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.     

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.     

Metabolism of PER.C6 cells cultivated under fed-batch conditions at low glucose and glutamine levels

This is the first study to examine PER.C6 cell glucose/energy and glutamine metabolism with fed-batch cultures at controlled low glutamine, low glucose, and simultaneous low glucose and low glutamine levels. PER.C6(TM) cell metabolism was investigated in serum-free suspension bioreactors at two-liter scale. Control of glucose and/or glutamine concentrations had a significant effect on cellular metabolism leading to an increased efficiency of nutrient utilization, altered byproduct synthesis, while having no effect on cell growth rate. Cultivating cells at a controlled glutamine concentration of 0.25 mM reduced q(Gln) and q(NH(4)(+)) by approximately 30%, q(Ala) 85%, and q(NEAA) 50%. The fed-batch control of glutamine also reduced the overall accumulation of ammonium ion by approximately 50% by minimizing the spontaneous chemical degradation of glutamine. No major impact upon glucose/energy metabolism was observed. Cultivating cells at a glucose concentration of 0.5 mM reduced q(Glc) about 50% and eliminated lactate accumulation. Cells exhibited a fully oxidative metabolism with Y(O(2)/Glc) of approximately 6 mol/mol. However, despite no increase in q(Gln), an increased ammonium ion accumulation and Y(NH(4)(+)/Gln) were also observed. Effective control of lactate and ammonium ion accumulation by PER.C6 cells was achieved using fed-batch with simultaneously controlled glucose and glutamine. A fully oxidative glucose metabolism and a complete elimination of lactate production were obtained. The q(Gln) value was again reduced and, despite an increased q(NH(4)(+)) compared with batch culture, ammonium ion levels were typically lower than corresponding ones in batch cultures, and the accumulation of non-essential amino acids (NEAA) was reduced about 50%. In conclusion, this study shows that PER.C6 cell metabolism can be confined to a state with improved efficiencies of nutrient utilization by cultivating cells in fed-batch at millimolar controlled levels of glucose and glutamine. In addition, PER.C6 cells fall into a minority category of mammalian cell lines for which glutamine plays a minor role in energy metabolism.     

Large-scale propagation of a replication-defective adenovirus vector in stirred-tank bioreactor PER.C6 cell culture under sparging conditions

Large-scale propagation of replication-defective adenovirus vectors has not been well studied to date. One of the challenges for efficient propagation at large scale is to overcome the sensitivity of virus infected cells to gas sparging required for oxygenation and CO(2) removal. In our initial experiments, it was observed that productivity of an adenovirus vector was significantly reduced under sparging conditions as compared to nonsparged, i.e., surface-aerated controls in serum-free cultures. Investigations led to the identification of a buffer containing surfactant (Polysorbate-80, PS-80) that was included in the virus seed stock formulation and introduced through virus infection into the culture at a very low concentration as the cause of the reduced virus productivity. This finding was not obvious and trivial, as neither uninfected sparged nor infected nonsparged PER.C6 trade mark cells in serum-free cultures were affected by the buffer at such a low PS-80 concentration of 0.00025% (v/v), which is a common component of serum-free cell culture media. These results strongly suggest that virus-infected cells behave very differently from uninfected cells under sparging conditions. To mitigate the deleterious effects of sparging, the virus seed stock was prepared in the absence of the buffer containing PS-80. At the same time, the concentration of Pluronic-F68 (PF-68) in the serum-free medium was increased to 1 g/L, at which cell growth and metabolism were unaffected, even though this measure alone did not result in virus productivity improvement. Only by implementing the two measures together was virus productivity loss completely eliminated under sparging conditions. After demonstration of the process robustness in 2-L bioreactors, this adenovirus propagation process was successfully scaled up to 250 L in a 300-L bioreactor under the worst-case sparging conditions projected for 10,000-L scale.     

Viral vectors for the treatment of alcoholism: Use of metabolic flux analysis for cell cultivation and vector production

The HEK293 cell line has been used for the production of adenovirus vectors to be used in the potential treatment of alcoholism using a gene therapy strategy. Culture optimization and scale-up has been achieved by first adapting the cells to serum-free media and secondly by growing them in suspension. Adenovirus production after infection was increased, resulting in higher specific glucose consumption and lactate accumulation rates compared to the growth phase. We applied media design tools and Metabolic Flux Analysis (MFA) to compare the metabolic states of cells during growth and adenovirus production and to optimize culture media according to the metabolic demand of the cells in terms of glucose and glutamine concentrations. This allowed obtaining a higher maximum cell concentration and increased adenovirus production by minimizing the production of metabolites that can have an inhibitory effect on cell growth. We have proposed a stoichiometric equation for adenovirus synthesis. MFA results allowed determination of how these changes in composition affected the way cells distribute their nutrient resources during cell growth and virus production. Virus purification was successfully achieved using chromatography and Aqueous Two-Phase Systems (ATPS).     

