Recombinant human interferon-gamma. Differences in glycosylation and proteolytic processing lead to heterogeneity in batch culture.

Recombinant human interferon-gamma (Hu-IFN-gamma) produced by Chinese-hamster ovary (CHO) cells was analysed by immunoprecipitation and SDS/PAGE. Up to twelve molecular-mass variants were secreted by this cell line. Three variants were recovered after enzymic removal of all N-linked oligosaccharides or when glycosylation was inhibited by tunicamycin. The presence of three polypeptide forms rather than a single form suggested that proteolytic cleavage had occurred at two sites in both the glycosylated and non-glycosylated forms. Proteolytically cleaved IFN-gamma was more prevalent in cell lysates than in the secreted glycoprotein. In common with naturally produced IFN-gamma, both fully glycosylated IFN-gamma (asparagine residues 28 and 100 occupied) and partially glycosylated product (thought to be substituted at position Asn28) were secreted. This was deduced from the Mr of the glycosylated products and the relative amounts of sialic acid expressed by each variant. In contrast with naturally produced IFN-gamma, non-glycosylated IFN-gamma was also secreted by the transfected CHO cells. When the cells were grown in batch culture in serum-free medium under pH and dissolved-oxygen control, the proportion of non-glycosylated IFN-gamma increased from 3 to 5% after 3 h, to 30% of the total IFN-gamma present after 195 h. This change in the proportion of glycosylated protein produced was not seen when metabolically labelled IFN-gamma was incubated for 96 h with cell-free supernatant from actively growing CHO cells. This implied that an alteration in intracellular glycosylation was occurring rather than a degradation of oligosaccharide side chains after secretion. The decrease in IFN-gamma glycosylation was independent of the glucose concentration in the culture medium, but could be related to specific growth and IFN-gamma production rates, as these declined steadily after 50 h of culture, in line with the increased production of non-glycosylated IFN-gamma.     

The effect of the dilution rate on CHO cell physiology and recombinant interferon-gamma production in glucose-limited chemostat culture

The physiology of a recombinant Chinese hamster ovary cell line in glucose-limited chemostat culture was studied over a range of dilution rates (D = 0.008 to 0.20 h(-1)). The specific growth rate (mu) deviated from D at low dilution rates due to an increased specific death rate. Extrapolation of these data suggested a minimum specific growth rate of 0.011 h(-1) (mu(max) = 0.025 h(-1)) The metabolism at each steady state was characterized by determining the metabolic quotients for glucose, lactate, ammonia, amino acids, and interferon-gamma (IFN-gamma). The specific rate of glucose uptake increased linearly with mu, and the saturation constant for glucose (K(s)) was calculated to be 59.6 muM. There was a linear increase in the rate of lactate production with a higher yield of lactate from glucose at high growth rates. The decline in the rate of production of lactate, alanine, and serine at low growth rate was consistent with the limitation of the glycolytic pathway by glucose. The specific rate of IFN-gamma production increased with mu in a manner indicative of a growth-related product. Despite changes in the IFN-gamma production rate and cell physiology, the pattern of IFN-gamma glycosylation was similar at all except the lowest growth rates where there was increased production of nonglycosylated IFN-gamma. (c) 1993 John Wiley & Sons, Inc.     

Effects of ammonia and lactate on hybridoma growth, metabolism, and antibody production

The influence of ammonia and lactate on cell growth, metabolic, and antibody production rates was investigated for murine hybridoma cell line 163.4G5.3 during batch culture. The specific growth rate was reduced by one-half in the presence of an initial ammonia concentration of 4 mM. Increasing ammonia levels accelerated glucose and glutamine consumption, decreased ammonia yield from glutamine, and increased alanine yield from glutamine. Although the amount of antibody produced decreased with increasing ammonia concentration, the specific antibody productivity remained relatively constant around a value of 0.22 pg/cell-h. The specific growth rate was reduced by one-half at an initial lactate concentration of 55 mM. Although specific glucose and glutamine uptake rates were increased at high lacatate concentration, they showed a decrease after making corrections for medium osmolarity. The yield coefficient of lactate from glucose decreased at high lactate concentrations. A similar decrease was observed for the ammonia yield coefficient from glutamine. At elevated lactate concentrations, specific antibody productivities increased, possibly due to the increase in medium osmolarity. The specific oxygen uptake rate was insensitive to ammonia and lactate concentrations. Addition of ammonia and lactate increased the calculated metabolic energy production of the cells. At high ammonia and lactate, the contribution of glycolysis to total energy production increased. Decreasing external pH and increasing ammonia concentrations caused cytoplasmic acidification. Effect of lactate on intracellular pH was insignificant, whereas increasing osmolarity caused cytoplasmic alkalinization.     

