Characterization of changes in PER.C6 cellular metabolism during growth and propagation of a replication-deficient adenovirus vector

PER.C6 cells were cultivated for propagation of a replication-defective adenovirus vector in serum-free suspension bioreactors. Cellular metabolism during cell growth and adenovirus propagation was fully characterized using on-line and off-line methods. The energy metabolism was found to accelerate transiently after adenovirus infection with increases in glucose and oxygen consumption rates. Similar to other mammalian cells, glucose utilization was highly inefficient and a high lactate:glucose yield was observed, both before and after virus infection. A higher consumption of most of the essential amino acids was observed transiently after the infection, likely due to increased protein synthesis requirements for virus propagation. To improve virus propagation, a medium exchange strategy was implemented to increase PER.C6 cell concentration for infection. During cell growth, a 50% increase in glucose consumption and lactate production rates was observed after initiation of the medium exchange in comparison to the batch phase. This decrease in medium capacity only affected the central carbon metabolism and no increase in amino acid consumption was observed. In addition, even though cell concentrations of up to 10 x 10(6) cells/mL were reproducibly obtained by medium exchange, infections at cell concentrations higher than 1 x 10(6) cells/mL did not proportionally improve volumetric adenovirus productivities. No measured nutrient limitation was observed at those high cell concentrations, indicating that adenovirus cell-specific productivity at higher cell concentrations is highly dependent on cell physiology. These results provide a better understanding of PER.C6 cellular metabolism and a basis for intensifying PER.C6 growth and adenovirus propagation.     

Improvement of recombinant protein production with the human adenovirus/293S expression system using fed-batch strategies

The human adenovirus/293S cell expression system is used for the production of either recombinant protein or adenovirus vectors for use in gene therapy. In this work, the production of protein tyrosine phosphatase (PTP1C) was used as a model for the scale-up of both applications. Maximum specific production of 30 to 45 mug of active protein/10(6) cells was maintained upon infection with adenovirus vectors at cell densities between 2 x 10(6) to 3 x 10(6) cells/mL in a 3.5-L bioreactor. This was achieved by resuspending the culture in fresh medium at infection time. The pH was kept at 7.0 throughout the experiment and, at 24 h postinfection, glucose and essential amino acids were added. Attempts to replace the complete change of medium at the time of infection with nutrient supplementation of the used medium led to lower production levels, suggesting that protein expression was limited not by the absence of a key nutrient but by inhibitory factors. Two potentially inhibitory factors were investigated: lactic acid accumulation and increased osmolarity. Medium acidification such as that which would be brought about by lactic acid accumulation was shown to depress PTP1C production. The lactate molecule itself decreased the cell viability when added in concentrations of 20 mM or more. But the specific productivity was affected at higher lactate concentrations of 40 mM or more. Additions of glucose, amino acids, and NaHCO(3) used to control pH, led to increases in osmolarity. Osmolarities above 400 mOsm lowered cell density. However, specific production was not significantly affected below 500 mOsm. But, at 500 mOsm, PTP1C production peak was shifted from 48 to 72 hpi. Because of the cell loss, this per cell yield increase did not translate into higher volumetric production. When glucose concentrations was kept at 5 mM by fed-batch addition, lactate production and increases in osmolarity were reduced. In shake flasks, this method permitted maximum production with cells resuspended either in fresh or spent medium at infection. This fed-batch process was implemented successfully at the 3.5-L scale. Fed-batch with glucose may provide a means to increase infected-cell density beyond 3 x 10(6) cells/mL.     

