Propagation ofSpodoptera frugiperda cells (Sf9) and production of recombinant proteins with the baculovirus expression system using improved spinner flasks with membrane aeration

Summary It has been shown that the growth of Spodoptera frugiperda cells is significantly reduced or ceased under oxygen limiting culture conditions. This paper describes the use of a new membrane-aerated spinner flask which was compared to conventional surface-aerated spinner flasks with regard to growth of the insect cell line Sf9 and recombinant protein production after infection with baculovirus. Using a commercially available serum-free culture medium Sf9 cells reached highest cell densities (3×10⁶ ml^–1) in the membrane-aerated spinner flask. Production of recombinant protein was also influenced by the oxygen supply. In the membrane-aerated spinner flask and in a surface-aerated spinner flask with reduced filling volume more than 20000 U ml^–1 of a recombinant interleukin-2 variant were accumulated whereas only 100 U ml^–1 were produced in a surface-aerated spinner flask with insufficient oxygen supply. Sufficient oxygenation appears to be essential for proliferation of Sf9 cells as well as recombinant protein production after infection with baculovirus. Membrane oxygenation allows sufficient oxygen supply at high cell density and an at least 2.5 fold higher filling volume per spinner unit.     

The culture of rat myeloma and rat hybridoma cells in a protein-free medium

Y0 is a rat x rat hybridoma cell line, which does not secrete immunoglobulin, produced using a fusion partner derived from the Y3 (Y3,Ag.1.2.3) rat myoloma cell line. Y0 and Y3 have both been widely used as fusion partners in the production of rat x rat hybridomas. Y0 has also been used in recombinant gene technology. Y0 cells grown in shake flask culture, using RPMI 1640 medium with 4mM l-glutamine and 5% foetal bovine serum, reached a maximal cell density of 1.5×10⁶ cells ml^–1 with 86% viability. Y0 cells which has been adapted to grow in ABC protein-free medium reached a maximal density, in shake flask culture, of 8.75×10⁵ cells ml^–1 with 79% viability. An improved protein-free medium, designated W38 medium, was developed. In shake flask culture, W38 medium supported Y0 cell growth to a density of 2.02×10⁶ cells ml^–1 with 96% viability. Two Y3 hybridomas, YID 13.9.4 cells and SAM 618 cells were adapted to growth in W38 medium. For both hybridomas, cell growth and product yield in shake flask culture using W38 medium was superior to that obtained with serum-containing RPMI 1640 medium.Abbreviations F12 Hams F12 medium - DMEM Dulbeccos medium - RPMI RPMI 1640 medium - FBS foetal bovine serum     

Development of a serum-free culture medium for the large scale production of recombinant protein from a Chinese hamster ovary cell line

A serum-free medium, WCM5, has been developed for the large scale propagation of CHO (Chinese hamster ovary) cells which express recombinant protein using dihydrofolate reductase as a selectable marker. WCM5 was prepared by supplementing Iscoves medium without lecithin, albumin or transferrin with a number of components which were shown to benefit growth. WCM5 medium contained 5 mg l^–1 human recombinant insulin (Nucellin) but was otherwise protein-free. CHO 3D11^* cells which had been engineered to express a humanised antibody, CAMPATH^*-1H, were routinely grown using serum-containing medium. From a seeding density of 10⁵ cells ml^–1, cells grown in static culture with serum reached a maximal cell density of 6.5×10⁵ cells ml^–1 after 6 days in culture and produced a maximal antibody concentration of 69 mg l^–1 after 11 days in culture. CHO 3D11^* cells grown with serum were washed in serum-free medium then cultured in WCM5 medium. Following a period of adaptation the cell growth and product yield was superior to that achieved with serum-containing medium. CHO cells producing CAMPATH-1H grown in an 8000 l stirred bioreactor seeded with 2×10⁵ cells ml^–1 reached a maximal viable cell density of 2.16×10⁶ cells ml^–1 after 108 h in culture and a maximal antibody concentration of 131.1 mg l^–1 after 122 h in culture.Abbreviations CHO Chinese hamster ovary - dhfr dihydrofolate reductase - dhfr dihydrofolate reductase deficient - MTX methotrexate - H hypoxanthine - T thymidine - T/V trypsin versene - F12 Hams F12 medium - NEAA non essential amino acids     