Online detection of feed demand in high cell density cultures of Escherichia coli by measurement of changes in dissolved oxygen transients in complex media

A starvation-based dissolved oxygen (DO) transient controller was developed to supply growth-limiting substrate to high cell density fed-batch cultures of recombinant Escherichia coli. The algorithm adjusted a preexisting feed rate in proportion to the culture's oxygen demand, which was estimated from transients in the DO concentration after short periods of feed interruption. In this manner, the addition of glucose feed was precisely controlled at a rate that did not exceed the acetate production threshold, thus preventing acetate accumulation. In comparison to exponential feed algorithms commonly used in industry, the implementation of the new feeding strategy increased the final cell density from 32 to 44 g (dry cell weight).L(-1), with less than 16 mM acetate accumulated, producing an ideal culture for subsequent induction. Despite a constant starvation level and relatively low levels of acetate, experimental cultivations still tended to produce acetate towards the end of the process. The use of a simple Monod model provided an explanation as to why this may occur in high cell density cultivations and suggests how it may be overcome.     

Dependence on glucose limitation of the pCO2 influences on CHO cell growth, metabolism and IgG production

The culture levels of glucose and CO(2) have been reported to independently have important influences on mammalian cell processes. In this work the combined effects of glucose limitation and CO(2) partial pressure (pCO(2)) on monoclonal antibody (IgG) producing Chinese Hamster Ovary cells were investigated in a perfusion reactor operated with controlled cell specific medium feed rate, pH and osmolality. Under high glucose conditions (14.3 +/- 0.8 mM), the apparent growth rate decreased (from 0.021 to 0.009 h(-1)) as the pCO(2) increased to approximately 220 mmHg, while the cell specific IgG productivity was almost unchanged. The lactate yield from glucose was not affected by pCO(2) up to approximately 220 mmHg and glucose was mainly converted to lactate. A feed medium modification from high (33 mM) to low (6 mM) glucose resulted in <0.1 mM glucose in the culture. As a result of apparently shifting metabolism towards the conversion of pyruvate to CO(2), both the ratio of lactate to glucose and the alanine production rate were lowered (1.51-1.14 and 17.7-0.56 nmol/10(6) cells h, respectively). Interestingly, when the pCO(2) was increased to approximately 140 mmHg, limiting glucose resulted in 1.7-fold higher growth rates, compared to high glucose conditions. However, at approximately 220 mmHg pCO(2) this beneficial effect of glucose limitation on these CHO cells was lost as the growth rate dropped dramatically to 0.008 h(-1) and the IgG productivity was lowered by 15% (P < 0.01) relative to the high glucose condition. The IgG galactosylation increased under glucose- limited compared to high-glucose conditions.     

Adaptive control at low glucose concentration of HEK-293 cell serum-free cultures.

Fed-batch cultures were implemented to study the metabolism of HEK-293 cells. Glucose, measured every 30 min by a FIA biosensor system, was maintained at 1 mM throughout the culture using an adaptive nonlinear controller based on minimal process modeling. The controller performed satisfactorily at both low and high cell concentrations without the need for retuning between different culture phases. Overall, lactate production was significantly reduced by maintaining a low glucose concentration, thus decreasing the rate of glycolysis. The rates of glucose and glutamine uptake as well as the lactate and ammonia production were compared to those obtained in batch mode with an initial glucose concentration of 21 mM. Basically, three phases were observed in both culture modes. The metabolic shift from the first to the second phase was characterized by a significant reduction in glucose consumption and lactate production while maximum growth rate was maintained. The specific respiration rate appeared unchanged during the first two phases, suggesting that no change occurred in the oxidative pathway capacity. In the third phase, cell growth became slower very likely due to glutamine limitation.     

