Relationship between hybridoma growth and monoclonal antibody production.

Factors affecting cell growth and antibody production in a mouse hybridoma were investigated. Antibody was produced during the growth and decline phases of a batch culture with an increase in the specific rate of antibody production during the decline phase. The specific rate of antibody production was also increased in cells arrested by 2 mM thymidine, suggesting that cell proliferation and antibody production can be uncoupled. Reduced serum concentrations resulted in lower cell growth rates but increased antibody production rates. However, this trend was reversed in hybridomas which had been arrested by thymidine, since the highest antibody production rate was associated with high serum concentrations. Likewise, in proliferating cells, the optimum pH for antibody production (pH 6.8) was lower than the optimum pH for cell growth (pH 7.2), whereas in thymidine-blocked cells, the highest antibody production rate was at pH 7.2. High antibody production rates and product yields were also associated with low growth rates in continuous cultures. The possibility that antibody was under cell cycle control was investigated in synchronized hybridoma cultures. Antibody production occurred during G1 and G2 with a decline in the M phase and evidence of a further decline in the S phase. Thus antibody production was not restricted to the G1 and S phase in this hybridoma.     

Media for hybridoma growth and monoclonal antibody production

For the economical production of monoclonal antibodies (MAbs), the cell-culture medium must be optimized for three different phases: growth of the hybridomas, MAb productivity of the hybridomas, and MAb purification or downstream processing. Medium improvements are necessary to meet these requirements for large-scale MAb production. Information bearing on this issue is being addressed in two research areas, cell biology and biochemical engineering, and is reviewed in this article.     

Effects of CO2 and osmolality on hybridoma cells: growth, metabolism and monoclonal antibody production

CO2 partial pressure (pCO2) in industrial cell culture reactors may reach 150–200 mm Hg, which can significantly inhibit cell growth and recombinant protein production. Due to equilibrium with bicarbonate, increased pCO2 at constant pH results in a proportional increase in osmolality. Hybridoma AB2-143.2 cell growth rate decreased with increasing pCO2 in well-plate culture, with a 45% decrease at 195 mm Hg with partial osmolality compensation (to 361 mOsm kg- 1). Inhibition was more extensive without osmolality compensation, with a 63% decrease in growth rate at 195 mm Hg and 415 mOsm kg-1. Also, the hybridoma death rate increased with increasing pCO2, with 31- and 64-fold increases at 250 mm Hg pCO2 for 401 and 469 mOsm kg- 1, respectively. The specific glucose consumption and lactate production rates were 40–50% lower at 140 mm Hg pCO2. However, there was little further inhibition of glycolysis at higher pCO2. The specific antibody production rate was not significantly affected by pCO2 or osmolality within the range tested. Hybridomas were also exposed to elevated pCO2 in continuous culture. The viable cell density decreased by 25–40% at 140 mm Hg. In contrast to the well-plate cultures, the death rate was lower at the new steady state at 140 mm Hg. This was probably due to higher residual nutrient and lower byproduct levels at the lower cell density (at the same dilution rate), and was associated with increased cell-specific glucose and oxygen uptake. Thus, the apparent effects of pCO2 may vary with the culture system. VMdZ and RK contributed equally to the results in this article. This revised version was published online in August 2006 with corrections to the Cover Date.     

Effect of hypoosmotic stress on hybridoma cell growth and antibody production

To investigate the response of hybridoma cells to hypoosmotic stress, S3H5/gamma2bA2 and DB9G8 hybridomas were cultivated in the hypoosmolar medium [Dulbecco's modified Eagle's medium (DMEM) supplemented with 10% serum] resulting from sodium chloride subtraction. Both hybridomas showed similar responses to hypoosmotic stress in regard to cell growth and antibody production. The cell growth and antibody production at 276 mOsm/kg were comparable to those at 329 mOsm/kg (standard DMEM). Both cells grew well at 219 mOsm/kg, though their growth and antibody production were slightly decreased. When the osmolality was further decreased to 168 mOsm/kg, the cell growth did not occur. When subjected to hyperosmotic stress, both cells displayed significantly enhanced specific antibody productivity (q(Ab)). However, the cells subjected to hypoosmotic stress did not display enhanced q(Ab). Taken together, both hyperosmotic and hypoosmotic stresses depressed the growth of S3H5/gamma2bA2 and DB9G8 hybridomas. However, their response to hypoosmotic stress in regard to q(Ab) was different from that to hyperosmotic stress. (c) 1997 John Wiley & Sons, Inc. Biotechnol Biong 55: 565-570, 1997.     

