Continuous hybridoma suspension cultures with and without cell retention: kinetics of growth, metabolism and product formation.

A laboratory scale bioreactor was constructed from glass and polycarbonate materials whereby a track-etch membrane (3 microns pore diameter) was integrated into its two-part bottom flange. The reactor performance was evaluated for continuous hybridoma suspension cultures under various conditions of cell retention. A total retention experiment demonstrated that this type of stirred tank reactor cannot be operated at near zero growth rate conditions. Instead, at steady viable cell concentrations of congruent to 3 x 10(6) cells per ml, specific growth and death rates were estimated at 0.60 +/- 0.06 d-1. Specific substrate (glucose, glutamine, O2, amino acids) consumption, by-product (ammonia, alanine, amino acids) and product (antibody) production rates as well as various apparent molar yield coefficients were obtained and are compared to metabolic quotients and yield coefficients previously calculated from standard continuous culture experiments, i.e., without cell retention, at specific growth rates of 0.63 and 1.24 d-1. Furthermore, steady-state data on viable cell and antibody concentrations, spec. mAb productivities, and space-time yields determined before and after a step change (2.5-fold increase) in dilution rate at identical specific growth rates mu are presented.     

Transient kinetics of hybridoma growth and monoclonal antibody production in serum-limited cultures

A quantitative study of the influence of initial serum concentration on hybridoma growth rate, maximum viable and total cell yield, and specific antibody production rate is presented. The specific growth rate varied in a Monod fashion with initial serum levels (2-10% FCS), giving K(m) = 1.6 v/v% and mu(max) = 0.92 d(-1). The maximum cell yields (total and viable) were linear with initial serum level, indicating stoichiometric as well as kinetic limitation by serum component(s). The specific antibody production rate for each individual run fitted well to a non-growth-associated model. However, the non-growth-associated parameter varied monotonically with initial serum concentration, suggesting the catalytic role of serum component(s) in antibody production. Also, glutamine was utilized inefficiently, with at least a third of it secreted back into the culture supernate in the form of glutamate. While very simple model equations describe the specific growth and product formation rate for an individual batch run, the larger picture indicates need for a more detailed unstructured or structured model.     

Comparison of specific rates of hybridoma growth and metabolism in batch and continuous cultures

For the mouse hybridoma cell line VO 208, kinetics of growth, consumption of glucose and glutamine, and production of lactate, ammonia and antibodies were compared in batch and continuous cultures. At a given specific growth rate, different metabolic activities were observed: a 40% lower glucose and glutamine consumption rate, but a 70% higher antibody production rate in continuous than in batch culture. Much higher metabolic rates were also measured during the initial lag phase of the batch culture. When representing the variation of the specific antibody production rate as a function of the specific growth rate, there was a positive association between growth and antibody production in the batch culture, but a negative association during the transient phase of the continuous culture. The kinetic differences between cellular metabolism in batch and continuous cultures may be result of modifications in the physiology and metabolism of cells which, in continuous cultures, were extensively exposed to glucose limitations.Institut National Polytechnique de Lorraine, ENSAIA BP 172, 2 avenue de la forêt de Haye, 54505, Vandoeuvre Cedex France     

A study of hybridoma cell growth and antibody production kinetics in continuous culture

Summary A detailed study of cell growth and antibody production kinetics in continuous culture found that the specific rate of antibody production reached a maximum saturated profile at a specific growth rate less than the maximum. This observation is novel and of importance in the understanding of the mechanism of antibody production and/or antibody transport.     

Growth and production modeling in hybridoma continuous cultures

Several experimental data on continuous cultures of hybridoma cells show that monoclonal antibody productivity is a decreasing function of dilution rate. It has been suggested that this unusual behavior may be due to the arrest of a fraction of cycling cells at a critical point of Phase G(1). Although this hypothesis has been recently investigated by using population balance models, mathematical analysis has been performed without accounting for the dynamics of the arrested cells properly. In this article, a more general and accurate approach is presented and new specific assumptions are introduced to characterize the arrest and the later progress through the cycle. Two different models (stochastic and deterministic) and two different critical points for the arrest (at the beginning and at the end of G(1)) are considered. The cell cycle parameters are estimated so that data predicted by the model fit those reported in the literature. In particular, the fraction of arrested cells, the cell arrest probability, and the mean cell generation time are computed as functions of the dilution rate. Results so far obtained predict that there is an optimal value of dilution rate for maximizing specific production rate of monoclonal antibody. (c) 1993 John Wiley & Sons, Inc.     