Insights into adenoviral vector production kinetics in acoustic filter-based perfusion cultures

One of the major limitations in the production of adenoviral vectors is the reduction in cell-specific productivity observed for increasing cell density at infection in batch cultures. This observation strongly suggests some nutrient depletion and/or metabolite inhibition in the media. These limitations have been partially overcome through other feeding strategies, such as fed-batch and sequential batch operations. To improve these results, we evaluated perfusion as a strategy to increase the volumetric productivity of HEK-293 cell cultures, by allowing productive infection at higher cell densities. An acoustic cell separator was employed in consideration of the increased shear sensitivity of the cells during the infection phase. The effects of perfusion rate and cell density at infection on the production of a recombinant adenovirus expressing the GFP were investigated. The perfusion mode allowed successful infection at cell densities in the range of 2.4-3 x 10(6) cell/mL, while maintaining a similar cell specific productivity (17,900 +/- 2400 VP/cell) to that of a batch infected at a low cell density (5 x 10(5) cell/mL). The highest virus concentrations (4.1 +/- 0.6 x 10(10) VP/mL) were attained for a feed rate of 2 vol/d and constituted a fivefold increase compared to a batch with medium replacement. Rapid assessment of the infection status was achieved through the use of on-line monitoring of respiration, fluorescence, and biovolume. Analysis of the kinetics of nutrient consumption and metabolite production revealed that a reduction in specific productivity is correlated with reduced metabolic activity.     

Metabolic flux analysis of HEK-293 cells in perfusion cultures for the production of adenoviral vectors

To meet increasing needs of adenovirus vectors for gene therapy programs, development of efficient and reproducible production processes is required. Perfusion cultures were employed to allow infection at greater cell concentrations. In an effort to define culture conditions resulting in enhanced productivities, experiments performed at different feed rates and infected at various cell densities were compared using metabolic flux analysis. The highest specific product yields were achieved in experiments performed at high perfusion rates and/or low cell concentrations. The intracellular flux analysis revealed that these experiments exhibited greater glycolytic fluxes, slightly higher TCA fluxes, and greater ATP production rates at the time of infection. In contrast, cultures infected at high cell density and/or low medium renewal rates were characterized by a more efficient utilization of glucose at the time of infection, but the specific product yields achieved were lower. The intracellular flux analysis provided a rational basis for the implementation of a feeding strategy that allowed successful infection at a density of 5x10(6)cells/ml.     

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 x 10(5) 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 x 10(6) 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 x 10(6) 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 x 10(6) cells/mL. One of the cultures was set at 37 degrees C and the two others at 35 degrees C. After a rapid initial cell loss, the average cell density stabilized at 5.75 x 10(6) 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 x 10(9) infectious viral particles/mL (IVP/mL) at 37 degrees C and 7.8 x 10(9) IVP/mL at 35 degrees 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 degrees C can improve viral titer by 2.4-fold compared to 37 degrees C, in accordance with a previous study on adenovirus batch production.     

The improvement of adenovirus vector production by increased expression of coxsackie adenovirus receptor

Adenoviruses are promising vectors for gene therapy. The production of adenoviral vectors (AdV), however, is limited by the cell density effect, namely when cell infection is performed at above 10⁶ cells/ml, a drop in cell-specific adenovirus productivity occurs. Our results also show that the coxsackie adenovirus receptor (CAR) plays an important role in AdV production. CAR expression of infected cells varied with culture time and the cell-specific AdV productivity dropped rapidly along with decreased CAR expression. Furthermore, CAR expression of cells was maintained at a high level by replacing the medium or supplementing it with trichostatin A, which could improve the cell-specific productivity. Thus, a higher CAR expression level at infection time could improve cell-specific AdV productivity at high cell densities.     

Reassessing culture media and critical metabolites that affect adenovirus production

