Effect of Bcl-2 Expression on Hybridoma Cell Growth in Serum-Supplemented, Protein-Free and Diluted Media

Two transfected hybridoma cell lines TB/C3-bcl2 (overexpressing the Bcl-2 protein) and TB/C3-pEF (control cell line), were compared in batch suspension cultures using a medium supplemented either with horse serum or with a protein-free, iron-rich supplement. The membrane intact index (percentage of cells with intact membranes determined by trypan blue staining) of the TB/C3-bcl2 cell line decreased much slower than that of the control cell line during the dying phase of the cultures. No significant difference in antibody, lactate and ammonia production as well as glucose and glutamine consumption was noted in the exponential phase of the experiments. Both cell lines were also compared in batch experiments using media diluted with saline to further investigate the effect of Bcl-2 under sub-optimal conditions. The Bcl-2 overexpressing cell line again exhibited a higher membrane intact index at increasing dilution steps. This revised version was published online in June 2006 with corrections to the Cover Date.     

Glycosylation of an immunoglobulin produced from a murine hybridoma cell line: the effect of culture mode and the anti-apoptotic gene, bcl-2

The impact of bcl-2 over-expression on the glycosylation pattern of an antibody produced by a bcl-2 transfected hybridoma cell line (TB/C3.bcl-2) was investigated in suspension batch, continuous and high cell density culture (Flat hollow fibre, Tecnomouse system). In all culture modes bcl-2 over-expression resulted in higher cell viability. Analysis of the glycans from the IgG of batch cultures showed that >95% of the structures were neutral core fucosylated asialo biantennary oligosaccharides with variable terminal galactosylation (G0f, G1f and G2f) consistent with previous analysis of glycans from the conserved site at Asn-297 of the IgG protein. The galactosylation index (GI) was determined as an indicator of the glycan profile (=(G2 + 0.5* G1)/(G0 + G1 + G2)). GI values in control cultures were comparable to bcl-2 cultures during exponential growth (0.53) but declined toward the end of the culture when there was a loss in cell viability. Low dilution rates in chemostat culture were associated with reduced galactosylation of the IgG glycans in both cell lines. However, at the higher dilution rates the GI for IgG was consistently higher in the TB/C3.bcl-2 cultures. In the hollow fibre bioreactor the galactosylation of the IgG glycans was considerably lower than in suspension batch or continuous cultures with GI values averaging 0.38. Similar low galactosylation values have been found previously for high density cell cultures and these are consistent with the low values obtained when the dissolved oxygen level is maintained at a low value (10%) in controlled suspension cultures of hybridomas.     

Prevention of hybridoma cell death by bcl-2 during suboptimal culture conditions

TB/C3 hybridoma cells were transected with either pEF-MClneopA or pEF bcl2-MClneopA vectors to produce a control cell line (TB/C3 pEF) and a cell line that overexpresses the "antiapoptotic" human bcl-2 protein (TB/C3 bcl2). Flow cytometry analysis of intracellular bcl-2 protein levels enabled near on-line monitoring of the stability of bcl-2 expression in the absence of drug selection. It was possible to maintain spontaneous selection of cells with the overexpression of bcl-2 protein during semicontinuous cultures at very low dilution rates, where cells were subjected to the selective conditions of nutrient limitation and high toxic metabolite concentrations. Interestingly, cells that overexpressed bcl-2 were adapted to suspension culture conditions significantly faster than control cells. Dual fluorescence staining with acridine orange and propidium iodide allowed for discrimination between viable, apoptotic, secondary necrotic, and necrotic cells, respectively. Compared with the usual trypan blue method of establishing culture viability, dual staining demonstrated that under stressful conditions a significant proportion of cells that excluded trypan blue were also undergoing cell death through apoptosis. In batch cultures the overexpression of bcl-2 more than doubled the membrane intact (MI) cell productive period (the integral of Ml cell density with respect to culture time) and increased the monoclonal antibody (mAb) production by approximately 40% when compared with the control cell line. The overexpression of bcl-2 protein also significantly extended the cell integrity and viability by the suppression of apoptosis in conditions of hypoxia, hyperoxia, glutamine deprivation, glucose deprivation, and serum limitation. The suppression of apoptosis in anaerobic conditions suggests that bcl-2 exerts its antiapoptotic activity by a mechanism that does not involve an oxidative reactive pathway. In conditions of excess thymidine, which suppressed cell proliferation, Ml cell density and specific mAb productivity were further enhanced by the overexpression of bcl-2, which suggests the possibility of accomplishing a controlled proliferation in immortalized cell lines without invoking cell death. Cell size and intracellular mAb were increased for TB/C3 bcl2 cells compared with TB/C3 pEF control cells when analyzed by flow cytometry. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 1-16, 1997.     