Factors affecting growth and product formation in plant cells grown in continuous culture

In the present work we examined the potential benefits of the continuous culture (chemostat) technique at improving biomass yields of Mentha and Dioscorea cells and product formation (diosgenin) by Dioscorea cells. In contrast to Mentha cells, Dioscorea cells were sensitive to mechanical agitation in the exponential growth phase and could only be grown in a bubble column type fermentor. Maximal biomass yield of 0.5 and 0.4 g cell dry weight g^?1sucrose were obtained for Mentha and Dioscorea cells, respectively. When the phosphate concentration during the growth phase of Dioscorea was increased, a maximal concentration of 7.8% diosgenin (of dry weight) was obtained. Productivity of diosgenin was 12 mg 1^?1 day^?1 in a two-stage continuous process as compared to 7.3 mg 1^?1 day^?1 in a batch culture.     

High-density continuous cultures of hybridoma cells in a depth filter perfusion system

A depth filter perfusion system (DFPS) for animal cell culture was developed and its use in continuous highdensity cultures of hybridoma cells was investigated. In the DFPS, based on cell immobilization in a cylindrical depth filter matrix, cells were easily immobilized and cultivated by simple medium recirculation. The cell density in the 20-mum pore size filter matrix reached up to 3 x 10(7) cells/mLin less than 10 days. This resulted in a high monoclonal antibody productivity of 744 mg/L/day, which was 25-35 times higher than that of continuous-suspension cultures using the same cell line. The 20-mum pore filter retained more cells than the 30-mum filterin a shorter period. The DFPS provides advantages of low-cost set-up, easy operation, and scale-up in the cultures of anchorage-independent cells. It also has a high potential for anchorage-dependent cell cultures because of its unusually high surface-to-volume ratio of 450-600 cm(2)/cm(3). (c) 1994 John Wiley & Sons, Inc.     

Effects on growth behavior in continuous hybridoma cell cultures: The role of viral contamination

This article describes the retrovirus expression with optimal nutrient supply and its potential growth inhibition effects in continuous hybridoma cell cultivation. A special reactor setup with total cell retention was developed to examine growth inhibition effects. Using this fermentation strategy we observed a decrease of viability cell rate which occurred at a defined state of the process despite sufficient nutrient supply. Therefore we assume that inhibitory substances are responsible for these effects. The molecular weight range of the inhibitory substances and the possible retrovirus cooperation of these growth inhibition effects were examined. To determine the molecular weight range we used the following methods: ultrafiltration, gelfiltration, ultracentrifugation and gel electrophoresis. Furthermore, RT-PCR and western-/immunoblot are used to detect retrovirus particles in the supernatant and to show a retrovirus participation on growth inhibition effects. The possible growth modulation was tested in a biological assay (MTT-assay). This revised version was published online in August 2006 with corrections to the Cover Date.     

Cell cycle model for growth rate and death rate in continuous suspension hybridoma cultures

As a result of recent advances in flow cytometry, renewed interest is shown in modeling the kinetic behavior of cells in culture on the basis of cell cycle parameters. An important but often overlooked kinetic variable in hybridoma cultures is the cell death rate. Not only the overall cell growth but also the kinetics of nutrient metabolism and monoclonal antibody production have been shown to depend on the cell death rate in continuous suspension hybridoma cultures. The present study shows that the death rate in hybridoma cultures is proportional to the fraction of cells arrested in the G(1) phase of the cell cycle. The steady-state cell age distributions in the various phases of the division cycle have been calculated analytically. A simple mathematical model has been used to produce the profiles of the cycling and arrested cell fractions with respect to the dilution rate. The calculated steady-state growth rate, death rate, and viability profiles are shown to be in agreement with recently published experimental data from continuous suspension hybridoma cultures. (c) 1992 John Wiley & Sons, Inc.     

Bcl-2 over-expression reduces growth rate and prolongs G1 phase in continuous chemostat cultures of hybridoma cells.

