Glycolipid membrane anchored recombinant protein production from CHO cells cultGred on porous microcarriers

Recombinant proteins were harvested from Chinese hamster ovary (CHO) cells by a controlled release process, which increased the purity and concentration of the harvested protein. Recombinant human melano-transferrin (p97) was expressed linked to the outer surface of CHO cells by a glycosyl-phosphatidylinositol (GPI) membrane anchor. Cells were grown to confluence in T-flask culture, and the p97 harvested by replacing the growth medium for 30 min with phosphate-buffered saline (PBS) containing 10 mU/mL phosphatidylinositol-phospholipase C (PI-PLC). The GPI anchor was selectively cleaved by PI-PLC. In fresh medium, the CHO cells regained over 95% of their p97 expression within 40 h. The process was repeated for eight harvests. Harvested protein concentrations varied from 1.5 to 3.8 mug/mL due to difficulties in maintaining stable confluent T-flask cultures. Harvesting from cells growing on porous microcarriers was investigated to increase p97 product concentrations and to overcome culture stability problems. Semicontinuous cultures were maintained in spinners for up to 76 days with average bioreactor cell densities of over 10(7) cell/mL. The p97 was harvested at up to 100 mug/mL and 30% purity with protein production remaining stable for 4 harvest cycles. Production of high levels of p97 from CHO cells was maintained at 0.5% serum. (c) 1994 John Wiley & Sons, Inc.     

Effect of culture pH on erythropoietin production by Chinese hamster ovary cells grown in suspension at 32.5 and 37.0 degrees C

To investigate the effect of culture pH in the range of 6.85-7.80 on cell growth and erythropoietin (EPO) production at 32.5 and 37.0 degrees C, serum-free suspension cultures of recombinant CHO cells (rCHO) were performed in a bioreactor with pH control. Lowering culture temperature from 37.0 to 32.5 degrees C suppressed cell growth, but cell viability remained high for a longer culture period. Regardless of culture temperature, the highest specific growth rate (mu) and maximum viable cell concentration were obtained at pH values of 7.00 and 7.20, respectively. Like mu, the specific consumption rates of glucose and glutamine decreased at 32.5 degrees C compared to 37.0 degrees C. In addition, they increased with increasing culture pH. Culture pH at 32.5 degrees C affected specific EPO productivity (q(EPO)) in a different fashion from that at 37 degrees C. At 37 degrees C, the q(EPO) was fairly constant in the pH range of 6.85-7.80, while at 32.5 degrees C, the q(EPO) was significantly influenced by culture pH. The highest q(EPO) was obtained at pH 7.00 and 32.5 degrees C, and its value was approximately 1.5-fold higher than that at pH 7.00 and 37.0 degrees C. The proportion of acidic EPO isoforms, which is a critical factor for high in vivo biological activity of EPO, was highest in the stationary phase of growth, regardless of culture temperature and pH. Although cell viability rapidly decreased in death phase at both 32.5 and 37.0 degrees C, the significant degradation of produced EPO, probably by the action of proteases released from lysed cells, was observed only at 37.0 degrees C. Taken together, through the optimization of culture temperature and pH, a 3-fold increase in maximum EPO concentration and a 1.4-fold increase in volumetric productivity were obtained at pH 7.00 and 32.5 degrees C when compared with those at 37.0 degrees C. These results demonstrate the importance of optimization of culture temperature and pH for enhancing EPO production in serum-free, suspension culture of rCHO cells.     

