杂交瘤细胞培养中摄氧速率(OUR)的在线检测及其与细胞生长及代谢的关系

在批式及灌流培养条件下研究了杂交瘤细胞在无血清培养基中的生长、代谢情况与氧消耗的关系。应用动力学方法在线进行OUR的检测,同时离线取样检测其他参数。结果发现OUR与谷氨酰胺的消耗、抗体的生成及活细胞密度间有明显的相关关系,进一步的分析还发现在对数生长期,OUR与活细胞密度间具有良好的线性关系,qOUR(0.103±0.028)×10^-12mol/cell/h,可以通过它来进行细胞密度的在线检测。并通过以ΔOUR=0时刻作为灌流调整点进行连续灌流培养的初步实验验证了OUR作为培养过程反馈控制参数的可能性。     

Alteration of mammalian cell metabolism by dynamic nutrient feeding

The metabolism of hybridoma cells was controlled to reduce metabolic formation in fed-batch cultures by dynamically feeding a salt-free nutrient concentrate. For this purpose, on-line oxygen uptake rate (OUR) measurement was used to estimate the metabolic demand of hybridoma cells and to determine the feeding rate of a concentrated solution of salt-free DMEM/F12 medium supplemented with other medium components. The ratios among glucose, glutamine and other medium components in the feeding nutrient concentrate were adjusted stoichiometrically to provide balanced nutrient conditions for cell growth. Through on-line control of the feeding rate of the nutrient concentrate, both glucose and glutamine concentrations were maintained at low levels of 0.5 and 0.2 mM respectively during the growth stage. The concentrations of the other essential amino acids were also maintained without large fluctuations. The cell metabolism was altered from that observed in batch cultures resulting in a significant reduction of lactate, ammonia and alanine production. Compared to a previously reported fed-batch culture in which only glucose was maintained at a low level and only a reduced lactate production was observed, this culture has also reduced the production of other metabolites, such as ammonium and alanine. As a result, a high viable cell concentration of more than 1.0 × 10⁷ cells/mL was achieved and sustained over an extended period. The results demonstrate an efficient nutrient feeding strategy for controlling cell metabolism to achieve and sustain a high viable cell concentration in fed-batch mammalian cell cultures in order to enhance the productivity. This revised version was published online in July 2006 with corrections to the Cover Date.     

Cell cycle- and growth phase-dependent variations in size distribution, antibody productivity, and oxygen demand in hybridoma cultures

Simultaneous determination of cell size and DNA content of hybridomas (HB-32) revealed a direct correlation between average cell volume and progression through the cell cycle. Pseudocontinuous experiments showed that G(1) cells, as estimated from cell size measurements, secreted monoclonal antibody at rates higher than those of cells in other stages of interphase and mitosis. Similarly, fed-batch and batch experiments suggested that specific oxygen uptake rate (qO(2)) is also a function of cell cycle, being minimum for cells in G(0) and G(1) phase. In batch cultures, HB-32 showed a rapid decrease in oxygen uptake rate (OUR) just prior to reaching maximum cell concentration. The OUR steadily increased from 0.01-0.05 to 0.5-0.7 mmol O(2)/L h as the cells went from the lag to the midexponential phase. The qO(2) increased from 0.3 x 10(-10)-0.9 x 10(-10) mmol O(2)/cell h at inoculation to 3.3 x 10(-10)-3.7 x 10(-10) mmol O(2)/cell h during the early exponential phase where it remained relatively constant. Several hours before maximum cell concentration was reached, OUR and qO(2) rapidly decreased to levels below those observed at inoculation. The time at which the shift in OUR and qO(2) occurred and the onset of decrease in the average cell size corresponded to the time of glutamine depletion. Based on monitoring OUR on-line in batch cultures, glutamine was supplemented, resulting in increased cell concentration, extension of culture viability, and increased MAb concentration.     