Tetracycline-controlled expression of glycosylated porcine interferon-gamma in mammalian cells

Tetracycline-controlled expression plasmids that allow inducible expression of proteins in mammalian cells (Gossen & Bujard, 1992), have been used to express porcine interferon-gamma in the RK-13 rabbit kidney cell line. Following neomycin selection, stable clones produced recombinant, glycosylated porcine interferon-gamma (rGPoIFN-gamma) only after removal of tetracycline (Tc). Southern blot analysis of one clone showed that approximately 50 copies of IFN-gamma cDNA were present in the cell genome. In the absence of Tc, stable clones secreted large amounts of rGPoIFN-gamma (up to 16 microg/ml) into the medium supplemented with 10% FCS and high glucose concentration. Molecular weight comparison of 35S-Methionine, labelled rGPoIFN-gamma with natural leukocytic IFN-gamma after immunoprecipitation, revealed 4 major glycoforms with apparent Mr of 27,000; 25,000; 20,000 and 18,500, that are almost identical in both IFN-gamma species. In both cases, all 4 glycoforms resolved into 2 polypeptide monomers with apparent Mr of 16,500 and 14,500 upon deglycosylation with N-glycosydase F. The biological activity of rGPoIFN-gamma was in the same range as that of natural leukocytic PoIFN-gamma (2 x 10(6) U/mg). Eventually, this recombinant mammalian IFN-gamma should constitute a very useful substitute for leukocyte PoIFN-gamma in in vitro or in vivo experiments.     

Increased t-PA yields using ultrafiltration of an inhibitory product from CHO fed-batch culture

Fed-batch operation for the production of t-PA using Chinese Hamster Ovary (CHO) cells was optimized using serial and parallel experimentation. The feed, an isotonic concentrate, was improved to obtain 2- to 2.5-fold increases in integrated viable cell days versus batch. With a low glucose inoculum train, the viability index was further increased up to 4.5-fold. Hydrolysates were substituted for the amino acid portion of the concentrate with no significant change in fed-batch results. The concentrate addition rate was based on a constant 4 pmol/cell.day glucose uptake rate that maintained a relatively constant glucose concentration (approximately 3 mM). Increased viable cell indices did not lead to concomitant increases in t-PA concentrations compared to batch. The fed-batch concentrate and feeding strategy were shown to be effective in hybridoma culture, where a 4-fold increase in viable cell index yielded a 4-fold increase in antibody concentration. The half-life of t-PA decreased from 43 to 15 days with decreasing cell viability (from 92% to 71%), but this was not sufficient to explain the apparent t-PA threshold. Instead, the CHO results were explained by a reduction in t-PA production at higher extracellular t-PA concentrations that limited the fed-batch maximum at 35 mg/L for the cell line investigated. Analysis of both the total and t-PA mRNA levels revealed no response to increasing extracellular t-PA concentrations upon exogenous additions. Instead, intracellular t-PA levels were increased, revealing a possible secretory pathway limitation. A new reactor configuration was developed using an acoustic filter to retain the cells in the reactor while an ultrafiltration module stripped t-PA from the clarified medium before the permeate was returned to the reactor. By adding this harvesting step, the t-PA fed-batch production was increased over 2-fold, up to a yield of 80 mg/L.     

Continuous, high level production and excretion of a plasmid-encoded protein by Escherichia coli in a two-stage chemostat

The stable continuous overproduction of a plasmidencoded protein, beta-lactamase, for at least 50 days by Escherichia coli K-12, RB791(pKN), with release into the culture medium has been demonstrated in two-stage chemostats. The second-stage culture was continuously induced with 0.1 mM IPTG. Continuous expression of beta-lactamase could not be sustained with this strain in a single-stage chemostat because of cell death and selection for lac(-1) cells. beta-Lactamase production in the second stage was sensitive to the second-stage dilution rate and the distribution of the limiting substrate (i.e., glucose) between the first and second stages. The fraction of viable, excreting cells and the average copy number in the induced culture was measurably higher under those conditions of dilution rate and substrate distribution which yielded high beta-lactamase levels. The best operating conditions found at 20 degrees C were a first-stage dilution rate of 0.12 h(-1), a second-stage dilution rate of 0.03 h(-1), and equal glucose feed supplied to each stage. Enzymatically active beta-lactamase was produced at a level of 25% of total cellular protein with 90% excretion yielding 300 mg beta-lactamase/L that was 50% pure at an OD(600) < 6. (c) 1993 Wiley & Sons, Inc.     