Co-expression of bcl-2 and bag-1, apoptosis suppressing genes, prolonged viable culture period of hybridoma and enhanced antibody production

Human bcl-2 and bag-1 DNA were introduced into mouse hybridoma 2E3- O cells and expressed. The expression of bcl-2 in BCMGneo-bcl2 transfectants was confirmed by ELISA and that of bag-1 in pZeo-bag1 was confirmed by western blotting. In batch cultures, the over-expression of bcl-2 prolonged the culture period by 2 days and co-expression of bcl-2 and bag-1 prolonged the culture period by 3 days. The delayed increase in the dead cell number in culture of the bcl-2 and bag-1 cotransfectant indicated the additional antiapoptosis effect of bcl-2 and bag-1 cotransfection in comparison with the bcl-2 only transfection. The bcl-2 transfectants (2E3O-Bcl2) produced antibody twofold per batch culture in comparison with 2E3-O cells transfected with BCMGSneo (2E3O-Mock). Enhancement of this MoAb production was due to the improved survival of the cells and was not due to stimulation of antibody production rate per cell by Bcl-2 expression. And the bcl-2 and bag-1 co-transfectant (2E3O-Bcl2-BAG1) produced antibody approximately fourfold of 2E3O-Mock per batch culture. Enhancement of this MoAb production was due to the improved survival of the cells and was partly due to stimulation of MoAb production rate per cell in the non-growing phase by the cotransfection. The method to engineer hybridoma cells genetically with bcl-2 and bag-1 for increasing viability and productivity would be widely applied for improving antibody productivity of hybridoma cultures. This revised version was published online in August 2006 with corrections to the Cover Date.     

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.     

Hybridoma growth and antibody production as a function of cell density and specific growth rate in perfusion culture

Steady state metabolic parameters for hybridoma cell line H22 were determined over a wide range of cell densities and specific growth rates in a filtration based homogeneous perfusion reactor. Operating the reactor at perfusion rates of 0.75, 2.0, and 2.9 day(-1)(each at four different specific growth rates), viable cell densities as high as 2 x 10(7) cells/mL were obtained. For the cell line under investigation, the specific monoclonal antibody production rate was found to be a strong function of the viable cell density, increasing with increasing cell density. In contrast, most of the substrate consumption and product formation rates were strong functions of the specific growth rate. Substrate metabolism became more efficient at high cell densities and low specific growth rates. The Specific rates of metabolite formation and the apparent yields of lactate from glucose and ammonia from glutamine decreased at low specific growth rates and high cell densities. While the specific oxygen consumption rate was independent of the specific growth rate and cell density, ATP production was more oxidative at lower specific growth rate and higher cell density. These observed shifts are strong indications of the production potential of high-density perfusion culture. (c) 1995 John Wiley & Sons, Inc.     

Physiological changes during the adaptation of hybridoma cells to low serum and serum-free media

Two murine hybridoma cell lines (167.4G5.3 and S3H5/gamma2bA2) were adapted to grow in low-serum and serum-free media by a weaning procedure. The changes in cell growth, metabolic, and antibody production rates with adaptation were examined using biochemical and flow cytometric analyses. After adaptation to a particular serum level, the short-term serum response of the cells was experimentally determined. Specific growth rates, glucose and glutamine uptake and lactate and ammonia production rates, and specific antibody production rates were evaluated from the data. For both cell lines, an improvement in cell growth was observed after adaptation, and both higher growth rates and higher cell concentrations were obtained. The specific glucose and glutamine uptake rates and the lactate and ammonia production rates changed insignificantly with adaptation. Conversely, changes in the specific antibody production rate of the two cell lines differed. Cell line 167.4G5.3 showed a loss in antibody productivity at low serum levels, while the S3H5/gamma2bA2 kept its original productivity in low-serum-containing media. The intracellular antibody content for S3H5/gamma2bA2 cells remained unaltered by adaptation, but a low antibody containing cell population appeared in the 167.4G5.3 culture. The loss of specific antibody productivity in this cell line was due to the appearance of this population.     

