Danielle Jacob

293SF metabolic flux analysis during cell growth and infection with an adenoviral vector.

Metabolic flux quantification of cell culture is becoming a crucial means to improve cell growth as well as protein and vector productions. The technique allows rapid determination of cell culture status, thus providing a tool for further feeding improvements. Herein, we report on key results of a metabolic investigation using 293 cells adapted to suspension and serum‐free medium (293SF) during growth and infection with an adenoviral vector encoding the green fluorescence protein (GFP). The model developed contains 35 fluxes, which include the main fluxes of glycolysis, glutaminolysis, and amino acids pathways. It requires specific consumption and production rate measurements of amino acids, glucose, lactate, NH3, and O2, as well as DNA and total proteins biosynthesis rate measurements. Also, it was found that extracellular protein concentration measurement is important for flux calculation accuracy. With this model, we are able to describe the 293SF cell metabolism, grown under different culture conditions in a 3‐L controlled bioreactor for batch and fed‐batch with low glucose. The metabolism is also investigated during infection under two different feeding strategies: a fed‐batch starting at the end of the growth phase and extending during infection without medium change and a fed‐batch after infection following medium renewal. Differences in metabolism are observed between growth and infection, as well as between the different feeding strategies, thus providing a better understanding of the general metabolism.

Scalable production of influenza virus in HEK-293 cells for efficient vaccine manufacturing

Cell culture processes offer an attractive alternative to conventional chicken egg-based influenza vaccine production methods. However, most protocols still rely on the use of adherent cells, which makes process scale-up a challenging issue. In this study, it is demonstrated that the HEK-293 human cell line is able to efficiently replicate influenza virus. Production in serum-free suspension of HEK-293 cultures resulted in high titers of infectious influenza viruses for different subtypes and variants including A/H1, A/H3 and B strains. After virus adaptation and optimization of infection conditions, production in 3-L bioreactor resulted in titers of up to 10(9)IVP/mL demonstrating the scale-up potential of the process.

Production of Recombinant Adeno-Associated Viral Vectors Using a Baculovirus/Insect Cell Suspension Culture System: From Shake Flasks to a 20-L Bioreactor

Production of recombinant adeno‐associated viral vectors using a baculovirus/insect cell system at various scales is presented. Shake flask studies were conducted to assess conditions to be used in bioreactors. Two insect cell lines, Trichoplusia ni (H5) and Spodoptera frugiperda (Sf9), were compared for their ability to produce rAAV‐2 after infection with recombinant baculoviruses coding for the essential components of the vector. The effect of varying the ratio between individual baculoviruses and the effect of the overall multiplicity of infection (MOI), as well as the cell density at infection, were also examined. Infectious rAAV‐2 particles were proportionally produced when increasing the individual MOI of BacRep virus up to 1.6. When equal amounts of each virus were used, a leveling effect occurred beyond an overall MOI of 5 and a maximum titer was obtained. Increasing the cell density at infection resulted in higher yields when infecting the cells in fresh medium; however, for the production of bioactive particles, an optimal peak cell density of ∼1 × 106 cells/mL was observed without medium exchange. Infection in 3‐ and 20‐L bioreactors was done at an overall MOI of 5 with a ratio of the three baculoviruses equal to 1:1:1. Under these conditions and infecting the cells in fresh medium, a total of ∼2.2 × 1012 infectious viral particles (bioactive particles) or 2.6 × 1015 viral particles were produced in a 3‐L bioreactor. Without replacing the medium at infection, similar titers were produced in 20 L. Our data demonstrates the feasibility of rAAV‐2 production by BEVS at various scales in bioreactors and indicates that further optimization is required for production at high cell densities.

High-titer adenovirus vector production in 293S cell perfusion culture.

Human 293S cells culture for recombinant adenovirus production is traditionally carried out in batch at a maximum of 6 × 105 cells/mL. A previous report demonstrated that fed‐batch, applied to the adenovirus/293S cells system, improves the volumetric production of viral proteins by increasing the cell density at which cells can be infected, up to 2 × 106 cells/mL, without reducing the per‐cell yield of product. To increase this cell density limit, the adenovirus production was performed in a perfusion system where the cells were separated by means of a tangential flow filtration device. 293S cell growth to 14 × 106 cells/mL was achieved in 10 days, at a medium renewal rate of 1 volume of medium per reactor volume and day (VVD). For adenovirus production, three 293S cell cultures were perfused at 1 VVD in parallel and infected at an average density of 8 × 106 cells/mL. One of the cultures was set at 37 °C and the two others at 35 °C. After a rapid initial cell loss, the average cell density stabilized at 5.75 × 106 cells/mL, 12 h postinfection, which was 8 times higher than the cell density in the batch control. This allowed the production of 3.2 × 109 infectious viral particles/mL (IVP/mL) at 37 °C and 7.8 × 109 IVP/mL at 35 °C, this last result being 5.5 times higher than the control. To our knowledge, this nonconcentrated titer is the highest value that has ever been published for adenovirus vector production. These observations lead to the conclusion that perfusion is an efficient tool to maintain, at high cell density, a specific production rate level sufficient to increase significantly the adenovirus volumetric production. Furthermore, it shows that perfusion at 35 °C can improve viral titer by 2.4‐fold compared to 37 °C, in accordance with a previous study on adenovirus batch production.

