Glutamine-limited batch hybridoma growth and antibody production: experiment and model

The influence of glutamine (a major energy source) on both hybridoma growth and monoclonal antibody production was examined. A series of batch experiments were performed in T-flasks containing initial glutamine levels ranging from 0.5 to 4.0 mM in RPMI 1640 with 20% v/v fetal calf serum. The maximum final cell concentration increased with initial glutamine levels in the range of 0.5-2 mM; further glutamine increases had little or no effect. Earlier studies in our laboratories demonstrated that serum component(s) strongly influence the maximum specific growth rate. Here, the present studies reveal also the stoichiometric limitation by glutamine in the later stages of growth when its concentration is drastically reduced. For 0.5 to 1.5 mM initial glutamine, complete substrate utilization coincided with the cessation of cell growth and the onset of the death phase. For initial glutamine concentrations higher than 2.0 mM, growth halted prior to glutamine exhaustion, presumably because serum or RPMI component(s) were exhausted. The specific antibody secretion rate was essentially non-growth-associated above a critical low glutamine concentration in both the growth and death phases. At or below this critical value, an apparent emergence of stoichiometnc or energy limitation resulted in a dramatic drop in the secretion rate to zero. A simple unstructured model was developed that simulates these trends well. All parameters were determined using only subsets of the data. Nevertheless, these parameter values provided simulations in good agreement with all the glutamine-limited cultures.     

Analysis of growth and production coupling for batch cultures of Lactobacillus helveticus with the help of an unstructured model

An unstructured model has been developed by assuming a sigmoidal variation with time of specific growth rate and introducing an additional term in Luedeking and Piret production kinetics. The model fitted growth and production kinetic data. The model was helpful for examining the influence of initial yeast extract concentration on growth and production coupling. In richly supplemented media, the growth associated production mechanism prevailed, while in the case of poor nitrogen supplementation, most lactic acid production was non-growth-associated. Both contributions might be calculated from model parameters; this was especially interesting when the forms of growth and production kinetics did not allow a clear conclusion. The additional term in the production rate expression was a convenient way to characterize ‘usable nitrogen’ concentration in the medium. From the model a clear criterion has been derived for optimizing the nitrogen supplementation from an economic point of view.     

A kinetic analysis of hybridoma growth and metabolism in batch and continuous suspension culture: effect of nutrient concentration, dilution rate, and pH

Hybridomas are finding increased use for the production of a wide variety of monoclonal antibodies. Understanding the roles of physiological and environmental factors on the growth and metabolism of mammalian cells is a prerequisite for the development of rational scale-up procedures. An SP2/0-derived mouse hybridoma has been employed in the present work as a model system for hybridoma suspension culture. In preliminary shake flask studies to determine the effect of glucose and glutamine, it was found that the specific growth rate, the glucose and glutamine metabolic quotients, and the cumulative specific antibody production rate were independent of glucose concentration over the range commonly employed in cell cultures. Only the specific rate of glutamine uptake was found to depend on glutamine concentration. The cells were grown in continuous culture at constant pH and oxygen concentration at a variety of dilution rates. Specific substrate consumption rates and product formation rates were determined from the steady state concentrations. The specific glucose uptake rate deviated from the maintenance energy model(1) at low specific growth rates, probably due to changes in the metabolic pathways of the cells. Antibody production was not growth-associated; and higher specific antibody production rates were obtained at lower specific growth rates. The effect of pH on the metabolic quotients was also determined. An optimum in viable cell concentration was obtained between pH 7.1 and 7.4. The viable cell number and viability decreased dramatically at pH 6.8. At pH 7.7 the viable cell concentration initially decreased, but then recovered to values typical of pH 7.1-7.4. Higher specific nutrient consumption rates were found at the extreme pH values; however, glucose consumption was inhibited at low pH. The pH history also influenced the behavior at a given pH. Higher antibody metabolic quotients were obtained at the extreme pH values. Together with the effect of specific growth rate, this suggests higher antibody production under environmental or nutritional stress.     