Effect of re-feed strategies and non-ammoniagenic medium on adenovirus production at high cell densities

Recombinant adenoviruses became one of the vectors of choice for delivery and expression of foreign proteins for gene therapy and vaccination purposes. 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 (CCI). This work describes the characterisation and optimisation of the infection process in order to improve recombinant adenovirus type 5 yields at high cell densities. For that purpose, 293 cells adapted to suspension were grown in 2l bioreactors and infected at different cell concentrations, using different re-feed strategies, while evaluating cell metabolism. The consumption of amino acids is enhanced during infection, although no amino acid limitation was detected for cells infected at concentrations in the range of 2 x 10(6)cell/ml, for which the highest volumetric productivity was obtained in batch mode. Conversely, infecting at cell concentrations in the range of 3 x10(6)cell/ml led to complete depletion of glucose, glutamine and threonine before the optimal harvesting time, a significant decrease in volumetric productivity being observed; the effect of amino acids and glucose addition at infection time on cell specific and volumetric productivity of adenovirus was assessed, no improvement on adenovirus production being achieved. The effect of ammonia, present in high concentrations at 3 x10(6)cell/ml, was evaluated and seem to be detrimental; an 1.8-fold increase on adenovirus volumetric productivity was obtained for infections performed at 3 x10(6)cell/ml when non-ammoniagenic medium was used.     

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.     

Comparison of manufacturing techniques for adenovirus production

We have compared three different production methods, which may be suitable for the large scale production of adenovirus vectors for human clinical trials. The procedures compared 293 cells adapted to suspension growth in serum-free medium in a stirred tank bioreactor, 293 cells on microcarriers in serum-containing medium in a stirred tank bioreactor, and 293 cells grown in standard tissue culture plasticware. With a given virus, yields varied between 2000 and 10,000 infectious units/cell. The stirred tank bioreactor routinely produced between 4000 and 7000 infectious units/cell when 293 cells were grown on microcarriers. The 293 cells adapted to suspension growth in serum-free medium in the same stirred tank bioreactor yielded between 2000 and 7000 infectious units/cell. Yields obtained from standard tissue culture plasticware were up to 10,000 infectious units/cell. Cell culture conditions were monitored for glucose consumption, lactate production, and ammonia accumulation. Glucose consumption and lactate accumulation correlated well with the cell growth parameters. Ammonia production does not appear to be significant. Based on virus yields, ease of operation and linear scalability, large-scale adenovirus production seems feasible using 293 cells (adapted to suspension/serum free medium or on microcarriers in serum containing medium) in a stirred tank bioreactor. This revised version was published online in July 2006 with corrections to the Cover Date.     

Energetic and Morphological Plasticity of C6 Glioma Cells Grown on 3-D Support; Effect of Transient Glutamine Deprivation

The energetic metabolism of rat C6 glioma cells has been investigated as a function of the proliferative and differentiation states under three-dimensional (3-D) growing conditions on microcarrier beads. First, the transient deprivation of glutamine from the culture medium induced a marked decrease in the growth rate and a differentiation of C6 cells through the oligodendrocytic phenotype. Second, the respiratory capacity of the C6 cells during short-term subcultures with or without glutamine continuously declined as a function of the cell density, in part due to the mitochondrial content decrease. During the transition from the early exponential to the plateau growth phase in glutamine-containing medium, the oxygen consumption rate per single cell decreased concomitantly with a decrease in the glucose consumption and lactate production rates. This phenomenon led to a sixfold decrease in the total ATP production flux, without significantly affecting the cellular ATP/ADP ratio, thus indicating that some ATP-consuming processes were simultaneously suppressed during C6 proliferation. In glutamine-free medium, the cellular ATP/ADP ratio transiently increased due to growth arrest and to a reduced ATP turnover. Moreover, the results indicated that glutamine is not an essential respiratory substrate for rat C6 glioma under short-term glutamine deprivation. Worth noting was the high contribution of the mitochondrial oxidative phosphorylation toward the total ATP synthesis (about 80%), regardless of the proliferation or the differentiation status of the C6 cells.     