Development of a simple and high-yielding fed-batch process for the production of influenza vaccines

A robust and reliable GMP-compatible fed-batch process was successfully developed for the production of recombinant hemagglutinin (rHA) proteins by expresSF cells. The feeding solution, feeding strategy as well as the cell density at infection were optimized to maximize the final rHA production yields without affecting the existing rHA recovery protocol and downstream process. A simple and stable feeding solution was formulated and a rational feeding regimen designed to yield, depending on the rHA baculovirus used, between 2- and 3-fold enhancements in volumetric rHA production with increased specific productivity compared to the batch culture. Recombinant HA from fed-batch cultures could be simply recovered following cell lysis and purified through chromatographic steps. Overall, the increased rHA yield was maintained throughout the whole process. The performance, reproducibility and scalability of the fed-batch process was successfully demonstrated in 12 bioreactor runs of 2- and 10-L working volume using five different rHA encoding baculoviruses.

Metabolic and Kinetic analyses of influenza production in perfusion HEK293 cell culture

BackgroundCell culture-based production of influenza vaccine remains an attractive alternative to egg-based production. Short response time and high production yields are the key success factors for the broader adoption of cell culture technology for industrial manufacturing of pandemic and seasonal influenza vaccines. Recently, HEK293SF cells have been successfully used to produce influenza viruses, achieving hemagglutinin (HA) and infectious viral particle (IVP) titers in the highest ranges reported to date. In the same study, it was suggested that beyond 4 × 106 cells/mL, viral production was limited by a lack of nutrients or an accumulation of toxic products.ResultsTo further improve viral titers at high cell densities, perfusion culture mode was evaluated. Productivities of both perfusion and batch culture modes were compared at an infection cell density of 6 × 106 cells/mL. The metabolism, including glycolysis, glutaminolysis and amino acids utilization as well as physiological indicators such as viability and apoptosis were extensively documented for the two modes of culture before and after viral infection to identify potential metabolic limitations. A 3 L bioreactor with a perfusion rate of 0.5 vol/day allowed us to reach maximal titers of 3.3 × 1011 IVP/mL and 4.0 logHA units/mL, corresponding to a total production of 1.0 × 1015 IVP and 7.8 logHA units after 3 days post-infection. Overall, perfusion mode titers were higher by almost one order of magnitude over the batch culture mode of production. This improvement was associated with an activation of the cell metabolism as seen by a 1.5-fold and 4-fold higher consumption rates of glucose and glutamine respectively. A shift in the viral production kinetics was also observed leading to an accumulation of more viable cells with a higher specific production and causing an increase in the total volumetric production of infectious influenza particles.ConclusionsThese results confirm that the HEK293SF cell is an excellent substrate for high yield production of influenza virus. Furthermore, there is great potential in further improving the production yields through better control of the cell culture environment and viral production kinetics. Once accomplished, this cell line can be promoted as an industrial platform for cost-effective manufacturing of the influenza seasonal vaccine as well as for periods of peak demand during pandemics.

Process optimization and scale-up for production of rabies vaccine live adenovirus vector (AdRG1.3).

Rabies virus is an important causative agent of disease resulting in an acute infection of the nervous system and death. Although curable if treated in a timely manner, rabies remains a serious public health issue in developing countries, and the indigenous threat of rabies continues in developed countries because of wildlife reservoirs. Control of rabies in wildlife is still an important challenge for governmental authorities. There are a number of rabies vaccines commercially available for control of wildlife rabies infection. However, the vaccines currently distributed to wildlife do not effectively immunize all at-risk species, particularly skunks. A replication competent recombinant adenovirus expressing rabies glycoprotein (AdRG1.3) has shown the most promising results in laboratory trials. The adenovirus vectored vaccine is manufactured using HEK 293 cells. This study describes the successful scale-up of AdRG1.3 adenovirus production from 1 to 500 L and the manufacturing of large quantities of bulk material required for field trials to demonstrate efficacy of this new candidate vaccine. The production process was streamlined by eliminating a medium replacement step prior to infection and the culture titer was increased by over 2 fold through optimization of cell culture medium. These improvements produced a more robust and cost-effective process that facilitates industrialization and commercialization. Over 17,000 L of AdRG1.3 adenovirus cultures were manufactured to support extensive field trials. AdRG1.3 adenovirus is formulated and packaged into baits by Artemis Technologies Inc. using proprietary technology. Field trials of AdRG1.3 rabies vaccine baits have been conducted in several Canadian provinces including Ontario, Quebec and New Brunswick. The results from field trials over the period 2006-2009 demonstrated superiority of the new vaccine over other licensed vaccines in immunizing wild animals that were previously difficult to vaccinate.