Effect of anchorage dependency on growth rate and monoclonal antibody production of hybridoma cells

Hybridoma cells (S3H5/2bA2) are found to grow either in suspension or as attached to the surface of cell culture T flask. Cell growth rates and monoclonal antibody (MAB) production rates of both suspended and attached cells were examined. Although the percentage of viable cells was higher for the attached cells, cells growing in suspension showed almost the same charateristics as cells attached to the flasks with respect to cell growth and MAB production rate. Cell attachment increased with increasing serum concentrations up to 5% and remained essentially constant at cell densities of about 2·10⁵/cm².No differences in cell growth rate and MAB production could be attributed to anchorage dependent growth.     

A flow-cytometric analysis of hybridoma growth and monoclonal antibody production

A flow cytometric kinetic study of hybidoma growth and monoclonal antibody production is presented, along with the influence of glutamine on intracellular responses such as (relative) cell size, and cell RNA and total protein content. Specific findings are: (1) RNA content remained constant throughout the growth phase, then fell drastically as the cells entered the stationary phase. Also, in stationary phase, RNA content of antibody-producing cells was higher than for those not secreting antibody. (2) The cell size was constant and maximal throughout exponential phase, and diminished monotonically during later stages. (3) Average protein and antibody cellular content declined dramatically upon glutamine exhaustion. Thus, relative RNA levels and cell size provided quantitative determinants of both cell growth state and antibody secretion conditions. These results encourge consideration of structured kinetic studies which recognize the quality of the biophase.     

Effects of growth factors on cell proliferation and monoclonal antibody production of batch hybridoma cultures

Summary Effects of growth factors such as EGF, FGF and IL-2 on cell proliferation and monoclonal antibody production in a hybridoma cell line adapted to a completely defined serum-free medium were determined in batch cultures. The results indicate that the presence of growth factors in the medium enhances the antibody secretion without significantly affecting the growth rate. The specific antibody secretion rate of cells grown in serum-free medium supplemented with growth factors was 35% higher than those grown in serum-free medium alone.     

Effects of dissolved oxygen on hybridoma cell growth, metabolism, and antibody production kinetics in continuous culture.

The effects of dissolved oxygen concentration (DO) on hybridoma cell physiology were examined in a continuous stirred tank bioreactor with a murine hybridoma cell line (167.4G5.3). Dissolved oxygen concentration was varied between 0% and 100% air saturation. Cell growth and viability, carbohydrate, amino acid, and energy metabolism, oxygen uptake, and antibody production rates were investigated. Cell growth was inhibited at both high and low DO. Cells could grow at 0% DO and maintain viability under a nitrogen atmosphere. Cell viability was higher at low DO. Glucose, glutamine, and oxygen consumption rates changed little at DO above 1% air saturation. However, the metabolic uptake rates changed below 1% DO, where growth became oxygen limited, and a Km value of 0.6% DO was obtained for the specific oxygen uptake rate. The metabolic rates of glucose, glutamine, lactate, and ammonia increased 2-3-fold as the DO dropped from 1% to 0%. Amino acid metabolism followed the same general pattern as that of glutamine and glucose. Alanine was the only amino acid produced. The consumption rates of amino acids changed little above 1% DO, but under anaerobic conditions the consumption rates of all amino acids increased severalfold. Cells obtained most of their metabolic energy from glutamine oxidation except under oxygen limitation, when glucose provided most of the energy. The calculated ATP production rate was only slightly influenced by DO and rose at 0% DO. Antibody concentration was highest at 35% DO, while the specific antibody production rate was insensitive to DO.     