Recent studies have suggested that Bcl-2 can affect cell cycle re-entry by inhibiting the transition from G0/G1 to S phase. In this study, we have taken a novel route to the study of the relationship between Bcl-2 expression and cell cycle progression. Continuous cultures of pEF (control) and Bcl-2 transfected murine hybridoma cells were operated at a range of dilution rates from 0.8 day-1 down to 0.2 day-1. The specific growth rate of the pEF cell line was the same as the dilution rate down to a value of 0.6 day-1. However, as the dilution rate was reduced stepwise to 0.2 day-1, the growth rate levelled-off at approximately 0.55 day-1 and this coincided with a fall in culture viability. By contrast, the specific growth rate of the Bcl-2 transfected cell line followed the dilution rate down to a value of 0.3 day-1 with high levels of cell survival. At high dilution rates, the cell cycle distributions were very similar for both cell lines. However, the distributions diverged as the dilution rate was reduced and, at a rate of 0.2 day-1, the percentage of G1 cells in the Bcl-2 culture was 80%, compared to only 56% in the pEF cell population. This corresponded with a greater extension in the duration of the G1 phase in the Bcl-2 cells, which was 1.7 days at the lowest dilution rate tested, compared to only 0.6 day for the pEF cell line. The durations of the G2/M and S phases remained constant throughout the culture. The maximum doubling time was 1.2 days in the pEF culture compared to 2.3 days in the Bcl-2 culture. Analysis of amino acids, ammonia and lactate concentrations indicated that the observed effects on cell cycle dynamics were probably not due to differences in the culture environment. It is suggested that the expression of Bcl-2 can effect G1 to S phase transition in continuously cycling cells, but this is only apparent at suboptimal growth rates.     

Shear sensitivity of hybridoma cells in batch, fed-batch, and continuous cultures.

Previously, we observed that CRL-8018 hybridoma cells were more sensitive to well-defined viscometric shear during the lag and stationary phases than during the exponential phase of batch cultures. Some potential hypotheses for explaining the increase in shear sensitivity are (1) nutrient limitations that result in a decrease in production of specific cellular components responsible for the mechanical strength of the cell, (2) nutrient limitations that lead to synchronization of the culture in a cell cycle phase that is more sensitive to shear, or (3) a link between cell growth and shear sensitivity, such that slowly growing cells are more sensitive to shear. Here, the duration of the exponential phase was increased with use of fed-batch, and the effect on shear sensitivity of the cultures was measured with a viscometric technique. Extension of exponential growth resulted in an increased period during which the cells were insensitive to shear. Additionally, the shear sensitivity of the cells was constant over a wide range of growth rates and metabolic yields in chemostat cultures. These observations suggest that as long as the cells are actively (exponentially) growing, their shear sensitivity does not depend on the growth rate or metabolic state of the cell as expressed by metabolic yields. Thus, hypothesis 3 above can be dismissed.     

Determination of cell lysis and death kinetics in continuous hybridoma cultures from the measurement of lactate dehydrogenase release

The death of the hybridoma VO 208 in a continuous culture at pH 7 and 6.8 was investigated by measuring both the appearance of visible dead cells which do not exclude the trypan blue dye and the release of lactate dehydrogenase (LDH) in the culture medium. The intracellular LDH was found to be completely released either when live cells lysed or when they were transformed into visible dead cells. No significant lysis of blue dead cells could be observed at the two different pH. Using a LDH balance over the culture system, cell lysis was found negligible at pH 7, but accounted for 20% of the total cell death at pH 6.8. A methodology is proposed to evaluate the rate constants of hybridoma lysis and total death. For the investigated cell line in continuous culture, the calculated total cell death rate constant was found to increase from 0.002 h^–1 to 0.01 h^–1 when decreasing the pH from 7 to 6.8.Abbreviations D dilution rate (h^–1) - k_b specific trypan-blue dead cells appearance rate (h^–1) - k_L specific lysis rate of viable cells (h^–1) - k_d specific death rate (h-1) - LDH₀ lactate dehydrogenase activity in the feed culture medium (IU.l^–1) - LDH lactate dehydrogenase activity in the outlet culture medium (IU.l^–1) - LDH_i intracellular lactate dehydrogenase activity of viable cells (IU.10^–9 cells) - r_LDH total rate of LDH release (IU.h^–1.L^–1) - r_b transformation rate of viable cells into blue dead cells (10⁹ cells.h^–1.L^–1) - x_v viable cell concentration (10⁹ cells.l^–1) - x_b trypan-blue dead cell concentration (10⁹ cells.l^–1)     