Adaptation of cholesterol-requiring NS0 mouse myeloma cells to high density growth in a fully defined protein-free and cholesterol-free culture medium

NS0 has been used as a fusion partner for the production of hybridomas and has more recently been engineered to produce recombinant protein. A protein-free culture medium, designated W38 medium, has previously been developed which supported high density growth of rat myeloma and hybridoma cell lines. NS0 cells failed to grow in W38 medium and in a number of protein-free culture media which support the growth of other myeloma cell lines. NS0 cells are derived from the NS-1 cell line, which is known to require exogencus cholesterol. It was found that NS0 cells grew in W38 medium supplemented with phosphatidylcholine, cholesterol, and albumin and that NS0 were auxotrophic for cholesterol. Protein-free growth of NS0 cells was achieved by using -cyclodextrin to replace albumin as a lipid carrier. The maximal cell density reached in this protein-free medium was in excess of 1.5×10⁶ cell ml^–1. The lipid supplements in the medium precipitated after a few days storage at +4°C. In order to overcome this problem a protocol was developed which allowed NS0 cells to be adapted to cholesterol-independent growth in W38 medium. NS0.CF (cholesterol-independent NS0 cells) were cultured continuously in W38 medium for several months. In shake flask culture a cell density of 2.4×10⁶ cells ml^–1 was achieved in W38 medium compared with 1.41×10⁶ cells ml^–1 in RPMI 1640 medium containing 10% foetal bovine serum. NS0.CF cells readily grew in a 1 litre stirred bioreactor using W38 medium supplemented with Pluronic F68 reaching a density of 3.24×10⁶ cells ml^–1. NS0.CF were cloned protein-free by limiting dilution in W38 medium, giving colonies in wells that were seeded at an average density of 0.32 cells per 200 l. This study has demonstrated for the first time the growth of a cholesterol-requiring mouse myeloma cell line in a completely defined protein-free medium and its subsequent adaptation to cholesterol-independence.Abbreviations BSA bovine serum albumin - C cholesterol - CD cyclodextrin - F68 Pluronic F68 - GS glutamine synthetase - P phosphatidylcholine - PC-FBS phosphatidylcholine, cholesterol and foetal bovine serum - RPMI RPMI 1640 medium - MSX methionine sulphoximine     

Improved methods for investigating the external redox potential in hybridoma cell culture

Because of the interest in understanding and optimizing secretion of proteins from mammalian cells, reliable and more reproducible methods are needed to monitor the external redox potential of animal cells in suspension culture. An improved off-line method was established that greatly reduces the typically long response time of redox electrodes in cell culture media and improves the standardization of redox probes. In addition, the dependence of medium redox potential on dissolved oxygen concentrations and pH was investigated using cell-free medium. Off-line as well as on-line redox potential measurements were then applied to spinner or bioreactor cultures of murine hybridoma cells. Serum containing or protein-free medium were used. The time dependence of the experimentally determined external redox potential was found to be affected not only by oxygen, pH, and medium composition. but to a significant extent by the rate of generation of reductants by hybridoma cells. The observed specific rate of medium reduction by generation of reductants (mV h^–1 viable cell^–1) decreased during exponential growth while cell number increased from 2×10⁵ viable cells ml^–1 to 3.5×10⁶ viable cells ml^–1. This rate, however, was essentially constant at –7.3 mV h^–1±3.7 mV h^–1 per 10¹⁰ viable cells during growth under conditions of constant dissolved oxygen tension and constant pH. Using these observations, the quantity of reductants synthesized and secreted into the medium by viable hybridoma cells was estimated to be approximately 1.3 mole h^–1 per 10¹⁰ viable hybridoma cells. The time course of specific monoclonal antibody secretion rate did not correlate with changes in the external oxidation/reduction potential in either serum containing or protein-free medium.     