The use of culture redox potential and oxygen uptake rate for assessing glucose and glutamine depletion in hybridoma cultures

Culture redox potential (CRP) and oxygen uptake rate (OUR) were monitored on-line during glucose- and glutamine-limited batch cultures of a murine hybridoma cell line that secretes a neutralizing monoclonal antibody specific to toxin 2 of the scorpion Centruroides noxius Hoffmann. It was found that OUR and CRP can be used for assessing the viable cell concentration and growth phases of the culture. Before nutrient depletion, OUR increased exponentially with viable cell concentration, whereas CRP decreased monotonically until cell viability started to decrease. During the death phase, CRP gradually increased. A sudden decrease in OUR occurred upon glucose or glutamine depletion. CRP traced the dissolved oxygen profile during a control action or an operational eventuality, however, during nutrient depletion it did not follow the expected behavior of a system composed mainly by the O(2)/H(2)O redox couple. Such a behavior was not due to the accumulated lactate or ammonia, nor to possible intracellular redox potential changes caused by nutrient depletion, as inferred from respiration inhibition by rotenone or uncoupled respiration by 2,4-dinitrophenol. As shown in this study, operational eventualities can be erroneously interpreted as changes in OUR when using algorithms based solely on oxygen balances. However, simultaneous measurements of CRP and OUR may be used to discriminate real metabolic events from operational failures. The results presented here can be used in advanced real-time algorithms for controling glucose and glutamine at low concentrations, avoiding under- or over-feeding them in hybridoma cultures, and consequently reducing the accumulation of metabolic wastes and improving monoclonal antibody production. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 555-563, 1997.     

Phosphate feeding improves high-cell-concentration NS0 myeloma culture performance for monoclonal antibody production

Phosphorus depletion was identified in high-cell-concentration fed-batch NS0 myeloma cell cultures producing a humanized monoclonal antibody (MAb). In these cultures, the maximum viable and total cell concentration was generally ca. 5 x 10(9) and 7 x 10(9) cells/L, respectively, without phosphate feeding. Depletion of essential amino acids, such as lysine, was initially thought to cause the onset of cell death. However, further improvement of cell growth was not achieved by feeding a stoichiometrically balanced amino acid solution, which eliminated depletion of amino acids. Even though a higher cell viability was maintained for a longer period, no increase in total cell concentration was observed. Afterwards, phosphorus was found to be depleted in these cultures. By also feeding a phosphate solution to eliminate phosphorus depletion, the cell growth phase was prolonged significantly, resulting in a total cell concentration of ca. 17 x 10(9) cells/L, which is much greater than ca. 7 x 10(9) cells/L without phosphate feeding. The maximum viable cell concentration reached about 10 x 10(9) cells/L, twice as high as that without phosphate feeding. Apoptosis was also delayed and suppressed with phosphate feeding. A nonapoptotic viable cell population of 6.5 x 10(9) cells/L, as compared with 3 x 10(9) cells/L without phosphate feeding, was obtained and successfully maintained for about 70 h. These results are consistent with the knowledge that phosphorus is an essential part of many cell components, including phospholipids, DNA, and RNA. As a result of phosphate feeding, a much higher integral of viable cell concentration over time was achieved, resulting in a correspondingly higher MAb titer of ca. 1.3 g/L. It was also noted that phosphate feeding delayed the cell metabolism shift from lactate production to lactate consumption typically observed in recombinant NS0 cultures. The results highlight the importance of phosphate feeding in high-cell-concentration NS0 cultures.     

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.     

Characterization of a recombinant antibody produced in the course of a high yield fed-batch process

Many mammalian cell fed-batch processes rely on maintaining the cells in a viable and productive state for extended periods of time in order to reach high final concentrations of secreted protein. In the work described herein, a nonamplified NSO cell line was transfected with a vector expressing a recombinant human anti-HIV gp 120 monoclonal antibody (Mab) and a selectable marker, glutamine synthetase. A fed-batch process was developed which improved product yields tenfold over the yields reached in batch culture. In this case, the clone was cultured for a period of 22 days and produced 0.85 g Mab/L. To gauge the effect of extended culture lifetime on product quality, biochemical characteristics of MAb isolated from different time points in the fed-batch culture were determined. The apparent molecular weight of the MAb was constant throughout the course of the culture. Isoelectric focusing revealed four major charged species, with a fifth more acidic species appearing later in the culture. The antigen binding kinetics were constant for MAb isolated throughout the culture period. Glycosylation analysis, on the other hand, revealed that MAb produced later in the culture contained greater percentages of truncated N-acetylglucosamine and highmannose N-glycans. Possible contributions to this underglycosylated material from either cell lysis or synthesis from noviable cells were found to be negligible. Instead, the viable cells appeared to be secreting more truncated and high mannose MAb glycoforms as the culture progressed. (c) 1994 John Wiley & Sons, Inc.     