Determinants and rate laws of growth and death of hybridoma cells in continuous culture

Experimental data from six hybridoma cell lines grown under diverse experimental conditions in both normal continuous and perfusion cultures are analyzed with respect to the significance of nutrients and products in determining the growth and death rates of cells and with respect to their mathematical modeling. It is shown that neither nutrients (glucose and glutamine) nor the common products lactic acid, ammonia, and monoclonal antibody can be generally assumed to be the clear-limiting or inhibiting factors for most of the cultures. Correspondingly, none of the unstructured models existing in the literature can be generally applied to describe the experimental data obtained over a relatively wide range of cultivation conditions as considered in this work. Surprisingly, for all cultures the specific growth rate (mu) almost linearly correlates with the ratio of the viable cell concentration (NV) to the dilution (perfusion) rate (D). Similarly, the specific death rate (kd) is a function of the ratio of the total cell concentration (Nt) to the dilution (perfusion) rate. These results strongly suggest the formation of not yet identified critical factors or autoinhibitors that determine both the growth and death rates of hybridoma cells. Based on these observations, simple kinetic models are developed for mu and kd which describe the experimental data satisfactorily. Analysis of the experimental data with the kinetic models reveals that under the current cultivation conditions the formation rate of the autoinhibitor(s) or the sensitivity of cell growth and death to the autoinhibitor(s) is mainly affected by the medium composition. Irrespective of the cell lines, cells grown on serum-containing media have almost the same model parameters, which are distinctively different from those of cells grown on serum-free media. Furthermore, in contrast to the prevailing view, kd is shown to positively correlate with mu if the effects of cell concentration and dilution (perfusion) rate are considered. Several important implications of these findings are discussed for the optimization and control of animal cell culture.     

Comparison of growth kinetics of producing and nonproducing hybridoma cells in batch culture.

Several clones of nonproducing cells were isolated from a continuous culture of hybridoma cells, which were originally producing antibody. Their behavior was compared to that of the producing cells in batch culture. The growth kinetics of five out of six clones exhibited higher specific growth rate, higher yield of cell mass on glutamine, and lower yields of lactate and ammonium. The implications of the comparisons for growth of hybridoma cultures are discussed.     

Actual and potential rates of substrate oxidation and product formation in continuous cultures ofChromatium vinosum

Kinetics of electron-donor oxidation, storage-polymer formation and growth were studied in continuous cultures ofChromatium under conditions of balanced growth as well as during transient states.Under steady-state conditions, glycogen was accumulated at all dilution rates. This observation is consistent with previously postulated ideas about an ineffective glycogen-synthesis regulation.Upon perturbing the steady states, brought about by injection of extra sulfide into steady-state cultures, the following phenomena were observed immediately, irrespective of the dilution rate: the specific rate of sulfide oxidation increased to the value found in batch cultures, the sulfur-oxidation rate was decreased, the specific glycogen-synthesis rate increased, the increment being higher the lower the dilution rate, but an increase in the specific growth rate, if any, was below the limit of detection. The inverse relationship between the specific rates of glycogen synthesis and growth after removing the substrate limitation is to be explained by a shortage of intermediates, rather than by a growth-rate dependent intrinsic glycogen-synthesis limitation, because upon complete inhibition of growth a further increase in the rate of glycogen synthesis was observed. Essayed in this way, identical glycogen-synthesis rates were found at all dilution rates.Competitive advantages of such an apparently not adapted metabolism in environments with diurnal fluctuations in substrate concentrations are discussed.Non-Standard Abbreviations N_c cell nitrogen - TS total sugar - PHB poly--hydroxybutyrate - D dilution rate - S_R reservoir concentration of the growth-limiting substrate - CAP chloramphenicol     

Viability measurements of hybridoma cells in suspension cultures

Several methods were applied to determine the viability of hybridoma cells in suspension. These methods include dye inclusion and exclusion assays such as the classical trypan blue exclusion assay, the propidium iodide (PI) exclusion assay and the fluorescein diacetate (FDA) inclusion assay. Furthermore, the relation was studied between release of lactate dehydrogenase (LDH) by hybridoma cells and their viability. Also the ATP content of the cells and cellular heterogeneity as measured with a flow cytometer were determined in relation to cellular viability. The dye inclusion and exclusion assays using trypan blue, FDA, PI were shown to be useful methods to determine cellular viability. With the FDA and PI methods it was possible to obtain additional information about cells which are in a transition state between viable and non-viable. The viability according to the scatter properties of the cells appears to reflect the overall condition of the cells, although interpretation of the results is difficult. Measurement of LDH release in the culture fluid or the cytoplasmic ATP content could not be used as parameters for cell viability.     

