Human T-cell hybridomas producing lymphokines. II. Enhancement of lymphotoxin secretion from human T-cell hybridomas by phorbol myristate acetate

Human lymphotoxin (LT)-producing T-cell hybridomas were constructed by fusing concanavalin A-activated human peripheral blood lymphocytes with emetine-actinomycin D-pretreated human acute lymphatic leukemia cells. LT secretion from these hybridomas was considerably enhanced by stimulation with phorbol-12-myristate-13-acetate (PMA) and concanavalin A or PMA alone. A study using cloned hybrid lines revealed that PMA/Con A acted directly on the LT-producing clones. Furthermore, PMA/Con A stimulated A-B9-24, one of the cloned hybridomas, and secreted fourfold larger amounts of LT under serum-free conditions than under serum-containing conditions. However, MIF/MAF and LT-producing cloned hybrid line E10-20 secreted rather decreased amounts of MIF/MAF when stimulated with PMA, while the LT secretion from the same hybridoma was enhanced with PMA.     

Ammonia inhibition of hybridomas propagated in batch, fed-batch, and continuous culture

The nature and temporal development of ammonia inhbition were investigated in batch, fed-batch, and continuous cultures. Significant inhibition was observed when cells were inoculated in serum-containing or chemically defined medium containing more than 2 mM of ammonia. In contrast, no inhibition was observed at greater than 10 mM when the ammonia concentration was gradually increased over the span of a batch culture by feeding ammonium chloride. Strong growth inhibition was observed after each of five step changes (2.8 --> 3.7 --> 4.0 --> 4.9 --> 7.7 --> 13.5 mM) in continuous culture. Following a period of adaptation at each higher value, the viable cell density stabilized at a new lower value. The lowering in viable cell density was caused by an increase in specific death rate and a decreased cell yield on glucose, glutamine, and oxygen. Increased ammonia concentration had little or no effect on the steady-state specific growth kinetics or specific antibody productivity. (c) 1994 John Wiley & Sons, Inc.     

Comparison of growth kinetics of producing and nonproducing hybridoma cells in batch culture.

Several clones of nonproducing cells were isolated from a continuous culture of hybridoma cells, which were originally producing antibody. Their behavior was compared to that of the producing cells in batch culture. The growth kinetics of five out of six clones exhibited higher specific growth rate, higher yield of cell mass on glutamine, and lower yields of lactate and ammonium. The implications of the comparisons for growth of hybridoma cultures are discussed.     

Growth of Nitrosomonas europaea in batch and continuous culture

Summary A clear medium has been used to grow pur cultures of Nitrosomonas europaea in flasks and in a continuous culture apparatus.Of several metallic ions examined in flask cultures of Nitrosomonas, Fe at 2 ppm and Co, Mn and Zn at 1 ppm were not toxic, Ni and Cr at concentrations greater than 0.25 ppm inhibited growth and Cu stopped growth completely at 0.5 ppm and inhibited at 0.1 ppm. Stainless steel of the specification EN58 B did not affect growth.In the continuous culture vessel, Nitrosomonas showed a growth response to Fe only when the population exceeded about 500×10⁶ organisms/ml. The minimum doubling time was about 8 hours in flasks and 11 hours in the culture vessel. With effective aeration and automatic P_H control, cultures of Nitrosomonas were grown successfully in continuous culture and gave a yield of 2.14 g dry weight of bacteria from 30 litres of culture in 5 days.     

Transient behavior of T-cell hybridomas in response to changes in metabolite concentrations in continuous culture.

Effects of pulse and step changes in major metabolite concentrations such as glucose, glutamine, lactic acid, and ammonium on behavior of T-cell hybridomas in continuous culture were investigated in order to develop a strategy to maximize specific rate of lymphokine formation. Step increases in glucose, lactic acid, and ammonium concentrations decreased, and a step increase in glutamine concentration increased, the specific rate of lymphokine formation. Effects of step and pulse changes on specific rates of glucose and glutamine consumption and viability of cells were also investigated.     

Growth of Nitrosomonas europaea in batch and in continuous culture

Summary Techniques are described in this paper for growing Nitrosomonas europea in batch and in continuous culture with apparatus constructed from readily available laboratory materials.The methods employed in batch culture have enabled the collection of cells concentrated in small volumes. Nitrosomonas europaea has been grown successfully in continuous culture and yields of 23 g wet weight were obtained, an average of 0.16 g/l with a flow rate of 300 ml/h over twenty days. Results show that high levels of nitrite do not materially affect the growth of the bacterium. The continuous culture equipment has also been used to grow Azotobacter vinelandii and Thiobacillus concretivorus.     