A kinetic analysis of hybridoma growth and metabolism in batch and continuous suspension culture: effect of nutrient concentration, dilution rate, and pH. Reprinted from Biotechnology and Bioengineering, Vol. 32, Pp 947-965 (1988)

Hybridomas are finding increased use for the production of a wide variety of monoclonal antibodies. Understanding the roles of physiological and environmental factors on the growth and metabolism of mammalian cells is a prerequisite for the development of rational scale-up procedures. An SP2/0-derived mouse hybridoma has been employed in the present work as a model system for hybridoma suspension culture. In preliminary shake flask studies to determine the effect of glucose and glutaminE, it was found that the specific growth rate, the glucose and glutamine metabolic quotients, and the cumulative specific antibody production rate were independent of glucose concentration over the range commonly employed in cell cultures. Only the specific rate of glutamine uptake was found to depend on glutamine concentration. The cells were grown in continuous culture at constant pH and oxygen concentration at a variety of dilution rates. Specific substrate consumption rates and product formation rates were determined from the steady state concentrations. The specific glucose uptake rate deviated from the maintenance energy model(1) at low specific growth rates, probably due to changes in the metabolic pathways of the cells. Antibody production was not growth-associated; and higher specific antibody production rates were obtained at lower specific growth rates. The effect of pH on the metabolic quotients was also determined. An optimum in viable cell concentration was obtained between pH 7.1 and 7.4. The viable cell number and viability decreased dramatically at pH 6.8. At pH 7.7 the viable cell concentration initially decreased, but then recovered to values typical of pH 7.1-7.4. Higher specific nutrient consumption rates were found at the extreme pH values; however, glucose consumption was inhibited at low pH. The pH history also influenced the behavior at a given pH. Higher antibody metabolic quotients were obtained at the extreme pH values. Together with the effect of specific growth rate, this suggests higher antibody production under environmental or nutritional stress.     

Model simulation and analysis of perfusion culture of mammalian cells at high cell density.

Rate equations recently proposed by the authors for growth, death, consumption of nutrients, and formation of lactic acid, ammonium, and monoclonal antibody of hybridoma cells are used to simulate and analyze the behavior of perfusion cultures. Model simulations are in good agreement with experimental results from three different cell lines under varied perfusion and cell bleed rates except for cultures with very low viability. Analysis of simulations and experimental results indicates that in perfusion cultures with a complete cell separation cell bleed rate is a key parameter that strongly affects all the process variables, whereas the perfusion rate mainly affects the total and viable cell concentrations and the volumetric productivity of monoclonal antibody. Growth rate, viability, and specific perfusion rate of cells are only a function of the cell bleed rate. This also applies to cultures with partial cell separation in the permeate if the effective cell bleed rate is considered. It is suggested that the (effective) cell bleed rate of a perfusion culture should be carefully chosen and controlled separately from the perfusion rate. In general, a low cell bleed rate that warrants a reasonable cell viability appears to be desirable for the production of antibodies. Furthermore, model simulations indicate the existence of an optimum initial glucose concentration in the feed. For the cell lines considered, the initial glucose concentration used in normal cell culture media is obviously too high. The initial glutamine concentration can also be reduced to a certain extent without significantly impairing the growth and antibody production but considerably reducing the ammonia concentration. The mathematical model can be used to predict these optimum conditions and may also be used for process design.     

Bcl-2 over-expression reduced the serum dependency and improved the nutrient metabolism in a NS0 cells culture

The over-expression of Bcl-2 has greatly improved the culture period, specific growth rate, and maximum viable cell density of NS0 cells culture under low serum condition. Further analysis of these data suggests that a saturation model of the Monod type can be used to represent the relationships of specific growth rate and initial serum concentration. The μ_max andK _s for the Bcl-2 cell line is 0.927 day⁻¹ and 0.947% (v/v) respectively, which are 21% greater and 7% lower respectively than its control counterpart. Study on the amino acid supplementation revealed that Bcl-2 cell lines possess greater improvement in the specific growth rate and maximum viable cell density compared to the control cell lines. A further increase in the amino acid supplementation has resulted a 17% decrease in specific growth rate and no improvement in maximum viable cell density in the control culture. However, the Bcl-2 cell line exhibited a better growth characteristic in this culture condition compared to that of control cell lines. The higher specific growth rate and maximum viable cell density of the Bcl-2 cell line in medium fortified with serum and MEM EAA suggested a more efficient nutrient metabolism compared to that in the control cell line. The low serum and amino acid utilisation rate and the higher cell yield may prove to be important in the development of serum/protein free culture.     

Growth, metabolic, and antibody production kinetics of hybridoma cell culture: 2. Effects of serum concentration, dissolved oxygen concentration, and medium pH in a batch reactor.