Adenovirus production is currently operated at low cell density because infection at high cell densities still results in reduced cell‐specific productivity. To better understand nutrient limitation and inhibitory metabolites causing the reduction of specific yields at high cell densities, adenovirus production in HEK 293 cultures using NSFM 13 and CD 293 media were evaluated. For cultures using NSFM 13 medium, the cell‐specific productivity decreased from 3,400 to 150 vp/cell (or 96% reduction) when the cell density at infection was increased from 1 to 3 × 10⁶ cells/mL. In comparison, only 50% of reduction in the cell‐specific productivity was observed under the same conditions for cultures using CD 293 medium. The effect of medium osmolality was found critical on viral production. Media were adjusted to an optimal osmolality of 290 mOsm/kg to facilitate comparison. Amino acids were not critical limiting factors. Potential limiting nutrients including vitamins, energy metabolites, bases and nucleotides, or inhibitory metabolites (lactate and ammonia) were supplemented to infected cultures to further investigate their effect on the adenovirus production. Accumulation of lactate and ammonia in a culture infected at 3 × 10⁶ cells/mL contributed to about 20% reduction of the adenovirus production yield, whereas nutrient limitation appeared primarily responsible for the decline in the viral production when NSFM 13 medium was used. Overall, the results indicate that multiple factors contribute to limiting the specific production yield at cell densities beyond 1 × 10⁶ cells/mL and underline the need to further investigate and develop media for better adenoviral vector productions. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Two Different Serum-free Media and Osmolality Effect Upon Human 293 Cell Growth and Adenovirus Production

Adenoviruses are promising vectors for gene therapy and vaccination protocols. Consequently, the market demands for adenovirus are increasing, driving the search for new methodologies for large-scale production of concentrated vectors with warranted purity and efficacy, in a cost-effective way. Nevertheless, the production of adenovirus is currently limited by the so-called ‘cell density effect’, i.e. a drop in cell specific productivity concomitant with increased cell concentration at infection. Of two different serum-free culture media (CD293 and EX-Cell), evaluated for their effect on human 293 cells growth and adenovirus production at cell densities higher than 1×10⁶ cells/ml, EX-Cell proved the better medium for cell growth. Although adenovirus production was equivalent in both media when the infection was performed at 1×10⁶ cells/ml, at 3×10⁶ cells/ml CD293 was the better. This result related to the high ammonia content in EX-Cell medium at the highest cell concentration at infection. Besides this, the large-scale production of these vectors at high cell densities often requires re-feed strategies, which increase medium osmolality. While a negative effect on cell growth was observed with increasing osmolalities, adenovirus productivity was only affected for osmolalities higher than 430 mOsm. Revisions requested 24 August 2005; Revisions received 9 September 2005     

Establishment of higher passage PER.C6 cells for adenovirus manufacture

PER.C6 cells, an industrially relevant cell line for adenovirus manufacture, were extensively passaged in serum-free suspension cell culture to better adapt them to process conditions. The changes in cell physiology that occurred during this passaging were characterized by investigating cell growth, cell size, metabolism, and cultivation of replication-deficient adenovirus. The changes in cell physiology occurred gradually as the population doubling level, the number of times the cell population had doubled, increased. Higher passage PER.C6 (HP PER.C6) proliferated at a specific growth rate of 0.043 h(-1), 2-fold faster than lower passage PER.C6, and were capable of proliferation from lower inoculation cell densities. HP PER.C6 cell volume was 16% greater, and cellular yields on glucose, lactate, oxygen, and amino acids were greater as well. In batch cultures, HP PER.C6 cells volumetrically produced 3-fold more adenovirus, confirmed with three different constructs. The increase in productivity was also seen on a cell-specific basis. Although HP PER.C6 were more sensitive to the "cell density effect", requiring lower infection cell densities for optimal specific productivity, they proliferated more after infection than lower passage PER.C6, increasing the number of cells available for virus production. The extensive passaging established HP PER.C6 cells with several desirable attributes for adenovirus manufacture.     