Growth and development kinetics of Bacillus thuringiensis in batch culture

The kinetics of Bacillus thuringiensis growth and its assimilation of nutrient substances were studied under the conditions of batch cultivation in a complex medium containing yeast extract and in a chemically defined medium with amino acids. The growth of B. thuringiensis can be divided into five phases: exponential growth; decelerated growth; stationary phase when protein crystals are formed; stationary phase when spores are formed; lysis of sporangia releasing spores. The first phase may in turn be subdivided into three stages according to changes in the specific growth rate and substrate assimilation: a high specific growth rate and no glucose assimilation; an abrupt drop in mu and the beginning of intensive glucose assimilation from the medium; a new rise in the specific growth rate. As follows from the results of studying the kinetics of B. thuringiensis growth in a chemically defined medium, the above changes in the exponential growth phase are due to the fact that the culture assimilates yeast extract components in the complex medium or amino acids in the chemically defined medium during this phase, and then starts to assimilate glucose and ammonium in the following phases of growth.     

Kinetics of product formation in batch and continuous culture of Clostridium barkeri

Summary The main fermentation end products in batch culture (unlimited glucose supply) of Clostridium barkeri were butyrate and lactate. The specific rate of butyrate production was linearly proportional to the growth rate while the specific rate of lactate production increased at low growth rates. In a glucose limited chemostat culture butyrate production was partly growth associated while acetate and lactate production was growth associated. Lactate was, however, only produced at high dilution rates. By varying the glucose concentration in the inflowing medium it was shown that lactate production was stimulated by a high feeding rate of the carbon source. These results are discussed in view of the fructose-1,6-diphosphate dependent lactate dehydrogenase activity in many other organisms.     

Growth kinetics of a bacteriophage in continuous culture

Lytic coliphage Qbeta was grown in continuously cultured host bacteria using a cascade of stirred flow reactors. The apparatus was constructed so that the steady stream of exponentially growing bacterial cells passing through the stirred flow reactors served to prevent coevolution brought about by host-parasite interactions. Wall growth was the primary cause for deviation from ideal continuous culture conditions and is largely dependent on the surface structure of the host bacteria. Using an Escherichia coli strain deficient in adhesive type I pili expression, the desynchronization of single burst events could easily be followed over the course of four infection latency periods. Computer simulations based on a two-stage model for the Qbeta infection cycle were in perfect agreement with the experimental data. Applications of the optimized system to strategies of molecular evolution are discussed. (c) 1996 John Wiley & Sons, Inc.     

Growth kinetics of Dioscorea deltoidea and Catharanthus roseus in batch culture

Sugar-limited batch growth of Dioscorea deltoidea and Catharanthus roseus plant cell cultures was studied in a 14-L stirred tank fermentor. With dissolved oxygen concentration monitored and maintained at nonlimiting levels, growth rates and ratios of dry weight to fresh weight were found to be strongly influenced by sugar concentration. Linear relationships between respiration rate and growth rate were observed, and respiration rate was found to drop to a maintenance level after sugar had been fully depleted from the medium. Diosgenin biosynthesis by D. deltoidea was shown to be independent of growth rate. Ajmalicine biosynthesis in C. roseus was negligible during sugar-limited growth but was induced by inoculation into an 80-g/L glucose solution.     

Growth kinetics of Acetobacterium sp. on methanol-formate in continuous culture

The fermentative metabolism of Acetobacterium sp. grown on methanol-formate in continuous culture is described. The reaction stoichiometry of methanol-formate, including cells, were as follows: CH3OH + 1.13HCOOH --> 0.87CH3COOH + 0.47 cell C. Formate enhanced growth yields by approximately 60% compared with methanol-CO2-grown cultures. Comparison of yields on methanol-formate allowed calculation of an energy yield of 1.3 mol ATP per mol acetate formed during homoacetate fermentation. The magnitudes of YEG,the theoretical maximum yield of YE, and m, the maintenance coefficient, were determined by growing the organism in methanol-formate and resulted in 16.5 g cell (mol methanol catabolized)-1 and 0.674 mmol methanol catabolized (g cell)-1 h-1, respectively. It is concluded that formate might replace CO2 as a source of carboxyl donor.     