Induction of apoptosis in oxygen-deprived cultures of hybridoma cells

It is now well documented that apoptosis represents the prevalent mode of cell death in hybridoma cultures. Apoptotic or programmed cell death occurs spontaneously in late exponential phase of batch cultures. Until lately, no specific triggering factors had been identified. Recently, we observed that glutamine, cystine or glucose deprivation induced apoptosis in both hybridoma and myeloma cell lines whereas accumulation of toxic metabolites induced necrotic cell death in these cells. Other triggering factors such as oxygen deprivation might also be responsible for induction of apoptosis. In the present study, induction of cell death by exposure to anoxia was examined in batch culture of the SP2/0-derived hybridoma D5 clone. The mode of cell death was studied by morphological examination of acridine orange-ethidium bromide stained cells in a 1.5 L bioreactor culture grown under anoxic conditions for 75 hours. Under such conditions, viable cell density levelled off rapidly and remained constant for 25 hours. After 45 hours of anoxia, cell viability had decreased to 30% and the dead cell population was found to be 90% apoptotic. In terms of cellular metabolism, anoxia resulted in an increase in the utilization rates of glucose and arginine, and in a decrease in the utilization rate of glutamine. The lactate production rate and the yield of lactate on glucose increased significantly while the MAb production rate decreased. These results demonstrate that glycolysis becomes the main source of energy under anoxic conditions.Cells incubated for 10 hours or less under anoxic conditions were able to recuperate almost immediately and displayed normal growth rates when reincubated in oxic conditions whereas cells incubated for 22 hours or more displayed reduced growth rates. Nonetheless, even after 22 h or 29 h of anoxia, cells reincubated in oxic conditions showed no further progression into apoptosis. Therefore, upon removal of the triggering signal, induction of apoptosis ceased.Abbreviations VNA Viable non-apoptotic cells - VA Viable apoptotic cells - NVNA Nonviable non-apoptotic or necrotic cells - NVA Nonviable apoptotic cells - CF Chromatin-free cells (late nonviable apoptotic cells) - AO Acridine orange - EB Ethidium Bromide - MAb Monoclocnal antibody - D.O. Dissolved oxygen - qMAb Specific MAb production rate (mg. (10⁹ cells)^–1.day^–1) - Specific growth rate (h^–1) - X_v Viable cell number (10⁵ cells.mL^–1) - X_t Total cell number (10⁵ cells.mL^–1) - Y_lac/glc Yield coefficient of lactate on glucose (mM lactate produced/mM glucose consumed)     

Cultivation of hybridoma cells in an inclined bioreactor

Murine hybridoma cells were grown in a bubble column that was inclined up to 45 degrees from vertical. Inclining the column by a few degrees separated the rising bubbles against the upper surface, leaving the bulk of the liquid bubble free. The liquid was circulated well by the rising bubbles, but collection of cells by rising bubbles and exposure of cells to bursting bubbles were minimized. Maximum viable cell count and exponential growth of the cells were not affected by inclination, but an inclination of 30 degrees gave an antibody titer of 42 mg/L, which more than doubled the yield of 17 mg/L in the vertical position. By comparison, the culture gave yields of 30 mg/L when grown in spinner flasks. The enhanced antibody production in the inclined bioreactor corresponded to a prolonged stationary phase of 45 h. (c) 1995 John Wiley & Sons, Inc.     

Maturity and product formation in cultures of microorganisms

The concept of a maturation time (t_m) for a product formation by a microbial culture is developed and a simple method is described for determining this parameter and also the product formation rate constant (k_p) from batch culture experiments. The concept has been utilized in a general model for the prediction of steady state product concentrations in single-stage continuous-flow culture systems.