Effect of feed rate on growth rate and antibody production in the fed-batch culture of murine hybridoma cells

Batch and fed-batch cultures of a murine hybridomacell line (AFP-27) were performed in a stirred tankreactor to estimate the effect of feed rate on growthrate, macromolecular metabolism and antibodyproduction. Macromolecular composition was foundto change dynamically during batch culture ofhybridoma cells possibly due to active production ofDNA, RNA and protein during the exponential phase.Antibody synthesis is expected to compete with theproduction of cellular proteins from the amino acidpool. Therefore, it is necessary to examine therelationship between cell growth in terms of cellularmacromolecules and antibody production. In this study,we searched for an optimum feeding strategy bychanging the target specific growth rate in fed-batchculture to give higher antibody productivity whileexamining the macromolecular composition. Concentratedglucose (60 mM) and glutamine (20 mM) in DR medium(1:1 mixture of DMEM and RPMI) with additional aminoacids were fed continuously to the culture and thefeed rate was updated after every sampling to ensureexponential feeding (or approximately constantspecific growth rate). Specific antibody productionrate was found to be significantly increased in thefed-batch cultures at the near-zero specific growthrate in which the productions of cellular DNA, RNA,protein and polysaccharide were strictly limited byslow feeding of glucose, glutamine and other nutrients. Possible implications of these results are discussed.     

Biological responses of hybridoma cells to hydrodynamic shear in an agitated bioreactor.

Effects of long-term hydrodynamic shear on hybridoma cells were investigated in a 250-ml continuous stirred-tank reactor (CSTR). Cells grown at steady state were subjected to step changes in agitation rates. Cell viability, glucose consumption, and monoclonal antibody (MAb) production were determined at high agitation rates and compared with the control (100 rev min-1). Impeller tip speeds higher than 40 cm s-1 caused a significant drop in cell concentration and respiration activity, and increased lactate dehydrogenase (LDH) release to the culture medium. Also, high agitation speeds caused a decrease in MAb concentration and an increase in specific glucose consumption rate. The effects of dilution rate and serum concentration on the sensitivity of hybridoma cells to hydrodynamic shear were determined. Serum was found to protect the cells against shear damage and had a significant positive effect on hybridoma growth and MAb production. Shear damage on cells in CSTR was approximated to first-order kinetics. The death rate constant increased sharply at impeller tip speeds above 40 cm s-1.     

Optimization of the medium perfusion rate in a packed-bed bioreactor charged with CHO cells

In the present study, the optimal medium perfusion rate to be used for the continuous culture of a recombinant CHO cell line in a packed-bed bioreactor made of Fibra-Cel^® disk carriers was determined. A first-generation process had originally been designed with a high perfusion rate, in order to rapidly produce material for pre-clinical and early clinical trials. It was originally operated with a perfusion of 2.6 vvd during production phase in order to supply the high cell density (2.5×10⁷ cell ml⁻¹ of packed-bed) with sufficient fresh medium. In order to improve the economics of this process, a reduction of the medium perfusion rate by −25% and −50% was investigated at small-scale. The best option was then implemented at pilot scale in order to further produce material for clinical trials with an improved second-generation process. With a −25% reduction of the perfusion rate, the volumetric productivity was maintained compared to the first-generation process, but a −30% loss of productivity was obtained when the medium perfusion rate was further reduced to −50% of its original level. The protein quality under reduced perfusion rate conditions was analyzed for purity, N-glycan sialylation level, abundance of dimers or aggregates, and showed that the quality of the final drug substance was comparable to that obtained in reference conditions. Finally, a reduction of −25% medium perfusion was implemented at pilot scale in the second-generation process, which enabled to maintain the same productivity and the same quality of the molecule, while reducing costs of media, material and manpower of the production process. For industrial applications, it is recommended to test whether and how far the perfusion rate can be decreased during the production phase – provided that the product is not sensitive to residence time – with the benefits of reduced cost of goods and to simplify manufacturing operations.     

Effect of bioreactor angle and aeration rate on growth and hydromechanics parameters in bioreactor culture of ginseng suspension cells

Suspension cells of Panax ginseng C.A. Meyer were cultivated in 3-L balloon-type bubble bioreactors and the bioreactor with the angle of 90° at the bottom side was optimized. The gaseous composition in plant cell and tissue cultures is regarded as an important factor affecting the plant growth. Gas hold-up was remarkably higher in the bioreactor with an angle of 90° than the other ones. Aeration rates impacted on the growth ratio, the specific O₂ uptake rate (SOUR) of ginseng cells were investigated. 0.4 vvm was selected as the optimal aeration rate with a dry weight of 6.45 g L^?1. The specific O₂ uptake rate in the culture time was detected and reached the top value at the maximum growth ratio.     