The effects of serum, dissolved oxygen (DO) concentration, and medium pH on hybridoma cell physiology were examined in a controlled batch bioreactor using a murine hybridoma cell line (167.4G5.3). The effect of serum was also studied for a second murine hybridoma cell line (S3H5/gamma 2bA). Cell growth, viability, cell density, carbohydrate and amino acid metabolism, respiration and energy production rates, and antibody production rates were studied. Cell growth was enhanced and cell death was decreased by increasing the serum level. The growth rates followed a Monod-type model with serum being the limiting component. Specific glucose, glutamine, and oxygen uptake rates and specific lactate and ammonia production rates did not change with serum concentrations. Amino acid metabolism was slightly influenced by the serum level. Cell growth rates were not influenced by DO between 20% and 80% air saturation, while the specific death rates were lowest at 20-50% air saturation. Glucose and glutamine uptake rates increased at DO above 10% and below 5% air saturation. Cell growth rate was optimal at pH 7.2. Glucose and glutamine uptake rates, as well as lactate and ammonia production rates, increased above pH 7.2. Metabolic rates for glutamine and ammonia were also higher below pH 7.2. The consumption or production rates of amino acids followed the glutamine consumption very closely. Cell-specific oxygen uptake rate was insensitive to the levels of serum, DO, and pH. Theoretical calculations based on experimentally determined uptake rates indicated that the ATP production rates did not change significantly with serum and DO while it increased continually with increasing pH. The oxidative phosphorylation accounted for about 60% of total energy production. This contribution, however, increased at low pH values to 76%. The specific antibody production rate was not growth associated and was independent of serum and DO concentrations and medium pH above 7.20. A 2-fold increase in specific antibody production rates was observed at pH values below 7.2. Higher concentrations of antibody were obtained at high serum levels, between 20% and 40% DO, and at pH 7.20 due to higher viable cell numbers obtained.     

Kinetics of recombinant immunoglobulin production by mammalian cells in continuous culture

A clonal derivative of a transfectant of the SP2/O myeloma cell line producing a chimeric monoclonal antibody was maintained in steady-state, continuous culture at dilution rates ranging from 0.21 to 1.04 day(-1). The steady-state values for nonviable and total cell concentrations increased as the dilution rate decreased, while the viable cell concentration was roughly independent of the dilution rate. At steady state, the specific growth rate increased and the specific death rate decreased as the dilution rate increased. The maximum specific growth rate was 1.15 day(-1). Antibody production was growth associated and the specific rate of antibody production increased linearly as the specific growth rate increased.     

Effect of initial cell density on hybridoma growth, metabolism, and monoclonal antibody production.

A murine hybridoma cell line (167.4G5.3) was cultivated in batch mode with varying inoculum cell densities using IMDM media of varying fetal bovine serum concentrations. It was observed that maximum cell concentrations as well as the amount of monoclonal antibody attainable in batch mode were dependent on the inoculum size. Specifically, cultures with lower inoculum size resulted in lower cell yield and lower antibody concentrations. However, in the range of 10(2) to 10(5) cells per ml, the initial cell density affected the initial growth rate by a factor of only 20%. Furthermore, specific monoclonal antibody production rates were independent of initial cell density and the serum concentration. Glutamine was the limiting nutrient for all the cultures, determining the extent of growth and the amount of antibody produced. Serum was essential for cell growth and cultures with initial cell concentrations up to 10(6) cells per ml could not grow without serum. However, when adapted, the cells could grow in a custom-made serum-free medium containing insulin, transferrin, ethanolamine, and selenium (ITES) supplements. The cells adapted to the ITES medium could grow with an initial growth rate slightly higher than in 1.25% serum and the growth rate showed an initial density dependency-inocula at 10(3) cells per ml grew 30% slower than those at 10(4) or 10(5). This difference in growth rate was decreased to 10% with the addition of conditioned ITES medium. The addition of conditioned media, however, did not improve the cell growth for serum-containing batches.     