Enhanced antibody production associated with altered amino acid metabolism in a hybridoma high-density perfusion culture established by gravity separation

A high density hybridoma perfusion culture was established by separating and recycling cells from the product stream to the reactor using a simple external sedimentation-based separator — an inclined modified Erlenmeyer flask. After 3 weeks, when the optimal perfusion rate of 1.0 day^–1 had been reached, viable cell density stabilized at around 10×10⁶ cells ml^–1, a level five times that obtained by simple batch culture. The efficiency of the separator was enhanced by cell flocculation. Specific antibody productivity, which was initially 0.4 g 1×10⁶ cells^–1 h^–1, decreased to half that value while cell density was increasing, but recovered to the initial level when the culture finally stabilized at a high cell density. During the final phase, when viable cell density and specific antibody production were high, there was a marked shift in metabolism. Consumption of the two most important substrates for energy generation, glucose and glutamine, caused their broth concentrations to decrease to 1.5 mM and 1 mM, respectively, from input medium concentrations of 25 mM and 10 mM, respectively. At the same time there was an increase in the specific production of glycine and aspartate, their broth concentrations reaching 1.5 mM and 0.02 mM, respectively. We suggest that this shift in metabolism results in enhanced production of ATP from glutamine. The specific glucose consumption and lactate production also indicate that there is a shift to more energy efficient metabolism. The mechanism whereby this leads to enhanced specific antibody production remains to be elucidated. Nevertheless, the combination of high cell density and enhanced productivity obtained with the present perfusion culture resulted in a high monoclonal antibody production –100 mg l^–1 d^–1.     

Software sensors for the monitoring of perfusion cultures: Evaluation of the hybridoma density and the medium composition from glucose concentration measurements

New software sensors based on the Extended Kalman Filter technique have been developed for the monitoring of animal cell perfusion cultures. They use a kinetic model describing the growth, death and metabolism of hybridoma cells as a function of the medium composition. The model was initially validated on a batch culture and found to correctly predict the continuous perfusion culture kinetics, except for the production of ammonia and lactate. Using the measurement of a single component in the culture medium, in this case glucose, the Extended Kalman Filter provides an excellent evaluation of the time variation of the concentrations of living and dead cells, of glutamine and antibodies, during the whole perfusion culture for a retained cell density rising from 1 to 11×10⁶ cells.ml^–1 inside the reactor.     

Optimization of monoclonal antibody production: combined effects of potassium acetate and perfusion in a stirred tank bioreactor

To increase the yield of monoclonal antibody in a hybridoma culture, it is important to optimize the combination of several factors including cell density, antibody productivity per cell, and the duration of the culture. Potassium acetate enhances the production of antibodies by cells but sometimes depresses cell density. The production of anti-(human B-type red blood cell surface antigen) antibody by Cp9B hybridoma was studied. In batch cultures, potassium acetate inhibited Cp9B cells growth and decreased the maximal cell density but the productivity of antibody per cell was increased. The balance of the two effects resulted in a slight decline of antibody production. In a stirred tank bioreactor, the inhibitory effect of potassium acetate on cell density was overcome by applying the perfusion technique with the attachment of a cell-recycling apparatus to the bioreactor. In such a reactor, potassium acetate at 1 g l^-1 did not cause a decrease in the cell density, and the antibody concentration in the culture supernatant was increased from 28 μg ml^-1 to 38 μg ml^-1. Potassium acetate also suppressed the consumption of glucose and the accumulation of lactate in batch cultures, but the glucose and lactate levels were kept stable by applying the perfusion technique in the stirred tank bioreactor. This revised version was published online in July 2006 with corrections to the Cover Date.     

Improvement of the culture stability of non-anchorage-dependent animal cells grown in serum-free media through immobilization