Design and performance of a trickle-bed bioreactor with immobilized hybridoma cells

A trickle-bed system employing inert matrices of vermiculite or polyurethane foam packed in the downcomer section of a split-flow air-lift reactor has been developed for hybridoma culture to enhance antibody productivity. This quiescent condition favoured occlusion and allowed the cells to achieve densities twelve fold greater (12.8×10⁶ cells/ml reactor for polyurethane foam) than in free cell suspension. The reactor was operated in a cyclic batch mode whereby defined volumes of medium were periodically withdrawn and replaced with equal volumes of fresh medium. The pH of the medium was used as the indicator of the feeding schedule. Glucose, lactate and ammonia concentrations reached a stationary value after 5 days. With vermiculite packing, a monoclonal antibody (MAb) concentration of 2.4 mg/l was achieved after 12 days. The MAb concentration declined then increased to a value of 1.8 mg/l. In the polyurethane foam average monoclonal antibody (MAb) concentrations reached a stationary value of 1.1 mg/l in the first 20 days and increased to a new stationary state value of 2.1 mg/l for the remainder of the production. MAb productivity in the trickle-bed reactor was 0.3 mg/l·d (polyurethane foam) and 0.18 mg/l.d (vermiculite) in comparison to 0.12 mg/l·d for free cell suspension. This trickle-bed system seems to be an attractive way of increasing MAb productivity in culture.     

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.     

Effect of shear rate on hybridoma cell metabolism

The effect of shear rate on cell growth and monoclonal antibody production of hybridoma cells was studied. The dependence of agitation rate on antibody production is discussed by measuring the amount of monoclonal antibody in cells cultured by a spinner vessel. The effect of shear rate is also studied by exposing a homogeneous shear flow to hybridoma cells in a cone-and-plate viscometer. The dependence of shear rate on hybridoma cells was observed and the increase of antibody production was arised from the increase of secretion from cells.     

High density culture of hybridoma cells in a dual hollow fiber bioreactor

Summary Hybridoma cells were cultured for two months in the dual hollow fiber bioreactor (DHFBR) which had been successfully used for high cell density cultures of various microbial cells. In batch suspension culture the concentration of monoclonal antibody (Mab) against human Chorionic Gonadotropin (hCG) and the cell density of Alps 25-3 hybridoma cells were obtained in 30 μg/mL and 2.35×10⁶ cells/mL, respectively. The continuous culture with DHFBR produced Mab of 100–130 μg/mL for 30 days and the estimated cell density in the extracapillary space of DHFBR was 1.87×10⁸ cells/mL based on the antibody production rate. The productivity of Mab was 205 mg/day per litre of the total reactor volume while that of the batch suspension culture was only 10 mg/L day.     

Use of a spin-filter can reduce disruption of hybridoma cells in a bioreactor

Summary The possibility of damage to suspended cells arising from the introduction of a spin-filter rotating at high speed is examined experimentally and theoretically. Far from increasing damage, it is shown that a spin-filter, even when rotating at high speed, can markedly improve the survival of cells in a stirred unbuffled bioreactor. Analysis of the shear stress generated at the filter surface shows values that are orders of magnitude below those shown elsewhere to be damaging to cells. The improvement in survival seen in addition of a spin-filter to an impeller-agitated bioreactor are explained in terms of the events associated with the suppression of vortices, and bubble entrainment and disengagement.     

Effect of pulse frequency on the osteogenic differentiation of mesenchymal stem cells in a pulsatile perfusion bioreactor

Perfusion bioreactors are a promising in vitro strategy to engineer bone tissue because they supply needed oxygen and nutrients and apply an osteoinductive mechanical stimulus to osteoblasts within large porous three-dimensional scaffolds. Model two-dimensional studies have shown that dynamic flow conditions (e.g., pulsatile oscillatory waveforms) elicit an enhanced mechanotransductive response and elevated expression of osteoblastic proteins relative to steady flow. However, dynamic perfusion of three-dimensional scaffolds has been primarily examined in short term cultures to probe for early markers of mechanotransduction. Therefore, the objective of this study was to investigate the effect of extended dynamic perfusion culture on osteoblastic differentiation of primary mesenchymal stem cells (MSCs). To accomplish this, rat bone marrow-derived MSCs were seeded into porous foam scaffolds and cultured for 15 days in osteogenic medium under pulsatile regimens of 0.083, 0.050, and 0.017 Hz. Concurrently, MSCs seeded in scaffolds were also maintained under static conditions or cultured under steady perfusion. Analysis of the cells after 15 days of culture indicated that alkaline phosphatase (ALP) activity, mRNA expression of osteopontin (OPN), and accumulation of OPN and prostaglandin E(2) were enhanced for all four perfusion conditions relative to static culture. ALP activity, OPN and OC mRNA, and OPN protein accumulation were slightly higher for the intermediate frequency (0.05 Hz) as compared with the other flow conditions, but the differences were not statistically significant. Nevertheless, these results demonstrate that dynamic perfusion of MSCs may be a useful strategy for stimulating osteoblastic differentiation in vitro.     