Improvement of interferon-gamma sialylation in Chinese hamster ovary cell culture by feeding of N-acetylmannosamine

Because the presence of sialic acid can extend circulatory lifetime, a high degree of sialylation is often a desirable feature of therapeutic glycoproteins. In this study, the incomplete intracellular sialylation of interferon-gamma (IFN-gamma), produced by Chinese hamster ovary cell culture, was minimized by supplementing the culture medium with N-acetylmannosamine (ManNAc), a direct intracellular precursor for sialic acid synthesis. By introducing 20 mM ManNAc into the culture medium, incompletely sialylated biantennary glycan structures were reduced from 35% to 20% at the Asn97 glycosylation site. This effect was achieved without affecting cell growth or product yield. The intracellular pool of CMP-sialic acid, the nucleotide sugar substrate for sialyltransferase, was also extracted and quantified by HPLC. Feeding of 20 mM ManNAc increased this intracellular pool of CMP-sialic acid by nearly thirtyfold compared with unsupplemented medium. When radiolabeled ManNAc was used to trace the incorporation of the precursor, it was found that supplemental ManNAc was exclusively incorporated into IFN-gamma as sialic acid and that, at 20 mM ManNAc feeding, nearly 100% of product sialylation originated from the supplemental precursor.     

Monitoring recombinant human interferon-gamma N-glycosylation during perfused fluidized-bed and stirred-tank batch culture of CHO cells

Chinese hamster ovary cells producing recombinant human interferon-gamma were cultivated for 500 h attached to macroporous microcarriers in a perfused, fluidized-bed bioreactor, reaching a maximum cell density in excess of 3 x 10(7) cells (mL microcarrier)-1 at a specific growth rate (mu) of 0.010 h-1. During establishment of the culture, the N-glycosylation of secreted recombinant IFN-gamma was monitored by capillary electrophoresis of intact IFN-gamma proteins and by HPLC analysis of released N-glycans. Rapid analysis of IFN-gamma by micellar electrokinetic capillary chromatography resolved the three glycosylation site occupancy variants of recombinant IFN-gamma (two Asn sites occupied, one Asn site occupied and nonglycosylated) in under 10 min per sample; the relative proportions of these variants remained constant during culture. Analysis of IFN-gamma by capillary isoelectric focusing resolved at least 11 differently sialylated glycoforms over a pI range of 3.4 to 6.4, enabling rapid quantitation of this important source of microheterogeneity. During perfusion culture the relative proportion of acidic IFN-gamma proteins increased after 210 h of culture, indicative of an increase in N-glycan sialylation. This was confirmed by cation-exchange HPLC analysis of released, fluorophore-labeled N-glycans, which showed an increase in the proportion of tri- and tetrasialylated N-glycans associated with IFN-gamma during culture, with a concomitant decrease in the proportion of monosialylated and neutral N-glycans. Comparative analyses of IFN-gamma produced by CHO cells in stirred-tank culture showed that N-glycan sialylation was stable until late in culture, when a decline in sialylation coincided with the onset of cell death and lysis. This study demonstrates that different modes of capillary electrophoresis can be employed to rapidly and quantitatively monitor the main sources of glycoprotein variation, and that the culture system and operation may influence the glycosylation of a recombinant glycoprotein.     

Catabolic control of hybridoma cells by glucose and glutamine limited fed batch cultures

Substrate limited fed batch cultures were used to study growth and overflow metabolism in hybridoma cells. A glucose limited fed batch, a glutamine limited fed batch, and a combined glucose and glutamine limited red batch culture were compared with batch cultures. In all cultures mu reaches its maximum early during growth and decreases thereafter so that no exponential growth and decreases thereafter so that no exponential growth rate limiting, although the glutamine concentration (>0.085mM) was lower than reported K(s) vales and glucose was below 0.9mM; but some other nutrients (s) was the cause as verified by simulations. Slightly more cells and antibodies were produced in the combined fed batch compared with the batch culture. The specific rates for consumption of glucose and glutamine were dramatically influenced in fed batch cultures resulting in major metabolic changes. Glucose limitation decreased lactate formation, but increased glutamine consumption and ammonium formation. Glutamine limitation decreased ammonium and alanine formation of lactate, alanine, and ammonium was negligible in the dual-substrate limited fed batch culture. The efficiency of the energy metabolism increased, as judged by the increase in the cellular yield coefficient for glucose by 100% and for glutamine by 150% and by the change in the metabolic ratios lac/glc, ala/ln, and NH(x)/ln, in the combined fed culture. The data indicate that a larger proportion of consumed glutamine enters the TCA cycle through the glutamate dehydrogenase pathway, which releases more energy from glutamine than the transamination pathway. We suggest that the main reasons for these changes are decreased uptake rates of glucose and glutamine, which in turn lead to a reduction of the pyruvate pool and a restriction of the flux through glutaminase and lactate dehydrogenase. There appears to be potential for further cell growth in the dual-substrate-limited fed batch culture as judged by a comparison of mu in the different cultures. (c) 1994 John Wiley & Sons, Inc.     