The production of monoclonal antibody in growth-arrested hybridomas cultivated in suspension and immobilized modes.

The effects of the microenvironment and the nature of the limiting nutrient on culture viability and overall MAb productivity were explored using a hybridoma cell line which characteristically produces MAb in the stationary phase. A direct comparison was made of the changes in the metabolic profiles of suspension and PEG-alginate immobilized (0.8 mm beads) batch cultures upon entry into the stationary phase. The shifts in glucose, glutamine, and amino acid metabolism upon entry into the stationary phase were similar for both microenvironments. While the utilization of most nutrients in the stationary phase decreased to below 20% of that in the growth phase, antibody production was not dramatically affected. The immobilized culture did exhibit a 1.5-fold increase in the specific antibody rate over the suspension culture in both the growth and stationary phases. The role of limiting nutrient on MAb production and cell viability was assessed by artificially depleting a specific nutrient to 1% of its control concentration. An exponentially growing population of HB121 cells exposed to these various depletions responded with dramatically different viability profiles and MAb production kinetics. All depletions resulted in growth-arrested cultures and nongrowth-associated MAb production. Depletions in energy sources (glucose, glutamine) or essential amino acids (isoleucine) resulted in either poor viability or low antibody productivity. A phosphate or serum depletion maintained antibody production over at least a six day period with each resulting in a 3-fold higher antibody production rate than in growing batch cultures. These results were translated to a high-density perfusion culture of immobilized cells in the growth-arrested state with continued MAb expression for 20 days at a specific rate equal to that observed in the phosphate- and serum-depleted batch cultures.     

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.     

Fed-batch cultivation of animal cells using different medium design concepts and feeding strategies

In animal cell cultivation, cell density and product concentration are often low due to the accumulation of toxic end-products such as ammonia and lactate and/or the depletion of essential nutrients. A hybridoma cell line (CRL-1606) was cultivated in T-flasks using a newly devised medium feeding strategy. The goals were to decrease ammonia and lactate formation by the design of an initial medium which would provide a starting environment to achieve optimal cell growth. This was followed by using a stoichiometric equation governing animal cell growth and then designing a supplemental medium for feeding strategy used to control the nutritional environment. The relationship between the stoichiometric demands for glutamine and nonessential amino acids was also studied. Through stoichiometric feeding, nutrient concentrations were controlled reasonably well. Consequently, the specific production rate of lactate was decreased by fourfold compared with conventional fed-batch culture and by 26-fold compared with conventional batch culture. The specific production rate of ammonia was decreased by tenfold compared with conventional fed-batch culture and by 50-fold compared with conventional batch culture. Most importantly, total cell density and monoclonal antibody concentration were increased by five- and tenfold respectively, compared with conventional batch culture. (c) 1994 John Wiley & Sons, Inc.     

Enhanced cell culture performance using inducible anti-apoptotic genes E1B-19K and Aven in the production of a monoclonal antibody with Chinese hamster ovary cells