An investigation of cell density effects on hybridoma metabolism in a homogeneous perfusion reactor

In this work, metabolite and antibody production kinetics of hybridoma cultures were investigated as a function of cell density and growth rate in a homogeneous perfusion reactor. Hydrophilized hollow fiber polypropylene membranes with a pore size of 0.2 m were used for medium perfusion. Oxygen was supplied to the cells through thin walled silicone tubing. The mouse-mouse hybridoma cells were grown in three identical bioreactors at perfusion rates of 1.1, 2.0, and 3.2/day for a period of eight days during which the viable cell concentrations reached stable values of 2.6×10⁶, 3.5×10⁶, and 5.2×10⁶ cells/ml, respectively. Total cell densities reached values ranging from 8×10⁶ to 1×10⁶ cells/ml. Specific substrate consumption and product formation rates responded differently to changes in cell density and apparent specific growth rate, which were not varied independently. Using multiple regression analysis, the specific glucose consumption rate was found to vary with viable cell density while the specific glutamine uptake and lactate production rates varied with both viable cell density and apparent specific growth rate. These results suggest that cell density dictates the rate of glucose consumption while the cell growth rate influences how glucose is metabolized, i.e., through glycolysis or the TCA cycle. The specific antibody production rate was found to be a strong function of cell density, increasing as cell density increased, but was essentially independent of the specific growth rate for the cell line under study.List of Symbols MAb monoclonal antibody - X _v viable cell density (cells/ml) - X _d nonviable cell density (cells/ml) - specific growth rate (1/day) - k _d specific death rate (1/day) - D dilution rate (1/day) - S _f substrate concentration in feed (g/l or mM) - S substrate concentration (g/l or mM) - P _f product concentration in feed (g/l or g/ml) - P product concentration (g/l or ug/ml) - q _s specific consumption rate of substrate (g/hr/cell or mmol/hr/cell) - q _p specific production rate of product (g/hr/cell) - q _MAb specific production rate of monoclonal antibody (g/hr/cell) This work was supported in part by a grant for the National Science Foundation (BCS-9157851) and by matching funds from Merck and Monsanto. We sincerely thank Mr. Roland Buchele of Akzo Inc. (Germany) for donation of the polypropylene membranes, Dr. Michael Fanger (Dartmouth Medical School) for the hybridoma cell line, Dr. Sadettin Ozturk (Verax Corp., Lebanon, NH) for technical discussions regarding reactor design, and Dr. Derrick Rollins (Iowa State University) for advice on statistical methods.     

Enhancement of monoclonal antibody yield by hybridoma fed-batch culture, resulting in extended maintenance of viable cell population

Hybridoma batch cultures were extended using feed formulations based on nutrient consumption measured during different batch culture phases when (a) growth but negligible antibody production was taking place; (b) maximum antibody production rate and declining viable cell growth rate were observed. Strategy (a) was the more successful (2.8-fold compared with 1.8-fold antibody titer increase) and maintained cell viability for longer. Analysis of the effects of omitting individual amino acids yielded results which were consistent with those from the feeding experiment (c) 1994 John Wiley & Sons, Inc.     

Modelling the growth and bacteriocin production by Lactobacillus amylovorus DCE 471 in batch cultivation

A model was set up to describe the production of amylovorin L471 by Lactobacillus amylovorus DCE 471, on a laboratory scale, in which the cells are grown in MRS (deMau-Rogosa-Sharpe) broth. The main features of the dynamic model are : (i) increase of the biomass according to a logistic equation ; (ii) non-growth-associated consumption of substrate (maintenance metabolism) ; and (iii) primary metabolite kinetics for the bacteriocin production. The main purpose was to set up a simple empirical model to examine growth and bacteriocin production in different conditions. Parameters estimated from a fermentation with 20 g l⁻¹ glucose (w/v) could be used to predict the evolution of cell dry mass, glucose and lactic acid concentration of fermentations, performed with 5, 30, 40 and 60 g l⁻¹ initial glucose. The influence of the operating temperature (30, 37 and 45 °C) on the model parameters was also investigated. The proposed model was able to describe growth and bacteriocin production in all cases. The specific bacteriocin production rate was found to vary strongly with temperature, with 30 °C as the best value. Variation of the operating temperature from 37 to 30 °C appeared to significantly enhance the specific bacteriocin production.     