Maximum production in a bakers' yeast fed-batch culture by a tubing method

A feedback control system of the glucose feed rate in a bakers' yeast fed-batch culture was developed by keeping the ethanol concentration constant. A PID controller and on–off controller were applied and discussed with the aid of the porous Teflon tubing method. Experimental results showed the effectiveness of the control system for avoiding the glucose effect and glucose starvation. It was shown that the feedback control system developed hare could achieve a maximum specific growth rate of 0.3 h^?1 or a maximum cell yield of 0.5 g cell/g glucose in the fedhyphen;batch culture.     

Optimization of Vi capsular polysaccharide production during growth of Salmonella enterica serotype Typhi Ty2 in a bioreactor

Vi capsular polysaccharide is synthesized during growth of Salmonella typhi Ty2 and is spontaneously released from the bacterial cells into the culture medium during culture. Vi production was dependent on cell growth and the greater the cell mass the greater the production of Vi. Using fed batch culture to optimize bacterial growth resulted is an increase in cell mass and consequently Vi production. The yield of Vi obtained in fed batch culture was 415 mg l⁻¹, which was over three times that, obtained in batch culture. A proportion of the Vi remained cell associated in the form of a capsule and at least part of this was released from the bacterial surface by sonication. The size of the Vi polysaccharide produced was consistently high and did not change during the different phases of bacterial growth. The synthesis of Vi was also dependent upon the media components and the fermentation conditions. The presence of high concentrations of glucose at the beginning of growth inhibited the production of Vi, particularly during the stationary phase. At a concentration of 400 mM sodium phosphate the synthesis of Vi was strongly inhibited.     

Growth conditions of clostridium perfringens type B for production of toxins used to obtain veterinary vaccines

The diseases caused for Clostridium perfringens are generically called enterotoxemias because toxins produced in the intestine may be absorbed into the general circulation. C. perfringens type B, grown in batch fermentation, produced toxins used to obtain veterinary vaccines. Glucose in concentrations of 1.4–111.1 mM was used to define the culture medium. The minimum concentration for a satisfactory production of vaccines against clostridial diseases was 55.6 mM. Best results were brought forth by meat and casein peptones, both in the concentration 5.0 g l^?1 in combination with glucose and a culture pH maintained at 6.5 throughout the fermentation process. The production of lactic, acetic and propionic organic acids was observed. Ethanol was the metabolite produced in the highest concentration when cultures maintained steady pH of 6.5 with exception of cultures with initial glucose concentration of 1.4 mM, where the highest production was of propionic acid. Maximal cell concentration and the highest toxin title concomitantly low yield coefficient to organic acids and ethanol were obtained using basal medium containing 111.1 mM glucose under a controlled pH culture (pH) 6.5 in batch fermentations of C. perfringens type B. These data contribute to improve process for industrial toxin production allowing better condition to produce a toxoid vaccine.     

Cultivation of hybridoma cells in continuous cultures: kinetics of growth and product formation

Mouse hybridoma cells were grown in suspension in continuous stirred bioreactors. Cell growth, substrate utilization, and monoclonal antibody (MAb) production were studied using serum-free medium. Steady-state data were obtained at different dilution rates, between 0.012 and 0.039 h(-1) Viability was profoundly affected by dilution rate, particularly near the lower end of the dilution-rate range investigated. MAb concentration and productivity went through a maximum with respect to dilution rate. Lactate yield on glucose declined with in creasing dilution rate. Experiments were carried out to study the effects of medium glucose concentration on cell growth, product formation, and lactate yield on glucose. Reduction of glucose concentration in the feed medium did not considerably affect cell density and MAb concentration in the culture, but lactate levels dropped sharply; lactate yield on glucose declined substantially, indicating alterations in cell metabolic path ways for energy metabolism. Optimization strategy for continuous cell culture is discussed.     