Mammalian cells are used for the production of numerous biologics including monoclonal antibodies. Unfortunately, mammalian cells can lose viability at later stages in the cell culture process. In this study, the effects of expressing the anti-apoptosis genes, E1B-19K and Aven, separately and in combination on cell growth, survival, and monoclonal antibody (MAb) production were investigated for a commercial Chinese Hamster Ovary (CHO) mammalian cell line. CHO cells were observed to undergo apoptosis following a model insult, glucose deprivation, and at later stages of batch cell culture. The CHO cell line was then genetically modified to express the anti-apoptotic proteins E1B-19K and/or Aven using an ecdysone-inducible expression system. Stable transfected pools induced to express Aven or E1B-19K alone were found to survive 1-2 days longer than the parent cell line following glucose deprivation while the expression of both genes in concert increased cell survival by 3 days. In spinner flask batch studies, a clonal isolate engineered to express both anti-apoptosis genes exhibited a longer operating lifetime and higher final MAb titer as a result of higher viable cell densities and viabilities. Interestingly, survival was increased in the absence of an inducer, most likely as a result of leaky expression of the anti-apoptosis genes confirmed in subsequent PCR studies. In fed-batch bioreactors, the expression of both anti-apoptosis genes resulted in higher growth rates and cell densities in the exponential phase and significantly higher viable cell densities, viabilities, and extended survival during the post-exponential phase. As a result, the integral of viable cells (IVC) was between 40 and 100% higher for cell lines engineered to express both Aven and E1B-19K in concert, and the operational lifetime of the fed-batch bioreactors was increased from 2 to 5 days. The maximum titers of MAb were also increased by 40-55% for bioreactors containing cells expressing Aven and E1B-19K. These increases in volumetric productivity arose primarily from enhancements in viable cell density over the course of the fed-batch culture period since the specific productivities for the cells expressing anti-apoptosis genes were comparable or slightly lower than the parental hosts. These results demonstrate that expression of anti-apoptosis genes can enhance culture performance and increase MAb titers for mammalian CHO cell cultures especially under conditions such as extended fed-batch bioreactor operation.     

Multi-rate nonlinear state and parameter estimation in a bioreactor

This paper concerns real-time, multi-rate, nonlinear state and parameter estimation in a pilot-scale biochemical reactor in which cultivation of mouse-mouse hybridoma cells takes place. A multi-rate estimator is designed and implemented to estimate specific growth rate and concentrations of viable cells, total cells, glucose, glutamine, and monoclonal antibodies (MAb) in the reactor. These are estimated from frequent measurement (inferred values) of oxygen uptake rate (OUR) and infrequent and delayed measurements of the concentrations of viable cells, total cells, glucose, glutamine, and MAb. The infrequent measurements are available every 2 to 17 h with a time delay of 0.08 to 2.00 h, and OUR is inferred from dissolved oxygen concentration measurements that are available very 0.17 h. For each of the process variables, its infrequent measurement data and the profile of its estimate are presented to show the performance of the multi-rate estimator.     

Low-glutamine fed-batch cultures of 293-HEK serum-free suspension cells for adenovirus production

Recent developments in gene therapy using adenoviral (Ad) vectors have fueled renewed interest in the 293 human embryonic kidney cell line traditionally used to produce these vectors. Low-glutamine fed-batch cultures of serum-free, suspension cells in a 5-L bioreactor were conducted. Our aim was to tighten the control on glutamine metabolism and hence reduce ammonia and lactate accumulation. Online direct measurement of glutamine was effected via a continuous cell-exclusion system that allows for aseptic, cell-free sampling of the culture broth. A feedback control algorithm was used to maintain the glutamine concentration at a level as low as 0.1 mM with a concentrated glucose-free feed medium. This was tested in two media: a commercial formulation (SFM II) and a chemically defined DMEM/F12 formulation. The fed-batch and batch cultures were started at the same glucose concentration, and it was not controlled at any point in the fed-batch cultures. In all cases, fed-batch cultures with double the cell density and extended viable culture time compared to the batch cultures were achieved. An infection study on the high density fed-batch culture using adenovirus-green fluorescent protein (Ad-GFP) construct was also done to ascertain the production capacity of the culture. Virus titers from the infected fed-batch culture showed that there is an approximately 10-fold improvement over a batch infection culture. The results have shown that the control of glutamine at low levels in cultures is sufficient to yield significant improvements in both cell densities and viral production. The applicability of this fed-batch system to cultures in different media and also infected cultures suggests its potential for application to generic mammalian cell cultures.     