Perfusion culture of baculovirus-infected BTI-Tn-5B1-4 insect cells: a method to restore cell-specific beta-trace glycoprotein productivity at high cell density

The impact of different cultivation-infection strategies on the productivity of baculovirus-infected BTI-Tn-5B1-4 (High Five) cells was investigated. Using beta-trace protein as the recombinant glycoprotein, the effects of multiplicity of infection (MOI) and time of infection (TOI) were studied on growth after infection as well as the degree of infection and recombinant protein productivity in batch culture. The highest productivities were found when infecting Tn5 cells at early exponential growth phase (EGP) (low cell density) using a high MOI. To increase the productive cell density of Tn5 cells after beta-trace-baculovirus infection, we performed studies infecting cells in the range of 1 to 5 x 10(6) cells/mL in fresh medium. Although the protein production was increased twofold, a strong negative cell density effect was still observed when maximal productive cell density exceeded 1 x 10(6) cells/mL. To verify whether the changing cell environment of the batch experiments was responsible for the decrease in protein productivity at increasing cell density at infection, several perfusion experiments were designed by infecting Tn5 cells at cell densities over 2 x 10(6) cells/mL under more steady-state conditions. The use of this experimental setup enabled successful infections at high cell densities with volumetric productivities of up to 1.2 g L(-1) day(-1) of beta-trace protein, which is very high for a glycoprotein expressed with the baculovirus expression vector system (BEVS). The cell specific protein productivity observed after infections at higher cell densities in perfusion mode was the same as in batch experiments at low cell concentrations, which clearly demonstrates that the cell density effect could be completely overcome with perfusion cultivation.     

Serum-free suspension cultivation of PER.C6(R) cells and recombinant adenovirus production under different pH conditions

PER.C6(R) cell growth, metabolism, and adenovirus production were studied in head-to-head comparisons in stirred bioreactors under different pH conditions. Cell growth rate was found to be similar in the pH range of 7.1-7.6, while a long lag phase and a slower growth rate were observed at pH 6.8. The specific consumption rates of glucose and glutamine decreased rapidly over time during batch cell growth, as did the specific lactate and ammonium production rates. Cell metabolism in both infected and uninfected cultures was very sensitive to culture pH, resulting in dramatic differences in glucose/glutamine consumption and lactate/ammonium production under different pH conditions. It appeared that glucose metabolism was suppressed at low pH but the efficiency of energy production from glucose was enhanced. Adenovirus infection resulted in profound changes in cell growth and metabolism. Cell growth was largely arrested under all pH conditions, while glucose consumption and lactate production were elevated post virus infection. Virus infection induced a reduction in glutamine consumption at low pH but an increase at high pH. The optimal pH for adenovirus production was found to be 7.3 under the experimental conditions used in the study. Deviations from this optimum resulted in significant reductions of virus productivity. The results indicate that culture pH is a very critical process parameter in PER.C6(R) cell culture and adenovirus production.     

High concentration cultivation of Bifidobacterium bifidum in a submerged membrane bioreactor

In batch cultures, after 25 h, the maximum cell mass of Bifidobacterium bifidum BGN4 was 4.5 g/L, and the maximum cell count was 3.0 x 10(9) cfu/mL at pH 6.0 and 50 g/L sucrose. To increase the viable counts of bifidobacteria, cell retentive culture was applied using a submerged membrane bioreactor with suction and gas sparging. The maximum mass, count, and productivity of the cells after 36 h were 12.0 g/L, 2.2 x 10(10) cfu/mL, and 6.1 x 10(8) cfu/mL x h, respectively, at the feeding (dilution) rate of 120 mL/h (0.06 h-1) in the feeding medium. The accumulated levels of organic acids and ammonium ions at the end of the cultivation were 1.5 and 1.0 g/L, respectively. The viable counts and volumetric productivity of the cells after the cell retentive culture were 7.3- and 5.1-fold higher, respectively, than the values obtained during batch culture. These high viable counts and volumetric productivities were obtained by maintaining lower concentrations of organic acids and ammonium ions so that the growth of B. bifidum BGN4 was not inhibited. The submerged membrane bioreactor produced the highest viable counts of B. bifidum without membrane fouling and cell damage.     