Stable hybridoma cultivation in a pilot-scale acoustic perfusion system: long-term process performance and effect of recirculation rate

Perfusion systems have the possibility to be operated continuously for several months. It is important that the performance of the cell retention device does not limit the operation time of a perfusion process used in the production of active pharmaceutical ingredients. Therefore, the aim of this study was to investigate the reliability and long-term stability of an acoustic perfusion process using the 200 L/d BioSep. As the BioSep is an external device, it is possible that dependent on the recirculation rate nutrient gradients occur in the external loop, which could affect the cell metabolism. Therefore, the effect of possible nutrient gradients on cell metabolism, viability and productivity was studied by varying the recirculation rate. In this study, it is shown that a perfusion process using a pilot-scale acoustic cell-retention device (200 L/d) is reliable and simple to operate, resulting in a stable 75-day cultivation of a hybridoma cell line producing a monoclonal antibody. The recirculation rate had a significant effect on the oxygen concentration in the external loop, with oxygen being depleted within the cell-retention device at recirculation rates below 6 m3/m(reactor)3.d (=600 L/d). The oxygen depletion at low circulation rates correlated with a slightly increased lactate production rate. For all other parameters no effect of the recirculation rate was observed, including cell death measured through the release of lactate dehydrogenase and specific productivity. A maximum specific productivity of 12 pg/cell.d was reached.     

Production of immunoglobulin A in different reactor configurations

A murine hybridoma line (Zac3), secreting an IgA monoclonal antibody, was cultivated in different systems: a BALB/c mouse, a T-flask, a stirred-tank bioreactor and a hollow fiber reactor. These systems were characterized in terms of cell metabolism and performances for IgA production. Cultures in T-flask and batch bioreactor were found to be glutamine-limited. Ammonia and lactate were produced in significant amounts. IgA productivity was found to be constant and growth associated. Final IgA concentration was similar in both systems. In fed-batch cultures, supplemented with glutamine and glucose, maximum viable cell concentration was increased by 60% and final IgA concentration by 155%. The hollow fiber reactor was able to produce very large amounts of IgA at very high concentrations, similar to the value found in ascites fluid. The productivity ofZac3 is similar to the values reported for IgG-producing cell lines.     

Loofa sponge as a scaffold for the culture of human hepatocyte cell line

Loofa sponge was investigated as a three-dimensional scaffold for stationary and perfusion culture of human hepatoblastoma cell line C3A/HepG2. In stationary culture, C3A/HepG2 cells in loofa cubes showed higher alpha-fetoprotein and albumin secretion rates than those in polyurethane foam (PU). To use loofa cylinders in a packed-bed reactor, immobilization of C3A/HepG2 cells by recirculating medium at 26 mL/min (superficial velocity = 51.7 cm/min) resulted in a cell loading density of 5.15 x 10(7) cells/cm(3)-loofa. This cell loading density is higher than values reported in the literature for packed-bed reactor intended for bioartificial liver. During 9 days of perfusion culture in the reactor, immobilized C3A/HepG2 showed steady synthesis of albumin with an average synthesis rate at 42.2 microg/10(6) cells/day. These experimental results and observations by SEM suggested that loofa sponge is a suitable scaffold for high-density culture of human hepatocyte cell line and the immobilized cells could express high levels of liver-specific functions.     

A perfusion system for antibody production by shear-sensitive hybridoma cells in a stirred reactor

Summary A shear-sensitive hybridoma cell line, incapable of growth or antibody production in spinner or shake flasks agitated at 40 rpm, was grown successfully in a perfusion propagation system consisting of a bioreactor (1.5 liter), stirred with a cell-lift impeller at 60 rpm, and a tangential flow filtration unit for removal of spent culture medium from the reactor. The culture was maintained over a 48 day period and cell numbers reached 1.8 × 10⁷ cells/ml. Maximal monoclonal antibody concentration was 800 ug/ml, indicating a productivity of 504 mg/day.     