A murine hybridoma cell line producing a monoclonal antibody against penicillin-G-amidase and a murine transfectoma cell line secreting a monovalent chimeric human/mouse Fab-antibody fragment were cultivated in three different media (serum-containing, low protein serum-free, and iron-rich protein-free) in flask cultures, stirred reactors and a fixed bed reactor. In static batch cultures in flasks both cell lines showed similar good growth in all three media.In suspension in a stirred reactor, the hybridoma cell line could be cultivated satisfactory only in serum-containing medium. In low protein serum-free medium, Pluronic F68 had to be added to protect the hybridoma cells against shear stress. But even with this supplement only batch, not chemostat mode was possible. In iron-rich protein-free medium the hybridoma cells grew also in continuous chemostat mode, but the stability of the culture was low. The transfectoma cell line did not grow in stirred reactors in any of the three media.Good results with both cell lines were obtained in fixed bed experiments, where the cells were immobilized in macroporous Siran^®-carriers. The media, which were optimized in flask cultures, could be used without any further adaptation in the fixed bed reactor. Immobilization improved the stability and reliability of cultures of non-adherent animal cells in serum-free media tremendously compared to suspension cultures in stirred reactors. The volume-specific glucose uptake rate, an, indicator of the activity of the immobilized cells, was similar in all three media. Deviations in the metabolism of immobilized and suspended cells seem to be mainly due to low oxygen concentrations within the macroporous carriers, where the cells are supplied with oxygen only by diffusion.List of symbols c substrate or product concentration mmol l^–1 - c₀ substrate or product concentration in the feed mmol l^–1 - c_Glc glucose concentration mmol l^–1 - c_Gln glutamine concentration mmol l^–1 - c_Amm ammonia concentration mmol l^–1 - c_Lac lactate concentration mmol l^–1 - c_FAB concentration of Fab# 10 antibody fragment g l^–1 - c_MAb monoclonal antibody concentration mg l^–1 - D dilution rate d^–1 - q cell-specific substrate uptake or metabolite production rate mmol cell^–1 h^–1 - q_Glc cell-specific glucose uptake rate mmol cell^–1 h^–1 - q_Gln cell-specific glutamine uptake rate mmol cell^–1 h^–1 - q_MAb cell-specific MAb production rate mg cell^–1 h^–1 - q^* volume-specific substrate uptake or metabolite production rate mmol l^–1 h^–1 - q^*FB volume-specific substrate uptake or metabolite production rate related to the fixed bed volume mmol l_FB ^–1 h^–1 - q^*FB,Glc volume-specific glucose uptake rate related to the fixed bed volume mmol l_FB ^–1 h^–1 - q^*FB,Gln volume-specific glutamine uptake rate related to the fixed volume mmol l_FB ^–1 h^–1 - q^*FB,MAb volume-specific MAb production rate related to the fixed volume mg l_FB ^–1 h^–1 - q^*FB,02 volume-specific oxygen uptake rate related to the fixed bed volume mmol l_FB ^–1 h^–1 - t time h - U superficial flow velocity mm s^–1 - V medium volume in the conditioning vessel of the fixed bed reactor l - V_FB volume of the fixed bed l - x_v viable cell concentration cells ml^–1 - y_Amm,Gln yield of Ammonia from glutamine - y_Lac,Glc yield of lactate from glucose - specific growth rate h^–1 - _d specific death rate h^–1     

Peptone,a low-cost growth-promoting nutrient for intensive animal cell culture

The effect of addition of peptone to serum-free and serum supplemented media for the growth of hybridoma cells in various systems was studied. Supplementation of defined medium with either proteose peptone or meat peptone resulted in significant increases in cell number and specific monoclonal antibody production in batch culture system. Other peptones were either inactive or less effective. In continuous culture, using medium supplemented with new born calf serum, the addition of peptone resulted in 125% and 150% increases in cell and antibody concentrations respectively. Similar increase in cell number (128%) was also obtained in spin-filter perfusion culture when medium was supplemented with peptone. By comparison, the substitution of a defined 1xMEM amino acids mixture resulted in only a 50% increase. At higher perfusion rates the cell number maintained in steady state using peptone supplement could be increased to 1.3×10⁷ cells ml^–1 while the serum concentration was reduced from 5% to 1% at a perfusion rate of 2.5 volumes per day.     

Improved yields of the extracellular domain of the epidermal growth factor receptor produced using the baculovirus expression system by medium replacement following infection

The extracellular domain of the epidermal growth factor receptor (EGFR) was expressed using the baculovirus expression vector system. The maximum level of the EGFR extracellular domain secreted into the medium in Sf-9 (Spodoptera frugiperda or fall armyworm) cell batch culture was approximately 2.5 g ml^–1. In order to increase this yield, a process was developed that included the following sequence of steps: batch growth to maximum cell density, infection of the cells with recombinant virus, and replacement of spent medium. By using this process, the specific yield of recombinant protein, which in batch culture drops when infection is carried out at densities greater than 3 × 10⁶ cells ml^–1, can be maintained at a maximum in cultures infected at densities of 10⁷ cells ml^–1 or greater. The process, when applied to 3-1 and 11-1 bioreactor cultures, allowed a maximum volumetric yield of triple the maximum value attainable in batch culture. Spent-medium analysis indicates that medium replacement provides certain nutrients that could otherwise be limiting for recombinant protein production.     