Effect of culture temperature on erythropoietin production and glycosylation in a perfusion culture of recombinant CHO cells

To investigate the effect of culture temperature on erythropoietin (EPO) production and glycosylation in recombinant Chinese hamster ovary (CHO) cells, we cultivated CHO cells using a perfusion bioreactor. Cells were cultivated at 37 degrees C until viable cell concentration reached 1 x 10(7) cells/mL, and then culture temperature was shifted to 25 degrees C, 28 degrees C, 30 degrees C, 32 degrees C, 37 degrees C (control), respectively. Lowering culture temperature suppressed cell growth but was beneficial to maintain high cell viability for a longer period. In a control culture at 37 degrees C, cell viability gradually decreased and fell below 80% on day 18 while it remained over 90% throughout the culture at low culture temperature. The cumulative EPO production and specific EPO productivity, q(EPO), increased at low culture temperature and were the highest at 32 degrees C and 30 degrees C, respectively. Interestingly, the cumulative EPO production at culture temperature below 32 degrees C was not as high as the cumulative EPO production at 32 degrees C although the q(EPO) at culture temperature below 32 degrees C was comparable or even higher than the q(EPO) at 32 degrees C. This implies that the beneficial effect of lowering culture temperature below 32 degrees C on q(EPO) is outweighed by its detrimental effect on the integral of viable cells. The glycosylation of EPO was evaluated by isoelectric focusing, normal phase HPLC and anion exchange chromatography analyses. The quality of EPO at 32 degrees C in regard to acidic isoforms, antennary structures and sialylated N-linked glycans was comparable to that at 37 degrees C. However, at culture temperatures below 32 degrees C, the proportions of acidic isoforms, tetra-antennary structures and tetra-sialylated N-linked glycans were further reduced, suggesting that lowering culture temperature below 32 degrees C negatively affect the quality of EPO. Thus, taken together, cell culture at 32 degrees C turned out to be the most satisfactory since it showed the highest cumulative EPO production, and moreover, EPO quality at 32 degrees C was not deteriorated as obtained at 37 degrees C.     

Applications of improved stoichiometric model in medium design and fed-batch cultivation of animal cells in bioreactor

In our previous work (Xie and Wang, 1994a), a simplified stoichiometric model on energy metabolism for animal cell cultivation was developed. Fed-batch experiments were performed in T-flasks using this model in supplemental medium design (Xie and Wang, 1994b). In this work, the major pathways of glucose and glutamine metabolism were incorporated into the stoichiometric model. Fed-batch culture was conducted in a 2-liter bioreactor with appropriate process control strategies. Nutrient concentrations, especially glucose and glutamine, were maintained at constant but low levels through the automated feeding of a supplemental medium formulated using the improved stoichiometric model. The formation of toxic byproducts, such as ammonia and lactate (Hassellet al., 1991), was greatly reduced. The specific lactate production rate was decreased by 62-fold compared with batch culture in bioreactor and by 8-fold compared to fed-batch culture in T-flask using the previous stoichiometric model. Ammonia formation was also decreased compared with both the batch and fed-batch cultures. Most importantly, the monoclonal antibody concentration reached 900 mg l^?1, an increase of 17- and 1.6-fold compared with the batch and fed-batch cultures respectively.     

High-density transient gene expression in suspension-adapted 293 EBNA1 cells

Large-scale transient gene expression (TGE) in mammalian cells is an attractive method to rapidly produce recombinant proteins for pre-clinical studies, with some processes reported to reach 100 L. However, the yield remains low, hardly over 20 mg protein/L, mainly because the current TGEs have been performed at low cell density (approximately 5 x 10(5) cells/mL). In this study, the strategy to improve TGE focuses on facilitating transfection at high cell density. A high-density perfusion culture of 293 EBNA1 cells was established in 2-L bioreactor using Freestyle 293 expression medium (Invitrogen, Singapore) to grow the cells for transfection. Transfection was then carried out at 1 x 10(7) cells/mL using polyethylenimine (PEI) as DNA carrier, at the optimized conditions of 6 microg DNA/10(7) cells and 1:3 DNA to PEI mass ratio. During the post-transfection phase, 80.8 mg/L of the model protein, EPO was obtained at day 5.5 post-transfection (130 mg total EPO production) using a fed-batch culture mode. In comparison, perfusion cultures using an enriched SFM II medium resulted in a longer post-transfection production phase (8 days), and 227 mg of EPO was produced in 10.7 L medium, showing that high-density TGE enables the production of several hundreds of milligrams of protein in a 2 L bioreactor. In addition, a protocol for economical plasmid preparation based on anion exchange was also established to satisfy TGE's demand in terms of quality and quantity. To the best of our knowledge, this is the first report of transient transfections at a high cell density of up to 1 x 10(7) cells/mL.     