Control of redox potential in hybridoma cultures: effects on MAb production, metabolism, and apoptosis

Culture redox potential (CRP) has proven to be a valuable monitoring tool in several areas of biotechnology; however, it has been scarcely used in animal cell culture. In this work, a proportional feedback control was employed, for the first time, to maintain the CRP at different constant values in hybridoma batch cultures for production of a monoclonal antibody (MAb). Reducing and oxidant conditions, in the range of -130 and +70 mV, were maintained in 1-l bioreactors through automatic control of the inlet gas composition. Cultures at constant DOT, in the range of 3 and 300 %, were used for comparison. The effect of constant CRP on cell concentration, MAb production, metabolism of glucose, glutamine, thiols, oxygen consumption, and programmed cell death, was evaluated. Reducing conditions resulted in the highest viable cell and MAb concentrations and thiols production, whereas specific glucose and glutamine consumption rates remained at the lowest values. In such conditions, programmed cell death, particularly apoptosis, occurred only after nutrient exhaustion. The optimum specific MAb production rate occurred at intermediate CRP levels. Oxidant conditions resulted in a detrimental effect in all culture parameters, increasing the specific glucose, glutamine, and oxygen consumption rates and inducing the apoptotic process, which was detected as early as 24 h even when glutamine and glucose were present at non-limiting concentrations. In most cases, such results were similar to those obtained in control cultures at constant DOT.     

Defined protein and animal component-free NS0 fed-batch culture

A chemically defined protein and animal component-free fed-batch process for an NS0 cell line producing a human IgG(1) antibody has been developed. The fed-batch feed profile was optimised in a step-wise manner. Depletion of measurable compounds was determined by direct analysis. The cellular need for non-measurable compounds was tested by continued culturing of cell suspension, removed from the bioreactor, in shake-flasks supplemented with critical substances. In the final fed-batch culture, 8.4 x 10(6) viable cells mL(-1) and 625 mg antibody L(-1) was obtained as compared to 2.3 x 10(6) cells mL(-1) and 70 mg antibody L(-1) in batch. The increase in cell density, in combination with a prolonged declining phase where antibody formation continued, resulted in a 6.2-fold increase in total cell yield, a 10.5-fold increase in viable cell hours and an 11.4-fold increase in product yield. These improvements were obtained by using a feed with glucose, glutamine, amino acids, lipids, sodium selenite, ethanolamine and vitamins. Specifically, supplementation with lipids (cholesterol) had a drastic effect on the maximum viable cell density. Calcium, magnesium and potassium were not depleted and a feed also containing iron, lithium, manganese, phosphorous and zinc did not significantly enhance the cell yield. The growth and death profiles in the final fed-batch indicated that nutrient deprivation was not the main cause of cell death. The ammonium concentration and the osmolality increased to potentially inhibitory levels, but an imbalance in the supply of growth/survival factors may also contribute to termination of the culture.     

Improving an on-line feeding strategy for fed-batch cultures of hybridoma cells by dialysis and `Nutrient-Split'-feeding

The concept of the feeding strategy was to minimise the formation of inhibiting metabolites and to increase the yield of monoclonal antibodies in fed-batch cultures of hybridoma cells by a balanced supply of substrates. A process control system based on fieldbus technology was used for monitoring and control. External program routines were implemented to control dissolved oxygen (DO) and to calculate the oxygen uptake rate (OUR) and cumulative oxygen consumption (COC) simultaneously. A concentrated feed solution was supplied according to the off-line estimated stoichiometric ratio between oxygen and glucose consumption (GC). Feeding was initiated automatically when the OUR decreased due to substrate limitation. The antibody concentration increased three-fold compared to the conventional batch culture by applying this strategy. But it was not possible to avoid inhibition by ammonia during the fed-batch phase. This was accomplished by the use of a dialysis membrane. Dialysis fed-batch cultures were performed in a membrane dialysis reactor with a `nutrient-split' feeding strategy, where concentrated medium is fed to the cells and toxic metabolites are removed into a buffer solution. This resulted in a ten-fold increase of the antibody concentration compared to the batch. Amino acid concentrations were analysed to identify limiting conditions during the cultivation and to analyse the performance of the nutrient supply in the fed-batch and dialysis fed-batch.     