A novel process for the production of a veterinary rabies vaccine in BHK-21 cells grown on microcarriers in a 20-l bioreactor

We studied BHK-21 cells growth in a 2-l bioreactor and investigated the effects of microcarrier concentration, type of growth medium, culture mode and serum concentration. The highest cell density reached was equal to 4x10(6) cells/ml and was achieved in minimum essential medium supplemented with Hanks' salts, non-essential amino acids and 5% fetal calf serum, using a perfusion culture mode and a microcarrier concentration of 4 g Cytodex 3/l. We studied rabies virus production (PV/BHK-21 strain) by BHK-21 cells grown at the optimal conditions determined previously. We analyzed the effects of multiplicity of infection (MOI) and type of medium used for virus multiplication in spinner-flasks and showed that the highest virus titer reached (when the cells were infected at a MOI of 0.3) in M199 medium supplemented with 0.2% of bovine serum albumin was equal to 8.2x10(7) Fluorescent Focus Units (FFU)/ml. When we grew the cells in a 2-l perfused bioreactor, we obtained a maximal virus titer of 3x10(8) FFU/ml. In addition, we scaled-up to a 20-l bioreactor and obtained similar results for cell density and virus titer. The experimental vaccine we developed meets WHO requirements for vaccine potency. Each run yielded about 40,000 doses of potent vaccine.     

Effect of ammonia production on intracellular pH: Consequent effect on adenovirus vector production

Recombinant adenoviral vectors (AdV) have proven to be highly efficient for the delivery and expression of foreign genes in a broad spectrum of cell types and species both for vaccination and gene therapy in a number of specific applications. In this study, the effect of ammonia production on intracellular pH (pH(i)) and consequently inhibition of AdV production at high cell densities is assessed. Different specific ammonia production rates were obtained for 293 cells adapted to grow in glutamate supplemented medium (non-ammoniagenic medium) as compared with 293 cells growing in glutamine supplemented medium (ammoniagenic medium); pH(i) was observed to be lower during cell growth and AdV production at both high and low CCI in the ammoniagenic medium, where the specific ammonia production rate is higher. In addition, after infection at CCI of 3x10(6)cell/ml, the cell viability decreased significantly in the ammoniagenic medium, attributed to the activation of an acidic pathway of apoptosis. Furthermore, AdV DNA was observed to be degraded at the observed pH(i) in the ammoniagenic medium, decreasing significantly the amount of AdV DNA available for encapsulation. To elucidate the pH(i) effect upon AdV production, 293 cells were infected at a CCI of 1 x 10(6)cell/ml in the non-ammoniagenic medium with a manipulated pH(i) as observed at the time of infection at CCI of 3 x 10(6)cell/ml in the ammoniagenic (pH(i) 7.0) and non-ammoniagenic (pH(i) 7.3) media; AdV volumetric productivities were observed to be lower when the cells were exposed to the lower pH(i). Thus, the importance of controlling all the factors contributing to pH(i) on AdV production, such as ammonia production, has been established.     

Biochemical Consequences of Type 2 Adenovirus and Simian Virus 40 Double Infections of African Green Monkey Kidney Cells

African green monkey kidney (AGMK) cells were nonpermissive hosts for type 2 adenovirus although the restriction was not complete; when only 3 plaque-forming units/cell was employed as the inoculum, the viral yield was about 0.1% of the maximum virus produced when simian virus 40 (SV40) enhanced adenovirus multiplication. The viral yield of cells infected only with type 2 adenovirus increased as the multiplicity of infection was increased. Type 2 adenovirus could infect almost all AGMK cells in culture; adenovirus-specific early proteins and DNA were synthesized in most cells, but small amounts of late proteins were made in relatively few cells. Even when cells were infected with both SV40 and adenovirus, only about 50% were permissive for synthesis of adenovirus capsid proteins. Approximately the same quantity of adenovirus deoxyribonucleic acid (DNA) was synthesized in the restricted as in the SV40-enhanced infection. However, in cells infected with SV40 and type 2 adenovirus, replication of SV40 DNA was blocked, multiplication of SV40 was accordingly inhibited, and synthesis of host DNA was not stimulated. To enhance propagation of type 2 adenovirus, synthesis of an early SV40 protein was essential; 50 mug of cycloheximide per ml prevented the SV40-induced enhancement of adenovirus multiplication, whereas 5 x 10(-6)m 5-fluoro-2-deoxyuridine did not abrogate the enhancing phenomenon.     