Growth kinetics and nitrogenase induction inFrankia sp. HFPArI 3 grown in batch culture

Summary Kinetics of growth and nitrogenase induction inFrankia sp. Ar13 were studied in batch culture. Growth on defined medium with NH ₄ ⁺ as the N source displayed typical batch culture kinetics; however, a short stationary phase was followed by autolysis. Removal of NH ₄ ⁺ arrested growth and initiated vesicle differentiation. Vesicle numbers increased linearly and were paralleled by a rise in nitrogenase (acetylene reduction) activity. Nitrogenase activity (10 nM C₂H₄·mg protein^–1·min^–1) was sufficient to support growth on N₂ and protein levels rose in parallel with nitrogenase induction. Optimal conditions for vesicle and nitrogenase induction were investigated. Maximum rates of acetylene reduction were obtained with 5 to 10 mM K₂ HPO₄/KH₂PO₄, 0.1 mM CaCl₂ and MgSO₄. The optimum pH for acetylene reduction and respiration was around 6.7. The amount (5 to 10 g protein/ml) and stage (exponential) of growth of the ammonium-grown inoculum strongly influenced the subsequent development of nitrogenase activity. Propionate was the most effective carbon source tested for nitrogenase induction. Respiration in propionate-grown cells was stimulated by CO₂ and biotin, suggesting that propionate is metabolized via the propionyl CoA pathway.     

Growth kinetics and cellulase biosynthesis in the continuous culture of Trichoderma viride.

Continuous culture studies have been carried out growing Trichoderma viride QM 9123 in a 10 liter stirred fermentor on a medium containing commercial glucose as the carbon source. Experiments were carried out at 30 degrees C and at three controlled pH values of 2.5, 3.0, and 4.0 over a range of dilution rates from 0.01 to 0.11 hr-1. Steady-state values of cell, glucose, and cellulase concentration oxygen tension, and outlet gas oxygen partial pressure were recorded. Values of maximum specific growth rate, endogenous metabolism coefficient, Michaelis-Menten coefficient, yield and maintenance coefficient for glucose were derived and correlated the effect of the hydrogen ion concentration. Specific oxygen uptake rates were correlated with specific growth rates and absorption coefficients were shown to be a function of dilution rate independent of pH. Some data on cellulase biosynthesis were examined and correlated in terms of a maturation time model.     

Growth of Thermoanaerobium brockii in batch and continuous culture at supraoptimal temperatures

Summary Thermoanaerobium brockii was grown in batch and continuous culture at supraoptimal temperatures (>65° C). Specific growth rates were lower in batch (_max>1.0 h^-1) than in continuous cultures (_max1.2–1.4 h^-1). Acetone addition to the medium did not increase critical dilution rate significantly. The media used contained significantly less organic material and sulfide than previously reported media; however, yeast extract requirements were shown to be exceptionally high (60% of the glucose concentration used). Organic substrates inhibited growth and product formation in chemostat cultures whereas the slow formation of acetic acid was observed in batch cultures, but also with virtually no growth. The inhibiting concentration was found to be approximately 15 g organic carbon·l^-1. The maintenance requirements of T. brockii were in the same range as expected of aerobic extreme thermophiles (m_s0.5 g·g^-1·h^-1) and could be met only by glucose and not by yeast extract. Maintenance was obviously not independent of specific growth rate. Production of the stereospecific alcohol-aldehyde/ketone oxidore-ductase was strictly growth associated and its formation was not affected by acetone added to medium.     

Growth and physiology of a yeast cultivated in batch and continuous culture systems

Inoculum size has been found to affect significantly the maximum attainable specific growth rate during batch cultivation ofCandida utilis. Lower inoculum size resulted in an increased growth rate and relatively longer lag. The culture is found to be most active in the beginning of the exponential phase as regards its RNA synthesis rate. Batch data were used for predicting the conditions of the yeast population in single-stage continuous culture system. Predicted and the experimental values showed a reasonable agreement. In single-stage chemostat the physiology of the yeast was studied on the basis RNA, DNA and protein synthesis rates at various growth rates. The results indicate that the productivity of cells and the rate of synthesis of macromolecules is highest at the dilution rate values of 0.33 to 0.35 hr⁻¹. In order to attain so-called unrestricted conditions of growth a pluristage pluristream continuous system was employed. It is assumed that under such conditions the specific growth rate and the synthetic activity of yeasts may reach its maximum on a given medium. The results presented do not show such conditions of growth under the experimental conditions employed (D ₁=0.35 hr⁻¹ andD ₂=0.2 to 1.7 hr⁻¹) withCandida utilis cultivated on beet molasses medium. Second stage of a two-stage two-stream continuous system is constantly fed with the cells from the foregoing stage; this category of cells on entering the new conditions of the second stage is expected to show some adaptation period. Experiments are reported to this effect.     