Comparing BRIN-BD11 culture producing insulin using different type of microcarriers

This research was conducted to examine the growth profile, growth kinetics, and insulin-secretory responsiveness of BRIN-BD11 cells grown in optimized medium on different types of microcarriers (MCs). Comparisons were made on modified polystyrene (Hillex^® II) and crosslinked polystyrene Plastic Plus (PP) from Solohill Engineering. The cell line producing insulin was cultured in a 25 cm² T-flask as control while MCs based culture was implemented in a stirred tank bioreactor with 1 L working volume. For each culture type, the viable cell number, glucose, lactate, glutamate, and insulin concentrations were measured and compared. Maximum viable cell number was obtained at 1.47 × 10⁵ cell/mL for PP microcarrier (PPMCs) culture, 1.35 × 10⁵ cell/mL Hillex^® II (HIIMCs) culture and 0.95 × 10⁵ cell/mL for T-flask culture, respectively. The highest insulin concentration has been produced in PPMCs culture (5.31 mg/L) compared to HIIMCs culture (2.01 mg/L) and T-flask culture (1.99 mg/L). Therefore overall observation suggested that PPMCs was likely preferred to be used for BRIN-BD11 cell culture as compared with Hillex^® II MCs.     

Stirred culture of peripheral and cord blood hematopoietic cells offers advantages over traditional static systems for clinically relevant applications

The ability to culture hematopoietic cells in readily characterizable and scalable stirred systems, combined with the capability to utilize serum-free medium, will aid the development of clinically attractive bioreactor systems for transplantation therapies. We thus examined the proliferation and differentiation characteristics of peripheral blood (PB) mononuclear cells (MNC), cord blood (CB) MNC, and PB CD34(+) cells in spinner flasks and (control) T-flask cultures in both serum-containing and serum-free media. Hematopoietic cultures initiated from all sources examined (PB MNC, CB MNC, and PB CD34(+) cells) grew well in spinner vessels with either serum-containing or serum-free medium. Culture proliferation in spinner flasks was dependent on both agitator design and RPM as well as on the establishment of critical inoculum densities (ID) in both serum-containing (2 x 10(5) MNC/mL) and serum-free (3 x 10(5) MNC/mL) media. Spinner flask culture of PB MNC in serum-containing medium provided superior expansion of total cells and colony-forming cells (CFC) at high ID (1.2 x 10(6) cells/mL) as compared to T-flask controls. Serum-free spinner culture was comparable, if not superior, to that observed in serum-containing medium. This is the first report of stirred culture of PB or CB MNC, as well as the first report of stirred CD34(+) cell culture. Additionally, this is the first account of serum-free stirred culture of hematopoietic cells from any source.     

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.     

Long-term Continuous Production of Monoclonal Antibody by Hybridoma Cells Immobilized in a Fibrous-Bed Bioreactor