Bifidobacterium longum ATCC 15707 cell production during free- and immobilized-cell cultures in MRS-whey permeate medium

Bifidobacterium longum ATCC 15707 cell production was studied in MRS medium supplemented with whey permeate (MRS-WP) during free-cell batch fermentations and continuous immobilized-cell cultures. Very high populations were measured after 12 h batch cultures in MRS-WP medium controlled at pH 5.5 (1.7+/-0.5x10(10) cfu/ml), approximately 2-fold higher than in non-supplemented MRS. Our study showed that WP is a low-cost source of lactose and other components that can be used to increase bifidobacteria cell production in MRS medium. Continuous fermentation in MRS-WP of B. longum immobilized in gellan gum gel beads produced the highest cell concentrations in the effluent (4.9+/-0.9x10(9) cfu/ml) at a dilution rate (D) of 0.5 h(-1). However, maximal volumetric productivity (6.9+/-0.4x10(9) cfu ml(-1)h(-1)) during continuous cultures was obtained at D =2.0 h(-1), and was approximately 9.5-fold higher than during free-cell batch cultures at an optimal pH of 5.5 (7.2x10(8) cfu ml(-1)h(-1)).     

Scale-up of the adenovirus expression system for the production of recombinant protein in human 293S cells

Human 293S cells, a cell line adapted to suspension culture, were grown to 5×10⁶ cells/mL in batch with calcium-free DMEM. These cells, infected with new constructions of adenovirus vectors, yielded as much as 10 to 20% recombinant protein with respect to the total cellular protein content. Until recently, high specific productivity of recombinant protein was limited to low cell density infected cultures of no more than 5×10⁵ cells/mL. In this paper, we show with a model protein, Protein Tyrosine Phosphatase 1C how high product yield can be maintained at high cell densities of 2×10⁶ cells/mL by a medium replacement strategy. This allows the production of as much as 90 mg/L of active recombinant protein per culture volume. Analysis of key limiting/inhibiting medium components showed that glucose addition along with pH control can yield the same productivity as a medium replacement strategy at high cell density in calcium-free DMEM. Finally, the above results were reproduced in 3L bioreactor suspension culture thereby establishing the scalability of this expression system. The process we developed is used routinely with the same success for the production of various recombinant proteins and viruses.Abbreviations CFDMEM calcium-free DMEM - CS bovine calf serum - hpi hours post-infection - J+ enriched Joklik medium - MLP major late promoter - MOI multiplicity of infection (# of infectious viral particle/cell) - q specific consumption rate (mole/cell.h) - pfu plaque forming unit (# of infectious viral particle) - Y yield (g/E6 cells or mole/cell)     

Relationship between oxygen uptake rate and time of infection of Sf9 insect cells infected with a recombinant baculovirus

Oxygen uptake rates (OUR) of Sf9 insect cells propagated in a serum-free medium (SF900II, Gibco) and of cells infected with a recombinant AcNPV were investigated before and after infection in a laboratory-scale bioreactor. The volumetric OURs of uninfected and exponentially growing cells were found to be proportional to the cell density. For infected cultures, the specific OUR of cells increased immediately after addition of virus and a maximum of 1.3 times the value of uninfected cells was noted for all the cultures between 8 to 30 hours post infection, which coincides with the period at which most viral replication and the majority of DNA synthesis takes place. It was observed that the rate of rise in the specific OUR decreased as the cell density at the time of infection increased, which meant that the later the infection, the later the maximum sOUR was observed. We therefore suggest that OUR measurement can be used to reflect the efficiency of a batch infection. Carbohydrate and amino acid consumption rates from an infected run were analysed in an effort to identify substrate(s) that may be used at increased rates to fuel the rise in oxygen demand observed early in the infection cycle. No observable rise in the consumption rates of glucose or glutamine, which are the major energy sources for animal cells, were seen after infection but an increase in the consumption rates of some amino acids suggests that infected Sf9 cells may utilise amino acids at an enhanced rate for energy post infection.     