A low-cost chemically defined protein free medium for a recombinant CHO cell line producing prothrombin

A chemically defined protein free medium, DF6S, was developed for the cultivation of a recombinant Chinese hamster ovary cell line (CHO2DS) producing human prothrombin in suspension batch culture. DF6S was formulated by optimizing DME/F12 with amino acids and supplementing the optimized DME/F12 with aurintricarboxylic acid, ethanolamine, ferric sulfate, Pluronic F68, putrescine and sodium pyruvate. From a seeding density of 2.3 × 10⁵ cells ml^–1, CHO2DS cells grown in suspension in DF6S medium reached a maximal cell density of 1.92 × 10⁶ cells ml^–1 with an accumulated prothrombin concentration of 16.7 mg l^–1 after 6 days in culture.     

Production of a membrane-bound proteins,the human gamma-glutamyl transferase,by CHO cells cultivated on microcarriers,in aggregates and in suspension

Recombinant Chinese Hamster Ovary (CHO) cells, engineered for the production of human gamma-glutamyl transferase (GGT), have been grown on Cytodex 1 microcarriers, as aggregates, or as single cells in suspension after adaptation. GGT is a membrane bound enzyme which was not secreted during the culture period. The maximal enzyme activity was found to be directly related to the achieved maximal cell density. Culture of CHO on microcarriers yielded the fastest growth, with a specific growth rate of 0.04 h^–1, the highest cell density (near 1.3×10⁶ cells ml^–1), and the highest enzyme activity around 300 mU ml^–1, which corresponded to a specific cellular level of 20 mU 10^–5 cells. GGT could also be produced by growing CHO cells in suspension as single cells or as aggregates. Under these conditions, however, the specific CHO growth rate was significantly slower and the GGT level per cell was divided by a factor 6. Growing CHO cells without microcarriers also resulted in differences in cell metabolism, with a higher conversion yield of glutamine into ammonia, and a higher cell lysis. The catalytic kinetic constants of the enzyme were found identical for the three culture systems.     

CYTOKINES INVOLVING gp130 IN SIGNAL TRANSDUCTION SUPPRESSED GROWTH OF A MOUSE HYBRIDOMA CELL LINE AND ENHANCED ITS ANTIBODY PRODUCTION

Three cytokines, interleukin 6 (IL-6), leukaemia inhibitory factor (LIF), and oncostatin M (OSM), that bind to composite receptors including a common signal transducer gp130 suppressed proliferation of a mouse B-cell hybridoma cell line 2E3-O cultured in serum-free medium, while they enhanced antibody production of the cells. The specific growth rate of the cells reduced from 1.0/day for control to 0.6/day for the cultures supplemented with IL-6, LIF, or OSM at 1, 4, or 2 ng/ml, respectively. The antibody productivity increased five-fold when the cells were cultured with IL-6, LIF, or OSM at 1, 25, or 20 ng/ml, respectively. Transforming growth factor β1 (TGF-β1) similarly suppressed growth of the cells at the concentration of 5 ng/ml, while it did not enhance the antibody production. Cell cycle analysis revealed that IL-6 induced the cells to be arrested at G₁phase of the cell cycle more intensively than TGF-β1, indicating that IL-6 and TGF-β1 suppressed the growth through mutually different mechanisms. As a whole, this work suggests that gp130, which is commonly involved in each receptor for IL-6, LIF, OSM, transduces signals for suppressing proliferation and possibly for enhancing antibody production in the hybridoma cells.     

Efficient production by Escherichia coli of recombinant protein using salting-out effect protecting against proteolytic degradation

To produce glucoamylase efficiently as a recombinant protein, E. coli was grown with 20 g (NH₄)₂SO₄ l^–1 which removed proteolytic activity but did not effect cell growth. Growth in M9 medium with 20 g (NH₄)₂SO₄ l^–1 produced 11 U glucoamylase ml^–1 compared to 7 U ml^–1 without addition. Furthermore, the glucoamylase activity was maintained at about 9 U ml^–1.     

