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.     

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.     

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.     

Modulation of hybridoma cell growth and antibody production by coating cell culture material with extracellular matrix proteins

The influence of coating polystyrene tissue culture plates with different proteins on murine hybridoma cell growth and antibody production was investigated. Fibronectin, collagen I, bovine serum albumin and laminin were used to coat NUNC^® and COSTAR^® cell culture plates. Cell number and antibody concentration in culture fluids were quantified as indicators for cell viability, proliferation and productivity. Adhesive behaviour, morphology, expression of surface receptors of hybridoma cells and the presence of tyrosine-phosphorylated proteins in cell lysates were characterized by cell adhesion experiments, microscopy, flow cytometry and Western Blot analysis.It was shown that coatings with fibronectin (0.2 μg/ml) lead to a substantial improvement of cell growth by 50–70% and an increase of monoclonal antibody production by 100–120%.Collagen I coatings showed an improvement in cell growth by 30–70% and by 60% for the production of monoclonal antibodies. Coatings with BSA and laminin had minor effects on these parameters. It was found that the hybridoma cell lines used in this study did not express the α₂-chain of the α₂β₁-integrin, which is responsible for binding to collagen and laminin.However, the presence of β₁-integrin on the cell surface was shown, which should enable hybridoma cells to bind fibronectin. We propose, therefore, that fibronectin adsorption to cell culture materials may be a promising approach to enhance the production of monoclonal antibodies by cultivated hybridoma cells.     

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.     

Enhancement effects of BSA and linoleic acid on hybridoma cell growth and antibody production

The effects of linoleic acid and bovine serum albumin on hybridoma cell growth and antibody production were investigated. In dish cultivation, linoleic acid on its own promoted cell growth when used at concentrations below 50 mg L^–1, but strongly inhibited growth at a concentration of 100 mg L^–1 on more. However, linoleic acid bound to bovine serum albumin did not inhibit cell growth, even at a concentration as high as 100 mg L^–1. Also, linoleic acid did not affect the specific antibody production rate, with or without bovine serum albumin. In order to elucidate the enhancement of antibody production by bovine serum albumin, fractions were prepared by ultrafiltration (98% molecular weight cut-offs, 50,000 and 17,000) and the effects of the fractionation on antibody production were studied in batch cultivation. The high-molecular-weight fraction (50,000) promoted antibody production whereas the low-molecular-weight fraction (17,000) inhibited it. In continuous cultivation, the high-molecular-weight fraction was also found to enhance antibody production.     

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.     

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.     

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.     

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.     

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.     

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.     

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%.     

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.     

Enhancement of monoclonal antibody production by immobilized hybridoma cell culture with hyperosmolar medium

To determine the effect of hyperosmotic stress on the monoclonal antibody (MAb) production by calcium-alginate-immobilized S3H5/gamma2bA2 hybridoma cells, the osmolalities of medium in the MAb production stage were varied through the addition of NaCI. The specific MAb productivity (q(MAb)) of immobilized cells exposed to abrupt hyperosmotic stress (398 mOsm/kg) was increased by 55% when compared with that of immobilized cells in the control culture (286 mOsm/kg). Furthermore, this enhancement of q(MAb) was not transient. Abrupt increase in osmolality, however, inhibited cell growth, resulting in no increase in volumetric MAb productivity (r(MAb)). On the other hand, gradual increase in osmolality allowed further cell growth while maintaining the enhanced q(MAb) immobilized cells. The q(MAb) immobilized cells at 395 mOsm/kg was 0.661 +/- 0.019 mug/10(6) cells/h, which is almost identical to that of immobilized cells exposed to abrupt osmotic stress. Accordingly, the r(MAb) was increased by ca. 40% when compared with that in the control immobilized cell culture. This enhancement in i(MAb) of immobilized S3H5/gamma2bA2 hybridoma cells by applying gradual osmotic stress suggests the potential of using hyperosmolar medium in other perfusion culture systems for improved MAb production. (c) 1995 John Wiley & Sons, Inc.     

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.