Effect of culture temperature on follicle-stimulating hormone production by Chinese hamster ovary cells in a perfusion bioreactor

Follicle-stimulating hormone (FSH) was produced in Chinese hamster ovary (CHO) cells using a perfusion bioreactor. Perfusion culture at 37°C yielded a high cell density but a low FSH production. To investigate the effect of culture temperature in the range of 26–37°C on cell growth and FSH production, batch cultures were performed. Lowering culture temperature below 32°C resulted in growth suppression. However, specific productivity of FSH, q _FSH, increased as culture temperature decreased, and the maximum q _FSH of 43.4 ng/10⁶ cells/h was obtained at 28°C, which is 13-fold higher than that at 37°C. Based on the results obtained from batch cultures, we performed perfusion cultures with two consecutive temperatures. CHO cells were grown up to 3.2 × 10⁷ cells/ml at 37°C and culture temperature shifted down to 28°C to obtain a high FSH titer. Soon after the maximum FSH titer of 21 μg/ml was achieved, a rapid loss of not only viable cell concentration but also cell viability was observed, probably due to the low activities of enzymes related to cell growth. Thus, the extension of production period at 28°C is critical for the enhancement of FSH production, and the use of antiapoptotic genes seems to be promising.     

High density culture of hybridoma cells using a perfusion culture vessel with an external centrifuge

The influence of centrifugal force on the growth of cells was examined by exposing the cells of the mouse-human hybridoma X87 line to centrifugal force (100–500 G) for ten minutes twice a day and comparing the static culture with that of unexposed cells. In this experiment, both cell proliferation and specific antibody productivity were independent of the centrifugal effect, and gave the same results as in the case of no exposure to centrifugal force. High density cultivation of the mouse-human hybridoma X87 line was obtained by a perfusion system where the cells were separated from the culture medium by continuous centrifugation. In the serum-free culture, the maximum viable cell density exceeded 10⁷ cells/ml, and monoclonal antibody was stably produced for 37 days. The results in this culture were equivalent to those obtained by intermittent centrifugal cell separation from the culture medium, and separation by gravitational settlement.     

Variable functions of bcl-2 in mediating bioreactor stress- induced apoptosis in hybridoma cells

It has been demonstrated that the cell lines used for production of biopharmaceuticals are highly susceptible to apoptosis, and that over-expression of the bcl-2 oncogene can protect cells from death. Stress associated with the deprivation of nutrients has been shown to be the main cause of apoptosis in culture. We have extended these studies by investigating the mechanism of cell death under conditions of sub-optimal pH, shear stress and hyperosmolarity, and the protective action of bcl-2 over-expression. At pH 6, there was no clear evidence of protection from cell death. However, at pH 8, the viability of the bcl-2 transfected cells was about 20% higher relative to the control cells. Cultivation of control cells in a flat bottomed bioreactor with a magnetic stirrer bar without a pivot ring resulted in exposure of the cells to a high attrition effect. As a result, cell growth was retarded and a high level of cell death by apoptosis was observed. Under the same conditions, the bcl-2 transfected cell line exhibited a nearly five fold increase in viable cell number. This finding indicates that under apoptosis-suppressed conditions, shear stress can stimulate cell growth. Batch cultivation of both control and bcl-2 transfected cells in 350 and 400 mOsm media resulted in suppression of cell growth, athough the effect was most marked in the control cell line. Adaptation of control cells to 400 mOsm proved to be impossible to achieve. However, the bcl-2 transfected cells exhibited resistance to the osmotic stress resulting in long term adaptation to a high salt environment. Specific productivity of bcl-2 transfected cells grown in high osmolarity medium was 100% higher than that produced by non- adapted bcl-2 transfected cells grown in normal osmolarity medium. These results demonstrate that bcl-2 has a beneficial effect on hybridoma cultivation under a wide range of culture stresses. This revised version was published online in August 2006 with corrections to the Cover Date.     