Continuous culture of Methanococcus jannaschii, an extremely thermophilic methanogen

Methanococcus jannaschii, an extremely thermophilic methanogen isolated from a deep-sea hydrothermal vent, was grown at 80 degrees C in continuous culture on a mineral salts medium gassed with H(2) and CO(2) at three different flow rates. The maximum specific growth rate was 0.56 h(-1), and the maximum specific methane productivity was 0.32 (mol g(-1) h(-1)). Uncoupling of growth and methane production was evidenced by an increase in teh non-growth-associated rate of methane formation, beta, with increasing gaseous input. The specific hydrogenase activity exhibited growth-assiciated behaviour at low growth rates, but showed no dependence on growth at higher growth rates. The growth dependence of hydrogenase activity is consistent with the pressure dependence of hydrogenase activity measured in previous experiments. In contrast, the specific protease activity was independent of the growth rate over the entire range of dilution rates studied. (c) 1994 John Wiley & Sons, Inc.     

A maximum production strategy of lysine based on a simplified model derived from a metabolic reaction network

The aim of this study is to develop a strategy for maximum production of a target product with a simplified model derived from a metabolic reaction network through an example of lysine production. Based on the model, a search for the optimal specific growth rate profile was conducted among the available conditions of batch fermentation based on the derived model, when the total fermentation time was fixed. The optimal specific growth rate was obtained as a boundary control: initially, the specific growth rate was maintained at a maximum value and was subsequently switched to a critical value giving the maximum specific production rate. To make the specific growth rate follow this optimal profile as accurately as possible in batch mode, first, an appropriate initial concentration of leucine was employed in the experiment. Second, the feeding strategy of leucine was further studied. The specific growth rate profile with feeding was closer to the optimal one and the amount of lysine produced at the final stage of fermentation was increased about twofold, compared to that in the batch fermentation. Finally, the strategy was summarized as an algorithm for general use of this method.     

Hybridoma growth and productivity: effects of conditioned medium and of inoculum size

Apart from gas concentrations, temperature, and pH, generally only the initial conditions can be manipulated in batch culture. Inoculum size and initial conditioned medium concentration represent two important considerations for optimal batch production. Two hybridoma cell lines were used to assess the impact of these initial conditions on population growth and monoclonal antibody productivity in suspension batch culture. Varying initial cell concentration over the range of 1.0 × 105 cells mL-1 to 3.0 × 105 cells mL-1 did not affect maximum product titre or maximum volumetric cell-hours attained. Initial percent of conditioned medium up to 40 percent strongly impacted on population growth and productivity, with initial levels of 30 to 40% conditioned medium reducing or eliminating lag phase and increasing average viable cell density. However, specific productivity and product titre declined with increasing initial percent conditioned medium, even on a per volume of fresh medium basis. Glutamine and glucose depletion or ammonia toxicity could cause depressed product titres when conditioned medium is used. Glutamine and glucose levels can easily be replenished in conditioned medium at minimal cost, and ammonia can be removed. Specific productivity was higher during cyclic batch operating mode than during batch operating mode. This may be because cyclic batch operating mode results in an incidental volume of conditioned medium at the beginning of each cycle. A two stage, cyclic-batch/batch operating mode can be employed to fully utilize medium and maximize product titre.     

Enhanced specific antibody productivity of hybridomas resulting from hyperosmotic stress is cell line-specific

Hybridomas with non-growth-associated antibody production are thought to exhibit enhanced specific monoclonal antibody productivity (q _MAb) when subjected to hyperosmotic stress. Two hybridoma cell lines exhibiting non-growth-associated antibody production, S3H5/2bA2 and DB9G8 hybridomas, are cultivated in a batch mode using hyperosmolar media resulting from sodium chloride addition. Their response to hyperosmotic stress regarding q _MAb is quite different, though they show similar depression of cell growth in hyperosmolar media. The q _MAb of S3H5/2bA2 cells in a hyperosmolar medium (396 mOsm/kg, 10% fetal bovine serum (FBS)) is enhanced by approximately 180% when compared with that in a standard medium (283 mOsm/kg, 10% FBS), while q _MAb of DB9G8 cells in the same hyperosmolar medium is enhanced by only 10%. Thus, the enhanced q _MAb of hybridomas exhibiting non-growth-associated antibody production resulting from hyperosmotic stress is cell line-specific.     