Effects of ammonia and lactate on hybridoma growth, metabolism, and antibody production

The influence of ammonia and lactate on cell growth, metabolic, and antibody production rates was investigated for murine hybridoma cell line 163.4G5.3 during batch culture. The specific growth rate was reduced by one-half in the presence of an initial ammonia concentration of 4 mM. Increasing ammonia levels accelerated glucose and glutamine consumption, decreased ammonia yield from glutamine, and increased alanine yield from glutamine. Although the amount of antibody produced decreased with increasing ammonia concentration, the specific antibody productivity remained relatively constant around a value of 0.22 pg/cell-h. The specific growth rate was reduced by one-half at an initial lactate concentration of 55 mM. Although specific glucose and glutamine uptake rates were increased at high lacatate concentration, they showed a decrease after making corrections for medium osmolarity. The yield coefficient of lactate from glucose decreased at high lactate concentrations. A similar decrease was observed for the ammonia yield coefficient from glutamine. At elevated lactate concentrations, specific antibody productivities increased, possibly due to the increase in medium osmolarity. The specific oxygen uptake rate was insensitive to ammonia and lactate concentrations. Addition of ammonia and lactate increased the calculated metabolic energy production of the cells. At high ammonia and lactate, the contribution of glycolysis to total energy production increased. Decreasing external pH and increasing ammonia concentrations caused cytoplasmic acidification. Effect of lactate on intracellular pH was insignificant, whereas increasing osmolarity caused cytoplasmic alkalinization.     

The influence of cyclic nucleotides on hybridoma growth and monoclonal antibody production

Summary The influence of cyclic AMP and cyclic GMP, known regulatory mediators of cellular response, on hybridoma growth and monoclonal antibody production is studied. The cGMP-treated cells exhibited 41% higher specific antibody secretion rate, resulting in 52% higher antibody yields. Addition of 1 mM cAMP inhibited cellular growth but enhanced the specific production rate by 37%.     

Effect of ammonium ion and extracellular pH on hybridoma cell metabolism and antibody production

The effects of NH(4)Cl addition on batch hybridoma cell growth at different external pH values (pH(e)) were investigated in a bioreactor at constant pH and dissolved oxygen concentration. In agreement with measurements in flasks, changes in pH(e) over the range 6.8-7.6 had minor effects on growth. Addition of 3 mM NH(4)Cl had little effect on cell growth while 10 mM NH(4)Cl caused a substantial growth inhibition, Measurements of the effects of pH(e) and NH(4)Cl concentration on cell metabolism gave similar results for cells grown in flasks in an incubator and in the bioreactor. As pH(e) decreases, the integral cell yield on glucose increases. There is a correlation between the effects of pH(e) on glycolysis and previous measurements of its effects on intracellular pH (pH(i)). Increases in NH(4)Cl concentration were previously determined to decrease pH(i) and are shown here to decrease the integral cell yield on glucose. At all pH(e) values in the absence of NH(4)Cl, glutamine is depleted at the time the maximum cell density is reached. Both pH(e) decreases and NH(4)Cl concentration increases lead to decreases in the integral cell yield on glutamine. Changes in pH(e) and in the NH(4)Cl concentration that cause growth inhibition have no effect on the specific antibody production rate for cells grown in flasks in an incubator or in the bioreactor. Changes in the NH(4)Cl concentration have no effect on the quality of the antibody produced, to a first level of characterization.     

Rapamycin reduces hybridoma cell death and enhances monoclonal antibody production

Rapamycin was used as a medium additive to slow the progression of CRL 1606 hybridomas through the cell cycle, under the hypothesis that such a modulation might reduce cell death. Cell cycle distributions for CRL hybridomas in the G1 phase of the cell cycle ranged from 20% to 35% during batch, fed-batch, and continuous culture experiments, independent of culture time, dilution rate, growth rates, or death rates. Rapamycin, an mTOR signaling inhibitor, immunosuppressant, and G1-phase arresting agent, was identified and tested for efficacy in restraining cell cycle progression in CRL 1606 hybridoma cultures. However, in the presence of 100 nM rapamycin, the percentage of cells in the G1 phase of the cell cycle during fed-batch cultures was only increased from 28% to 31% in control cultures to 37% to 48% for those with rapamycin. Accordingly, rapamycin only slightly reduced culture growth rate. Instead, the use of rapamycin more notably kept viability higher than that of control cultures by delaying cell death for 48 h, thereby enabling viable proliferation to higher maximum viable cell densities. Furthermore, rapamycin enhanced specific monoclonal antibody production by up to 100% during high-viability growth. Thus, over the course of 6-day fed-batch cultivations, the beneficial effects of rapamycin on viable cell density and specific productivity resulted in an increase in final monoclonal antibody titer from 0.25 to 0.56 g/L (124%). As rapamycin is reported to influence a much broader range of cellular functions than cell cycle alone, these findings are more illustrative of the influence that signal transduction pathways related to mTOR can have on overall cell physiology and culture productivity.     