Characterization and fed-batch culture of hybridoma overexpressing apoptosis suppressing gene bcl-2

Mouse hybridoma 2E3 transfected with human bcl-2 gene survived longer with increasing expression level of bcl-2 when cultured in DME medium supplemented with 9% serum. One of the transfectants, 2E3BCMGbcl-2, overexpressed bcl-2 and could maintain viable cell density higher than the initial density for more than four days at a low 0.5% serum concentration. In comparison a mock transfectant 2E3BCMG remained viable for only one day. However, both hybridomas died out within a day in serum-free medium. These results suggested that bcl-2 needed a small amount of some serum components to suppress apoptosis of the hybridoma. Overexpression of bcl-2 also suppressed apoptosis of the hybridoma induced by glutamine deprivation. When hybridoma 2E3BCMGbcl-2 was inoculated in DME medium supplemented with 9% serum and cultured for 10 d with additional 2% serum feed at day 4 of the culture, viable cell density increased 2-fold and antibody produced 3-fold, in comparison with mock transfected 2E3 cultured in the same manner. The mock transfectant with additional feed of serum at day 4 of the culture showed no difference in viable cell density and antibody production. These results suggested that the mock transfectant committed to apoptosis before day 4 of the culture and the additional serum at day 4 could not reverse the commitment. This revised version was published online in July 2006 with corrections to the Cover Date.     

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.     

Cell retention-chemostat studies of hybridoma cells-analysis of hybridoma growth and metabolism in continuous suspension culture in serum-free medium

The steady-state metabolic parameters for a hybridoma cell line have been determined in continuous suspension-perfusion culture over a wide range of perfusion rates and cell bleed rates. Significant increases in viable cell concentrations and volumetric productivities were achieved at high perfusion rates and low cell bleed rates. At the low growth rates examined in this study, cellular metabolism shifted to become more oxidative, and as a result, the fraction of consumed substrate converted to inhibitory metabolic by-products was reduced. Specific antibody productivity was found to be non-growth associated. (c) 1993 John Wiley & Sons, Inc.     

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

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

Step-up/step-down perfusion approach for increased mAb 520C9 production by a hybridoma cell line

The hybridoma cell line, HB-8696, produces a monoclonal antibody, 520C9 (mouse IgG₁) that recognizes the breast cancer oncoprotein, c-erbB2. The effect of perfusion rate (volume of fresh feed/working volume of reactor/day) on cell growth and mAb production was investigated but perfusion at a constant rate and at an arbitrarily increased rate could not maintain exponential cell growth or a higher specific mAb production rate. An optimum step-up/step-down perfusion strategy is therefore proposed for maintaining a steady state production phase at high cell density for ten days. The optimum step-up perfusion could achieve fast cell growth by avoiding any nutrient limited condition and the following optimum step-down perfusion could potentially maintain high live cell density and reduced product dilution as well. The maximum viable cell achieved under optimum perfusion strategy was 2.3 × 10⁷ cells/ml which was 19-fold higher than in optimum batch culture. The mAb yield and volumetric productivity were significantly improved to 52 and 50 mg/l day compared to 25 and 3.8 mg/l day in optimum batch, respectively, and could be maintained for up to ten days.     

Overexpression of bcl-2, apoptosis suppressing gene: Prolonged viable culture period of hybridoma and enhanced antibody production

Human bcl-2 DNA was introduced into mouse hybridoma 2E3 cells and expressed at a high level by using BCMGSneo vector, which reportedly amplifies as multiple copies in the cells independently of their chromosomes. The high expression of bcl-2 in BCMGSneo-bcl-2 transfectants was confirmed by western blotting. In batch cultures, the overexpression of bcl-2 raised the maximum viable cell density by 45%, delayed the initiation of apoptosis by 2 days, and prolonged the viable culture period by 4 days. The delayed initiation of apoptosis was detected by emergence of the ladder pattern on DNA electrophoresis and increase of the dead cell number. The bcl-2 transfectants produced lgG(1) fourfold per batch culture in comparison with 2E3 cells transfected with BCMGSneo but not with bcl-2: a little less than twofold due to the improved survival of the cells and more than twofold due to the enhanced lgG(1) production rate per cell of the bcl-2 transfectants. The method to engineer hybridoma cells genetically with bcl-2 using BCMGSneo vector for increasing viability and productivity would be widely applied for improving antibody productivity of hybridoma cultures. (c) 1995 John Wiley & Sons, Inc.     