Influence of acetate on the growth of recombinant Escherichia coli JM103 and product formation

The influence of the acetate addeed to the M9 minimal medium and to the Luria-Bertani medium without and with glucose supplement on the growth of recombinant Escherichia coli J103 with three different types of multicopy plasmids and on the production of the fusion protein SpA :: EcoRI were investigated in shake flasks without and with induction of the gene expression by a temperature shift from 30 °C to 42 °C. At the beginning of the induction of gene expression concentrated LB-medium was added to the shake flask. Without this supplement of M9 medium no gene expression occurred.List of Symbols LB Luria Bertani cultivation medium (Table 2) - M9 cultivation medium (Table 1) - P enzym activity [U ml^–1] - te]TCC total cell count [10⁶ cells ml^–1] - specific growth rate [h-1]     

Metabolic and kinetic studies of hybridomas in exponentially fed-batch cultures using T-flasks

Exponentially fed-batch cultures (EFBC) of a murine hybridoma in T-flasks were explored as a simple alternative experimental tool to chemostats for the study of metabolism, growth and monoclonal antibody (MAb) production kinetics. EFBC were operated in the variable volume mode using an exponentially increasing and predetermined stepwise feeding profile of fresh complete medium. The dynamic and steady-state behaviors of the EFBC coincided with those reported for chemostats at dilution rates below the maximum growth rate. In particular, steady-state for growth rate and concentration of viable cells, glucose, and lactate was attained at different dilution rates between 0.005 and 0.05 h^–1. For such a range, the glucose and lactate metabolic quotients and the steady-state glucose concentration increased, whereas total MAb, volumetric, and specific MAb production rates decreased 65-, 6-, and 3-fold, respectively, with increasing dilution rates. The lactate from glucose yield remained relatively constant for dilution rates up to 0.03 h^–1, where it started to decrease. In contrast, viability remained above 80% at high dilution rates but rapidly decreased at dilution rates below 0.02 h^–1. No true washout occurred during operation above the maximum growth, as concluded from the constant viable cell number. However, growth rate decreased to as low as 0.01 h^–1, suggesting the requirement of a minimum cell density, and concomitant autocrine growth factors, for growth. Chemostat operation drawbacks were avoided by EFBC in T-flasks. Namely, simple and stable operation was obtained at dilution rates ranging from very low to above the maximum growth rate. Furthermore, simultaneous operation of multiple experiments in reduced size was possible, minimizing start-up time, media and equipment costs.Abbreviations EFBC exponentially-fed batch culture - CSC continuous suspended culture - MAb monoclonal antibody - D dilution rate - q _i metabolic quotient or specific rate of consumption or production of i     

Enhancing effect of mouse peritoneal exudate cells and their products on antibody productivity of hybridoma cells: Application of in vivo factors to in vitro culture

Mouse peritoneal exudate cells induced by casein enhanced in vitro antibody production rate per cell of a hybridoma in co-culture. Culture supernatant of the exudate cells also enhanced three-fold the antibody productivity when added to cultures of a hybridoma at 10% (v/v). Hence the enhancement of antibody productivity by the exudate cells seemed to be caused by soluble enhancing factors secreted by the exudate cells. The exudate cells maximally secreted the enhancing factors when harvested from mice on day 4 of the induction period following the injection of casein. A semi-continuous culture of the hybridoma demonstrated the applicability of the culture supernatant to enhance antibody production by producing a two-fold increase over the control for seven days when supplemented with the supernatant at 5%. Significant amounts of interleukin-6 were detected in culture supernatant of the exudate cells. Interleukin-6 obtained from other sources enhanced the antibody productivity two-fold when added to the hybridoma culture at the concentration of 5 unit/ml. Interleukin-6, therefore, is expected to be one of the principal antibody enhancing factors secreted by the exudate cells. Other interleukins examined, that is, interleukin-1 to-5 did not enhance the antibody productivity.     