Influence of different ammonium,lactate and glutamine concentrations on CCO cell growth

In this study the effects of ammonium and lactate on a culture of channel catfish ovary (CCO) cells were examined. We also made investigation on the influence of glutamine, since our previous research revealed that this amino acid stimulated CCO cell growth more than glucose in a concentration-dependent manner. The effect of ammonium in cell culture included the considerable decrease in cell growth rate with eventual growth arrest as well as the retardation of glucose consumption. At ammonium concentrations above 2.5 mM, the cells displayed specific morphological changes. The effect of lactate was different to that of ammonium since the cell growth rate was progressively decreasing with the increase of lactate concentration, whereas the glucose consumption rate remained almost unchanged. Besides that, it was found that lactate was steadily eliminated from the culture medium when its initial concentration was relatively high. The influence of glutamine on CCO cell propagation showed that nutrient requirements of this cell line were mainly dependent on glutamine rather than glucose. The increase in glutamine concentration led to the increase in cell growth rate and consequent ammonia accumulation while the glucose utilization and lactate production were reduced. Without glutamine in culture medium cell growth was arrested. However, the lack of glucose reversed the stimulating effect of glutamine by decreasing cell growth rate and affecting amino acid utilization.     

Transient responses of hybridoma cells to lactate and ammonia pulse and step changes in continuous culture

Ammonia and lactate are the major byproducts from mammalian cells grown in medium containing glutamine and glucose. Both can be toxic to cells, and may limit the productivity of commercial bioreactors. The transient and steady-state responses of hybridoma growth and metabolism to lactate and ammonia pulse and step changes in continuous suspension culture have been examined. No inhibition was observed at 40 mM lactate. Cell growth was inhibited by 5 mM ammonia, but the cells were able to adapt to ammonia concentrations as high as 8.2 mM. Ammonia production decreased and alanine production increased in response to higher ammonia concentrations. Increased ammonia concentrations also inhibited glutamine and oxygen consumption. The specific oxygen consumption rate decreased by an order of magnitude after an ammonia pulse to 18 mM. Under these conditions, over 90% of the estimated ATP production was due to glycolysis and a large fraction of glutamine was converted to lactate.     

Considerations on the lactate consumption by CHO cells in the presence of galactose

A CHO cell line producing t-PA was cultured using glutamate and glucose or galactose to decrease the formation of metabolic end-products and therefore improving the process. In batch cultures using glutamate (6 mM) with glucose at two different levels (5 and 20 mM) or with glucose and galactose (5 and 20 mM, respectively) a remarkable difference in cell culture parameters was evidenced. For 20 mM glucose, a usual cell pattern was observed with lactate built-up in the medium. For 5 mM glucose, cell growth was arrested due to glucose depletion and only a limited use of the excreted lactate could be observed, not supporting cell growth sufficiently. However, when glucose 5 mM and galactose 20 mM were used together, cells consumed the glucose first and, interestingly, in a second phase they continued growing on galactose with the simultaneous consumption of the endogenous lactate. Under these conditions, cell growth was even improved with respect to growth on 20 mM glucose, used as a control. This metabolic behavior is further investigated by using metabolic flux analysis, suggesting that the lactate produced is not used in the oxidative metabolism through the TCA cycle. Metabolic fate of the lactate consumed is discussed.     

High viable cell concentration fed-batch cultures of hybridoma cells through on-line nutrient feeding

A hybridoma cell line was cultivated in fed-batch cultures using a low-protein, serum-free medium. On-line oxygen uptake rate (OUR) measurement was used to adjust the nutrient feeding rate based on glucose consumption, which was estimated on-line using the stoichiometric relations between glucose and oxygen consumption. Through on-line control of the nutrient feeding rate, not only sufficients were supplied for cell growth and antibody production, but also the concentrations of glucose and other important nutrients such as amino acids were maintained at low levels during the cell growth phase. During the cultivation, cell metabolism changed from high lactate production and low oxygen consumption to low lactate production and high oxygen consumption. As a result the accumulation of lactate was reduced and the growth phase was extended. In comparison with the batch cultures, in which cells reached a concentration of approximately 2 x 10(6) cells/mL, a very high concentration of 1.36 x 10(7) cells/mL with a high cell viability (>90%) was achieved in the fed-batch culture. By considering the consumption of glucose and amino acids, as well as the production of cell mass, metabolites, and antibodies, a well-closed material balance was established. Our results demonstrate the value of coupling on-line OUR measurement and the stoichiometric realations for dynamic nutrient feeding in high cell concentration fed batch cultures. (c) 1995 John Wiley & Sons, Inc.     