The kinetics and long-term stability of continuous production of monoclonal antibody IgG2b by hybridoma HD-24 cells immobilized in a fibrous-bed bioreactor (FBB) were studied for a period of ～8 months. The cells were immobilized in the fibrous bed by surface attachment of cells and entrapment of large cell clumps in the void space of the fibrous matrix. A high viable cell density of 1.01 × 10⁸/ml was attained in the bioreactor, which was about 63 times higher than those in conventional T-flask and spinner flask cultures. The continuous FBB produced IgG at a concentration of ～0.5 g/l, with reactor productivity of ～7 mg/h·l, which was about 23 times higher than those from conventional T-flask and spinner flask cultures. The IgG concentration can be further increased to ～0.67 g/l by using higher feed (glucose and glutamine) concentrations and running the reactor at a recycle batch or fed-batch mode. The long-term performance of this bioreactor was also evaluated. For a period of 36 days monitored, the MAb produced in the continuous well-mixed bioreactor at 50 h retention time (0.02/h dilution rate) was maintained at a steady concentration level of ～0.3 g/l with less than 8% drift. At the end of the study, it was found that ～25% of the cells were strongly attached to the fiber surfaces and the other ～75% entrapped or weakly immobilized in the fibrous matrix. The strongly attached cells had a high viability of ～90%, compared to ～75% for cells weakly immobilized and only ～1.4% for freely suspended cells, suggesting that the fibrous matrix preferentially retained and protected the viable (productive) cells. The FBB thus was able to maintain its long-term productivity because nonviable and dead cells were continuously washed off from the fibrous matrix. The high MAb concentration and production rate and excellent stability for continuous long-term production obtained in this study compare favorably to other bioreactor studies reported in the literature. The reactor performance can be further improved by providing better pH and aeration controls at higher feed concentrations. The FBB is easy to operate and scale-up, and thus can be used economically for industrial production of MAb.     

Effects of cell density and glucose and glutamine levels on the respiration rates of hybridoma cells

The effects of cell density as well as the concentration levels of glucose and glutamine on the specific respiration rate of a hybridoma cell line were investigated. The experimental oxygen consumption rate was found to be constant over a wide range of dissolved oxygen levels if the suspension medium contained glutamine. In glutamine-free medium, however, the rate of oxygen consumption decreased slowly with time.In a stationary flask batch culture, the specific respiration rate decreased from about 7 to 2.9 mumol/min per 10(9) cells as the cell density increased exponentially from 1 x 10(5) to 1.2 x 10(6)/mL. To isolate the effect of cell density, cells were re suspended in fresh culture medium so that nutrient concentrations were the same for all experiments. The specific respiration rate decreased with increasing cell density in the same manner as in the stationary flask culture, falling from 8 to 4 mumol/min per 10(9) cells as the cell density increased from 10(5) to 10(6) cells/mL, then declining to 2 mumol/min per 10(9) cells when the cell density reached 10(7) cells/mL.Cells suspended in Hanks balanced sale solution (HBSS) were used to elucidate the effect of glucose and glutamine levels on respiration. The addition of glucose in concentrations of 0.25, 0.50, and 0.75 g/L had no observable effect on the specific oxygen uptake rate; however, a glucose concentration of 1 g/L reduced the uptake rate by 22%. Glutamine in a concentration of 0.30 g/L increased the specific respiration rate in HBSS containing 0 and 1 g/L glucose by approximately 13%.     

Growth characteristics in fed-batch culture of hybridoma cells with control of glucose and glutamine concentrations

An online system using HPLC was developed for the measurement of glucose, glutamine, and lactate in a culture broth. Using the system, the glucose and glutamine concentrations were controlled simultaneously by an adaptive-control algorithm within the ranges of 0.2 to 2.0 and 0.1 to 0.6 g/L, respectively. When the glucose concentration was controlled at the low level of 0.2 g/L, the intracellular lactate dehydrogenase activity decreased by one-half and the lactate concentration by one-third, whereas the uptake rates of serine and glycine were about twice as high, compared with the amounts when the glucose concentration was controlled at 1.0 g/L. On the other hand, ammonia production increased when the glucose concentration was kept low. To reduce the production of inhibitory metabolites such as ammonia and lactate and improve the antibody production rate in a hybridoma cell culture, the concentrations of glucose and glutamine were controlled at 0.2 and 0.1 g/L, respectively. With these low concentrations of glucose and glutamine, the cell concentration (4.1 x 10(6) cells/mL) and antibody production (172 mg/L) both increased about twofold compared with the amounts when the glucose was controlled at higher levels. From these results, simultaneous control of the glucose and glutamine concentrations was shown to be useful in the production of antibody by hybridoma cell cultivation. (c) 1994 John Wiley & Sons, Inc.     