Expression pattern of glucose metabolism genes in relation to development rate of buffalo (Bubalus bubalis) oocytes and in vitro–produced embryos

The expression pattern of glucose metabolism genes (hexokinase, phosphofructokinase, glucose-6-phosphate dehydrogenase [G6PDH], lactate dehydrogenase [LDH], and pyruvate dehydrogenase [PDH]) were studied in buffalo in vitro–matured oocytes and in vitro–produced embryos cultured under different glucose concentrations (0 mM, 1.5 mM, 5.6 mM, and 10 mM) during in vitro maturation of oocytes and culture of IVF produced embryos. The expression of the genes varied significantly over the cleavage stages under different glucose concentrations. Developmental rate of embryos was highest under a constant glucose level (5.6 mM) throughout during maturation of oocytes and embryo culture. Expression pattern of glucose metabolism genes under optimum glucose level (5.6 mM) indicated that glycolysis is the major pathway of glucose metabolism during oocyte maturation and early embryonic stages (pre-maternal to zygotic transition [MZT]) and shifts to oxidative phosphorylation during post-MZT stages in buffalo embryos. Higher glucose level (10 mM) caused abrupt changes in gene expression and resulted in shifting toward anaerobic metabolism of glucose during post-MZT stages. This resulted in decreased development rate of embryos during post-MZT stages. High expression of LDH and PDH in the control groups (0 mM glucose) indicated that in absence of glucose, embryos try to use available pyruvate and lactate sources, but succumb to handle the post-MZT energy requirement, resulting to poor development rate. Expression pattern of G6PDH during oocyte maturation as well early embryonic development was found predictive of quality and development competence of oocytes/ embryos.     

Feed development for fed‐batch CHO production process by semisteady state analysis

Semisteady state cultures are useful for studying cell physiology and facilitating media development. Two semisteady states with a viable cell density of 5.5 million cells/mL were obtained in CHO cell cultures and compared with a fed‐batch mode control. In the first semisteady state, the culture was maintained at 5 mM glucose and 0.5 mM glutamine. The second condition had threefold higher concentrations of both nutrients, which led to a 10% increase in lactate production, a 78% increase in ammonia production, and a 30% reduction in cell growth rate. The differences between the two semisteady states indicate that maintaining relatively low levels of glucose and glutamine can reduce the production of lactate and ammonia. Specific amino acid production and consumption indicated further metabolic differences between the two semisteady states and fed‐batch mode. The results from this experiment shed light in the feeding strategy for a fed‐batch process and feed medium enhancement. The fed‐batch process utilizes a feeding strategy whereby the feed added was based on glucose levels in the bioreactor. To evaluate if a fixed feed strategy would improve robustness and process consistency, two alternative feeding strategies were implemented. A constant volume feed of 30% or 40% of the initial culture volume fed over the course of cell culture was evaluated. The results indicate that a constant volumetric‐based feed can be more beneficial than a glucose‐based feeding strategy. This study demonstrated the applicability of analyzing CHO cultures in semisteady state for feed enhancement and continuous process improvement. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Pertussigen enhances antigen-driven interferon-gamma production by sensitized lymphoid cells

We have studied the effects on interferon-gamma (IFN-gamma) production of pertussigen, a protein toxin from Bordetella pertussis that augments and prolongs delayed-type hypersensitivity (DTH) reactions. Lymphoid cell suspensions from immunized mice were incubated with antigen or mitogen, and the culture supernatants were assayed for IFN-gamma. The production of IFN-gamma on exposure to specific antigen or concanavalin A was greatly enhanced if mice were given pertussigen at the time of immunization. There was no detectable IFN-gamma production when cells were exposed to saline or to an irrelevant antigen. The effect of pertussigen on antigen-driven IFN-gamma production correlated with its effect on the capacity of the same cell populations to transfer DTH. The enhanced IFN-gamma production by cells from mice given pertussigen could not be attributed to an increased antigen-presenting capacity of this cell population. Production of IFN-gamma was abolished if the cells were pretreated with emetine, but not with mitomycin C, and the release of IFN-gamma was not detected in the first 8 hr of culture. After immunization with pertussigen, IFN-gamma was produced by lymph node and spleen cells from 7 days onward and both cell types produced IFN-gamma until at least 30 days after immunization. It is suggested that the augmentation of antigen-specific IFN-gamma production may contribute to the prolonged DTH reactions induced by pertussigen in vivo.     

Cyclic fed-batch culture for production of human serum albumin in Pichia pastoris

Simple cyclic fed-batch culture (cfbc), consisting of a constant medium feed with periodic withdrawals of culture, resulted in a product yield (13.4 mg protein per gram biomass) similar to that obtained using the complex multiphase industrial production strategy (13.7 mg protein per gram biomass). In cfbc, productivity was ultimately limited by the rate at which the cells could assimilate methanol. Glycerol was inhibitory to growth at high concentrations. However, product yield continued to increase as the glycerol concentration was increased. In chemostat culture, dissolved oxygen concentration influenced product yield independently of any detectable influence on cell growth.