Modification of glucose and glutamine metabolism in hybridoma cells through metabolic engineering

The present work describes the genetic modification of a hybridoma cell line with the aim to change its metabolic behaviour, particularly reducing the amounts of ammonia and lactate produced by the cells. The cellular excretion of ammonia was eliminated by transfection of a cloned glutamine synthetase gene. The metabolic characterisation of the transformed cell line includes the analysis of the changes introduced in its intracellular metabolic fluxes by means of a stoichiometric model. Furthermore, the reduction of lactate accumulation was attempted through an antisense mRNA approach, aiming to generate a rate limiting step in the glycolytic pathway, thus lowering the glucose consumption rate. The physiological results obtained with the transformed cells are discussed. A maximum reduction of about 47% in the glucose consumption rate was obtained for one of the transformations. However a main drawback was the lack of stability of the transformed cells This revised version was published online in July 2006 with corrections to the Cover Date.     

Production of monoclonal antibodies by hybridoma cells in a flat sheet membrane bioreactor.

The purpose of this study was to investigate hybridoma growth and monoclonal antibody formation in a flat sheet membrane bioreactor. The effects of several different molecular weight cutoff membranes on growth and antibody formation were investigated. Nutrient and toxic product diffusion through the membranes were quantified, and the kinetic and physical constants of the system were determined.     

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.     

Optimization of fed-batch culture of hybridoma cells using dynamic programming: single and multi feed cases

The optimization of fed-batch culture of hybridoma cells is accomplished on a mathematical model using dynamic programming. Optimal feed trajectories are found using a seventh order model for a single feed stream containing both glucose and glutamine and for two separate feed streams of glucose and glutamine. Compared to a constant feed rate, optimal trajectories can improve the final MAb concentration by 11 % for the single feed case and by 20% for the multifeed case. Higher MAb concentrations can be expected for fed-batch optimization with feed enriched in nutrients.     

Effect of temperature change on the metabolic rate of an antarctic mite

Summary Measurements of metabolic rate in the terrestrial miteAlaskozetes antarcticus showed that the ability for metabolic temperature compensation is lacking in adults of this species. Animals cultured at 0 and 10°C displayed similar metabolic rates when transferred to 5 or 10°C, and individuals cultured at 0°C and measured at 0, 5 and 10°C showed the same metabolic response as animals cultured and measured at each of these temperatures. These findings, which suggest thatA. antarcticus does not regulate its metabolism in response to changes in temperature, are discussed in the context of the environmental temperature patterns experienced by the animal in the field.     

Effect of air flow rate on scleroglucan synthesis by Sclerotium glucanicum in an airlift bioreactor with an internal loop

The effects of several plant cell wall polysaccharides degrading enzymes on sugar beet pulps pressing were studied. Study was carried out using three two level fractional factorial experiment designs. With only 36 experiments, the effects of the presence of pectin methylesterase, pectin lyase, polygalacturonase, cellulase, arabinase, xylanase and two rhamnogalacturonases on pressing were examined. Pectin lyase, pectin methylesterase and cellulase had a negative effect and caused the decrease of sugar beet pulp pressability. On the contrary, the presence of polygalacturonase, arabinase and xylanase increased pressing efficiency. When increasing enzymes concentrations, these effects varied and positive interactions between xylanase and polygalacturonase appeared. The presence of each of the two rhamnogalacturonases improved pressability despite their antagonistic effects. These enzymes had a complex effect and strongly interacted with polygalacturonase, arabinase and xylanase.     

Cell cycle kinetics and monoclonal antibody productivity of hybridoma cells during perfusion culture

The flow-cytometric (FCM) analysis of bivariate DNA/lgG distributions has been conducted to study the cell cycle kinetics and monoclonal antibody (MAb) production during perfusion culture of hybridoma cells. Three different perfusion rates were employed to demonstrate the dependency of MAb synthesis and secretion on cell cycle and growth rate. The results showed that, during the rapid growth period of perfusion culture, the level of intracellular igG contents of hybridoma cells changed significantly at each perfusion rate, while the DNA histograms showing cell cycle phases were almost constant. Meanwhile, during the reduced growth period of perfusion culture, the fraction of cells in the S phase decreased, and the fraction cells in the G1/G0 phase increased with decreasing growth rate. The fraction of cells in the G2/M phase was relatively constant during the whole period of perfusion culture. Positive correlation was found between mean intracellular IgG contents and the specific MAb production rate, suggesting that the deletion of intracellular IgG contents by a flow cytometer could be used as a good indicator for the prediction of changes in specific MAb productivity following manipulation of the culture condition. (c) 1994 John Wiley & Sons, Inc.