An efficient and scalable process for helper-dependent adenoviral vector production using polyethylenimine-adenofection

Safety requirements for adenoviral gene therapy protocols have led to the development of the third generation of vectors commonly called helper‐dependent adenoviral vectors (HDVs). HDVs have demonstrated a high therapeutic potential; however, the poor efficiency and reliability of the actual production process hampers further large‐scale clinical evaluation of this new vector. The current HDV production methods involve a preliminary rescue step through transfection of adherent cell cultures by an HDV plasmid followed by a helper adenovirus (HV) infection. Amplification by serial co‐infection of complementary cells allows an increase in the HDV titer. Using a HEK293 FLP/frt cell system in suspension culture, an alternative protocol to the current transfection/infection procedure was evaluated. In this work, the adenofection uses the HDV plasmid linked to the HV with the help of polyethylenimine (PEI) and has shown to outperform standard protocols by producing higher HDV yield. The influence of complex composition on the HDV production was examined by a statistical design. The optimized adenofection and amplification conditions were successively performed to generate HDV at the 3 L bioreactor scale. Following only two serial co‐infection passages, up to 1.44 × 108 HDV infectious units/mL of culture were generated, which corresponded to 26% of the total particles produced. This production strategy, realized in cell suspension culture, reduced process duration and therefore the probability of vector recombination by introducing a cost‐effective transfection protocol, ensuring production of high‐quality vector stock. Biotechnol. Bioeng. 2009; 102: 800–810.

Virus-like Particle and Viral Vector Production Using the Baculovirus Expression Vector System/Insect Cell System

The ability to make a large variety of virus-like particles (VLPs) has been successfully achieved in the baculovirus expression vector system (BEVS)/insect cell system. The production and scale-up of these particles, which are mostly sought as candidate vaccines, are currently being addressed. Furthermore, these VLPs are being investigated as delivery agents for use as therapeutics. Recently, adeno-associated viral (AAV) vectors, which can be potentially used for human gene therapy, have been produced in insect cells using three baculovirus vectors to supply the required genes. The use of host insect cells allows mass production of VLPs in a proven scaleable system. This chapter focuses on the methodology, based on the work done in our lab, for the production of AAV-like particles and vectors in a BEVS/insect cell system.

Optimization and scale-up of cell culture and purification processes for production of an adenovirus-vectored tuberculosis vaccine candidate.

Tuberculosis (TB) is the second leading cause of death by infectious disease worldwide. The only available TB vaccine is the Bacille Calmette-Guerin (BCG). However, parenterally administered Mycobacterium bovis BCG vaccine confers only limited immune protection from pulmonary tuberculosis in humans. There is a need for developing effective boosting vaccination strategies. AdAg85A, an adenoviral vector expressing the mycobacterial protein Ag85A, is a new tuberculosis vaccine candidate, and has shown promising results in pre-clinical studies and phase I trial. This adenovirus vectored vaccine is produced using HEK 293 cell culture. Here we report on the optimization of cell culture conditions, scale-up of production and purification of the AdAg85A at different scales. Four commercial serum-free media were evaluated under various conditions for supporting the growth of HEK293 cell and production of AdAg85A. A culturing strategy was employed to take advantages of two culture media with respective strengths in supporting the cell growth and virus production, which enabled to maintain virus productivity at higher cell densities and resulted in more than two folds of increases in culture titer. The production of AdAg85A was successfully scaled up and validated at 60L bioreactor under the optimal conditions. The AdAg85A generated from the 3L and 60L bioreactor runs was purified through several purification steps. More than 98% of total cellular proteins was removed, over 60% of viral particles was recovered after the purification process, and purity of AdAg85A was similar to that of the ATCC VR-1516 Ad5 standard. Vaccination of mice with the purified AdAg85A demonstrated a very good level of Ag85A-specific antibody responses. The optimized production and purification conditions were transferred to a GMP facility for manufacturing of AdAg85A for generation of clinical grade material to support clinical trials.