Evaluation of the serum-free medium MDSS2 for the production of poliovirus on vero cells in bioreactors

The serum-free medium MDSS2 (Merten et al., 1994), was used for cultivating Vero cells as well as for producing poliovirus (Sabin type 1) in static and in perfused micro-carrier cultures. At slightly different growth rates of 0.0120/h and 0.0106/h, respectively, static cultures in serum-containing (SCM) and serum-free (SFM) medium produced titers of ^106.75 and 10^6.67 TCID50 per 50 μl; signifying a specific productivity of 0.89 and 1.07 TCID50/c. Serum-free bioreactor cultures of Vero cells on DEAE-dextran microcarriers at 6.25 g/l produced cell densities of about 1.5×10⁶c/ml. After infection with virus (multiplicity of infection (MOI) 0.1–0.3) titers of about 6.3×10⁸ TCID50/ml were obtained, signifying an average specific productivity of 7.1 TCID50/c.h. Although these values were 4 and 2 fold, respectively, higher than in classical resum-based production processes (Montagnon et al. Dev. biol. Stand. 1981, 47, 55), a reference culture, for which cell growth was done in SCM and only virus production was done in SFM, produced 2×10⁹ TCID/ml with an average specific virus production rate of 18.9 TCID50/c.h. The differences between the fully serum-free and our reference process were mainly due to physiological differences of cells grown in SCM and SFM and also due to strongly modified consumption kinetics after virus infection leading to limitations of one or several essential medium compounds, like glucose and amino acids. Avoiding these limitations by increasing the residual concentration of glucose, glutamine, histidine, and SH-amino acids, led to specific virus production rates (of about 17.9 TCID59/c.h.) comparable to those found in the reference virus production process. The optimisation of the production of the poliovirus (Sabin 1) will be described with respect to the modification of the medium composition. This revised version was published online in June 2006 with corrections to the Cover Date.     

Human 293 cell metabolism in low glutamine-supplied culture: interpretation of metabolic changes through metabolic flux analysis

Metabolic flux analysis is a useful tool to analyze cell metabolism. In this study, we report the use of a metabolic model with 34 fluxes to study the 293 cell, in order to improve its growth capacity in a DMEM/F12 medium. A batch, fed-batch with glutamine feeding, fed-batch with essential amino acids, and finally a fed-batch experiment with both essential and nonessential amino acids were compared. The fed-batch with glutamine led to a maximum cell density of 2.4x10(6) cells/ml compared to 1.8x10(6) cells/ml achieved in a batch mode. In this fed-batch with glutamine, it was also found that 2.5 mM ammonia was produced compared to the batch which had a final ammonia concentration of 1 mM. Ammonia was found to be growth inhibiting for this cell line at a concentration starting at 1 mM. During the fed-batch with glutamine, the flux analysis shows that a majority of amino acid fluxes and Kreb's cycle fluxes, except for glutamine flux, are decreased. This observation led to the conclusion that the main nutrient used is glutamine and that during the batch there is an overflow in the Kreb's cycle. Thus, a fed-batch with glutamine permits a better utilization of this nutrient. A fed-batch with essential amino acid without glutamine was also assayed in order to reduce ammonia production. The maximum cell density was increased further to 3x10(6) cells/ml and ammonia production was reduced below 1 mM. Flux analysis shows that the cells could adapt to a medium with low glutamine by increasing the amino acid fluxes toward the Kreb's cycle. Adding nonessential amino acids during this feeding strategy did not improve growth further and the nonessential amino acids accumulated in the medium.