Co-culture of the 55-6 B cell hybridoma with the EL-4 thymoma cell. Effect on cell growth and monoclonal antibody production

The cell growth and monoclonal antibody production of the 55-6 hybridoma cell co-cultured with the murine thymoma cell line EL-4 at different initial 55-6:EL-4 ratios were investigated. Both populations were seeded in co-culture without previous stimulation and therefore with low constitutive CD40 and CD40 ligand (CD154) expression levels, and in the absence of exogenous co-stimuli. Viable cell density and growth rate data seem to suggest a competition for nutrients, which is detrimental for both cells in terms of biomass production and also of growth rate for 55-6. Final concentrations of antibody and specific antibody production rates were affected by the initial 55-6:EL-4 ratio. The 4:1 ratio yielded the highest IgG2a concentration, whereas the highest specific antibody production rate was obtained at the 2:1 ratio. Changes mainly in CD154 and also in CD40 expression in co-cultures could suggest cross-talk between both populations. In conclusion, different types of interactions are probably present in this co-culture system: competition for nutrients, cognate interaction and/or autocrine or paracrine interactions that influence the proliferation of both cells and the hybridoma antibody secretion. We are hereby presenting a pre-scale-up process that could speed up the optimization of large-scale monoclonal antibodies production in bioreactors by emulating the in vivo cell–cell interaction between B and T cells without previous stimulation or the addition of co-stimulatory molecules.     

Continuous hybridoma growth and monoclonal antibody production in hollow fiber reactors-separators

Growth of a hybridoma culture, along with production of monoclonal antibody, was demonstrated over extended periods in polysulfone hollow fiber membrane modules. The molecular weight cutoffs of the membranes were 70,000, 50,000, and 100,000 daltons. The hybridoma cell line, designated 65/26, produced IgG (2b/kappa) directed at mouse thymus cell surface antigen, TL.1. Cell growth occurred in the shell space of the reactor, using supplemented RPMI 1640 (20% fetal bovine serum) supplied from a separate reservoir vessel through the hollow fiber lumen. The reservoir contained 125 mL media, which was changed every 4 days. Concentrations of immunoglobulin were determined by an enzyme immunoassay (using protein A and alkaline phosphatase-labeled antibody conjugate). For the 10K, 50K, and 100K hollow fiber membrane modules, the maximum IgG concentrations detected in the 2.5-mL shell space were 47.5-80, 510, and 740 mug/mL, respectively. In the 125-mL reservoir for the 100K hollow fiber membrane module, the IgG concentration was measured at 260 mug/mL These values compare with an IgG concentration of 1 mug/mL when grown in a standard tissue culture flask and 3.2-7.6 mug/mL when grown in 100 ml media in a spinner flask. In addition, 10K and 50K hollow fiber membrane modules were run in a mode that decreased the fetal bovine serum supplement with time. Differences between these systems suggest that it is possible to obtain high IgG accumulation rates, both during and after the exponential growth phase of the hybridoma population.     

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.     

