistant to arginine often have increased protein stability or membrane stabilizing matrix proteins. Since arginine can interact with both proteins and lipids, interaction with either entity may be key to understanding the inactivation mechanism. Here, we propose three hypotheses for the mechanisms of arginine induced inactivation. Hypothesis 1 describes arginine-induced viral inactivation through inhibition of vital protein function. Hypothesis 2 describes how arginine destabilizes the viral membrane. Hypothesis 3 describes arginine forming pores in the virus membrane, accompanied by further viral damage from the synergistic factor. Once the mechanisms of arginine viral inactivation are understood, further enhancement by the addition of functional groups, charges, or additives may allow the inactivation of all enveloped viruses in mild conditions.     

Structure of a membrane-binding domain from a non-enveloped animal virus: insights into the mechanism of membrane permeability and cellular entry

The gamma(1)-peptide is a 21-residue lipid-binding domain from the non-enveloped Flock House virus (FHV). Unlike enveloped viruses, the entry of non-enveloped viruses into cells is believed to occur without membrane fusion. In this study, we performed NMR experiments to establish the solution structure of a membrane-binding peptide from a small non-enveloped icosahedral virus. The three-dimensional structure of the FHV gamma(1)-domain was determined at pH 6.5 and 4.0 in a hydrophobic environment. The secondary and tertiary structures were evaluated in the context of the capacity of the peptide for permeabilizing membrane vesicles of different lipid composition, as measured by fluorescence assays. At both pH values, the peptide has a kinked structure, similar to the fusion domain from the enveloped viruses. The secondary structure was similar in three different hydrophobic environments as follows: water/trifluoroethanol, SDS, and membrane vesicles of different compositions. The ability of the peptide to induce vesicle leakage was highly dependent on the membrane composition. Although the gamma-peptide shares some structural properties to fusion domains of enveloped viruses, it did not induce membrane fusion. Our results suggest that small protein components such as the gamma-peptide in nodaviruses (such as FHV) and VP4 in picornaviruses have a crucial role in conducting nucleic acids through cellular membranes and that their structures resemble the fusion domains of membrane proteins from enveloped viruses.