Predictive macroscopic modeling of cell growth,metabolism and monoclonal antibody production: Case study of a CHO fed-batch production

We describe a systematic approach to establish predictive models of CHO cell growth, cell metabolism and monoclonal antibody (mAb) formation during biopharmaceutical production. The prediction is based on a combination of an empirical metabolic model connecting extracellular metabolic fluxes with cellular growth and product formation with mixed Monod-inhibition type kinetics that we generalized to every possible external metabolite. We describe the maximum specific growth rate as a function of the integral viable cell density (IVCD). Moreover, we also take into account the accumulation of metabolites in intracellular pools that can influence cell growth. This is possible even without identification and quantification of these metabolites as illustrated with fed-batch cultures of Chinese Hamster Ovary (CHO) cells producing a mAb. The impact of cysteine and tryptophan on cell growth and cell productivity was assessed, and the resulting macroscopic model was successfully used to predict the impact of new, untested feeding strategies on cell growth and mAb production. This model combining piecewise linear relationships between metabolic rates, growth rate and production rate together with Monod-inhibition type models for cell growth did well in predicting cell culture performance in fed-batch cultures even outside the range of experimental data used for establishing the model. It could therefore also successfully be applied for in silico prediction of optimal operating conditions.     

Modeling and optimization of alpha-amylase production in a recombinant yeast fed-batch culture taking account of the cell cycle population distribution.

A simple mathematical model describing the cell cycle dependency of rice alpha-amylase production by a recombinant yeast was constructed to investigate the efficiency of cell cycle population control. First, the effects of the glucose concentration and cultivation temperature on the specific growth rate, the specific production rate of rice alpha-amylase, and the distribution of the cell cycle population were studied under balanced growth conditions. On the basis of the results, parameter values for the mathematical model were then estimated. The proposed model was shown to be applicable for unbalanced as well as balanced growth phases. The optimal control strategy in respect of temperature and glucose concentration for maximum rice alpha-amylase production, taking into account the cell cycle population, was determined and the result was compared with that obtained by a simple mathematical model in which cell cycle distribution was not considered. Finally, the effect of the initial population of each cell cycle phase on the final amount of the product under optimal operational conditions was investigated. The simulation and experimental data coincided well with each other, and the model was used to optimize the control strategy for maximum alpha-amylase production.     

Kinetic study of hybridoma cell growth in continuous culture: II. Behavior of producers and comparison to nonproducers

A hybridoma cell line, AFP-27-P, was cultivated in continuous culture under glucose-limited conditions. The viable cell concentration, dead-cell concentration, and cell volume all varied with the dilution rate. A model previously developed for a nonproducing clone of the same cell line, AFP-27-NP, was extended to describe the behavior of the cells. The relationship between the specific growth rate and glucose concentration is described by a function similar to the Monod model. A threshold glucose concentration and a minimum specific growth rate are incorporated; the model is meaningful only at glucose concentration and a minimum specific growth rate are incorporated; the model is meaningful only at glucose concentrations and specific growth rates above these levels. The relationship between the death rate and the glucose concentration is described by an inverted Monod-type function. Furthermore, the yield coefficient based on glucose is constant in the lower range of specific growth rates and changes to a new constant value in the upper range of specific growth rates. No maintenance term for glucose consumption is used; in the plot of specific glucose consumption rate vs. specific growth rate, the line intercepts the specific growth rate at a value close to the minimum growth rate. The productivity of antibody as a function of the specific growth rate is described by a mixed type model with a noon-growth-associated term and a negative-growth-associated term. The values for the model parameters were determined from regression analysis of the steady state data.     

Metabolite profiles and growth characteristics of Rhizobium meliloti cultivated at different specific growth rates

Rhizobium meliloti (ATCC 55340) was grown at different specific growth rates in a chemostat apparatus. Metabolic products, relating to the Embden-Meyerhof-Parnas (EMP) pathway and the tricarboxylic acid (TCA) cycle, were measured and quantified to probe the influence of specific growth rate on the distribution of important metabolites. The detection of propionate in the fermentation broth implies that the imbalance of reducing equivalents of FADH(2) and NADH + H(+) resulted in a partially reductive operation of the TCA cycle. Additionally, experimental results show that the specific growth rate plays an essential role in modulating the biomass concentration, the specific substrate uptake rate, the cell length, the specific exopolysaccharide (EPS) production rate, the distribution of EPS molecular weight, and the profiles of carbohydrate and organic acid. The specific EPS production rate (varying from 13.3 to 111 mg EPS/g-DW/h) follows a growth-associated pattern at the specific growth rate ranging from 0.06 to 0.20 h(-1) and switches into non-growth-associated mode when the specific growth rate is over 0.20 h(-1).