Kinetic analysis of hybridoma growth and monoclonal antibody production in semicontinuous culture

Hybridoma I.13.17 was grown in semicontinuous culture in an attempt to investigate the steady-state concentrations of key components of monoclonal antibody (MAb) synthesis (e.g., intracellular MAb, IgG messenger RNAs) at different dilution rates between 0.008 and 0.055 h(-1). There was a general trend of increasing steady-state levels of total cytoplasmic RNA, total cell-associated MAb or cytoplasmic MAb, DNA synthesis rate, cellular metabolic activity, heavy (H-) and light (L-) chain IgG mRNAs with the increase in dilution rates. Increase in the half-lives of H- and L-chain mRNAs with increase in dilution rates may be sufficient to account for their increasing levels found under the same conditions. The specific growth rate was profoundly affected by the dilution rate, particularly near the lower end of the dilution rate range. Linear relationships were observed between the steady-state amounts of total cell-associated MAb and the relative levels of H- and L-chain mRNAs. Material balances on intracellular MAb demonstrated an increasing percentage of antibody not released into the growth medium (e.g., stored within the cell or anchored to the cell membrane) with increasing dilution rate. The MAb production rate per cell decreased significantly with the increase in dilution rates. No correlation was found between the relative levels of H- or L-chain mRNAs and the specific MAb production rate. Possible implications of rate-limiting steps in MAb synthesis and secretion are discussed.     

The role of vitamins and amino acids on hybridoma growth and monoclonal antibody production

A balanced supplementation method was applied to develop a serum and protein- free medium supporting hybridoma cell batch culture. The aim was to improve systematically the initial formulation of the medium to prevent limitations due to unbalanced concentrations of vitamins and amino acids. In a first step, supplementation of the basal formulation with 13 amino acids, led to an increase of the specific IgA production rate from 0.60 to 1.07 pg cell⁻¹ h⁻¹. The specific growth rate remained unchanged, but the supplementation enabled maintenance of high cell viability during the stationary phase of batch cultures for some 70 h. Since IgA production was not growth- related, this resulted in an approximately4-fold increase in the final IgA concentration, from 26.6 to 100.2 mgl⁻¹. In a second step, the liposoluble vitamins E and K₃ were added to the medium formulation. Although this induced a slightly higher maximal cell concentration, it was followed by a sharp decline phase with the specific IgA production rate falling to 0.47 pg cell⁻¹ h⁻¹. However, by applying a second cycle of balanced supplementation with amino acids this decline phase could be reduced and a high cell viability maintained for over 300 h of culture. In this vitamin- and amino acid- supplemented medium, the specific IgA production rate reached a value of 1.10 pg cell⁻¹h⁻¹ with a final IgA concentration of 129.8 mgl⁻¹. The latter represents an increase of approximately5-fold compared to the non- supplemented basal medium. This revised version was published online in August 2006 with corrections to the Cover Date.     

Influence of hyperosmolar basal media on hybridoma cell growth and antibody production

To investigate the influence of hyperosmolar basal media on hybridoma response, S3H5/γ2bA2 and DB9G8 hybridomas were cultivated in a batch mode using hyperosmolar basal media resulting from additional sodium chloride supplementation. The basal media used in this study were IMDM, DMEM, and RPMI 1640, all of which are widely used for hybridoma cell culture. In IMDM, two hybridomas showed different responses to hyperosmotic stress regarding specific MAb productivity (q _MAb), though they showed similar depression of cell growth in hyperosmolar media. Unlike S3H5/γ2bA2 hybridoma, the q _MAb of DB9G8 hybridoma was not enhanced significantly around 390 mOsm kg^?1. The variation of basal media influenced DB9G8 hybridoma response to hyperosmotic stress regarding q _MAb. In IMDM, the q _MAb of DB9G8 hybridoma was increased by more than 200% when the osmolality increased from 281 to 440 mOsm/kg. However, in RPMI 1640 and DMEM, similar amplitude of osmolality increase resulted in less than 100% increase in q _MAb. The variation of basal media also influenced the cell growth in hyperosmolar medium. Both hybridomas were more tolerant against hyperosmotic stress in DMEM than in IMDM, which was found to be due to the high osmolality of standard DMEM. The osmolalities of standard IMDM and DMEM used for inocula preparation were 281 and 316 mOsm kg^?1, respectively. Thus, when the cells were cultivated at 440 mOsm kg^?1, the cells in IMDM experienced higher osmotic shock than in DMEM. By using the inoculum prepared at 317 mOsm kg^?1 in IMDM, S3H5/γ2bA2 cell growth at 440 mOsm kg^?1 in IMDM was comparable to that in DMEM. Taken together, the results obtained from this study show that the selection of basal media is an important factor for MAb production by employing hyperosmotic stress.