Comparative metabolic analysis of lactate for CHO cells in glucose and galactose

t-PA producing CHO cells have been shown to undergo a metabolic shift when the culture medium is supplemented with a mixture of glucose and galactose. This metabolic change is characterized by the reincorporation of lactate and its use as an additional carbon source. The aim of this work is to understand lactate metabolism. To do so, Chinese hamster ovary cells were grown in batch cultures in four different conditions consisting in different combinations of glucose and galactose. In experiments supplemented with glucose, only lactate production was observed. Cultures with glucose and galactose consumed glucose first and produced lactate at the same time, after glucose depletion galactose consumption began and lactate uptake was observed. Comparison of the metabolic state of cells with and without the shift by metabolic flux analysis show that the metabolic fluxes distribution changes mostly in the reactions involving pyruvate metabolism. When not enough pyruvate is being produced for cells to support their energy requirements, lactate dehydrogenase complex changes the direction of the reaction yielding pyruvate to feed the TCA cycle. The slow change from high fluxes during glucose consumption to low fluxes in galactose consumption generates intracellular conditions that allow the influx of lactate. Lactate consumption is possible in cell cultures supplemented with glucose and galactose due to the low rates at which galactose is consumed. Evidence suggests that an excessive production and accumulation of pyruvate during glucose consumption leads to lactate production and accumulation inside the cell. Other internal conditions such as a decrease in internal pH, forces the flow of lactate outside the cell. After metabolic shift the intracellular pool of pyruvate, lactate and H⁺ drops permitting the reversal of the monocarboxylate transporter direction, therefore leading to lactate uptake. Metabolic analysis comparing glucose and galactose consumption indicates that after metabolic shift not enough pyruvate is produced to supply energy metabolism and lactate is used for pyruvate synthesis. In addition, MFA indicates that most carbon consumed during low carbon flux is directed towards maintaining energy metabolism.     

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, NH(3), and O(2), 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.     

Scale up cultivation of primary human umbilical vein endothelial cells on microcarriers from spinner vessels to bioreactor fermentation

Five types of dextran-based microcarriers (Dormacell, Pfeifer and Langen) with different concentrations of dimeric DEAE anion-exchange groups (nitrogen contents from 1.2 up to 2.9%) were tested as growth substrates for the cultivation of human umbilical vein endothelial cells (HUVECs). All microcarriers were gelatinized before use to improve cell adhesion. The one with the highest DEAE-group density was found to be most suitable for HUVEC propagation reaching final cell densities of 8×10⁵ viable cells ml^-1 (95% viability) using microcarrier concentrations of 3 g l^–1. Furthermore, metabolic data of glucose/lactate and amino acid metabolism are presented in this study. The concentrations of 18 amino acids were monitored throughout cultivation. A considerable decrease of glutamine and inverse increase of glutamate was observed. Cultivation with initial glucose concentration of 16.5 mmol l^–1 resulted in high glutamine consumption rates, whereas high glucose-supplemented starting culture medium (30 mmol l^-1) gave considerably lowered rates, indicating altered glutamine metabolism due to different glucose feeding. The glucose consumption and lactate production rates increased 2.6 fold and 3.5 fold, respectively, due to switch over from low to high glucose supplemented cultures. The rate of glucose metabolism was found not to be directly related to cell growth, because almost identical growth rates and doubling times were obtained. Considering the remaining 16 amino acids measured, serine concentrations considerably declined and glycine as well as alanine concentrations raised strongly. Most amino acid values were found insignificantly altered during 14 days of cultivation. Spinner vessel cultures served as inoculum for up scale propagation of HUVECs in membrane stirred 2 liter bioreactors. About 5×10⁹ HUVECs were produced, which were used for the isolation and structural characterization of glycosphingolipids, cell membrane compounds, which are suggested to be involved in e.g. selectin-carbohydrate interaction (cell-cell adhesion), carcinogenesis and atherogenesis.Abbreviations HUVECs human umbilical vein endothelial cells - PBS phosphate buffered saline     

Investigation of glucose catabolism in hypoxic Mcf 7 breast cancer culture

Hypoxia plays an important role in tumor phenotype and progression and alters glycolysis, with changes in signaling pathways that develop in response to hypoxia. In this study, the effects of oxygen (normoxia/hypoxia) and of glucose levels on the glucose metabolism was investigated in MCF-7 cancer cells. Under either normoxia or hypoxia conditions, the cells were exposed to glucose at different concentrations (0, 5.5, 15 or 55 mM) for either 3, 6, 12, 24 or 48 h. In all groups, cell viability, levels of key enzymes reflecting glycolytic metabolism in cell lysates, glucose consumed in the medium and extracellular lactate levels and wound closure percentages were determined. In hypoxic cells, intracellular consumption of glucose, and extracellular lactate levels due to increased glucose concentration were observed to be higher (compared to normoxia) and as a result of prolonged exposure to hypoxia, cells were observed to develop resistance to the prolonged exposure to hypoxia. The number of glycolytic enzymes obtained at different levels proved that cells had different potential capacities and changing mechanisms for the metabolic needs of the cell depending on the glucose amount in the medium and time in adapting to the oxygen tension. This study showed that there was an important interaction between hypoxia and glucose metabolism in general, and it was concluded that metabolic processes activated by hypoxia could offer new therapeutic targets.     