Perfusion culture of hybridoma cells for hyperproduction of IgG(2a) monoclonal antibody in a wave bioreactor-perfusion culture system

A novel wave bioreactor-perfusion culture system was developed for highly efficient production of monoclonal antibody IgG2a (mAb) by hybridoma cells. The system consists of a wave bioreactor, a floating membrane cell-retention filter, and a weight-based perfusion controller. A polyethylene membrane filter with a pore size of 7 microm was floating on the surface of the culture broth for cell retention, eliminating the need for traditional pump around flow loops and external cell separators. A weight-based perfusion controller was designed to balance the medium renewal rate and the harvest rate during perfusion culture. BD Cell mAb Medium (BD Biosciences, CA) was identified to be the optimal basal medium for mAb production during batch culture. A control strategy for perfusion rate (volume of fresh medium/working volume of reactor/day, vvd) was identified as a key factor affecting cell growth and mAb accumulation during perfusion culture, and the optimal control strategy was increasing perfusion rate by 0.15 vvd per day. Average specific mAb production rate was linearly corrected with increasing perfusion rate within the range of investigation. The maximum viable cell density reached 22.3 x 105 and 200.5 x 105 cells/mL in the batch and perfusion culture, respectively, while the corresponding maximum mAb concentration reached 182.4 and 463.6 mg/L and the corresponding maximum total mAb amount was 182.4 and 1406.5 mg, respectively. Not only the yield of viable cell per liter of medium (32.9 x 105 cells/mL per liter medium) and the mAb yield per liter of medium (230.6 mg/L medium) but also the mAb volumetric productivity (33.1 mg/L.day) in perfusion culture were much higher than those (i.e., 22.3 x 105 cells/mL per liter medium, 182.4 mg/L medium, and 20.3 mg/L.day) in batch culture. Relatively fast cell growth and the perfusion culture approach warrant that high biomass and mAb productivity may be obtained in such a novel perfusion culture system (1 L working volume), which offers an alternative approach for producing gram quantity of proteins from industrial cell lines in a liter-size cell culture. The fundamental information obtained in this study may be useful for perfusion culture of hybridoma cells on a large scale.     

Anti-apoptotic genes, bag-1 and bcl-2, enabled hybridoma cells to survive under treatment for arresting cell cycle

Hybridoma 2E3-O cells were transfected with bcl-2 alone or with bcl-2 and bag-1 in combination. The bcl-2/bag-1 transfectant survived maintaining viability above 75% for almost 5 days when the cells were treated with excess (30 mM) thymidine for arresting cell cycle, whereas the mock transfectant survived for only 2 days, and the bcl-2 alone transfectant lived for 4 days. Owing to this extended viable culture period, the bcl-2/bag-1 transfectant produced twofold amount of antibody in comparison with the mock transfectant in non-proliferating state prepared by the excess thymidine treatment. When their proliferation was arrested by serum limitation, the bcl-2/bag-1 transfectant and the bcl-2 alone transfectant survived for 3 days maintaining viability above 75% while the mock transfectant survived only 1 day. The bcl-2/bag-1 transfectans produced the antibody at the rate three times as high as the bcl-2 alone transfectant and the mock transfectant in non-proliferating state established by serum limitation. Such genetic engineering of hybridoma cells for improving survival in the non-proliferating state will be useful for using nutrients in culture medium efficiently to produce antibody, since nutrients could be diverted from cell proliferation to antibody production in such non-proliferating viable cell culture. This revised version was published online in June 2006 with corrections to the Cover Date.     

Development of apoptosis-resistant dihydrofolate reductase-deficient Chinese hamster ovary cell line

Apoptosis-resistant dihydrofolate reductase-deficient CHO cell line (dhfr(-) CHO-bcl2) was developed by introduction of the bcl-2 gene into the dhfr(-) CHO cell line (DUKX-B11, ATCC CRL-9096) and subsequent selection of clones stably overexpressing Bcl-2 in the absence of selection pressure. When the dhfr(-) CHO-bcl2 cell line was used as a host cell line for development of a recombinant CHO (rCHO) cell line expressing a humanized antibody, it displayed stable expression of the bcl-2 gene during rCHO cell line development and no detrimental effect of Bcl-2 overexpression on specific antibody productivity. Taken together, the results obtained demonstrate that the use of an apoptosis-resistant dhfr(-) CHO cell line as the host cell line saves the effort of establishing an apoptosis-resistant rCHO cell line and expedites the development process of apoptosis-resistant rCHO cells producing therapeutic proteins.