Effect of some vertebrate and invertebrate hormones on the population growth, mictic female production, and body size of the marine rotifer Brachionus plicatilis Müller

Eight vertebrate and invertebrate hormones were screened for theireffect on population growth, mictic female production, and body size of themarine rotifer Brachionus plicatilis. Growth hormone (GH) or human chorionicgonadotropin (HCG) at 0.0025–25 I.U. ml^–1 andestradiol-17 (E₂), triiodothyronine (T_{_3}),20-hydroxyecdysone (20-HE), 5-hydroxytryptamine (5-HT), gamma-aminobutyricacid (GABA) or juvenile hormone (JH) at 0.05–50 mg l^–1were added to 5-ml of Nannochloropsis oculata suspension (7×10⁶ cells ml^–1). From an initial densityof 1 individual ml^–1, rotifers were cultured with hormones for48 hours in 22 ppt seawater at 25 °C, in darkness.Rotifers were counted and classified into female types and transferred to anew algal food suspension without hormone every other day until day 8 whenbody size was measured. Population growth was significantly higher intreatments exposed to GABA (50 mg l^–1), GH (0.0025 and 0.025I.U. ml^–1), HCG (0.25 and 2.5 I.U. ml^–1), and5-HT (5 mg l^–1). E₂ caused a decrease inpopulation growth, whereas JH, 20HE, and T₃ had no effect.Mictic female production was significantly higher at 0.05 and 0.5 mgl^–1 JH and 0.05 and 5 mg l^–1 5HT. GH (0.0025 and0.025 I.U. ml^–1), E₂ (50 mg l^–1),GABA (0.5, 5 and 50 mg l^–1), and 20-HE (0.05 mgl^–1) treatments had significantly higher mictic femaleproduction only on day 8, 6, 4, and 6, respectively. T₃ andhCG had no effect on mictic female production. Lorica length increased by9.6% and 4.4% in rotifers treated with JH (0.05 mgl^–1) and GABA (5 mg l^–1), respectively. Correspondingly, lorica width increased by 8.9% and 2.6% inthese treatments. In comparison, 20-HE-, T₃-, and HCG-treatedrotifers were smaller (3.9–8.2%) and GH, 5-HT andE₂ had no effect on rotifer body size.     

Induction of apoptosis in oxygen-deprived cultures of hybridoma cells

It is now well documented that apoptosis represents the prevalent mode of cell death in hybridoma cultures. Apoptotic or programmed cell death occurs spontaneously in late exponential phase of batch cultures. Until lately, no specific triggering factors had been identified. Recently, we observed that glutamine, cystine or glucose deprivation induced apoptosis in both hybridoma and myeloma cell lines whereas accumulation of toxic metabolites induced necrotic cell death in these cells. Other triggering factors such as oxygen deprivation might also be responsible for induction of apoptosis. In the present study, induction of cell death by exposure to anoxia was examined in batch culture of the SP2/0-derived hybridoma D5 clone. The mode of cell death was studied by morphological examination of acridine orange-ethidium bromide stained cells in a 1.5 L bioreactor culture grown under anoxic conditions for 75 hours. Under such conditions, viable cell density levelled off rapidly and remained constant for 25 hours. After 45 hours of anoxia, cell viability had decreased to 30% and the dead cell population was found to be 90% apoptotic. In terms of cellular metabolism, anoxia resulted in an increase in the utilization rates of glucose and arginine, and in a decrease in the utilization rate of glutamine. The lactate production rate and the yield of lactate on glucose increased significantly while the MAb production rate decreased. These results demonstrate that glycolysis becomes the main source of energy under anoxic conditions.Cells incubated for 10 hours or less under anoxic conditions were able to recuperate almost immediately and displayed normal growth rates when reincubated in oxic conditions whereas cells incubated for 22 hours or more displayed reduced growth rates. Nonetheless, even after 22 h or 29 h of anoxia, cells reincubated in oxic conditions showed no further progression into apoptosis. Therefore, upon removal of the triggering signal, induction of apoptosis ceased.Abbreviations VNA Viable non-apoptotic cells - VA Viable apoptotic cells - NVNA Nonviable non-apoptotic or necrotic cells - NVA Nonviable apoptotic cells - CF Chromatin-free cells (late nonviable apoptotic cells) - AO Acridine orange - EB Ethidium Bromide - MAb Monoclocnal antibody - D.O. Dissolved oxygen - qMAb Specific MAb production rate (mg. (10⁹ cells)^–1.day^–1) - Specific growth rate (h^–1) - X_v Viable cell number (10⁵ cells.mL^–1) - X_t Total cell number (10⁵ cells.mL^–1) - Y_lac/glc Yield coefficient of lactate on glucose (mM lactate produced/mM glucose consumed)