Human T-cell hybridomas producing migration inhibitory factor and macrophage activating factors

Studies were carried out to determine the heterogeneity of factors that affect macrophage functions using human hybridomas constructed by fusing PHA-activated human peripheral blood lymphocytes with emetine-actinomycin D-pretreated cloned human acute lymphatic leukemia cells (CEM). Three assay systems were used to investigate the activity of the macrophage migration inhibitory factor and of the macrophage activation factors for glucose consumption (MAF-G) and for O2- formation. In the culture supernatant of hybridomas and other cells, various combinations of these activities were detected. The results indicate that at least three molecules are concerned in each of these activities.     

Comparison of a quadroma and its parent hybridomas in fed batch culture

A quadroma (#22 × 63), formed by the fusion of two hybridomas, and its parent hybridomas (#22 and FMC 63) were each grown in fed batch cultures in order to examine the change in antibody productivity over time of the quadroma compared to its parent hybridomas. The growth rate, glucose uptake rate and lactate production rate of the quadroma were found to be intermediate between those of its parent cells of origin. The specific antibody productivity and internal antibody content of the quadroma followed the same decreasing trends over time as those seen in both parent hybridomas. Losses in specific antibody production rate and antibody content, however, occurred at a faster rate for the quadroma than for either of its parent hybridomas. Although the growth of a non-producing subpopulation is presumed to account for the drop in antibody production, there was no direct correlation between the percentage of high antibody containing cells, as determined by flow cytometry, and the specific antibody production rate.     

Growth behavior and protease production by an icelandicthermus sp. isolate in batch and continuous culture

AThermus strain, producing an extracellular protease, was isolated in a hot spring in Iceland. The main growth characteristics of this isolate were studied with different cultivation vessels and different cultivation techniques. A clear and striking dependence of the growth behavior on the cultivation technique was apparent. Higher maximum yield of biomass, higher productivity of biomass, and higher maximum growth rate were found in continuous cultivations compared with batch cultivations. The substrate utilization and the yield of biomass of this strain were much higher than reported for several otherThermus strains. Reproducibility of kinetic data seemed not to depend on the type of cultivation vessel, on the basis of the types of vessels tested, and instability of the population was not observed during cultivations. Production of extracellular protease in our cultivations was apparently growth associated in batch culture, and the specific rate of production in continuous culture was dependent of the dilution rate, implying that certain kinds of regulatory mechanism(s) might be involved.     

Vancomycin production in batch and continuous culture

Production of the glycopeptide antibiotic vancomycin by two Amycolatopsis orientalis strains was examined in batch shake flask culture in a semidefined medium with peptone as the nitrogen source. Different growth and production profiles were observed with the two strains; specific production (Y(p/x)) was threefold higher with strain ATCC 19795 than with strain NCIMB 12945. A defined medium with amino acids as the nitrogen source was developed by use of the Plackett-Burman statistical screening method. This technique identified certain amino acids (glycine, phenylalanine, tyrosine, and arginine) that gave significant increased specific production, whereas phosphate was identified as inhibitory for high specific vancomycin production. Experiments made with the improved medium and strain ATCC 19795 showed that vancomycin production kinetics were either growth dissociated or growth associated, depending on the amino acid concentration. In chemostat culture at a constant dilution rate (0.087 h(-1)), specific vancomycin production rate (q(vancomycin)) decreased linearly as the medium phosphate concentration was increased from 2 to 8 mM. In both phosphate and glucose limited chemostats, q(vancomycin) was a function of specific growth rate; the maximum value was observed at D = 0.087 h(-1) (52% of the maximum specific growth rate). Under phosphate limited growth conditions, q(vancomycin) was threefold higher (0.37 mg/g dry weight/h) than under glucose limitation (0.12 mg/g dry weight/h). (c) 1996 John Wiley & Sons, Inc.