Large scale production of recombinant mouse and rat growth hormone by fed-batch GS-NSO cell cultures

Investigations of biological effects of prolonged elevation of growth hormone in animals such as mice and rats require large amounts of mouse and rat growth hormone (GH) materials. As an alternative to scarce and expensive pituitary derived materials, both mouse and rat GH were expressed in NSO murine myeloma cells transfected with a vector containing the glutamine synthetase (GS) gene and two copies of mouse or rat GH cDNA. For optimal expression, the mouse GH vector also contained sequences for targeting integration by homologous recombination. Fed-batch culture processes for such clones were developed using a serum-free, glutamine-free medium and scaled up to 250 L production scale reactors. Concentrated solutions of proteins, amino acids and glucose were fed periodically to extend cell growth and culture lifetime, which led to an increase in the maximum viable cell concentration to 3.5×10⁹ cells/L and an up to 10 fold increase in final mouse and rat rGH titers in comparison with batch cultures. For successful scale up, similar culture environmental conditions were maintained at different scales, and specific issues in large scale reactors such as balancing oxygen supply and carbon dioxide removal, were addressed. Very similar cell growth and protein productivity were obtained in the fed-batch cultures at different scales and in different production runs. The final mouse and rat rGH titers were approximately 580 and 240 mg/L, respectively. During fed-batch cultures, the cell growth stage transition was accompanied by a change in cellular metabolism. The specific glucose consumption rate decreased significantly after the transition from the growth to stationary stage, while lactate was produced in the exponential growth stage and became consumed in the stationary stage. This was roughly coincident with the beginning of ammonia and glutamate accumulation at the entry of cells into the stationary stage as the result of a reduced glutamine consumption and periodic nutrient additions.     

Fed-batch culture optimization of a growth-associated hybridoma cell line in chemically defined protein-free media

An investigation was made to study the processes of fed-batch cultures of a hybridoma cell line in chemically defined protein-free media. First of all, a strong growth-associated pattern was correlated between the production of MAb and growth of cells through the kinetic studies of batch cultures, suggesting the potential effectiveness of extending the duration of exponential growth in the improvement of MAb titers. Second, compositions of amino acids in the feeding solution were balanced stepwisely according to their stoichiometrical correlations with glucose uptake in batch and fed-batch cultures. Moreover, a limiting factor screening revealed the constitutive nature of Ca²⁺ and Mg²⁺ for cell growth, and the importance of their feeding in fed-batch cultures. Finally, a fed-batch process was executed with a glucose uptake coupled feeding of balanced amino acids together with groups of nutrients and a feeding of CaCl₂ and MgCl₂ concentrate. The duration of exponential cell growth was extended from 70 h in batch culture and 98 h in fed-batch culture without Ca²⁺/Mg²⁺ feeding to 117 h with Ca²⁺/Mg²⁺ feeding. As a result of the prolonged exponential cell growth, the viable and total cell densities reached 7.04 × 10⁶ and 9.12 × 10⁶ cells ml⁻¹, respectively. The maximal MAb concentration achieved was increased to approximately eight times of that in serum supplemented batch culture.     

Elevation of gamma-glutamyltransferase activity in 293 HEK cells constitutively expressing antisense glutaminase mRNA

Previous studies have shown that the use of dynamic nutrient feeding to maintain glutamine at low levels in fed-batch cultures reduced the overflow of glutamine metabolism. This strategy resulted in the shift of metabolism towards an energetically more efficient state signified by reduced lactate and ammonia production and thus achieving a higher cell density for enhanced productivity. In an effort to mimic the metabolic changes effected by this fed-batch strategy at the molecular level, 293 HEK cells were engineered via stable transfection with an antisense fragment of the rat phosphate-dependent glutaminase (PDG) gene. PDG is localized in the mitochondria and catalyzes the deamination of glutamine to glutamate with the release of ammonia. Stable single cell clones were isolated from the transfected populations. Characterization of these transfectants revealed indications of an altered glutamine metabolism affected by the antisense strategy. Contrary to our expectations, glutamine consumption and ammonia production in the antisense cells did not deviate significantly from that of untransfected cells. Glutamate was also observed to accumulate to high level extracellularly, as opposed to a consumption pattern normally observed in non-transfected cells. Subsequent analyses show that gamma-glutamyltransferase (gamma-GT) may be a significant pathway that resulted in the formation of glutamate and ammonia from glutamine catabolism extracellularly. gamma-GT has been widely investigated in renal glutamine metabolism, but has rarely been implicated in cultured cell metabolism. This study highlights the importance of this alternative glutamine metabolism pathway in cell culture.     

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.