Manganese peroxidase production by immobilized Phanerochaete chrysosporium BKM-F-1767 in a cell bioreactor

Manganese-dependent peroxidase (MnP) production was performed in an immobilized cell bioreactor in which Phanerochaete chrysosporium BKM-F-1767 was immobilized on polystyrene foam. The immobilized cell culture yielded significantly greater MnP activity than the conventional stationary liquid culture. Cultivation was carried out in batch mode; the effect of glucose concentration was investigated and growth kinetics parameters were found as, micromax=0.59 day(-1), Ks=0.33 g/L and Kss=14.5. Batch operation led to maximum MnP (770.82 U/L) in the culture medium containing 0.05% Tween 80, 10 g/L glucose, and 174 microM Mn2+ at 37 degrees C and pH 4.5. Enzyme productivity was obtained as 110.12 U/day/L.     

Cultivation of fall armyworm ovary cells in simulated microgravity

Summary A methodology is presented to culture Fall Armyworm Ovary cells in simulated microgravity using a novel bioreactor developed by NASA, the High-Aspect Ratio Vessel. In this vessel, the growth and metabolic profile for these insect cells were profoundly different than those obtained in shaker-flask culture. Specifically, stationary phase in the NASA vessel was extended from 24 h to at least 7 d while cell concentration and viability remained in excess of 1 × 10⁷ viable cells/ml and 90%, respectively. Measurements of glucose utilization, lactate production, ammonia production, and pH change indicate that simulated microgravity had a twofold effect on cell metabolism. Fewer nutrients were consumed and fewer wastes were produced in stationary phase by as much as a factor of 4 over that achieved in shaker culture. Those nutrients that were consumed in the NASA vessel were directed along different metabolic pathways as evidenced by an extreme shift in glucose utilization from consumption to production in lag phase and a decrease in yield coefficients by one half in stationary phase. These changes reflect a reduction in hydrodynamic forces from over 1 dyne/cm² in shaker culture to under 0.5 dyne/cm² in the NASA vessel. These results suggest that cultivation of insect cells in simulated microgravity may reduce production costs of cell-derived biologicals by extending production time and reducing medium requirements.     

Continuous stable production of von Willebrand Factor monoclonal antibody in spin filter bioreactor with bleeding technology

The characteristics of two different modes of perfusion culture, intermittent and continuous bleedings, were investigated by culturing the hybridoma cells producing von Willebrand Factor (vWF) monoclonal antibody (McAb) in a 15 L bioreactor without clogging the filter. Both culture methods exhibited similar profiles of cell density and metabolite concentrations during the culture period at the cell concentration of around 1×10⁷ cells/mL. When the perfusion rate was increased, the intermittent bleeding culture showed problems of ammonia accumulation and decrease of cell viability. The continuous bleeding culture exhibited higher physiological activity than that of the intermittent bleeding culture in terms of nutrient consumption and metabolite production kinetics. But the analysis of specific oxygen consumption rate showed that the specific oxygen consumption rate of intermittent bleeding culture was similar to that of exponential growth phase. The continuous bleeding culture showed higher specific vWF McAb productivity and cumulative production than those of the intermittent bleeding culture. Finally we proved the possibility of long-term operation of continuous bleeding culture and produced approximately 40 g of vWF McAb in a 15 L bioreactor after one-month operation.     