人皮肤成纤维细胞在不同培养系统中的生长代谢特性

大面积烧伤病人及多种皮肤溃疡病人很难用自体皮肤移植来进行治疗.早期治疗方法采用尸体来源的皮肤移植,但由于来源有限、且有传播疾病的危险,因此应用组织工程技术构建生物活性人工皮肤已成为近十几年来在组织工程和创伤治疗领域的研究热点,目前已有几种人工皮肤成功地走向临床[1].然而,在构建大面积皮肤组织过程中,如何大量制备皮肤种子细胞仍然是一大棘手的难题,成为人体皮肤组织工程迫切需要解决的技术关键.获得大量扩增的皮肤细胞,解决种子细胞的供应问题,是构建人工皮肤的一个关键.     

Metabolic shifts by nutrient manipulation in continuous cultures of BHK cells

The present work aims at characterizing the regulatory mechanisms of metabolism and product formation of BHK cells producing a recombinant antibody/cytokine fusion protein. This work was carried out through the achievement of several steady-states in chemostat cultures, corresponding to different glucose and glutamine levels in the feed culture medium. Results obtained indicate that both glucose and glutamine consumptions show a Michaelis-Menten dependence on residual glucose and glutamine concentrations, respectively. Similar dependence was also observed for lactate and ammonia productions. K(Glc)(Glc) and K(Gln)(Gln) were estimated to be 0.4 and 0.15 mM, respectively, while q(max)(Glc) and q(max)(Gln) were estimated to be 1.8 and 0.55 nmol 10(-6)cells min(-1), respectively. At very low glucose concentrations, the glucose-to-lactate yield decreased markedly showing a metabolic shift towards lower lactate production; also, the glucose-to-cells yield was increased. At very low-glutamine concentrations, the glutamine-to-ammonia and glutamine-to-cells yields increased, showing a more efficient glutamine metabolism. Overall, amino acid consumption was increased under low glucose or glutamine concentrations. Metabolic-flux analysis confirmed the metabolic shifts by showing increases in the fluxes of the more energetically efficient pathways, at low-nutrient concentrations. No effect of glucose or glutamine concentrations on the cell-specific productivity was observed, even under metabolically shifted metabolism; therefore, it is possible to confine the cells to a more efficient metabolic state maintaining the productivity of the recombinant product of interest, and consequently, increasing final product titers by increasing cell concentration and culture length. This work is intended to be a model approach to characterize cell metabolism in an integrated way; it is highly valuable for the establishment of operating strategies in mammalian cell fermentations in which cell metabolism is to be confined to a desired state.     

Influence of medium exchange schedules on metabolic, growth, and GM-CSF secretion rates of genetically engineered NIH-3T3 cells.

The metabolic and secretory characteristics of NIH-3T3 fibroblasts transfected with a cDNA encoding human granulocyte-macrophage colony stimulating factor (GM-CSF) were examined as a function of the culture medium exchange schedule. The rates of glucose and glutamine consumption and of lactate and ammonia production were measured over exchange schedules ranging from complete medium replacement weekly (1/week) to complete medium replacement daily (7/week). All measured metabolic rates increased with increased medium exchange rates and accelerated sharply between exchange rates of 3.5/week and 7/week. The lactate/glucose and ammonia/glutamine yield coefficients, however, remained invariant at about 1.9 and 1.0 mol/mol, respectively, under all medium perfusion conditions. A shift-up in medium perfusion rates from 3.5/week to 7/week resulted in increased metabolic rates that resembled those observed in the cultures that were exchanged at the 7/week rate throughout, showing that the metabolic rates could be directly controlled by the perfusion rate. Differential regulation of medium versus serum perfusion demonstrated that increased NIH-3T3 cell metabolism was directly proportional to the serum flux to which the cells were exposed. Thus a limiting serum component is responsible for the altered metabolic and growth rates. The GM-CSF production by the transfected 3T3 cells was stable but exhibited substantial transient increases during periods of cell proliferation, demonstrating that the secretion of transfected gene products can be highly modulated even when the cDNA is driven from a constitutive promoter. These studies show that the metabolic and secretory behavior of genetically engineered cells is influenced by the medium exchange schedule.