重组CHO-GS细胞降低氨毒副作用的代谢研究

在重组CHOGS细胞无血清批培养过程中,由于GS系统的引入,使氨对细胞的毒副作用显著降低,从而引起细胞生长和代谢途径发生变化。当起始氨浓度为1.42mmolL时,细胞最高密度可达到15.6×105cellsmL,随着氨浓度的增加,尽管细胞生长受到一定的抑制,但在氨浓度为12.65mmolL时,细胞密度仍可达到8.9×105cellsmL。当起始氨浓度从0.36mmolL增加到12.65mmolL时,细胞对葡萄糖的得率系数和乳酸对葡萄糖的得率系数降低,己糖激酶(HK)、丙酮酸激酶(PK)和乳酸脱氢酶(LDH)酶活分别提高了43%、140%和25%,表明细胞对葡萄糖的利用增加,糖代谢更倾向于高能量生成途径。在谷氨酰胺代谢途径中,氨促进了谷丙转氨酶(GPT)酶活,谷氨酸到α酮戊二酸的转化逐渐倾向于谷丙转氨途径,谷氨酸脱氢酶(GDH)酶活降低,脱氨途径相应受到抑制。此外,氨浓度的增加使细胞群体处于G0G1期的比例逐渐升高,当氨浓度为12.65mmolL时,重组蛋白比生产速率比氨浓度为0.36mmolL时提高了2.1倍。     

Production of Bacillus thuringiensis spores in total cell retention culture and two-stage continuous culture using an internal ceramic filter system

The production of Bacillus thuringiensis spores was investigated in a bioreactor incorporating a ceramic membrane filter to improve spore concentration and volumetric productivity. Two cultivation methods were used in this study: a total cell retention culture (TCRC), and a two-stage continuous culture with partial cell bleeding. In the TCRC, fed by 50 g/L of glucose, a spore concentration of 1.6 x 10(10) CFU/mL was obtained with a spore percentage of greater than 95% and a maximum cell mass of 82.2 g/L. The volumetric productivity was four times higher than that obtained from batch cultivation. In the two-stage continuous culture with partial cell bleeding spore concentration was strongly dependent on the bleed ratio. The spore concentration of 1.8 x 10(9) CFU/mL and the spore percentage of 70% were obtained at the second stage when a bleed ratio of 0.33 and a dilution rate of 0.23 h(-1) were used. (c) 1993 John Wiley & Sons, Inc.     

Effects of ammonia on CHO cell growth, erythropoietin production, and glycosylation

The effect of ammonium chloride was determined on a culture of CHO cells transfected with the human erythropoietin (EPO) gene. Cell growth was inhibited above a culture concentration of 5 mM NH(4)Cl with an IC-50 determined to be 33 mM. The specific production of EPO increased with the addition of NH(4)Cl above 5 mM. At 10 mM NH(4)Cl, the final cell density after 4 days in culture was significantly lower but the final yield of EPO was significantly higher. This appeared to be due to continued protein production after cell growth had ceased. The metabolic effects of added NH(4)Cl included higher specific consumption rates of glucose and glutamine and an increased rate of production of alanine, glycine, and glutamate. The EPO analyzed from control cultures had a molecular weight range of 33-39 kDa and an isoelectric point range of 4.06-4.67. Seven distinct isoforms of the molecule were identified by two-dimensional electrophoresis. This molecular heterogeneity was ascribed to variable glycosylation. Complete enzymatic de-glycosylation resulted in a single molecular form with a molecular mass of 18 kDa. Addition of NH(4)Cl to the cultures caused a significant increase in the heterogeneity of the glycoforms as shown by an increased molecular weight and pI range. Enzymatic de-sialylation of the EPO from the ammonia-treated and control cultures resulted in identical electrophoretic patterns. This indicated that the effect of ammonia was in the reduction of terminal sialylation of the glycan structures which accounted for the increased pI. Selective removal of the N-glycan structures by PNGase F resulted in two bands identified as the O-glycan linked structure (19 kDa) and the completely de-glycosylated structure (18 kDa). The proportion of the O-linked glycan structure was reduced, and its pI increased in cultures to which ammonia was added. Thus, the glycosylation pattern altered by the presence of ammonia included a reduction in terminal sialylation of all the glycans and a reduction in the content of the O-linked glycan. The addition of a sialidase inhibitor to the cultures had no effect on the ammonia-induced increase in EPO heterogeneity. Also, the effect of ammonia on glycosylation could not be mimicked using the weak base chloroquine in our system.     

Production of carbonyl reductase by Geotrichum candidum in a laboratory scale bioreactor

Fungal fermentation is very complex in nature due to its nonlinear relationship with the time, especially in batch culture. Growth and production of carbonyl reductase by Geotrichum candidum NCIM 980 have been studied in a laboratory scale stirred tank bioreactor at different pH (uncontrolled and controlled), agitation, aeration and dissolved oxygen concentration. The yield of the process has been calculated in terms of glucose consumed. Initial studies showed that fermenter grown cells have more than 15 times higher activity than that of the shake flask grown cells. The medium pH was found to have unspecific but significant influence on the enzyme productivity. However, at controlled pH 5.5 the specific enzyme activity was highest (306U/mg). Higher agitation had detrimental effect on the cell mass production. Dissolved oxygen concentration was maintained by automatic control of the agitation speed at an aeration rate of 0.6 volume per volume per minute (vvm). Optimization of glucose concentration yielded 21g/l cell mass with and 9.77x10(3)U carbonyl reductase activity/g glucose. Adaptation of different strategies for glucose feeding in the fermenter broth was helpful in increasing the process yield. Feeding of glucose at a continuous rate after 3h of cultivation yielded 0.97g cell mass/g glucose corresponding to 29.1g/l cell mass. Volumetric oxygen transfer coefficient (K(L)a) increased with the increasing of agitation rate.     

Expression of recombinant cytoplasmic yeast pyruvate carboxylase for the improvement of the production of human erythropoietin by recombinant BHK-21 cells.

Recently, a recombinant yeast pyruvate carboxylase expressed in the cytoplasm of BHK-21 cells was shown to reconstitute the missing link between glycolysis and TCA, thus increasing the flux of glucose into the TCA and resulting in a higher intracellular ATP content. Now, these metabolically engineered cells have been additionally transfected with a plasmid bearing the gene for human erythropoietin. EPO yield and substrate-specific productivity of the recombinant BHK-21 cells have been compared to control cells without the PYC2-gene but transfected with the plasmid coding for the expression of the selection genes and EPO. PYC2-expressing clones showed a 2-fold higher glucose-specific productivity and a 2-fold higher product concentration in a continuously perfused bioreactor. Moreover, the PYC2 expression enabled the cells to become more resistant to low glucose concentrations in the culture medium. They could produce at nearly maximum productivity under glucose-limiting conditions of 0.05-1 gl(-1) that guaranteed a reduced accumulation of lactate in fed-batch production systems. Due to the fact that PYC2-expressing cells are characterized by reduced glucose consumption, a prolonged production phase in bioreactors can be maintained. Based on the demand not to fall short of 80% cell viability for the production, EPO could be produced for 2 days (30%) longer compared to the control due to a more economic exploitation of glucose, and the prolonged viability period of the cells using a batch cultivation driven by glutamine limitation.     

连续灌流培养杂交瘤细胞生产单克隆抗体

自 2 0世纪 70年代以来 ,工程抗体在基础医学研究、临床诊断和治疗 ,以及免疫预防等领域中的广泛应用 ,大大促进了其产业化的进程。目前工业化生产单克隆抗体的主要方法是通过发酵罐、中空纤维和固定床等生物反应器培养系统 ,以微载体、微包囊法在体外大规模高密度培养杂交瘤细胞 ,再通过相关的纯化手段浓缩纯化制备抗体[1 ,2 ] 。就操作方式而言 ,一般采用两个基本策略 :①大容量高密度的悬浮培养 ,最多采用的是搅拌式气升式生物反应器 ,通过微载体依托细胞相对固定化 ,降低了搅拌培养时对细胞的剪切力 ,提高细胞的密度和稳定性及生产率。…